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Qatar Foundation Annual Research Conference Proceedings Volume 2016 Issue 1
- Conference date: 22-23 Mar 2016
- Location: Qatar National Convention Center (QNCC), Doha, Qatar
- Volume number: 2016
- Published: 21 March 2016
151 - 200 of 656 results
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Usefulness of In-Situ Synchrotron Study on Scale Formation during CO 2 Corrosion of Mild Steel: A Review
More LessDespite the availability of the detailed knowledge about the chemical, electrochemical and transport processes associated with the formation of ferrous carbonate during CO2- corrosion of mild steel, information available about the mechanism of early nucleation stages of FeCO3 (siderite) film formation was only speculative. In depth knowledge related to the early stage nucleation of siderite scale and its subsequent development and gradual growth were revealed only recently by judicious exploration of in-situ synchrotron based experimentation. Moreover, application of in-situ synchrotron x-ray diffraction technique rendered ability to monitor the gradual real time growth of FeCO3 scale with the efficacy of simultaneous controllability of the corrosion conditions electrochemically. This work shades light on how in-situ synchrotron study revealed apparent mysteries related to formation & growth of siderite scale during CO2- corrosion of mild steel. Keywords: In-situ synchrotron, CO2-Corrosion of mild steel, Nucleation mechanism during CO2- corrosion.
Figure 1 (a) and (b) illustrate the photograph and schematic of experimental set up for in-situ synchrotron X-ray diffraction experiments using the powder diffraction Australian beam line.
Figure 2 shows the anodic current as a function of time in a potentiostatic test in the NaCl solution at pH 6.3 (pCO2 = 1bar) and an applied potential of − 500 mV (vs SCE), together with the intensities of the Fe and FeCO3 signals from the in-situ synchrotron XRD [1]. There is a clear peak in the current transient, with the XRD results showing FeCO3 formation during the increasing portion of this transient and then a rapidly decreasing rate of FeCO3 formation as the anodic current decreases towards the end of the test, indicating the growth of a protective surface scale. In these studies, it is shown that siderite only forms once the critical super-saturation is exceeded within a defined boundary layer and that the steel microstructure has critical role in developing a surface texture within which the critical super-saturation could develop. This idea of siderite nucleation in solution with a critically saturated boundary layer close to the metal surface is unlike the heterogeneous nucleation and growth phenomenon which occurs directly on the surface via solid state formation [1]. Establishment of this ideology was able to resolve the apparent thermodynamic anomaly observed in practice.
One of the apparent thermodynamic anomalies in CO2- H2S mixed system is couched on the fact that in spite of the higher (∼3 time) aqueous solubility of H2S compared to CO2 under similar temperature and pressure conditions, the formation of iron sulfide has been observed to be faster and predominant over iron carbonate under most parametric conditions even at a trace level of H2S concentration in CO2-H2S system. This fact indicates the formation of iron sulfide and iron carbonate films to be regulated by different mechanisms. In-situ synchrotron study revealed the early stage nucleation of iron carbonate (siderite) film and indicated that to be a gradual process giving rise to the formation of crystalline siderite phase only after the critical supersaturation stage is reached. Given that, there is significant time lag between the start of supersaturation and critical supersaturation limit, there is a possibility for iron sulfide formation during that time lag, as it forms by solid state formation mechanism which is a faster process. It is the in-situ synchrotron study which made it possible to illustrate the appreciable time lag between the start of supersaturation and critical supersaturation limit.
Ingham et al. [2] used in-situ synchrotron small- and wide-angle X-ray scattering (SAXS and WAXS) to demonstrate that the formation of crystalline siderite (FeCO3) during the corrosion of steel in CO2-saturated brine is actually preceded by the formation of a colloidal precipitate and an amorphous surface layer, both assumed to be amorphous ferrous carbonate. Grazing incidence SAXS showed that upon the application of an anodic potential, film forms instantaneously and then a separate population of particles develops in the later stage followed by the formation of the ultimate crystalline FeCO3, observed by WAXS. Ingham et al. [2] interpreted these observations in terms of crystal nucleation within the amorphous surface layer. This observation was speculated to bear a significant consequence on the morphology of the corrosion scale and hence its protectiveness. However, it would be important to understand the effects of local pH change as well as variation in temperature in this gradual formation and development of siderite scale and then to find out a quantitative correlation of this process with the mentioned parameters.
The fact of stable, adherent and protective siderite film formation in presence of trace amount Cr3+ was known [3, 4]. However the associated mechanism was not clearly understood until in-situ synchrotron x-ray diffraction study revealed a clearer picture of the mechanistic aspect of the expedited siderite film formation in presence of traces of Cr3+[2, 5]. This recently done in-situ synchrotron study made it clear that traces of Cr3+ in the solution significantly expedites the precipitation rate of the colloidal precursor and thus accelerate the appearance of the crystalline scale through its catalyzing influence on the nucleation process by modulating the local pH level at the steel surface and thus reducing of the critical supersaturation for precipitation.
Another interesting and critical factor in developing surface texture within which the critical supersaturation can be developed is steel microstructure. Consequently, steel microstructure must have intimate relationship with the corrosion process and morphology of the scale as microstructure can change the diffusion conditions at the steel surface affecting the local supersaturation of siderite. However, in-depth mechanistic information related microstructural effect on adherent and protective scale formation was hardly available in the literature. It is recommended to perform in-situ synchrotron X-ray diffraction experiment in order to make a detailed investigation of such a phenomena. Ko et al [6] recently conducted such a study in order to investigate the effect of microstructure and boundary layer conditions on CO2 corrosion of low alloy steels. This recent investigation clearly demonstrated that the nucleation of crystalline scales onto the surface of steels under CO2 corrosion at elevated temperature is critically dependent on the initial surface roughness, microstructure-related surface roughness developed during corrosion. This study also indicated the interdependence between microstructure and chromium-enhanced siderite nucleation. However, finding out the quantitative effects of surface roughness on the initial nucleation process (rate) of the scale as well as the stability of the scale would be a good addition to this study.
References:
[1] B. Ingham, M. Ko, G. Kear, P. Kappen, N. Laycock, J. A. Kimpton and D. E. Williams, “In-situ synchrotron X-ray diffraction study of surface scale formation during CO2 corrosion of carbon steel at temperatures up to 90°C”, Corrosion Science, 52 (2010), 3052–3061.
[2] Bridget Ingham, Monika Ko, Nick Laycock, Nigel M. Kirby, David E. Williams, “First stages of siderite crystallisation during CO2 corrosion of steel evaluated using in-situ synchrotron small- and wide- angle X-ray Scattering”, Faraday Discussion, 2015.
[3] M B Kermani, J C Gonzales, G L Turconi, D Emonds, G. Dicken, L Scoppio, “Development of Superior Corrodion Resistance 3% Steels for Downhole Applications”, NACE Annual Conference & Exposition, paper 3116, 2003.
[4] R M Garrels, C L Christ, “Solution, minerals, and equilibria”: San Francisco, California, Freeman, Cooper & Company, 1965, p 450.
[5] M Ko, B Ingham, N Laycock, D E Williams, “In-situ synchrotron X-ray diffraction study on the effect of chromium additions to the steel and solution on CO2 corrosion of pipeline steels”, Corrosion Science, Vol 80, 2014, pp 237–246.
[6] M. Ko, B. Ingham, N. Laycock, D.E. Williams, “In situ synchrotron X-ray diffraction study of the effect of microstructure and boundary layer conditions on CO2 corrosion of pipeline steels”, Corrosion Science, Vol 90, 2015, pp 192–201.
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Resource Allocation Under Footprint Constraints in Industrial Parks
Authors: Dhabia M Al-Mohannadi, Kholoud Abdulaziz, Sabla Y. Alnouri and Patrick LinkeWith growing climate change concerns, depleting natural resources and decrease in oil and gas prices, it is more vital than ever to efficiently manage natural resource allocation. Methane, the key component in natural gas and a raw material for numerous chemicals, is Qatar's more abundant resource. Natural gas can be monetized through many alternative paths. It can be sold as natural gas, either through pipelines or in liquefied form, or converted into diverse sets of fuels and materials using many alternative processing technologies. In the meantime, concerns of the effects of increased carbon dioxide concentration in the atmosphere, majority of which are emitted from large industrial stationary sources and fuel consumption, have caused the global society to seek ambitious emission reduction targets.
While on the one hand natural gas provides a clean fuel associated and enables carbon dioxide emissions through fuel switching globally, its local processing is associated with significant footprints. In the case of Qatar and its small population, this has resulted in very high per capita emissions. Most of the emissions are stationary and spatially concentrated in industrial clusters, where they originate mainly from natural gas processing, hydrocarbon processing, petrochemicals and metals production, and power and water generation.
The industrial sector is challenged to balance profit making activities from natural gas monetization with increasing pressures to reduce overall carbon dioxide emissions. Conventional design of industrial parks centering on natural gas are carried out in an ad-hoc process that depends on the expertise of designers, available capital, market demand and regulations. Reduction methods in the past have been limited in technology, energy integration or geographical proximity to apply carbon capture and sequestration (CCS).
Recently, carbon integration (Al-Mohannadi and Linke, 2015a,b) has been introduced as a systematic approach to determine the most efficient carbon dioxide reduction options in industrial parks by considering multiple carbon dioxide sources, potential carbon sinks, the layout of the city and the associated costs of transmission and conditioning. Carbon integration looks into the various conversion routes that take carbon dioxide into value added products, which can be converted chemically, biologically or through geographical utilization such as Enhanced Oil Recovery (EOR) applications. This creates incentives to reduce carbon emissions, to create synergies between firms and to produce additional products in the cluster, while adhering to required emission reduction targets.
Beyond focusing on low cost carbon dioxide emissions reduction, the broader design challenge for a natural gas monetizing industrial cluster is to identify the most promising configurations from the vast number of alternatives that exist from the possible combinations of many alternative natural gas monetization processes, and the many alternative carbon management options that could be applied, whilst exploiting synergies between natural gas conversion and carbon management. Most previous works have focused on different aspects of the overall problem: optimizing gas conversion processes, and managing carbon dioxide emissions reductions. Very few works have considered monetization in industrial clusters, and there is no published work on how to systemically make gas monetization decisions under carbon dioxide emissions constraints.
This work introduces the first systematic approach to allocate natural resource under carbon dioxide footprint constraints. The approach yields integrated natural gas and carbon dioxide management schemes that yield the maximum profit for the given gas monetization and carbon dioxide management options and constraints that exist in the industrial cluster. The work explores different carbon dioxide emission reduction scenarios; expansion plans and determines most profitable product mix from an industrial cluster. By taking into consideration the tradeoff between environmental performance and potential profitability of natural resource allocation, it provides valuable information to decision makers from an optimization based tool. Policy makers and regulators can use the tool for developing strategies and for planning of more sustainable industrial clusters, parks or cities.
The work is illustrated using a case study to demonstrate the application of the method on industrial cluster resembling a configuration of gas monetization options often observed in oil and gas centered economies.
Keywords
Resource Allocation, Climate Change, Carbon Dioxide emissions, Carbon Integration, Natural Gas Allocation, Gas Monetization, Carbon Reduction, Process Integration, Industrial Parks, Planning, Modeling, Optimization.
References
Al-Mohannadi, D.M., P. Linke (2015). On the Systematic Carbon Integration of Industrial Parks for Climate Footprint Reduction. Journal of Cleaner Production, DOI: 10.1016/j.jclepro.2015.05.094.
Al-Mohannadi, D.M., S.K. Bishnu, P. Linke, S.Y. Alnouri (2015b). Systematic Multi-Period Carbon Integration in an Industrial City. Chemical Engineering Transactions 45, 1219–1224.
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Improved Gas and Water Pollution Sensors Based on AlGaN/GaN HEMTs for Air and Water Treatment Systems
At the present time, serious threats are being posed to the environment due to pollutants in both the air (e.g. automotive exhaust emissions) and water (e.g. phosphates, nitrates, heavy metals). In an effort to improve these environmental hazards, automotive emissions standards and regulations on water pollutants are becoming more and more strict each year. One of the major limitations in meeting these regulations is the ability to quickly and accurately detect low concentrations of the target molecules.
We report the fabrication and experimental testing of a new generation of microsensor technology that can detect a wide range of gases in the air as well as pollutants in a liquid environment. These sensors are based on AlGaN/GaN high electron mobility transistors (HEMT) with functionalized gate contacts acting as the sensing layer. The use of high bandgap, group-III nitride semiconductor materials gives the sensors a high thermal and chemical stability, making them suitable for high temperature applications (above 600°C) and in harsh chemical conditions. Depending on the type and structure of functional layer, the adsorption of the target molecules leads to change the surface depletion layer which has a direct affect on the sensitivity and the selectivity of the device. Extensive modeling and design of the AlGaN/GaN HEMTs has been performed to optimize the devices for detection of exhaust gases and water pollutants. This includes the design of each of the material parameters (e.g. AlGaN thickness, Al incorporation) and the functionalized contacts (e.g. material, dimensions, morphology).
Experimental results using a Pt sensing layer show detection of 10–1000 ppm NO and NO2 gas with changes in current of 0.8 and 2.8 mA, respectively. Detection of NH3 gas in a range of 150 ppb–15 ppm was also demonstrated, and can be compared to detection limits of only 35 ppm for similar devices. This is the first time that detection of NO has been demonstrated using a HEMT sensor, and the first time selective detection of NO, NO2, and NH3 has been demonstrated using a single transistor device. Furthermore, the sensitivity to NO2 and NH3 were significantly higher in our optimized device compared to other HEMT sensors. Dynamic response times were shown to be between 1–3 seconds for each gas, showing that these sensors can perform in real-time applications.
In addition to exhaust gas detection, an open-gate HEMT sensor was designed and fabricated as a water pollution sensor and showed detection of both phosphates and nitrates in water. This is the first time that phosphates have been detected using a HEMT sensor, and shows that HEMT sensors can be useful in the prevention of eutrophication of fresh water bodies. We are currently exploring HEMT sensor designs for the detection other water pollutants such as heavy metals, inorganic and organic molecules that damage or contaminate water supplies.
The experimental results presented in this abstract demonstrate that the functionalized AlGaN/GaN HEMT sensors we have developed are promising for real-time air and water treatment applications due to their low detection limits, high sensitivities, fast response times, and selectivity by functionalizing the sensing layer for specific target molecules. Therefore, this technology has the potential to drastically improve the reduction of pollution in the air caused by automotive exhaust and other gases, as well as pollution in lakes and other viable sources of water.
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Facile Synthesized Mo 2 C Electrocatalyst Supported on Mesoporous Carbon for Hydrogen Generations
More LessThe surge in the field of renewable energy aiming to develop clean energy technology is continuing to rise. Quest for a H2-based economy derived from non-fossil resources remains at the forefront of future fuels. During the past few decades there has been intense research on the utilization of electrical energy to produce H2 in an energy efficient and environmentally benign way. Electrocatalytic hydrogen generation via water electrolysis provides an important alternative to that extracted from hydrocarbon resources. One of the most crucial components which could revolutionize H2 production is that the design and development of a novel electrocatalyst that can efficiently split water to generate H2. Currently, platinum (Pt) is known as the state-of-the art electrocatalyst for hydrogen evolution reaction (HER). However, due to cost and scarcity of Pt, research focus shifted to precious-metal-free based materials for efficient HER reaction. As results, a wide variety of transition-metal-based electrocatalysts have been developed and investigated. To this end and due to unique d-band electronic structure, Mo-based electrocatalyst such as, Mo2C and MoS2 has been the subject of intense investigation for HER reaction. Yet, functional and robust catalysts operating with reasonable current densities (J) at low overpotential in brine water are still scarce.
Herein, we demonstrate a facile synthesis of β-Mo2C embedded on mesoporous carbon support; Metal Organic Framework (MIL 53(Al)) was utilized as a novel source for mesoporous carbon support. Microscopic studies revealed the formation of monodisperse Mo2C with
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Microbial Desalination Cell: An Integrated Approach for Wastewater Treatment and Desalination Systems for Sustainable Water Desalination and Wastewater Treatment
Authors: Suraj Sevda, Ibrahim M Abu Reesh and Zhen HeThe availability of drinking water from the current available sources is decreasing due to the high demand and population increase. Seawater is a potential source for drinking water but the current desalination technology is energy intensive, therefore energy efficient desalination technology is desired. In the past decade microbial fuel cells (MFC) were emerged for simultaneous wastewater treatment and bioelectricity generation, in the anodic chamber of MFCs, microbes work as a biocatalyst to generate electrons from the oxidation of the organic compounds (wastewater) and transfer them to the anode electrode. These electrons flow through an external circuit to the cathode electrode where they used to reduce terminal electron acceptors (e.g., oxygen). Microbial desalination cells (MDC) are new potential technique for seawater desalination, in this device energy from wastewater is extracted by using microbes and without any external energy source, water desalination is driven. To convert an MFC to an MDC, a middle chamber is inserted in between the anodic and cathodic chambers of MFC using a pair of anion and cation exchange membranes. This middle chamber works as a desalination chamber in the MDC (Fig. 1). The cations and anions from the desalination chamber moved to the anodic and the cathodic chambers, respectively, due to the cell potential difference between the anode electrode and the cathode electrode; as a result, salts are removed from the saltwater.
The first MDC study was reported in 2009 and since then there have been nearly 74 papers published about various aspects of MDC design and development, indicating a strong interest and rapid development of this technology. During this short period of time, various MDC designs were developed for salt removal and wastewater treatment. The desalination chamber volumes were increased from 3 ml to 105 liters and further progress is going on for salt removal and at the same time wastewater treatment. The performance of MDC was investigated using various concentrations of saline water in desalination chamber using industrial or synthetic wastewater in the anodic chamber. Different MDC designs were reviewed here. These developed new MDC designs named as air cathode MDC, stacked MDC (SMDC), up flow MDC (UMDC), recirculated MDC (RMDC), microbial electrodialysis cell (MEDC), submerged microbial desalination- denitrification cell (SMDDC), microbial capacitive desalination cell (MCDC) and osmotic microbial desalination cell (OsMDC). Different anion and cation exchange membranes were compared for power generation and desalination efficiency. This paper also reviews different substrates that have been used in MDCs so far. The MDCs provide an energy self-sustainable system in that water desalination and wastewater treatment conducted by using microbes as catalyst in the anodic chamber. Still the available MDCs were very small in volume that can't meet today's water desalination needs. In the long term operation of MDC, the membrane fouling and electrode stability are still two major problems limiting the development of MDCs. The possibility of scale-up, possible future potentials for synchrony of the MDCs with current desalination techniques were also discussed. Case study with real wastewater in the anodic chamber and real seawater in the desalination chamber were also discussed.
Acknowledgements
This work was made possible by NPRP grant # 6-289-2-125 from the Qatar National Research Fund (a member of Qatar Foundation). The statements made herein are solely the responsibility of the authors.
Reference
Sevda, S., Yuan, H., He, Z., Abu-Reesh, I.M., 2015. Microbial desalination cells as a versatile technology: Functions, optimization and prospective. Desalination 371, 9–17. doi:10.1016/j.desal.2015.05.021
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Toxicity of Chlorine to Five Marine Species from Various Trophic Levels of Qatari Waters
Authors: Suhur Saeed, Nandita Deb, Sarah Bacha and Christopher WarrenBackground
Chlorine is extensively used as a powerful oxidizing agent in the countries surrounding the Arabian Gulf for water treatments and biofouling control. The usage has been increasing significantly as demand for water grows considerably both in industry and domestic use. This is due to the fact that it is a well-tested technology, has had a history of long-term worldwide industrial use and is of acceptable cost. Sodium hypochlorite (NaOCl, commonly termed chlorine) is a common form of chlorine that is used and in all cases it is produced on site by means of an electro-chlorination plant (ECP). In seawater, chlorine produces a mixture of hypochlorous acid (HOCl) and hypochlorite ion (OCl − ). These rapidly react with the bromide ion to form a mixture of hypobromous acid (HOBr) and hypobromite ion (OBr − ). The acute oxidants formed by chlorination are therefore short lived and are not persistent in seawater, but can be quite toxic. Further complicating the environmental concern of chlorination is the production of numerous, and more persistent, compounds formed by complex reactions between chlorine/bromine and the organic constituents of seawater, collectively described as chlorination by-products (CBPs). Many CBPs are persistent and may be toxic to marine organisms subjected to long-term exposures. The Gulf waters support a range of coastal and marine habitats including mangrove swamps, seagrass beds and coral reefs. However, marine organisms in the Arabian Gulf are living close to their tolerance limits due to the extreme environmental stressors of temperature and salinity. Anthropogenic stressors such as chlorine may further exacerbate these natural stressors.
Objectives
In order to evaluate the risks of chlorine exposure to Arabian Gulf marine organisms, the aims of this study were to 1) develop protocols for acute and chronic toxicity tests involving native species at different trophic levels, 2) correlate sensitivity to other marine organisms used as indicator species in risk assessments, 3) draw conclusion from the results and explore ways that this could be used for informing environmental management activities.
Methodology
Materials and methods
Stock solution of calcium hypochlorite was prepared in filtered artificial seawater (0.45 μm filter paper) daily in dark bottles. Concentration of chlorine in the experimental chambers were verified daily by the N,N-diethyl-p-phenlenediamine (DPD) colorimetric method. Different concentrations of chlorine were either administered as a continuous flow through or via daily renewal.
Exposure to test species
Species were collected from different location around the coastal areas of Qatar. They were then cultured in the laboratory using conditions of the Arabian Gulf. Species used in the tests include phytoplankton (Synechococcus sp.), zooplankton (Uterpina acutifrons), pearl oysters (Pinctada radiata), sea urchins (Diadema setosum) and killifish embryos (Aphanius dispar).
Results
Sensitivity varied across the trophic levels for each species and was found to be in line with other test organisms that are used in established toxicity procedures. All five species used were found to be useful for certain types of toxicity testing. For example, Pinctada radiata and Diadema setosum were excellent in testing for successful fertilization and early development stages, while local Aphanius dispar embryos were useful for following sub-lethal effects such as malformation and hatchability. Embryos of oysters and urchins were found to be the most sensitive to chlorine (Fig. 1.). Effect of chlorine was only observed near or after hatching has occurred. Continuous exposure showed more effective than the semi-renewal method.
Discussion and conclusion
While chlorine continues to be used heavily globally, available toxicology data are either very limited or out dated especially those based on the Arabian Gulf. The purpose of this study was to increase the knowledge of chlorine chemistry and toxicity especially the sensitivity towards the Arabian Gulf species. Results obtained reveal that the sensitivities of all five species used in this study are in line with species used internationally in similar tests. LC50s were determined for all species and are currently being used in modelling tools to determine the fate and environmental risks of chlorine. Chlorine being a powerful oxidizing agent asserted its effect immediately after contact. It loses its potency within the first hour in seawater and this may contribute to the low effect shown in this study compared those in fresh water. Given the short-lived nature of chlorine as an oxidant in seawater, our attention has also been focused on the sub-lethal effects that may be attributed from the by-products. Work is ongoing in this area. Expanding tests with species used in this study to evaluate their sensitivity towards chlorine by-products will further increase our understanding of their chemistry and environmental risk in the Arabian Gulf and will provide a science-based tools for making management decisions.
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Lubrication in Desert Environments: Oil-Soluble Organo-Silver Molecules Designed for In-Situ Deposition of Metallic Silver at High Temperatures
The quest for improved engine performance and reduced emissions drives the design of increasingly sophisticated lubrication technologies. Lubricating oils and greases are engineered to function over a broad range of temperatures and loading conditions. Modern engines operate at higher temperatures, speeds and pressures than previous engines, and therefore require lubricants capable of handling harsher conditions. Reliable performance in extreme conditions is also necessary in emergency and combat situations. Thus, a major challenge for next-generation lubrication technology is to improve performance at extreme temperatures exceeding the thermal degradation limits of conventional engine oils.
In automotive engines, the surface temperature of critical tribological components can easily reach 200°C, while asperity contacts can generate ‘flash temperatures’ up to 1000°C. These extreme pressures and temperatures in the contact zones can lead to plastic deformation, wear away mating surfaces, and catalyze chemical reactions which damage the surfaces and lubricant. Tests carried out on PAO4 and 15W40 motor oils show that they decompose at 275°C, irreversibly losing viscosity and generating oil-insoluble acids and salts that corrode surfaces and form sludges.
Surface coatings, such as diamond-like carbon, and texturing can be used to reduce friction at temperatures which lead to motor oil thermal degradation. However, such treatments are costly for large components, and these coatings cannot be replenished without dismantling the treated machinery. Soft metal ductility can also be utilized in lubrication. The low shear-strengths of metallic films can form smooth “glaze layers” on tribosurfaces which lubricate sliding contact. Noble metals have oxidative stability, enabling lubricious performance at extreme temperatures. Silver-coated contact surfaces exhibit reduced friction and wear from 25–750°C. However, a method is required to dissolve metallic silver precursors in base oil for deposition at high temperatures.
Silver nanoparticles are known to increase surface fatigue life, decrease friction, and wear, and work synergistically with other lubricant additives. However, silver nanoparticles are expensive, difficult to suspend in nonpolar media, and typically require a surfactant to prevent agglomeration. An alternative, described here, is to use a silver-containing molecular precursor. Organic ligands impart solubility to silver atoms and control the organosilver complex decomposition temperature to deposit silver only when and where it is needed. Controlled silver deposition is arguably more economical than full protective coatings. Also, a lubricant additive can be replenished during oil changes to provide more lubricious silver to high asperity engine contact regions. We report here the synthesis, characterization, and tribological implementation of a silver-pyrazole complex, silver 3,5-dimethyl-4-n-hexyl-pyrazolate (HPzAg)3. This complex is oil-soluble and undergoes clean thermolysis at ∼310°C to deposit lubricious, protective metallic silver on mechanical surfaces. Temperature controlled tribometer tests show that an optimized 2.5 wt% (HPzAg)3 loading reduces wear by 60% in PAO4 (poly-α-olefin lubricant) and 70% in a commercial fully-formulated motor oil (military grade 15W40). This organosilver complex also imparts sufficient friction reduction that the tribological transition from oil as the primary lubricant through its thermal degradation, to (HPzAg)3 as the primary lubricant, is experimentally undetectable.
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Research in Irrigation Canal Lining: An Experience from Sudan
Authors: Tarig El Gamri Ibrahim and Amir Bakheit SaeedThe amount of water below 1000 m3 per capita per annum is considered as the water poverty zone. With business as usual scenario it is estimated that by the year 2025 half the world's people will live in countries with high water stress. Based on Global averages irrigation water demands accounts for about 70% of all water uses. Meanwhile water use efficiencies of irrigated projects are generally very low particularly those under traditional surface methods. On the other hand conveyance losses vary within a range of 25–50% of the total diversion. Generally canal lining can save about 75% of the conveyance losses. However, high quality linings were found to practically eliminate such losses. The paper reviews the benefits of canal lining, which include hydraulic, economic and environmental benefits. Since seepage from irrigation canals is the most important factor in lining considerations the paper presents some review on the phenomenon. Canal lining is usually classified into four main types: hard surface linings, membrane linings, earth linings and soil sealants. The paper critically discusses the different types and highlights the criteria for selecting the appropriate lining technique. The paper also reviews the recent technical developments and research at the global level in this field; these include the development of new materials and techniques. Finally the paper presents a review of the canal lining related research executed by the National Centre for Research, Sudan during the last 20 years. These include development of low cost lining (building) materials using locally available aggregates (sand and gravel), lining irrigation canals on expansive soils and development of low cost concrete pipes and production of precast canal-lets. Canal lining was found conserve irrigation water, reduce fuel consumption, reduce irrigation time and reduce labour requirements. Development of Low Cost Building Materials for Canal Lining:: Four low cost building materials have been studied, these are namely khafgi, ferrocement, kenaf sheets and concrete made of small-sized gravel available near RDRC. Kenaf sheets were rejected because of the low durability expected. The other three materials were found to be feasible based on strength, permeability and durability. Water transported sand near RRS was found to be suitable for building works including lining whereas wind transported sand can hardly be recommended for such works.
Hand placement cast in-situ was adopted using the semicircular configuration, as besides improving structural integrity of the canal, it is the most hydraulically efficient section particularly for small canals. A semi circular cast-in situ form was made to construct channel sections that accommodate maximum discharges at RDRC. The work is done in alternate sections and the lap-joint technique was used. Pipe Casting:: It have been noticed that some desert farms the canalization system is liable to be buried by wind-blown sand. To avoid this problem the system should adopt pipes instead of open channels; however, traditional farmers cannot afford to cover such expenses since such pipes are relatively expensive in the local market. To overcome such problems the study was extended to develop intermediate technologies for pipe casting. A form was designed and constructed in a local workshop. The form is made of PVC pipe equipped with a handle as an internal unit the external unit is made of sheet metal also a wooden base is used. The external unit is composed of two semi-cylinders; a steel channel is welded to each end of each semi-cylinder to facilitate fastening meanwhile a rubber strip used to prevent water leakage. Again locally available aggregates were used. Laboratory tests (Impact Value and Crushing Value) showed that locally available gravel is suitable for pipe casting. The internal unit of the form is removed about an hour after the end of the casting process and the external one after a day. The pipes were then cured for 7 days. Compressive Strength and permeability tests proved that the produced pipes comply with the Known International Standards. Additionally the pipes were tested in the field by passing a tractor, which represent the maximum expected load in such farms without being damaged. Lining Irrigation Canals on Expansive Soils:: Um Jawaseer Desert Farm Project, which is located in Wadi El Magadam, the Northern State was established in the year 1989 for the settlement of the nomads of El Hawaweer Tribe. The project harnesses water from an aquifer of about 40 m below ground surface for irrigation and other purposes. Evaluation studies showed that the project is successful in creating better livelihood for the people of the area.
Huge water losses were encountered in the first two phases. In the third phase the project adopted stone lining, which is estimated to conserve about 1/3 of the irrigation water. However, stone lining is known to be one of the least effective lining techniques. Identification tests were carried out in accordance with the British Standards and showed that Um Jawaseer soil possesses swelling properties.
To reduce (mitigate) the expansive potential of Um Jawaseer soil some additives (cement, lime, bituminous emulsion and refuse oil) were tested, these additives were added to the soil at a rate of 6% by weight as recommended by some authors.
To avoid damage the linings a combination of soil treatment and construction technique was used for the lining of Um Jawaseer irrigation system. The soil was first excavated to a depth of 60 cm and mixed with the additive (cement). Water is added to the soil/ cement mixture till the optimum moisture content (plastic limit) was reached. Finally the mixture was compacted into two layers (30 cm each). As for the construction technique the semi-circular channel cross section was used since it produces integrity in structure and the channels so constructed can resist external forces. This combination gave very encouraging results since it is found to mitigate upheaval damage and produce strong and efficient conduits. Precast concrete canal-lets:: The merits of precasting are attributed to the high quality control coupled with the technique. Precasting was advised by some authors for mass production of tertiary canals. The J- Section was selected for ease of casting the form is made of metal sheets.
The form was filled of concrete, while being compacted with steel rod, left for an hour to allow for setting of concrete and then released. The finished section is allowed to dry for 24 hours and then cured for 7 days by wetted kenaf sacks. Keyword: Seepage, Irrigation, Canal lining, Pre-casting, efficiency
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Solar Thermochemical CO 2 Utilization via Ceria Based Redox Cycle
According to the recent studies, it is expected that the global energy requirement will increase from 14 TW to 30 TW by the year 2050. Currently, fossil fuels are the major energy source utilized for the fulfillment of the energy requirement. Due to the excessive utilization of fossil fuels, the concentration of greenhouse gases in the atmosphere is increasing day by day and hence there is a pressing need to develop technologies to produce carbon free renewable fuels. The liberated CO2 can be re-energized into CO via ferrite based thermochemical looping process using concentrated solar energy. The CO produced via solar thermochemical CO2-splitting can be combined with H2 derived from ferrite based solar thermochemical water-splitting process to produce solar syngas which can be further processed to liquid fuels such as Methanol, Diesel, and Kerosene via the Fischer-Tropsch process. The current research trends in solar thermochemical community are focused towards high and constant levels of solar fuel production in multiple cycles and it is believed that non-volatile mixed metal oxides such as undoped and doped ceria will significantly improve the production of solar fuels. Ceria based redox cycle comprises of two steps. First step belongs to solar endothermic reduction of ceria at higher temperatures releasing O2. The second step corresponds to the non-solar exothermic re-oxidation of the reduced ceria at lower temperatures by H2O, CO2, or a mixture of the two producing H2, CO or syngas.
In this investigation, Zr and Hf doped ceria based redox nanoparticles (various doping combinations) were synthesized using a co-precipitation method. The respective metal precursors were dissolved in water. Upon complete dissolution, excess ammonium hydroxide (NH4OH) was added drop-wise to the mixture under vigorous stirring to precipitate the mixed-metal hydroxides (final pH = ∼9). The obtained precipitates were filtered, washed with water until free from anion impurities and oven dried at 100 °C for 8–10 h. Subsequently calcination was performed at different temperatures in air. The calcined powders were characterized by powder X-ray diffraction, BET surface area analysis, scanning electron microscopy (SEM) and transmission electron microscopy (TEM). The compositional purity of the derived Zr/Hf doped ceria was identified using powder XRD and the obtained results indicate phase pure composition of the derived materials (based on the stoichiometry selected during synthesis). The derived Zr/Hf doped ceria also possess high specific surface area (SSA) and porosity which is confirmed by BET analysis. The SEM and TEM analysis indicate formation of Zr/Hf doped ceria nanoparticles in the range of 10 to 50 nm. Synthesized Zr/Hf doped ceria nanoparticles were further tested for thermochemical CO2-splitting by using a high-temperature thermogravimetric analyzer (TGA). Multiple thermal reduction and oxidation (by CO2) cycles were performed at various operating conditions by using TGA while the O2 and CO was quantified by gas chromatography. Results obtained indicate that the derived Zr/Hf doped ceria is capable of producing higher amounts of solar CO as compared to previously investigated undoped and doped ceria materials. Also, the Zr/Hf doped ceria was examined in 20 thermochemical cycles towards successive thermal reduction and CO2 splitting reactions and the obtained findings indicate stable redox reactivity and thermal stability.
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Reactive Absorption of CO 2 Using Ethylaminoethanol Promoted Aqueous Potassium Carbonate Solvent
Atmospheric concentration of CO2, which is considered as one of the major greenhouse gases (GHGs), has increased up to 398 ppmv as of 2015. CO2 concentration in atmosphere was 280 ppmv in pre-industrial era, and due to the continuous discharge, it is expected to increase up to 550 ppmv by 2050. Many of the major industrial sources of CO2 emissions are natural gas fired power plants, synthesis gas used in integrated gasification combined cycle (IGCC) and power generation, gas streams produced after combustion of fossil fuels or other carbonaceous materials, and oxyfuels. Reactive absorption of CO2 from the industrial off gases by using chemical solvents is considered as one of the most common, efficient, and cost effective technologies utilized by the industry for CO2 capture. The captured CO2 can be stored by using the geological or oceanic sequestration approaches. As an alternative to geological or oceanic sequestration, the captured CO2 can be re-energized into CO by using solar energy and combined with H2, which can be generated from different methods, to produce syngas. The syngas produced can be further processed to liquid fuels such as methanol, gasoline, jet fuel, etc. via the catalytic Fischer-Tropsch process.
In past, a variety of chemical solvents (mostly aqueous amines and there derivatives) have been used for CO2 capture from different gaseous streams via reactive absorption. Though the amines are attractive for the CO2 capture application, there are several disadvantages such as very strong corrosion to equipment and piping, high energy requirement during the stripping of CO2 and they are prone to oxidative and thermal degradation. Recently, use of aqueous potassium carbonate (K2CO3) as a solvent for the absorption of CO2 has gained widespread attention. The usage of K2CO3 has been employed in a number on industries for the removal of CO2 and H2S. Due to its high chemical solubility of CO2, low toxicity and solvent loss, no thermal and oxidative degradation, low heat of absorption, and absence of formation of heat stable salts, K2CO3 seems to be more attractive compared to the conventional amines towards CO2 capture. However, K2CO3 solvent shows slow rate of reaction with CO2 and, consequently, low mass transfer in the liquid phase as compared to the amine solvents. Hence, several investigators are focused towards improving the rate of reaction of CO2 in K2CO3 solvent with the help of different types of promoters.
In this paper, the kinetics of absorption of CO2 into an aqueous K2CO3 (20 wt %) promoted by ethylaminoethanol (EAE) solution (hereafter termed as APCE solvent) was studied in a glass stirred cell reactor using a fall in pressure method. Reactive absorption of CO2 in EAE promoted aqueous K2CO3 solution (APCE solvent) was studied at different initial EAE concentrations (0.6 to 2 kmol/m3) and reaction temperatures (303 to 318 K). The reaction between the CO2 and APCE solvent was very well represented by the zwitterion mechanism. The N2O analogy was employed for the determination of H_(CO2) in the APCE solvent. The H_(CO2) was observed to be decreased by 5 and 31% due to the increase in the EAE concentration from 0.6 to 2 kmol/m3 and reaction temperature from 303 to 318 K, respectively. The D_(CO2) in the APCE solvent was also decreased by 21% due to the similar increase in the initial EAE concentration. In contrast, the D_(CO2) increased with the rise in the reaction temperature from 303 to 318 K by a factor of 1.678. The rate of absorption of CO2 in the APCE solvent was observed to increase by 35.10% and 47.59% due to the increase in EAE concentration (0.6 to 2 kmol/m3) and reaction temperature (303 to 318 K). The absorption kinetics was observed to be of overall second order i.e. first order with respect to both CO2 and EAE concentrations, respectively. The rate constant (k_2) for the absorption of CO2 in the APCE solvent was observed to be equal to 45540 m3/kmol√s at 318 K. The temperature dependency of k_2 for the CO2 – APCE solvent system was experimentally determined as: k_2 = (1.214 × [10]^18)√exp(( − 9822.7)/T). Findings of this study indicate EAE as a promising promoter for the aqueous K2CO3 solution.
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Mid-Infrared Dual Frequency Comb Spectroscopy for Time-Resolved Methane Detection
We performed dual frequency comb spectroscopy for time-resolved methane detection in real time, which is of demanding interest for the natural gas industry, environmental science, atmospheric monitoring and geoscience research. Broadband MIR frequency combs provide high brightness and frequency precision for many spectroscopic applications. To increase the detection sensitivity, a multipass cell or a high finesse cavity with mid-infrared frequency comb produced by difference frequency generation is used. This setup increases also the interaction length between the detection target molecules and the MIR frequency combs. Both frequency comb sources are based on femtosecond Er-doped fiber laser oscillators with stabilized repetition rates at ∼250 MHz, which is stabilized and locked to sophisticated frequency references or GPS system in order to achieve comb-teeth resolved spectral measurements. We implemented the mid-infrared dual frequency comb spectroscopy in the spectral range between 2900 cm− 1 and 3150 cm− 1 with 0.07 cm− 1 resolution with a novel multipass cell of ∼580 m interaction length to detect the trace amount of methane in ambient air. We determined the methane concentration in the ambient air of the laboratory to be ∼ (1.5 ± 0.1) ppmv. The minimum detection limit for the current setup is ∼60 ppbv with an 80 ms data acquisition time.
We note that most of current existing frequency comb technologies have relatively narrow bandwidth and microwatt power levels limited by the applications for sensitive and real time multi-target gas detection. Another approach based on OPO (optical parametric oscillator) sources provided hundred milliwatt power and broad spectra, but the repetition rates or the carrier-envelope offset frequencies were not fully controlled, which led to distorted spectral measurements. We resolved this problem by applying dual frequency comb lasers DFCS to use the later as Vernier scale for correcting the distortion of the first laser comb system. A simplified diagram of the experimental setup is presented in Fig.1.
In Fig. 1, the experimental setup includes two MIR comb sources, mirrors and lenses allowing to couple the MIR comb2 into the multipass cell, one 50:50 beam splitter (BS) to obtain the reference and signal pulses, one 92:8 beam splitter to combine pulses from two comb sources, and an MCT photodetector with electronics for data acquisition. The spectra measured with a scanning monochromator are shown in inset (a) for MIR comb1 (cyan) and MIR comb2 (red). Interferometric autocorrelation traces are shown in inset (b) for MIR comb1 (cyan) and (c) for MIR comb 2 (red). The absorption features in the spectra are due to water vapor in the laboratory environment. Spot patterns on the mirrors of the multipass cell with the visible red laser are shown in inset (d) and are produced when the alignment red laser is introduced with the flip mirror off. The entrance/exit hole of 5 mm diameter can be seen in the top left part of the right side mirror.
Our system is referenced to a Rb frequency standard (Stanford Research, PSR10). One advantage of these DFG sources is the passive carrier-envelope offset (CEO) frequency stabilization. Since the pump and signal fields originate from the same source, the generated idler field is carrier-envelope phase slip free. The MIR comb1 has ∼120 mW output power, covering a spectral range from 2.8 to 3.6 μm (2700 cm− 1 to 3600 cm− 1). The pulse duration is ∼80 fs. The MIR comb2, employing a higher power Ytterbium doped fiber amplifier, generates an MIR comb of ∼300 mW with a similar spectrum and pulse duration.
We lock two femtosecond DFG MIR combs with slightly different repetition rates at fr1 = 249,998,633 Hz and fr2 = 250,000,122 Hz, thus the difference is δfr = 1489 Hz. In the time domain, when a pulse pair from two sources overlaps in time, the center burst of an interferogram is formed. Subsequent pulse pairs impinge on the detector with linearly increasing time delay. As a result, the detector records an interferogram formed by many pulse pairs of various delays. Because pulse pairs repeatedly move through each other, a new interferogram starts to form as soon as the previous is completed in 1/δfr∼0.672 ms. We record the interferogram train with an oscilloscope (Tektronix, MDO4104B-3) at a sampling rate of 250 MSPS with ∼10 bit resolution. The maximum record length is 20 Mega points, corresponding to 80 ms, or ∼118 complete interferograms. We first block the reference pulses, and record only signal interferogram train; which can be fast Fourier transformed to comb-teeth resolved spectrum with a simple software phase correction. The magnitude and phase radio frequency (RF) spectra are presented in Fig. 2.
In figure2, fourier transformed magnitude (black) and phase (green) RF spectra from an 80 ms signal interferogram train with a software phase correction: (a) broad range from 18 to 63 MHz, (b) zoomed-in narrow range from 40.25 MHz to 40.45 MHz. The phase is only perceptible and plotted at comb teeth positions since the RF signals between comb teeth are simply noise and therefore have a random phase between − π < /AσΣETHιγηλιγητ> to π. Because of the broad absorption features, the absorption dips can be observed in (a). The discrete comb lines with a spacing of δfr = 1489 Hz can be observed in (b).
Because of the passive CEO frequency stabilization, the DFG MIR frequency combs have a simple form of vm = mfr, where v is the optical frequency in MIR, m is an integer, and fr is the source repetition rate. For the measurements in the frequency domain, the individual comb lines from two sources beat between (N+2)fr1 and Nfr2, where N is an integer between ∼347,600 and ∼377,600, and down convert the optical frequency information at about 87∼95 THz to RF at about 18∼63 MHz with a simple formula Nfr2 − (N+2)fr1 = fRF. Thus, the optical up conversion follows fRFfr2/δfr+2fr1fr2/δfr. The measured complex spectrum of the signal is S(ν) = S0(v)exp[ − α(v)L/2 − iφ(v)], where S0(v) is the complex spectrum of the reference, α(v) is the molecular absorption coefficient, L is the path length of the multipass cell, φ(v) is the phase shift. We evaluate the DFCS quality factor, which is the product of the SNR and the number of resolved spectral elements normalized by the square root of the total acquisition time. With a SNR ∼100, in 80 ms acquisition time, we obtain the number of resolved spectral elements as 250 cm− 1/0.07 cm− 1 ∼ < /AσΣETHιγηλιγητ>3600, and the experimental quality factor is ∼1.3 × 106 Hz1/2.
This work was funded by the Robert A. Welch Foundation, Grant No. A1546 and the Qatar Foundation under Grant No. NPRP 6-465-1-091.
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Electrochemical Analyses of Sodium based Mixed Pyrophosphate Cathodes for Rechargeable Sodium Ion Batteries
Authors: Arsalan Ahmad Raja, Rana Abdul Shakoor and Ramazan KahramanLithium ion batteries (LIB) are widely applied to energy storage systems, like electric vehicles, ships. While limited reserves of lithium and cost of lithium enforced to explore new materials. Hence, Low cost and abundance of sodium has made Sodium ion batteries (SIBs) an attractive alternative for energy storage. Li ion replacement with Na ion will not require change of design in present LIBs, except change of cathode material (based on Na) and respective electrolyte. But the challenge exists to develop sodium cathode with good electrochemical performance and excellent thermal stability. Therefore, various crystal structure for sodium cathode material were explored to meet these challenges. Among cathode materials, pyrophosphate family represented high theoretical capacity due to existence of two sodium ions in a repeating unit. In this report we synthesized mixed pyrophosphate cathode, Na2Fe1/2Mn1/2P2O7, via simple solid state process. The precursors, Na2CO3 (Aldrich), (NH4)2HPO4 (Aldrich), FeC2O4.2H2O (Aldrich) and MnC2O4.2H2O (Aldrich), were mixed in stoichiometric ratio and extensively grinded in mortar and pestle. The fine powder was subjected to heat treatment under inert atmosphere at 350 °C, cooled, grinded and then annealed in inert atmosphere at 600 °C for 6 hours. The compositional and structural analyses confirmed the formation of a crystalline pure phase. The optimization of operation temperature, time and atmosphere (inert); and the formation of mixed component systems (i.e., incorporation of more than one transition metal) not only lead to single phase mode but also tune the voltage potential for high energy density. The X-ray diffraction (XRD) data of as-synthesized Na2Fe1/2Mn1/2P2O7 was indexed to a triclinic structure. This triclinic structure has open framework which facilitated diffusion of Na-ions during charging and discharging. Thermogravimetric Analysis (TGA) showed negligible weight loss (∼5%) when heated to 550 °C, indicating decent thermal stability of the material and differential thermal Analyses (DTA) hardly observed any endothermic or exothermic peak. Carbon coating of Na2Fe1/2Mn1/2P2O7 was proceeded to impregnate electrical conductance in the material. SEM images showed the difference between pristine Na2Fe1/2Mn1/2P2O7 and carbon coated Na2Fe1/2Mn1/2P2O7. The carbon coated Na2Fe1/2Mn1/2P2O7 was, then, casted on aluminum to prepare cathode. The casted material (cathode) was dried at 70 °C under vacuum for two hours. The materials was then assembled into coin cell as a cathode in the glove box. The electrochemical measurements confirmed that Na2Fe1/2Mn1/2P2O7 is electrochemically active at room temperature. It showed a single-phase reaction during cycling. This single phase reaction is changed by the Na environment through a change in Na/Vacancy ordering. The Na2Fe0.5Mn0.5P2O7 cathode represented discharge capacity of 80 mAh/g at C/20 in the voltage range of 2.0 to 4.5 V. The average redox potential was observed to be approximately 3.2 V (vs. Na/Na+). The capacity retention of Na2Fe0.5Mn0.5P2O7 is 84% over 90 cycles. Between first charge capacity and second charge capacity, Na2Fe0.5Mn0.5P2O7 cathode showed a difference of 5mAh/g only. This employs that sodium based mixed iron-manganese pyrophosphate (Na2Fe0.5Mn0.5P2O7) cathode has increased occupancy. The rate capability of Na2Fe0.5Mn0.5P2O7 shows 70% retention from 0.05 C to 0.5 C. Synthesis of Na2Fe1/2Mn1/2P2O7 in nanometric size may result in further improvement in its electrochemical performance.
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An Investigation into Hydrophobic Membrane Fouling in Desalination Using Membrane Distillation Technology
More LessDemand for freshwater supplies is continuously increasing globally to the extent where some parts of the world became highly water stressed. In particular, the Arabian Gulf states rely heavily on seawater desalination for their freshwater supply which is met using commercial seawater desalination technologies like thermal and reverse osmosis (RO) desalination processes. However, these technologies require considerable power input and actually do have a negative impact on the environment in terms of carbon footprint.
An alternative technology to the conventional desalination processes with potentially lower environmental impacts is the Membrane Distillation (MD) process. Membrane Distillation is a thermally-driven process that utilizes a hydrophobic micro-porous membrane and can utilize low grade heat and solar energy. The driving force of the process is the vapor pressure difference between the sides of the membrane that is induced by the temperature difference between the feed and distillate. However, one of the challenges facing the deployment of MD in large commercial scale desalination of seawater is membrane fouling.
The objective of this study is to investigate and compare the fouling characteristics of three different commercial membranes (PP membrane of 0.22 μm, PP membrane of 0.45 μm, and PTFE membrane of 0.22 μm) using two feed solutions (seawater from the Arabian Gulf and synthetic 100,000 ppm NaCl solution) using a bench-scale direct contact membrane distillation (DCMD) flat sheet module at hot water inlet temperature of 75 °C, cold water inlet temperature of 20 °C, and hot and cold water flow rate of 1.5 L/min. The study was performed by evaluating the distillate flux performance of the various membranes, measuring their contact angle before and after fouling, testing the quality of the distillate produced and examining the salt rejection, and interpreting membrane surface analysis using Scanning Electron Microscopy (SEM) coupled with Energy Dispersive Spectroscopy (EDS) in order to study the morphology and the composition of the fouling layer.
Initially, the average flux obtained was 50.5 L/m2h, 50.3 L/m2h, and 38.3 L/m2h for PP membrane of 0.22 μm, PP membrane of 0.45 μm, and PTFE membrane of 0.22 μm, respectively. Therefore, PP membrane generated a higher flux than PTFE membrane. In terms of membrane pore size, the results showed that a larger pore size membrane is more prone to fouling and flux decay. In terms of membrane material, PP membrane showed a more rapid flux decline than PTFE membrane. Moreover, the percentage of drop in the average flux was more than 60%, 97%, and 94% for PP membrane of 0.22 μm, PP membrane of 0.45 μm, and PTFE membrane of 0.22 μm, respectively, after almost 19 h, 30 h, and 25 h of operation, respectively.
In terms of feed solution, a lower flux was obtained with the higher salinity feed, the 100,000 ppm NaCl solution. However, the difference was not very large, indicating that initially salinity does not have a great impact on the distillate flux.
The results also showed that fouling/scaling causes the quality of the distillates to deteriorate and that membrane wetting has occurred. A salt rejection of more than 99.9% was achieved initially; however, with continuous operation, a salt rejection as low as 83.5% and 69.9% was achieved when the seawater and the 100,000 ppm NaCl solution were used, respectively. PP membrane of 0.22 μm gave a better salt rejection followed by PTFE membrane of the same size then by PP membrane of 0.45 μm.
The contact angle of a clean PP membrane of 0.22 μm, PP membrane of 0.45 μm, and PTFE membrane of 0.22 μm, was found to be 134.8°, 133.2°, and 136.7°, respectively. However, after fouling, the contact angle dropped to 40.5°, 36.1°, and 13.8° for PP membrane of 0.22 μm, PP membrane of 0.45 μm, and PTFE membrane of 0.22 μm, respectively, indicating significant loss of hydrophobicity.
SEM-EDS analysis showed that the salt layer formed on the membranes was not uniform and that the major foulants were CaCO3 and CaSO4. In addition, membrane pore blocking by salts and a cake layer formation (which was a result of the elevated feed temperature that resulted in the formation of temperature polarization) were observed.
The results of the study show that fouling needs to be more investigated in MD process to be practically implemented and considered as competitive to the conventional desalination technologies. An optimum temperature and flow rate should be explored; however, the results of the study urge the need for developing new membranes and improved membrane modules and MD configurations as well as finding optimum procedures for membrane cleaning.
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Theoretical and Experimental Investigations on Passive Thermal Management of Solar Photovoltaic Systems using PCM-Metallic Cellular Absorbers
Authors: Abdelhakim Mohamed Hassabou, Torsten Klemm, Amir Abdallah and Olaf AndersenEnvironmental conditions such as irradiance, temperature, humidity and dust accumulation have impact on PV performance and reliability. In this paper, we will focus on the effect of temperature and how to mitigate this effect by using passive cooling approach.
Qatar is rich with solar irradiance favored for photovoltaic; however, the high temperature (a module temperature of 50°C was measured during summer months) has a negative impact on the power output of a PV module. Operation of solar PV systems under extremely high temperatures and high humidity in hot climates represents one of the major challenges to guarantee higher system's reliability. Therefore, thermal management in hot climates is crucial for reliable application of PV systems, as it has a potential to increase the efficiency and life expectancy and to stabilize the output power characteristics.
Apart from that, dust accumulation on PV module is known to be also as one of the challenges that affect the PV power output. Due to the difference in ambient temperature between day and night, water condensation on PV modules was observed. Dust accumulated on a PV module together with water condensation may cause a thick layer of mud that is difficult to be removed. In this paper, we will show that, condensation of water on the cell surface during night can be prevented by maintaining the temperature of solar PV panels above the dew point during night.
Application of Phase Change Materials (PCM) for passive or combined active-passive cooling systems offers various options for adequate thermal management solutions. The present research focuses on utilization of PCM for passive thermal management of solar systems. Passive cooling can be realized by integration of PCM layers with the back side of PV panels. Passive cooling use the high temperature differences between day and night in arid desert regions, due to sky radiation in the night. The high thermal capacity of PCM accumulates coolness during night to keep the PV cells at a moderate temperature during the day. This also can help maintaining the PV panel temperature well above the dew point to prevent condensation during day and night, thereby avoiding mud formation on the panel surface. In some instances, active cooling may still be needed during peak solar radiation hours around noon time in summer, however integration of PCM can also reduce significantly the pumping power required to circulate the cooling medium as well as the external thermal/cool storage size and cost.
Although PCM provides high energy storage density and nearly isothermal behavior around the phase change temperature, they suffer from low thermal conductivity, which limits the power density during charging and discharging. The low thermal conductivity of a PCM can be increased by combining them with highly conductive heat transfer structures. One advanced option is the application of cellular materials like metal fibers, which allow a significant enhancement of the PCM absorber thermal conductivity by more than 100 times. Hence it is proposed to hybridize PCM with cellular metallic matrices to enhance the thermal conductivity and provide a practical solution for easy encapsulation and integration with the PV panels.
The main focus of this study is therefore to explore the effect of utilization of PCM based cooling elements incorporating cellular metallic heat conducting structures on the thermal behavior of solar PV panels.
Preliminary laboratory experimental investigations have been carried out to characterize the thermal resistances between the PV panel and the PCM matrix absorber using different coupling mechanisms attached to the backside of PV panels. The coupling mechanisms include mechanical clamping, adhesive bonding, and double side thin and thick adhesive tapes. Based on the measured data, design recommendations for the desired performance will be discussed. The outcomes of the laboratory experimental investigations provide important input parameters that are needed in numerical analysis and design optimization of such systems under weather conditions in Qatar and elsewhere.
Beside the laboratory experimental work, theoretical analysis to optimize the properties of the PCM matrix absorber for application of solar PV systems in Qatar has been carried out. The simulation model has been developed using homogenization based on volume averaging techniques and interpenetration continua approach. Due to complexity of the underlying transport phenomena, solution of highly nonlinear coupled system of equations with moving boundaries is required as a function of space and time. Hence, numerical modeling and optimization of large scale PCM storage is both challenging and computationally expensive. However, in engineering systems microscopic details are neither easy to be captured nor needed, instead, the macroscopic aspects are much more interesting. Therefore, dealing with a large-scale PCM storage, a fundamental question arises as how to bridge the computational scale and reduce the problem to a simple one. A simplified modeling approach and numerical procedures shall be proposed to determine the macroscopic transport and time history of the PCM temperature field in a PCM thermal storage. The model is fairly general to be applied as a design and optimization tool for thermal energy storage and thermal management systems. Preliminary results of the numerical simulation shall be presented and discussed.
Due to similarity of climatic conditions in the GCC, the solution can be easily adapted to suit other countries in the Gulf. The fibrous porous structure can be manufactured using wastes of metals processing such as in manufacturing aluminum profiles. PCM candidates with low temperature and desired thermo-physical properties, such as paraffin waxes, are abundantly available with reasonable cost. Further cost reductions for manufacturing of PCM matrix absorbers can be achieved by integration with the PV support structure. This an important part of the ongoing research in collaboration with local industry partners in Qatar in order to produce these systems locally on a commercial scale effectively with lower costs. Preliminary analysis shows that the passive thermal management can increase both instantaneous conversion efficiency by 3–5%, while it can considerably increase the life span of PV modules and reduces maintenance and cleaning costs. These factors hold a great promise for supporting the economic viability of passive thermal management using PCM matrix absorbers. However, detailed technoeconomic analysis will be elaborated within the framework of this project and will be published later.
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Calibration & Temperature Controlled Setup for Air Quality Sensors
Authors: Ali Ijaz, Mohieddine Amor Benammar, Farid Touati and Abdullah KadriIndoor air pollution is a major issue affecting public health. Due to hot climate, humidity and lack of natural green spaces, life is mostly confined indoors in many countries of the MENA region. Vulnerable population, including young children and senior citizens who spend most of their time indoors, are at risk because of the effects of indoor air quality (IAQ) on their health. An indoor air quality monitoring system is a need of the hour to detect and improve Indoor Air Quality (IAQ). The monitoring systems presently available are bulky, expensive and need periodic calibration to maintain high degree of accuracy. Frequent recalibration of a number of densely deployed individual sensors in the network is a time-consuming and laborious task therefore self-calibration is indispensable. Gas sensors, even if factory-calibrated, tend to drift with time/usage. Therefore these should be regularly calibrated under controlled environments. Calibration may be carried out using test gas mixtures with known composition. Pre-mixed gas cylinders with known composition may be used for the purpose; however this solution is not flexible as the number of calibration points and testing conditions (e.g. effect of temperature and humidity on CO2 sensor) are limited. In the current project, a computer-controlled test and calibration test bed system is being designed and assembled along with temperature controller.
Calibration set-up would help in self calibration of the air quality sensors. Calibration curves obtained from proposed calibration test bed are updated automatically and fed into the sensor node through wireless communication without going in the field or replacing the sensor. A computer-controlled test and calibration test bed system is designed and assembled containing the sensor(s) under test and in which gas composition; temperature can be precisely and dynamically controlled. ATMEGA328 micro controller is used to receive the temperature set point from the computer running the test rig.
Gas composition, temperature and humidity can be precisely and dynamically controlled in our designed test chamber containing the sensor(s) under test. Given the number of air pollutants that may be present in the atmosphere, up to 6 different gases can be mixed to calibrate the sensor nodes and investigate the issue of cross-sensitivity.
Array of 6 gas cylinders, and a gas blending system that has been designed provides continuous variation of mixture composition and temperature. Gas blending is performed using mass-flow controllers, which control a number of different gas streams, including that of an inert gas or pure air. The composition of the test gas mixture resulting from blending is controlled by varying the flow of individual gas components through the mass-flow controllers. The test chamber is fitted with heating elements and temperature sensors to control the gas mixture temperature.
The gas composition is controlled by adjusting the flow of gases in each mass flow meter; the set points for these are controlled by a computer running under MATLAB/LABVIEW environment. Each gas line is equipped with the necessary safety valves (shut down valve and one way valve). Additionally, each line has a pressure gauge to monitor the inlet gas pressure.
The temperature controller was based on an Arduino Uno microcontroller, tow (2) driver modules that incorporate a H bridge (mosfet), four (4) heaters (each 100 W/24 V), an LM35 temperature sensor, and two (2) fans to ensure uniform temperature inside the test chamber.
The micro controller (ATMEGA328) receives the temperature set point from the computer running the test rig; then on/off control with hysteresis is used to control temperature from room temperature to 65 °C with a precision better than 1 °C; Hence temperature is precisely and dynamically controlled so that the sensors be tested under different temperatures.
Stainless steel tubes have been used for connecting the various parts. The sealed sensor test chamber included a door that incorporated a rubber seal; all connections to the chamber included rubber seal to ensure that the inner gas composition is controlled only by the mass flow controllers.
The inner walls of the chamber are covered with heat insulation material to minimize heat transfer from the chamber and thus minimize heating power requirements. The size of the chamber was selected to allow testing of a complete wireless sensor node that includes all air quality sensors.
Sensor measurement readings are compared with a professional air quality measurement analyser named “Gray wolf IAQ Monitor” (Acquired from USA) to verify the effectiveness of the proposed system.
In future, humidification of the gas mixture will be considered using different methods, including the saturation method based on water bubble technique. The system will have a fume hood (available in our labs) for safe extraction of gases out of the calibration lab. The test bed will allow:
Calibration of procured sensors and sensor nodes.
Checking sensors cross-sensitivity and effects of environmental conditions.
Training of ANN used with the array of sensors in each node to minimize cross-sensitivity.
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Novel Graphene-Zinc Iron Oxide Composite to Enhance Ultrafiltration Membrane Performance for Water Treatment and Desalination
The main target of membrane technologies such as the Ultrafiltration (UF), Nanofiltration (NF) and Reverse osmosis (RO) is to produce better filtration and separation of organic and inorganic substance from water as well as for longer life of the membrane. The phase inversion method is a well-known method to fabricate UF, NF and RO membranes for different application. The UF membrane is widely used in separation of macromolecules from solution as pretreatment stage with higher efficiency in hybrid process. The UF membrane made by pure polymer showed low flux, which affect on process performance of separation. The Polysulphone (PSF) is the most common polymer used in UF membrane which a hydrophobic material is making its surface prone to fouling due to adsorptive mechanism. This limitation of UF membranes have been solved by blended with nanoparticles incorporated membranes which showed significant enhancement on permeability, surface hydrophilicity, mechanical properties and other properties such as the selectivity. The main objective of this study to modify of UF membrane by blended with new composite nano-material for higher rejection of salt and organic substances. The graphene-zinc iron oxide composite as new nano-material was synthesized by sol gel method at low temperature of preparation. The composite was characterized using X-ray diffraction (XRD), field emission scanning electron microscopy (FESEM), transmission electron microscopy (TEM) to show the structure, morphology and particle size of nanoparticles. Thermal decomposition was determined using thermogravimetric–differential scanning calorimetry (TGDSC). The results showed that cubic system of zinc iron oxide nanoparticles with 8 nm of crystal size was obtained using XRD. The morphology using TEM showed zinc iron oxide composite graphene as layer of nanoparticles with size lower than 10 nm which confirmed the XRD results. The novel synthesized of zinc iron oxide nanoparticles embedded in graphene incorporated into polysulfone (PSF) with 0.5 wt. % loading which significant impact on the UF membrane properties was investigated. The effect of composite additive on membrane properties was investigated in terms of permeability, hydrophilicity (contact angle), zeta potential, porosity and pore size. However, the membrane cross section, surface, EDX and mapping were also analyzed using FESEM include EDX analyzer. This composite incorporated PSF showed significant improvement in terms of surface hydrophilicity with reduction of about 25% (reduce contact angle from 82 to 62°). This improvement confirms by increasing the zeta potential values and surface negatively charge of blended PSF with composite compared to pure PSF membrane. The permeability results showed that significant increased more than two times compared to pure PSF membrane. The phenomenon of permeability increasing was attributed to increase of porosity of blended membrane which becomes lower resistance of water permeation. Generally, the rate of pore production has been reported directly affected by rate of solvent and non-solvent exchange in phase inversion process. However, higher rejections of organic substances such as the dyes and humic acid as well as the salt such as Sodium sulfate (Na2SO4) were maintained using UF at low pressure. This enhancement affects on time and load of process especially when hybrid with Nanofiltration (NF) which can increase of membrane life and reduce of overall process cost. The results of this study will have bigger impact in the future for different application including for water treatment and desalination.
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Determining the Outdoor Air Ventilation with Carbon Dioxide (CO2) as a Tracer Gas
Authors: Ali Ijaz, Mohieddine Amor Benammar, Farid Touati and Abdullah KadriInsufficient ventilation can lead to occupant complaints of discomfort and reduced productivity as human and building generated pollutants build up. Some combinations of these elevated pollutants may have short or long-term detrimental health effects.
Carbon Dioxide (CO2) is very rarely a pollutant of direct health concern itself. Rather a tracer gas, because building occupants exhale CO2 and is used as a tracer gas that is an excellent indicator of adequate (or inadequate) ventilation.
Keeping in view this fact we measured CO2 as a marker, or tracer gas, to determine the outdoor air ventilation (dilution air) rate in an occupied space.
Low CO2 concentration, when measured during periods of average and higher occupancy, implies that human generated pollutants are being properly diluted. And in the absence of a specific pollutant source, it is a rough estimator that the thousands of potential building generated pollutants are being dispersed. This makes it a key indoor air quality indicator.
US Occupational Safety and Health Administration (OSHA)
OSHA states that 1,000 ppm CO2 should be used as an upper limit for indoor levels, as a guideline for occupant comfort. >1000 ppm indicates inadequate ventilation; complaints such as headaches, fatigue, and eye and throat irritation will be more widespread.
American Society of Testing and Materials (ASTM International)
Studies have concluded that about 7.5 L/s of outdoor air ventilation per person will control human body odour such that roughly 80% of visitors will find the odour at an acceptable level. These studies also showed that the same level of body odour acceptability was found to occur at a CO2 concentration that is about 650 ppm (v) above the outdoor concentration.
Us Environmental Protection Agency (Usepa)
EPA Testing for Indoor Air Quality, Baseline IAQ, and Materials, 2009 states that “Acceptance of respective portions of buildings by the Owner is subject to compliance within specified limits of IAQ contaminant.
Levels and CO2 not to exceed 800 ppm”
Observations/Readings
Reading start time: 20-Oct-15 11:31:23 AM
Reading End Time: 03-Nov-15 08:13:43 AM
Average: 547
A study was carried out with IAQ Meter acquired from USA (GrayWolf IAQ Meter) that has capability to measure CO2 along with other pollutants in air. In this paper we would focus only on CO2 values as a tracer gas.
Data comprises more or less for 11 days. Out of these days comparisons are made for Carbon dioxide at a particular time and date with respect to the occupancy of the space (lab).
The max/min of the CO2 concentration is summarised as follow:
Carbon Dioxide ppm:
Min = 373 at 02-Nov-15 05:43:43 AM
Max = 1489 at 20-Oct-15 05:31:23 PM
Average = 546.6
The highest value of 1489 was attained on 20 Oct 2015 Tuesday. If we analyze the lab time table we notice in that time the lab was occupied by students which lead to the highest level of carbon dioxide as it's exhaled by humans.
Rise in carbon dioxide value is evident with the number of occupants in the lab. Carbon dioxide value increases with increasing number of people inside the lab. It starts to rise by 3.30 PM (Lab started) and reaches maximum value of 1489 ppm by 5.31 PM.
It gradually decreases as occupants leave by the end of the lab time.
Average = 546.6 is still within American Society of Heating Refrigeration and Air Conditioning Engineers (ASHRAE) guidelines i.e. 700 ppm
ASHRAE Standard 62.1-2013 suggests maintaining a steady-state CO2 concentration in a space no greater than about 700 ppm above outdoor air levels will result in a substantial majority of visitors being satisfied in respect to human bio effluents (body odor).
Carbon Dioxide (21st Oct Wednesday to 28th Oct Wednesday)
Same lab was occupied on Wednesday 21 October 2015 and 28th October 2015.
If we analyse the trends for CO2 for 21st Oct and 28th Oct (Wednesday) we found that it's quite similar. This is obvious. As per lab time table lab starts by 2.00 PM and ends by 4.45 PM.
We can clearly see the values on the graph for CO2 a start increasing once it's occupied by the students at 2.30 PM and continue to rise until it reaches 900 ppm. The values gradually decrease by 4.45 PM indicating that students started vacating the lab at its end time.
The typical CO2 concentration indoors will increase above outdoor levels depending on the balance between occupancy (as occupants are all exhaling CO2), and the natural and forced ventilation. While levels of 600 ppm to 1000 ppm are typical in office buildings, many factors may result in higher levels (e.g. inadequate ventilation, elevated outdoor levels), or in lower values (e.g. low occupancy at the time of measurement, over-ventilation).
CO2 proved to be a tracer gas as its concentration was affected by number of occupants. This gives a clear picture for the ventilation. If the CO2 concentration increases this means ventilation isn't adequate and if its below the documented value i.e 700 ppm that means the space is well ventilated.
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Enhancing Energy and Water Use Efficiency in District Cooling Plants, An Innovative Approach for Sustainability in Hot Arid Regions
More LessWith around 60–80% of electricity used for air conditioning, and around 99% of potable water production being supplied by desalination plants, sustaining life in Qatar, as well as GCC and hot arid countries around the world, is uniquely energy intensive.
As District Cooling Plants (DCPs) have a potential to reduce energy consumption and CO2 emissions, Qatar and GCC are continuously shifting paradigm towards adoption of DC plants to satisfy the rapidly growing demand in all sectors. However, DC plants usually rely on wet cooling towers for disposing the excess heat to the ambient. Thus the heat disposal is accompanied by considerable loss of fresh water, a common problem in hot arid countries with highest demand for air cooling and also relies on costly and energy intensive desalination processes for securing fresh water supply. In addition to this, evaporative cooling devices and wet cooling towers can spread humidifier fever, a serious health risk with similar symptoms as mild influenza, and Legionella, which can be deadly. Hence huge evaporation loss in densely populated urban centers in Qatar and GCC is an imperative environmental issue which necessitates effective and practical solutions.
This study presents an invention, which involves an innovative process called the “SELF-SUSTAINABLE DISTRICT COOLING AND DESALINATION (SSDD)”. The patented solution is directed to construct a totally new concept for maximization of water and energy use efficiency in district cooling plants in hot arid countries while preserving the environment. The system couples district cooling plants with polishing of treated sewage effluents (TSE) using hybrid reverse osmosis and thermal desalination technologies with the district cooling plant. The desalination process is equipped with a zero liquid discharge (ZLD) system to achieve full recovery of the TSE resource and eliminate the common environmental problem related to brine disposal. The invention closes the water and energy circuits in DC plants, which considerably enhances the overall water and energy efficiencies.
The techno-economic analysis of the SSDD technology has revealed a breakthrough in the technology in terms of reducing energy consumption by 20–30% and water consumption by more than 50%. Considering, for instance, a planned capacity of 1.6 million refrigeration ton DCPs to be added in Qatar by 2022, the SSDD can save up to 200,000 m3/day evaporation losses and 650 MW of electrical power together with elimination of water distribution power needed for pumping potable water from desalination plants to the DCPs. The total energy saving corresponds with 3.5 Million ton reduction of CO2 emissions and more than 1.5 Billion QAR/year excluding the environmental benefits. Considering the ambitious development plans of other GCC states, the SSDD technology may play a significant role in achieving sustainable development goals not only in the region but also worldwide. Thus it holds a great promise for energy and water securities as well as combating global climate change.
The new RO/ZLD concept can be used for applications other than DC, e.g. waste water treatment and reuse, aquifer recharge, football stadia, irrigation for the Qatar National Food Security Program (QNFSP). Moreover, this process can be applied around GCC, Middle East and North Africa (MENA) as well as other hot parts of the world.
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Engineering of High Performance Solar Cells for Harsh Desert Environment Applications
Two major environmental factors affect drastically the performance of photovoltaic (PV) panels in the Gulf region, namely the dust accumulation (soiling) and the temperature-induced voltage decrease leading to a power loss. During the last years, intensive R&D activity has been conducted both by the industry and academia to address these major issues. However, recent results obtained in laboratory show that the power loss induced by an increase of the temperature of the panel from 200C to 750C can be reduced by 250% in the case of heterojunction silicon cells as compared to conventional homojunction silicon technology. Consequently, the temperature coefficient of the conversion efficiency represents an important figure of merit for the energy yield of a given photovoltaic technology, especially if planned to operate in Gulf region.
In this contribution, we will focus on reviewing current strategies addressing temperature effects on PV panels performance. More specifically, we analyze the dependence of the key characteristics of the solar cells with respect to the temperature and minority carrier injection level, and how various layers making the structure of the device can be engineered in order to maximize the resistance of the cell to temperature degradation.
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The Impacts of Anthropogenic and Climate Change Forcings on Water Resources Demands and Availability in Jordan in the Near Future
More LessAbstract
The present paper evaluates the composite risk of anthropogenic and climate change on the future water status in Jordan during the period 2030–2050. The projected water status in the country is evaluated based on the more likely population growth and climate change scenarios. The most likely figure for the population of Jordan, excluding refugees from neighboring countries, in 2040 would be ∼15 million people. Given this likely projection, though conservative, annual water needs for the domestic sector alone are expected to be between 700 and 800 million m3, with the current level of water consumption. A rise in near surface air temperature by 2 °C and a drop in total precipitation by 15%, as projected by most Global Circulation Models, would diminish renewable water resources in the mountainous region by ∼ < /AσΣETHιγηλιγητ>25–40%, being more severe as aridity increases.
1. Introduction
There is almost a consensus among earth scientists that the buildup of greenhouse gases in the atmosphere is leading to a global warming. Documented evidence suggests that global temperature observed over continental and marine regions has been rising for the past several decades (IPCC, 2007). The increased air temperature will intensify the hydrological cycle due to increased water vapor release into the atmosphere. Recent unprecedented severe meteorological events such as large scale torrential rains in many parts of the world and the recurrent tropical cyclones invading the southern parts of the Arabian Sea could be cited as a strong evidence of a global climate change. A climate change towards warmer conditions is expected to increase precipitation over the Arabian Peninsula due to the northward extension of the Monsoon Trough which will enhance the Red Sea Trough during the transitional periods, Fall and Spring.
There is almost a consensus among most GCM that a global warming will be most severe in the eastern Mediterranean, with a significant drop in precipitation and a large temperature rise (Zhang et al., 2005; IPCC, 2007; Kelley et al., 2012). Model results suggest that near surface air temperature will increase by 2–3.5 °C following an equivalent doubling of Carbon Dioxide in the atmosphere (Kelley et al., 2012). The projections for precipitation amount, its temporal distribution and variability are not as certain. Due to the northward retreat of the polar front during the winter months, however, the eastern Mediterranean is expected to experience less cyclogenic activities, and as such less winter storms, leading to a precipitation decline (Schulz et al., 2008). It is also projected that the timing and frequency of precipitation in this region will be more erratic, less frequent but more intense. Statistical evidence show a strong reduction in the number of rainy days with precipitation in excess of one mm day-1.
Population growth adds another negative dimension to the water crisis. This includes more water demands for the domestic, agricultural, tourism, and industrial sectors. Additionally, increased population causes severe deterioration to surface and underground water quality through large scale land use changes, release of large volumes of waste, gaseous and liquid effluents and solid waste disposal. It is clear that anthropogenic and natural forcings work hand in hand to adversely impact Jordan's limited water resources. As such, two operational questions need to be answered:
1- What is the near future water needs in the country?,
2- What is the water availability for the near future following a climate change?
Answering these two questions adequately is essential for a better assessment of the relative impacts of climate change and population growth on water availability, demands, and stress during the near future. This projection can be used to minimize the potential risks of the projected climate change and population growth.
2. Current water availability in jordan
Around 70% of precipitation in Jordan falls in the winter months, December through February, due mainly to cyclogenic activities; the other 30% fall in the transitional periods. Average annual precipitation in the country ranges from a ∼600 mm in a small enclave in northwestern Jordan to less than 5 mm near the Saudi borders (Fig. 1). Additionally, this area receives large quantities of solar radiation year around due to persistently clear skies triggered by large scale subsidence. The combination of scanty precipitation along with a large global radiation enhances direct evaporation and substantially limits blue water availability. The average annual renewable water resources in Jordan are estimated at about 800–850 million cubic meters (M m3) (Ministry of Water and Irrigation, Jordan, 2015).
There is observational evidence that precipitation in the country is declining; Fig. 2 shows a time series of precipitation in two stations, one in northern Jordan during the period, 1945 through 2005, and the other one in central Jordan, Rabbah in the Karak Plateau. Both linear regression and Mann-Kendall non-parametric tests reveal that annual precipitation in all stations in the country is declining.
3. Future population
The population of Jordan experienced a large growth during the past 60 years due to natural growth and as a result of political conflicts. The population of the country, however, swelled by about 20 times during the past 60 years. The invasion of Iraq caused a mass movement of Iraqis towards Jordan. The current civil war in Syria paints another unpleasant, in fact very gloomy, portrait of the population dynamics in Jordan, with current population close to 11 million people.
The population growth was paralleled by a similar increase in irrigated agriculture. The area of irrigated lands in the Jordan Valley increased from ∼15 thousand hectares in the early 1960's to ∼38 thousand hectares in 2011. Likewise, irrigated agriculture in the desert region increased from virtually nil in the early 1970's to ∼17 thousand hectares in 2008 (Ministry of Water and Irrigation, 2012). The substantial increase in the irrigated agricultural land caused further demands on freshwater. The availability of irrigation water will shrink in the near future, however, because of growing demands on this resource from other sectors, mainly the domestic sector. The future water status in the country would indeed look quite bleak should population growth continues unabated and a climate change towards warmer and/or drier conditions prevail in the near future.
4. Future Water Needs
Official figures provided by the Ministry of Water and Irrigation, Jordan (2015) indicated that current domestic freshwater supply is ∼150 liters per person/day, which gives a total annual freshwater need of 370 M m3. Nowadays, with only 7.5 million inhabitants (excluding fresh refugees), most households in Jordan receive a specified amount of water during the summer months, and domestic water is supplied once (few hours) per week. Renewable water resources in the country were not enough to meet the water demands, and as such non-renewable fossil freshwater resources have been intensively exploited during the past several decades. These measures have caused steady drop in the level of underground aquifers and resulted in poor water quality. The Dissi Project, conveying fossil water is expected to provide freshwater for several decades before it dries up completely.
Projections based on future population growth scenarios indicate that annual domestic water needs alone will range from a minimum of 550 M m3 to a value close to 1100 M m3 by 2050. A more likely figure would probably be between 700–800 M m3. Thus, renewable freshwater resources of the entire country will barely meet domestic water needs even without a climate change.
Currently, the agricultural sector accounts for about 65% of total freshwater consumed in Jordan (MWI, 2015). Paradoxically, the amount of water allocated for irrigation must drop in the near future because of demands by relatively more needy sectors, the domestic one in
particular. Based on population growth alone, it is obvious that the future water status in the country looks quite bleak even without a climate change. Should the climate of the eastern Mediterranean become warmer and/or drier or both, the country will face a serious, probably tragic, freshwater dilemma in the very near future which will ultimately lead to economic, social and political unrest. The anticipated climate change will seriously influence the future water crisis in Jordan.
5. Projected climate change impact
A climate change in the eastern Mediterranean will impact water resources in at least three ways: 1) reduces blue water availability due to increase direct evaporation from soils, 2) intensifies irrigation water demands, and 3) increases evaporation losses from dams and open water canals. The impact of climate change on the available water resources in Jordan is investigated using a water balance model with a temporal resolution of one day. The model is run over the mountainous areas of Jordan where around 65% to 70% of blue water is generated (Oroud, 2015). A detailed description of the model is presented elsewhere (Oroud, 2008; 2011). Figure 4 shows the linkage between annual blue water availability and annual precipitation as calculated by the daily model. Conservative calculations show that a 2 °C temperature increase along with a 15% reduction in precipitation decreases water availability, on average, by ∼ 25%–40% depending on the level of aridity, being more sever as in more arid regions. This means that renewable water resources in the country following a warmer, drier climate will probably be between 500–650 M m3 by 2050. This conclusion is commensurate with those presented by other investigators (e.g., IPCCk 2007; Margane et al. 2008; Suppan et al. 2008; Giorgi and Lionello, 2008; Kelley et al., 2012).
Irrigation water needs under current climate conditions and following a climate change were simulated for the Jordan Valley using a spatially distributed daily model. Following a climate change, the irrigation water needs will increase by around 15%. This is equivalent to 40 to 50 M m3 of extra irrigation water needed to maintain the irrigation water demands in the Jordan Valley at the current land use regime.
References
Giorgi, F., Lionello, 2008, Climate change projections for the Mediterranean region, Global and Planetary Change, 63, 90–104.
Inter Governmental Panel on Climate Change (IPCC), 2007, The physical science basis, Geneva.
Margane A., et al., 2008, Water resources protection efforts in Jordan and their contribution to a sustainable water resources management. In F. Zereini and H. Hotzl (eds) Climatic Changes and Water Resources in the Middle East and North Africa, Springer, pp. 325–345.
Kelley, C., et al., 2012, Mediterranean precipitation climatology, seasonal cycle and trend as simulated by CMIP5, Geophysical Research Letters, 39, DOI: 10.1029/2012GL053416
Oroud, I. M., 2008. The impact of climate change on water resources in Jordan. In: F. Zereini and H. Hotzl (eds) Climatic Changes and Water Resources in the Middle East and North Africa, Springer, pp 109–123.
Oroud, I. M., 2012a, The relative impacts of climate change on water resources in Jordan, in: National Security and Human Health Implications of Climate Change (H. Fernando et al., eds.), DOI 10.1007/978-94-007-2430-3-31, Springer Science.
Oroud, I. M., 2012b, Climate change impact on green water fluxes in the eastern Mediterranean.: pp 3–15. In: Leal Filho, W. (ed) “Climate Change and the Sustainable Management of Water Resources.
Oroud, I. M. and Alrousan, N., 2004, Urban encroachment on agricultural lands in Jordan during the second half of the twentieth Century, The Arab World Geographer, 7, 165–180.
Oroud, I. M., 2015, Water budget assessment within a typical semiarid watershed in the Eastern Mediterranean, Environmental Process 06/2015; 3(2):1–15. DOI: 10.1007/s40710-015-0072-8
Suppan, P. et al. 2008, Impact of climate change on water availability in the Near East. In F. Zereini and H. Hotzl (eds) Climatic Changes and Water Resources in the Middle East and North Africa.
6- Schulz, O., Busche, H., Benbouziane, A. (2008) Decadal precipitation variances and reservoir inflow in the semi-arid upper Draa basin. In: F. Zereini and H. Hotzl (eds) Climatic Changes and Water Resources in the Middle East and North Africa, Springer, pp. 165–178.
Zhang, X., et al., 2005, Trends in Middle East climate extremes indices from 1950 to 2003. J. Geophys. Res. 110.
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Bio-Facades; An Innovative Design Solution Towards Sustainable Architecture in Hot Arid Zones
Authors: Fodil Fadli, Payam Bahrami, Irina Susorova, Meysam Tabibzadeh, Sara Zaina and El-Shaimaa El-EkhteyarThe United Nations forecasts that 70% of the World's projected population of nine billion people will be urbanized by the year 2050, a 51% increase from seven billion people urbanized as of 2010. The enormity of this total figure of 2.8 billion people moving into cities over the next 40 years is can be more clearly appreciated when converted into an annual rate of 70 million people per year, or a daily rate of nearly 200,000 people. This means that the human race needs to build a new city of more than one million people every week for the next 40 years to cope with this urban growth (UN, 2011).
Creating comfortable urban and building environments is challenging in hot climate conditions of many countries of the MENA (Middle East and North Africa) and Gulf region, such as Qatar. Hot ambient air temperature and a high level of solar radiation lead to large heat gains through building envelopes. In addition, heat gained by building surfaces is emitted back into the atmosphere which leads to the increase in ambient air temperature in urban environments. This phenomenon is often called the urban heat island (UHI) effect. As a result, buildings constantly have to rely on mechanical cooling systems in order to achieve comfortable indoor conditions. To balance the weather conditions of hot climates, buildings generally require a large amount of energy for cooling consumption.
Buildings located in hot and arid desert environment of the MENA and Gulf region traditionally relied on different passive measures and devices for cooling and ventilation. These passive measures based on natural phenomena included natural cooling and ventilation by wind, evaporative cooling from water, and shading from the sun. Typically, buildings combine a few passive cooling techniques that give a distinctive look to MENA region architecture in its multiple variations from North Africa to the Middle East, and from the Gulf to Levant countries. For example, buildings often include one or two wind towers that capture strong wind high above the roof and redirect it down into the building core for cooling and air circulation (Oliver, 1998).
The link between humans and nature becomes important as more than 50% of the World's population lives in cities. In the last 20 years as part of the environmental sustainability movement, there was a new interest in incorporating plants into building construction, including buildings with green roofs and green walls. The significant positive effects of vegetation and landscape elements on building thermal and energy performance and the urban heat island effect are well known. Many countries located in hot climates had the tradition to grow vines along building perimeters and above atria to provide shade from excessive sun exposure and to cool the air. The recent sustainability movement has renewed the interest in integrating plants into various architectural features, such as building roofs, facades, or atria. While green roofs covered with layers of vegetation have long been prominent features of buildings in many cities, green walls integrating plants into buildings’ vertical elements are still a relatively new architectural concept (Dunnett & Kingsbury, 2010). We can learn valuable lessons by adopting design concepts from indigenous buildings and architecture (Fadli & Sibley, 2009).
The purpose of this paper is to discuss the bio-facade concept and its benefits as an environmental solution for creating a sustainable architecture and urbanism in hot climate areas such as MENA region. Bio-facades can be considered to new or existing building construction of commercial, residential, and public buildings with great imagination by using such architectural features as green walls, hanging gardens, green roofs, or pergolas. In addition to their striking visual effect, vertical vegetation increases building energy efficiency, creates a positive effect on the psychological and physiological health of individuals, helps mitigate the urban heat island effect, reduces greenhouse gases, improves air quality by acting as a bio-filter, protects wall construction materials from ultraviolet radiation, reduces noise pollution, and creates natural habitat areas in cities. These benefits create a path towards making cities more environmentally sustainable. Bio-facades can be incorporated either into the traditional courtyard architecture or contemporary buildings to create a better microclimate, to provide shade, and to reduce energy consumption, enhancing the energy performance of building envelopes, the buildings themselves, and their surrounding environment.
The current study led by the authors, indicated that bio-facades can be used as an environmental sustainable solution for energy efficient building in different climates. This paper will answer the questions: “How does bio-facades may create sustainable architecture and urbanism in the hot and dry climate and what are their benefits?”, “how does bio-facades affect thermal and energy performance of buildings in the hot and dry climate?” Acknowledgements: “This research/publication was made possible by a National Priority Research Program NPRP award [NPRP-07-1406-2-507] from the Qatar National Research Fund (a member of The Qatar Foundation). The statements made herein are solely the responsibility of the author(s).”
Note: This QNRF-NPRP funded project number 7-1406-2-507, titled “The design, development and use of innovative bio-green facades: towards improved urban microclimates and enhanced building thermal performance in Qatar” is a joint collaboration between Qatar University (QU), Optim Design Inc, Cyclone Energy Group, and Mingo Design LLC (USA).
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Life Cycle Assessment of Tall Buildings in Qatar, A focus on Construction Materials Use and Techniques
Authors: Fodil Fadli, Tommy Dacanay, Cristopher Moen, James Guest and Payam BahramiBuildings represent one of the most significant sources of negative impacts to the natural ecosystems on which Qatar's inhabitants health and environmental quality depend. The market has identified Qatar as one of the busiest construction areas in the world (Ibrahim 2011), While rapid economic development, population growth, and construction boom are positive indicators of growth, they may also present issues related to the negative impact on the socio-environmental components of cities. Such is the case of the Gulf Cooperation Council (GCC) countries where increasing economic prosperity has led to a surge in tall building construction and a sense of competition to erect the tallest skyscrapers in the world (Mahgoub and Abarra 2012).
While tall buildings are a source of national pride and cultural identity enabled by economic prosperity, they pose several challenges to integrate with the urban fabric of the city while also having a tremendous environmental impact. Tall buildings are especially massive consumers of energy (Ali and Armstrong 2008). They are the dominant elements in urban architecture due to their scale and purpose, and should be the focus of sustainable design. With large number of towers constructed and to be constructed in Al Dafna and West Bay areas of Doha, these buildings affect different aspects of the built and urban environment, i.e., city image, traffic, urban spaces and physical conform. Therefore, more architectural design strategies have to be planned well ahead in order to tackle the issues of sustainability and adaptability to climate change and to foster sustainable built environment in the state of Qatar.
With Qatar slated to host a ‘zero carbon’ World Cup in 2022, Qatar Green Building Council (QGBC) has set up a group to foster green infrastructure as a national resource. Qatar is utilizing Leadership in Energy and Environmental Design (LEED) and the Global/Qatar Sustainability Assessment System (GSAS/QSAS) to this end. Furthermore, shortages in raw materials between 2013 and 2017 are expected to challenge the construction sector, as the period is expected to be the peak for the sector. Therefore, the sector will have to bridge the gap during this period by mutual agreements with the companies in Saudi Arabia and the UAE (QCB 2012).
The objectives of this paper are as follows: 1- to Identify sustainability metrics for tall buildings with focus on construction materials and methods used in Qatar; 2- Explore existing literature and identify analogies in optimization consistent with design variables; 3- to examine sustainability of construction materials used in Qatar by utilizing software which is based on currently available databases to perform life cycle assessment.
To meet the objectivess described above, the currently available software platforms to perform life cycle analysis of building materials were explored. A commercial software, SimaPro, which utilizes the environmental impact database Ecoinvent, was chosen for its flexibility in defining custom mix designs for concrete, as well as database information on steel and many other building materials. With SimaPro, a sustainability model for concrete and steel was developed which reflects the environmental implications of manufacture of materials in Qatar as appropriate. Quantitative results from the model for the sustainability of constituents of building materials were extracted, to form the basis of sustainability metrics in the forthcoming tall building topology optimization protocol.
Furthermore, Blanco-Carrasco et al (2010) outline reduced use of Portland cement, increased use of alternate cementitious materials, and reduced water use to improve the sustainability of the concrete industry in Qatar. Using structural models and the SimaPro model, ultra-high performance concrete was explored as a potential solution for all these problems, to be applied in the gravity/lateral structural components of Qatar tall buildings. In addition to identifying a novel material which fits well with the current tall building designs of the region, the process of examining the structural and environmental improvements from using ultra-high performance concrete has resulted in the formation of a procedure to compare multiple materials used in Qatar.
This paper is a result of a funded research project by QNRF, entitled “Multi–Objective Tall Building Topologies – Optimizing for Structural Performance, Economy, and Sustainability” and a jointly collaboration between researchers from Qatar University, Virginia Tech, Johns Hopkins University, Optim Design Inc, and MZ & Partners.
“This research/publication was made possible by a National Priority Research Program NPRP award [NPRP- 7 - 1518 - 2 – 549] from the Qatar National Research Fund (a member of The Qatar Foundation). The statements made herein are solely the responsibility of the author(s).”
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Development of a Life Cycle Assessment Tool for the Analysis of Food Production Systems within the Energy, Water and Food Nexus
Authors: Tareq Al-Ansari and Anna KorreAs the demand for services and products continues to increase in light of rapid population growth, it is vital to ensure the sustainability of the natural resources. Critical to this growth is the question of energy, water and food security. The systems representing these three resources are intrinsically interdependent where impact on any one of them will have a simultaneous impact in the remaining two. As such, there is a need to develop assessment tools that consider the interdependencies of energy, water and food (EWF) systems in order to ensure that system dynamics are understood and disturbances are avoided where possible. For instance, when evaluating the environmental performance of a food production system, aggregating the system in terms of its agriculture, water and energy components is critical to develop a lifecycle blueprint of the system. The EWF Nexus tool has been used to describe food security in Qatar from a local environment perspective. The tool is a culmination of well-established theories related to system design and analysis such as Industrial Ecology and LCA with emphasis on EWF inter-linkages. The modularity of the nexus model enables the integration of a variety of different technologies which promote the de-materialization of the system and the subsequent evaluation of different configurations. The basis of which is to identify and achieve maximum emission reduction. This paper reports recent work expanding the LCA modelling tool of the EWF Nexus developed by the authors (Al Ansari et al, 2015). Through the integration of greenhouse gas control technologies, sub-system analsysis and scenario development, the objective is to enhance the environmental performance of Qatar's food production system. Using de-materilization and waste minimisaiton strategies promoted by Industrial Ecology, the objective of EWF Nexus tool is to reduce environmental degradation in business as usual scenarios. This includes the integration of waste management strategies and technologies to reduce the overall life cycle environmental impact of the Qatar Food system. Waste management strategies and greenhouse gas control technologies are represented by additional sub-systems which convert waste material to energy and capture of CO2 from power generation. As part of the LCA, sub-system LCI models representing the EWF systems have been developed. The food portion of the nexus is represented by the production of fertilizers and agricultural activities such as the application of fertilizers and the raising of livestock. The livestock under management include broilers, dairy, beef, sheep and camels. The water portion of the nexus includes Multi-Stage Flash (MSF) and Reverse Osmosis (RO) for the production of water. Finally, the energy sub-system considers power generation from a combined cycle gas turbine plant (CCGT) and renewable energy from solar Photovoltaics (PV). Furthermore, a biomass integrated gasification combined cycle (BIGCC) is integrated to recycle solid waste into useful forms of energy to be re-used within the nexus. Finally, carbon capture (CC) technology is integrated to capture and recycle CO2 from both the CCGT and the BIGCC. The integration of CC with the BIGCC transforms the carbon neutral BIGCC process to a negative GHG emission technology with carbon capture and storage (BECCS). For the different scenarios and subsystem configurations considered, the global warming potential can be theoretically balanced (i.e. eliminated) through the integration of PV's, BIGCC and CC technology. The peak GWP, i.e. a fully fossil fuel dependent system, is recorded at 1.73 × 107 kg CO2 eq./year whilst the lowest achievable GWP is 2.18 × 107 when utilising a combination of PV, CC integrated with CCGT in addition to BECCS technology. The natural gas consumption to − 7.8 × 107 kg/year in the best case configuration achieving a credit. In the same scenario, the PV land footprint required is calculated to a maximum of 660 ha. The maximum theoretical achievable negative emission is 1.09 × 109 kg CO2/year.
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Carbon Dioxide Enhanced Oil Recovery and Storage: Experimental Investigation to Maximize Energy Resources while Reducing Carbon Footprint in Qatar
Authors: Ali Al-Menhali and Samuel KrevorQatar is the biggest exporter of liquefied natural gas, LNG, in the world and is a main oil-producing member of The Organization of Petroleum Exporting Countries, OPEC. A fossil fuel-based industry emerged around the ports of Ras Laffan and Mesaieed, Qatar's industrial cities, perusing industrial diversity and maximising the huge fossil fuel reserves that serve as the primary feedstock for the industrial sector. LNG, crude oil, and petroleum products has given Qatar a per capita GDP that ranks among the highest in the world with the lowest unemployment. This also has given Qatar a per capita CO2 emissions among the highest in the world. A recent report from The World Health Organisation, stated that the capital of Qatar, Doha, is one of the world's most polluted cities and its air ranked the 12th highest average levels of small and fine particles which are particularly dangerous to health [1]. The people and wise leadership of Qatar recognizes the significance of the problem and made environmental development one of the four pillars of Qatar National Vision 2030. The vision places environmental preservation for Qatar's future generations at the forefront. Qatar Carbonates and Carbon Storage Research Centre is an example demonstrating Qatar's commitment to preserve the envioronment by investigating and implementing key technologies such as carbon capture and storage (CCS) to address the next step in climate change. CCS in deep saline aquifers is an important process for CO2 reduction on industrial scales. The aim of CCS is to safely sequester CO2 generated from stationary sources, such as power-plants, into aquifers and depleted oil reservoirs. It is considered a valuable option to reduce greenhouse gases and has been proposed as a practical technology to tackle climate change [2–4]. The importance of CCS as a key option to mitigate CO2 emissions and combat climate change has been highlighted also in a report by the International Energy Agency (IEA) and suggests that CCS could contribute to a 17% reduction in global CO2 emissions by 2035 [5]. Previously, carbon dioxide injection into the subsurface has mainly been used for enhanced oil recovery (EOR) purposes. That gave rise to Carbon capture, utilization and storage (CCUS) processes in mature oil reservoirs where CO2 is first used to enhance oil recovery and then ultimately stored in the reservoir. The incremental hydrocarbon recoveries associated with CCUS make it more attractive to implement compared to CCS. It have significant energy, economic and environmental benefits and is considered an important component in achieving the widespread commercial deployment of CCS technology. Residual trapping of CO2 through capillary forces within the pore space of the reservoir is one of the most significant mechanisms for storage security and is also a factor determining the ultimate extent of CO2 migration within the reservoir. Observations and modelling have shown how capillary, or residual, trapping leads to the immobilisation of CO2 in saline aquifer reservoirs, limiting the extent of plume migration, enhancing the security and capacity of CO2 storage [6,7]. In contrast, carbonate hydrocarbon reservoirs are characterised by a mixed-wet state in which the capillary trapping of nonpolar fluids have been observed to be significantly reduced relative to trapping in rocks typical of saline aquifers unaltered by the presence of hydrocarbons [8,9]. There are, however, no observations characterising the extent of capillary trapping that will take place with CO2 in mixed-wet carbonate rocks, the same rock type found in Qatar's subsurface geological formations and many other giant oil reservoirs in the Middle East that hold most of the oil in the world [10, 11]. Experimental tests of CO2 and brine in carbonate rocks at reservoir conditions are very challenging due to the complex and reactive nature of carbonates when dealing with corrosive fluids pair of CO2 and brine. In this study, we compare residual trapping efficiency in water-wet and mixed-wet carbonates systems on the same rock sample before and after wettability alteration by aging with oil mixture of Arabian medium crude oil. The experimental work was conducted using a state of the art multi-scale imaging laboratory (core and pore scale) developed at Imperial College London designed to characterise reactive transport and multiphase flow, with and without chemical reaction for CO2-brine systems in both sandstone and carbonate rocks at reservoir conditions [12]. The flow loop included stir reactor to equilibrate rock with fluids, high precision pumps, temperature control, the ability to recirculate fluids for weeks at a time and an x-ray CT scanner and micro x-ray scanner for in situ saturation monitoring. The wetted parts of the flow-loop are made of anti-corrosive material that can handle co-circulation of CO2 and brine at reservoir conditions with the ability to preserve the rock sample from reacting to carbonic acid. We report the initial-residual CO2 saturation curve and the resulting parameterisation of hysteresis models for both water-wet and mixed-wet systems. A novel core-flooding approach was used, making use of the capillary end effect to create a large range in initial CO2 saturation in a single core-flood. Upon subsequent flooding with CO2-equilibriated brine, the observation of residual saturation corresponded to the wide range of initial saturations before flooding resulting in a rapid construction of the initial residual curve. Observations were made on a single Estaillades limestone core sample. It was made first on its original water-wet state, then were measured again after altering the wetting properties to a mixed-wet system. In particular, CO2 trapping was characterized before and after wetting alteration so that the impact of the wetting state of the rock is observed directly on both core and pore scales. A carefully designed wettability alteration programme was designed in this study to replicate a mixed-wet carbonate system similar to those found in Qatari oil reservoirs. At the pore level, oil can precipitate asphaltene and other heavy components after long exposure with the rock changing the wetting state of the surface to oil-wet. A mixture of the evacuated crude oil with an organic precipitant, n-heptane, was used to deposit a stable oil-wet film. The precipitant substituted some of the evaporated and oxidised light hydrocarbon originally existed in the crude and deposited asphaltene to generate a stable strongly oil-wet film layer. Filtration experiments were carried out to sensibly precipitate enough asphaltene for a stable and strong oil-wet film without over precipitating and causing fine migration that can damage the core sample. The weight fraction of asphaltene precipitated with different fractions of crude-precipitant mixtures were measured. The diluent consisted of toluene as the solvent and heptane as the precipitant. 40 ml of the diluent was thoroughly mixed with 1 ml of Arabian Medium crude oil at 11 different precipitant/solvent volume ratios ranging from 0–100% at 10% increments and then left in the dark for 48 hours to allow the system to come to equilibrium. The mass of precipitated asphaltenes was measured in each mixture by vacuum filtration using a 0.45 micron polytetrafluoroethylene hydrophobic filter paper (Millipore) and evaporation of any remaining liquid oil from the filter paper. No asphaltene was precipitated at low precipitant volume fraction and only above the onset of precipitation, a linear relationship was seen between the wt% precipitated asphaltenes and the volume % of the precipitant in the mixture. The onset for asphaltene precipitation for an oil mixture of Arabian Medium crude oil and heptane alone without solvent was calculated at the onset using the volume fractions of the components with the mixing rule. The sample's wettability was altered to a mixed-wet using the appropriate oil mixture as measured using the filtration test and the oil was then removed from the sample by CO2 enhanced oil recovery injected above the minimum miscibility pressure. This allowed for producing unique dataset and a great complement to the more theoretical analysis. That is if we make a surface oil-wet (to water), how does it behave in the presence of a gas. Here we show that residual CO2 trapping in mixed-wet carbonate rocks characteristic of hydrocarbon reservoirs is significantly less than trapping in water-wet systems characteristic of saline aquifers. We found that in the native water-wet state of the carbonate sample, the extent of trapping of CO2 and N2 were indistinguishable, consistent with past studies of trapping and multiphase flow properties in water-wet sandstones [13, 14]. After alteration of the wetting state of the same rock sample with oil, the residual trapping of N2 was reduced compared to the amount in the pre-altered rock. Surprisingly, the trapping of CO2 was reduced even further. The unique results were complemented with pore scale observations to investigate the balance of interfacial tensions and contact angles in three-phase flow. Our results show that one of the key processes for maximising CO2 storage capacity and security is significantly weakened in hydrocarbon reservoirs relative to saline aquifers. We anticipate this work to highlight a key issue for the early deployment of carbon storage – that those sites which are economically most appealing as initial project opportunities are the very locations in which the contribution of capillary trapping to storage security will be minimised. This should serve as a starting point for modelling studies to incorporate the reduced impact of capillary trapping on CO2 injection projects using hydrocarbon reservoirs.
References
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Al-Menhali, A., B. Niu, and S.Krevor (2015), “Capillarity and wetting of carbon dioxide and brine during drainage in Berea sandstone at reservoir conditions”, Water Resour. Res., 51, doi:10.1002/2015WR016947.
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Dynamic Tariff Development for Effective Demand Side Management (DSM) in the Presence of Increased Penetration of Photovoltaics (PV)
I. Introduction
The trend towards high penetration of renewable energy sources (RES) in the energy mix and particularly grid-connected photovoltaic (PV) systems in the low voltage (LV) network, offers the benefits of green decentralized generation, at the cost of the development of energy management tools to alleviate potential problems. More specifically, the fact that for most consumption profiles the PV energy production does not coincide with the electricity demand, forces the grid to act as a sink and a source thus requiring re-adaptation of the grid operation [1]. To this extent, an advanced demand side management (DSM) scheme can be introduced to mitigate RES operational issues and contribute to managing effectively congestion problems. In this work, a price-based DSM tool has been developed in order to arrive at an effective Time of Use (ToU) tariff with improved DSM results. In this scope, smart meters (SMs) have been deployed at three hundred households with grid-connected PV systems installed at their rooftops, in order to acquire consumption and production profile details of typical Cypriot prosumers. The selected pilot sites that already have a 3 kWp grid-connected PV system, have been offered a ToU tariff allowing rates and charges to vary based on the time and date of consumption, i.e. day or night and seasonality. This aims to examine how financial implications can alter the energy behavior of prosumers [2]. In addition, the prosumers are divided into three groups each receiving a distinct method of monitoring their energy habits: one group will have In-House Displays (IHDs), the other will have access through a web application, and the third will receive information about their energy habits through the traditional bi-monthly mail bill. This will facilitate an in-depth examination of the prosumers’ response based on the information sent to them [2].
II. Background
Theory Price-based DSM programs offer an alternative to the traditional flat tariffs and comprise of Critical Peak Pricing (CPP), Real-Time Pricing (RTP) and Time-of-Use (ToU) tariffs [3], [4]. Amongst the different schemes, ToU tariffs are commonly preferred because the price of energy consumption is fixed for different periods of the day in contrast to other price-based DSM programs where the price fluctuates following the real time cost of electricity [3], [4]. The development of an efficient DSM system offers the advantage of generating cost reductions for grid utilities and the increase of operational efficiency. However, in order to achieve a balanced DSM scheme, the existing flat tariffs need to be transformed to ToU tariffs providing the necessary monetary incentives for domestic consumers to flatten their load profile. Even though, ToU tariff schemes offer the advantage of price certainty, the effectiveness of such tariff schemes must be verified prior to implementation because of the risk of a new peak appearing through load shifts at cheaper price periods, posing negative effects on the optimal operation of the system [5]–[8].
III. Prosumer Features
In support of this work, three hundred prosumers in Cyprus have been selected through the implementation of the SmartPV project (http://www.smartpvproject.eu/), in order to acquire real-time information of the consumption and production profiles and to identify the potential problems and limitations of the existing energy policy. All participating prosumers are geographically spread in Cyprus, in order to cover different socio-geographical conditions and thus targets a variety of consumers. In addition, prosumers with higher total yearly electricity consumption (in kWh) compared to the typical energy production from a 3 kWp grid-connected PV system were selected.
IV. Methodology
The development of a dynamic ToU tariff tool to enable price-based DSM relies strongly on the analysis of the basic input parameters such as electricity demand and PV electricity production profiles. Consumption and production data acquired from the three hundred prosumers was used to optimize the dynamic ToU tariff algorithm for the case of Cyprus. It has to be pointed out that this is a benchmark tool which can be used by any other country. The first step in the development of the algorithm was to identify the maxima and minima power consumption periods of the provided average domestic consumption profiles, an approach already implemented and verified [9]. The load duration curve of the provided average domestic consumption profile in Cyprus for each season was analyzed in order to identify possible inflection points. The different inflection points of the curve represent the various load segments which were used in order to obtain the probability density function (PDF) (at a 95% confidence interval) [1]. The PDF of each segment represented the ToU block period. The dynamic tariff tool developed from the above statistical analysis is capable of deriving the ToU blocks with a mean absolute percentage error (MAPE) and root mean square error (RMSE) between the ToU block periods and the load profile of 8.65% and 19.95%, respectively [1]. In order to further improve the initial algorithm, a function based model was developed. Optimization methods were used in combination with the statistical results [1]. In this approach the statistical output ToU block periods are used as the initial condition of the optimization procedure using the Matlab Optimization ToolboxTM. The ToU blocks are directly compared with the load profile rather than extracting the ToU blocks from the load duration curve. The objective function of the optimization procedure minimizes the RMSE as described by (1): where is the derived ToU block period, is the load profile and is the total sampling interval. Based on this equation, is the variable to be optimized and changes according to the desired levels. To achieve this, the developed optimization tool uses a hybrid optimization function such as simulated annealing [10] and pattern search [11]. In summary, two different methods were used to derive the final ToU block periods: a) combining statistical analysis using the load duration profile and b) optimization methods applied to the load profile.
V. Results
A. Dynamic ToU Tariff tool A software application tool was developed in order to assist users to visualize the impact on their electricity bill from the different ToU blocks. The derived ToU blocks for the winter period were compared using two different approaches (figure 1). The MAPE and RMSE between the load curve and the ToU blocks were improved by utilizing the optimization tool reducing them by 2.43% and 7.63%, respectively when compared to the statistical approach. Furthermore, the optimization approach clearly demonstrated that the peak consumption period is charged with the higher tariff, while the lowest tariff occurs during the valley period. Through this approach another period is clearly identified representing the transitional period: from the minima to the maxima and vice-versa. These time periods are important as they can be used by prosumers to cover their needs that can be shifted from the peak periods but cannot wait until the off-peak period (e.g. cooking, devices without smart control etc). B. Acquired data from three hundred prosumers Data-sets collected during the summer period from the three hundred prosumers equipped with Smart Meters (SMs), before the application of ToU tariffs, were analysed in order to evaluate the self-consumption index. Figure 2 presents the consumption and PV production profiles from the pilot sites. The evaluation of the self-consumption energy was calculated using the equations below [12] and the results are presented in Table I. The average self-consumption energy for the participating prosumers during the summer months is calculated to be 738.87 kWh hence, 53.52% of the energy produced is directly consumed on site while the remaining energy is exported to the grid. Comparing this with the typical prosumer of Cyprus, the self-consumption rate is more than 10% higher. This is mainly due to the fact that the SmartPV sample has on average a higher load demand when compared to the typical prosumer.
VI. Conclusions
In this work, the application of DSM schemes aiming at raising the awareness of the consumers, coupled with financial incentives has been demonstrated through dataset collection from 300 prosumers. In this domain, a new tool for evaluating the dynamic ToU tariffs has been developed based on two different methods, in order to promote effective price-based DSM practices in the electricity network of Cyprus. This is based on statistical analysis of the provided average consumption profiles and optimization procedures, aiming to derive the most appropriate ToU tariffs. The statistical method showed a MAPE and RMSE of 8.22% and 19.95%, respectively, by comparing the resulted ToU blocks to the load profile. On the other hand, the optimization method resulted in a MAPE and RMSE of 6.22% and 12.32% respectively, proving its effectiveness and improved accuracy. In addition, energy data-sets have been collected from participating prosumers before the implementation of the ToU tariff and comparisons between measured data and a typical prosumer was made. The results indicated an average self-consumption index with the existing net metering scheme for the summer months of about 53%.
Acknowledgment
The project is co-financed by the program LIFE (LIFE+ Environment Policy and Governance) of the European Union under the grant agreement number LIFE 12/ENV/CY/000276.
References
[1] N. Philippou, M. Hadjipanayi, G. Makrides, V. Efthymiou, and G. E. Georghiou, “Effective dynamic tariffs for price-based Demand Side Management with grid-connected PV systems,” in PowerTech, 2015 IEEE Eindhoven, 2015, p. 5.
[2] B. Davito, H. Tai, and R. Uhlaner, “The smart grid and the promise of demand-side management,” 2010.
[3] M. H. Albadi and E. F. El-Saadany, “A summary of demand response in electricity markets,” Electr. Power Syst. Res., vol. 78, no. 11, pp. 1989–1996, Nov. 2008.
[4] B. Severin, M. Jaske, and A. Rosenfeld, “Dynamic Pricing, Advanced Metering, and Demand Response in Electricity Markets.” Center for the Study of Energy Markets, p. 103, 2002.
[5] S. Gottwalt, W. Ketter, C. Block, J. Collins, and C. Weinhardt, “Demand side management—A simulation of household behavior under variable prices,” Energy Policy, vol. 39, no. 12, pp. 8163–8174, Dec. 2011.
[6] J. Torriti, “Price-based demand side management: Assessing the impacts of time-of-use tariffs on residential electricity demand and peak shifting in Northern Italy,” Energy, vol. 44, no. 1, pp. 576–583, Aug. 2012.
[7] J. Thumim, “Investigating the potential impacts of Time of Use (TOU) tariffs on domestic electricity customers Report to Ofgem,” 2014.
[8] C. M. Flath, “An optimization approach for the design of time-of-use rates,” in IECON - 39th Annual Conference of the IEEE Industrial Electronics Society, 2013, pp. 4727–4732.
[9] Q. Hui-ting and L. Yi-jie, “Research of Peak and Valley Period Partition Approach on Statistics,” in 4th International Conference on Electric Utility Deregulation and Restructuring and Power Technologies (DRPT), 2011, pp. 1774–1779.
[10] L. Ingber, “Adaptive simulated annealing (ASA): Lessons learned,” Invit. Pap. to a Spec. issue Polish J. Control Cybern. “Simulated Annealing Appl. to Comb. Optim., 1995.
[11] T. G. Kolda, R. M. Lewis, and V. Torczon, “A generating set direct search augmented Lagrangian algorithm for optimization with a combination of general and linear constraints,” 2006.
[12] O. Schaefer, S. Willborn, S. Goeke, J. A. Toledo, V. Cassagne, and A. Roesch, “Self Consumption of PV Electricity,” EPIA, 2013.
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Investigation Into the Effects of Non-Linear Loading of Domestic Power Network on Home Appliances
Authors: Ajad Hossain, Jassim Zaman, Mahmood Saeed, Atif Iqbal and Syed RahmanNon-Linear loads such as Compact Fluorescent lamps (CFLs), Light Emitting diodes (LEDs),Solid state voltage regulators, and variable speed electric drives are increasingly being added tothe domestic, residential and industrial power network. These light sources and other house-hold appliances using power electronic converters are termed as non-linear loads and they introduce distortion in the power network by generating harmonics in the current, leading to poor power quality [1 − 4]. Power quality issues are now becoming a major concern because of several reasons: a) Increasing dependence on electrical supply and even small disruption or interruption are not bearable because it can halt the modern lifestyle, b) new modern electrical equipment are highly sensitive to the power quality and c) the power electronic components such as variable speed drives and switched mode power supplies poses new disturbance challenges to the electrical supply network [5 − 7]. Power quality standards such as IEEE 519 is proposed to: a)assure that the electric supply company should deliver clean electric power to the consumers, b) assure that the electric supply company can protect electrical equipment from excessive voltage stress, overheating and loss of operational life of equipment. The IEEE 591 standard is in place that puts a limit on the allowed harmonic distortion of 3% on individual harmonic components and 5% on total harmonic distortion (THD). This standard is of utmost importance on the present day situation due to increasing non-linear loading. Although the distortion limits are not applied to specific equipment, however, with a high penetration of non-linear loads, it is likely that some harmonic suppression may be necessary [8 − 12]. The power quality problem is a distortion in the voltage waveform of the power source which is deviation from sine wave. Another power quality problem is a change in the amplitude from an established reference level. Other disturbance can be caused by harmonics in the current. With increasing the number of harmonics generating devices in a power system network, the problem of their impact on the performance of system components like induction motors needs is becoming a serious problem that need further consideration. It is well known that approximately 60–70% of loads in all over the world are motor loads. Most of the motors used in the world are three-phase induction motors. However, single-phase induction motors are major load in a domestic or residential setup. The modern day home uses large number of house hold appliances that uses different kind of single-phase motors as given in Table 1. A power network is shown for a domestic house in Fig. 1. Mix of loads are connected across the line. The effects of increasing non-linear loads in residential setting can be significant especially on single-phase motors connected to the same line. This paper investigate the effect of increasing distortion in the supplied voltage on the performance of single-phase induction motor behavior. Firstly the effect of increasing distortion in the applied voltage waveform on stator current is investigated. It is found that increasing a small %age of 3rd harmonic in the applied stator voltage significantly increases the 3rd harmonic component in the stator current. When voltage is pure sine wave, the current contains 1.7% 3rd harmonic. When the stator voltage is injected with 2.5% of 3rd harmonic the resulting current contain 11% 3rd harmonic. Hence it is concluded that current harmonic content is strongly dependent on the harmonic content in the stator voltage waveform. A Matlab/Simulink model is developed with single-phase capacitor start machine. The procedure adopted is as follows:
• Pure sine wave is applied to a capacitor start single-phase induction motor.
• Distorted supply is produced from inverter using appropriate PWM scheme and supplied to a capacitor start single-phase induction motor Non-linear loads such as CFLs and LEDs are emulated using thyristor based converter.
The thyristors are switched at different firing angle in order to vary the harmonic content in the supply voltage. The behavior of single-phase induction motor under distorted voltage conditionis recorded. The setup shown in Fig. 2 is consist of a single phase capacitor start induction motor supplied with PWM Converter. The motor is rated for 110V rms, 1500 rpm and 0.5 HP. The reference of the converter is generated by adding 3rd and 5th harmonic component to the fundamental component. The loads are switched in this order: Fig. 2. Single-phase induction machine (capacitor start) setup. a) At t = 0, the controlled rectifier with thyristor switching at 30° is turned on. This rectifier will always be on. The current drawn from the supply is analyzed for harmonic components. Each harmonic component contribution becomes input for reference generation for PWM Inverter. b) At t = 2 Sec, the controlled rectifier with thyristor switching at 60° is turned on. Now we have two controlled rectifier connected to the same ac supply. The resultant current is analyzed for harmonic component contribution. c) At t = 4 Sec, the controlled rectifier with thyristor switching at 90° is turned on. d) At t = 6 Sec, the controlled rectifier with thyristor switching at 120° is turned on. Efficiency estimation, a) The output of the system is calculated by multiplying load torque with the motor speed (in rad/sec). b) The input of the system is calculated by extracting P, Q, S from the bridge output voltage and current drawn by the motor from the block as shown below in Fig. 3. Efficiency computation of a single-phase capacitor start machine. c) Fundamental frequency, 3rd harmonic and 5th harmonic power is estimated by using the above block. The resultant power is calculated as: d) With the resultant absolute power drawn from the system, efficiency is calculated as: The simulation results are presented in Fig. 4–6. Ripple is seen in the current, torque and speed when voltage is distorted. The FFT of stator current (main winding) is shown in Fig. 7. Strong 3rd harmonic current is seen and also 5th harmonics.Sinusoidal Supply: Fig. 4. Single-phase IM behavior when pure sine wave is applied. Supply from a single-phase Inverter with Fundamental frequency (50 Hz) only: Fig. 5. Single-phase IM behavior when supplied from a DC/AC inverter. Supply from a single-phase Inverter with Fundamental, third and fifth harmonic: Fig. 6. Single-phase IM behavior when supplied from a DC/AC inverter with distorted waveform Fig. 7. Harmonic spectrum of stator current under distorted voltage source. Different powers are measured and shown in Fig. 8 for pure sine-wave supply and distorted voltage supply to a single-phase capacitor start induction machine. It is observed that the requirement of active, reactive and apparent power increases and efficiency decreases with the increase in the voltage distortion.
Acknowledgment
This publication was made possible by UREP grant # [17-061-2-017] from the Qatar National Research Fund (a member of Qatar Foundation). The statements made herein are solely the responsibility of the authors.
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[5] A.M. Eltamaly, “Power quality considerations of heavy loads of CFL on distribution system” IEEE Int. Symposium on Industrial Electronics (ISIE), pp. 1632–1638, 2011.
[6] Kesharvani, S.K.; Singh, A.; Badoni, M., “Conductance based fryze algorithm for improving power quality for non-linear loads,” in Signal Propagation and Computer Technology (ICSPCT), 2014 International Conference on, vol., no., pp. 703–708, 12–13 July 2014.
[7] Pattnaik, M.; Kastha, D., “Power quality improvement in a speed sensorless stand-alone DFIG feeding general unbalanced non-linear loads,” in Renewable Power Generation Conference (RPG 2014), 3rd, vol., no., pp.1–6, 24–25 Sept. 2014.
[8] Sharma, R.; Singh, A.; Jha, A.N., “Performance evaluation of tuned PI controller for power quality enhancement for linear and non linear loads,” in Recent Advances and Innovations in Engineering (ICRAIE), 2014, vol., no., pp. 1–6, 9–11 May 2014.
[9] Singh, A.; Baredar, P., “Power quality analysis of shunt active power filter based on renewable energy source,” in Advances in Engineering and Technology Research (ICAETR), 2014 International Conference on, vol., no., pp. 1–5, 1–2 Aug. 2014.
[10] Priyadharshini, K.M.; Srinivasan, S.; Srinivasan, C., “Power quality disturbance detection and islanding in micro grid connected distributed generation,” in Computational Intelligence and Computing Research (ICCIC), 2014 IEEE International Conference on, vol., no., pp. 1–6, 18–20 Dec. 2014.
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[12] Ejlali, A.; Arab Khaburi, D., “Power quality improvement using non linear-load compensation capability of variable speed DFIG based on DPC-SVM method,” in Power Electronics, Drive Systems and Technologies Conference (PEDSTC), 2014 5th, vol., no., pp. 280–284, 5– Feb. 2014.
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Investigating the Effect of High Pressures and Temperatures on Corrosion Inhibition for Water-Based Muds
Authors: Abdul Salam M. Abd, Abdulrahman Al-Hardan, Alireza Roustazadeh and Mahmood AmaniCorrosion is defined as gradual degradation of metal caused by a chemical or electrochemical reaction with its environment. In oil and gas sector, components can corrode at any stage in the life of a field starting from drilling through to abandonment. Recent estimations showed that corrosion costs the oil industry in US yearly around $170 billion. In general, 50% of the operating expenditures in the drilling sector worldwide are for taming corrosion in drill pipe and down-hole equipment. On the other hand, “a corrosion inhibitor is a substance when added in a small concentration to an environment reduces the corrosion rate of a metal exposed to that environment. Inhibitors often play an important role in the oil extraction and processing industries where they have always been considered to be the first line of defense against corrosion” (SLB Glossary). Since corrosion process in mostly due to chemical reaction on the surface of the metal under HPHT condition, water-based mud properties used are hence greatly affected. Mitigating corrosion is a very serious challenge for oil and gas industry as it can't be totally eliminated. Because it is almost impossible to prevent corrosion, it is becoming more apparent that controlling the corrosion rate may be the most economical solution. Thus, the first step to tackle this problem is by determining the cause of the corrosion itself. This is vital as it helps understand the mechanism and the process behind corrosion to suggest more practical and helpful solutions. The corrosion has to have 4 main elements to happen: anode, cathode, electrolyte (Fluid) and external connection. In case any of these elements is absent, corrosion will not take place. In our research, Water based mud is the electrolyte of interest. In general, water helps in speeding the corrosion of metal where the steel itself serves as the external connection. The rate of corrosion depends purely on the grade of the metal and the generated potential due the dry cell effect. Oxygen (O2) which plays an important role in corrosion is only present at the drilling stage and not in the producing formations. Water and Carbon dioxide (CO2) injected at recovery operation can cause severe corrosion of completion string. Also, the presence of hydrogen sulfide (H2S) gases at HPHT has a major role in the dynamics of corrosion. Thus, finding the effect of those elements (O2, CO2 and H2S) in the corrosion process is the main focus of our research. First, the most common element that interfere in the corrosion process is the dissolved oxygen. The reaction of the iron to the oxygen contained in water will form iron rust. The equation below shows the reaction governing the process: 2 Fe+++ ½ O2 + H2O = 2 Fe++++ 2 OH− . The formed rust is called ferric hydroxide which is characterized as insoluble. While drilling, we will have infinite oxygen as it is an open system operation, thus the corrosion will not cease. The corrosion rate is usually higher when the concentration of oxygen is low thus leading to rust that is impermeable to O2 diffusion compared to that at high O2 concentrations. Second, the presence of dissolved CO2 in water causes the steel to corrode where the rate of corrosion depends mainly on the quantity of CO2 and O2 present as well as temperature and composition of the material. This reaction is weaker than that induced by the presence of O2 for equal quantities. In CO2 based corrosion, carbon dioxide reacts with water to form bicarbonate. The following equation governs the reaction: 2CO2 + 2H2O + 2e- = 2HCO-3 + H2. This equation indicates that the CO2, upon dissolving in water, acts like an acid. Thus, if we have dissolved CO2 and O2 combined in water, stronger corrosion rates will be observed. Third, dissolved H2S can be corrosive if dampness is present. The fact that H2S is highly soluble in water creates a weak dibasic acid, which causes the degradation of iron because of the presence of oxygen. The reaction will be as follows: H2S + ½ O2 = H2O + S. The rate of corrosion is controlled by the concentration of the dissolved gas. If the dissolved H2S is present in low quantities the corrosion will be severe. However, if the concentration of the dissolved H2S is very, it might have reverse effect where it will act to inhibit the corrosion reaction. When both CO2 and H2S are present, while having direct contact with O2, there will sever localized corrosion damage causing the material to crack and fail (Bonis 2014) To go further with the influence of external factors on corrosion rate, we should consider the temperature of the medium. We should not only consider the fact that the reaction rate will increase simultaneously with temperature, but we should account for solubility and viscosity. The solubility of gases in water will decrease with temperature increase as well as the viscosity. However, this is scenario is not true in all cases. For example, when dissolved oxygen is present, the corrosion rate will increase with temperature till a critical point then it will start decreasing with oxygen solubility. If the system is open, the oxygen will escape. Otherwise, the oxygen will be trapped causing the rate of corrosion to increase at high temperatures. Nowadays, the urge to drill deeper to recover larger amounts of hydrocarbons exposes the drillers to High pressure/High Temperature (HPHT) zones. Wells with temperatures greater than 300F and pressures of 1000 psig are classified as HPHT wells. (Bronlee 2005). Moreover, using water based muds (WBM's) will increase the likelihood of a severe corrosion to happen under HPHT conditions. This research is vital to the oil industry as it discusses a problem that has been ongoing for a long time. Corrosion is causing the oil companies a tremendous economic loss. In some cases, and in order to continue the drilling process, the tubing should be changed completely. There have been a lot of experiments on how to mitigate corrosion; however the success rates are still low. Corrosion cannot be inhibited completely; however the aim is to control it. Adding special additives to the drilling fluid or coating the tube with certain chemical are some ways to stop corrosion. The aim of this research is to subject various metal samples of different grades to stress and strain similar to those caused by severe HPHT condition downhole, and compare the results of two main categories: treated samples and untreated samples. The metals are expected to handle more stress when treatment is applied, proving the efficiency of the corrosion inhibitors compare to untreated samples. The challenge is to be able to manufacture an inhibitive chemical that can provide long term resistance as well as durable adherence on the steel. In the laboratory, a drilling water based fluid was prepared using mainly Drill water, Barite and Bentonite. Other additives such as NaCl, Flowzan, Soda Ash and Fine CaCO3 were used as well. Also, different corroding solutions with varying composition were prepared and stored in plastic vessels. The vessels were divided mainly into categories of mediums based on temperate: ambient and HPHT. The samples were prepared specific for each medium. 15 corrosion rings were cut into 4 pieces in Texas A&M University – Qatar machine shop. The initial weight of each sample was measured using a high accuracy electronic balance. The purpose of the Initial weights is to determine the loss after all exposure and treatment operation. This will also help us understand how the condition of each set-up affects the corrosion rate. One sample (1/4 of a corrosion ring) was immersed in each of the two mediums. The variation between the different samples was mainly the size of the corrosion ring, the type of inhibitor used and its concentration. Each sample of mud will contain each size of corrosion ring to determine corrosion accumulation and inhibition based on the size and type of corrosion ring. After approximately 100 hours of exposure, all corrosion rings will undergo the same procedures of inspection for the evaluation of the results. The weight of each sample was recorded before being immersed in the corrosion mediums and after their removal and cleaning From the weight data collected, the corrosion rates was estimated. The initial results showed that when only water based mud is presented without any type of inhibition, the corrosion rate is severe in HPHT medium (4.1 lbs/ft2-year) compared to ambient temperature conditions (2.2 lbs/ft2-year). Moreover, the corrosion rate is less whenever we have a thicker pipe. When adding inhibitor Concor 404 to our media, we see that the corrosion rate diminishes significantly at HPHT for the all corrosion ring sizes compared to base fluid media. On the other hand, using another inhibitor OS1-L will mitigate the corrosion effect in HPHT temperatures to around 1.3 lbs/ft2-year for corrosion ring of size 5.5”. This value is almost triple the rate that we got when using Concor 404. Hence, we deduce that Concor 404 is more effective than OS1-L while using water based mud. In the last batch of samples, Concor 404 and OS1-L were applied together to compare there raltive effect to each other. The inhibition effectiveness was still high under HPHT (around 1.1 lbs/ft2-year) but less than Concor 404 alone and more than OS1-L. It can be deduced that the presence of OS1-L is inhibiting the Concor 404 to perform in full capacity thus lowering the mitigation effectiveness. In general, all three inhibitors with their different combinations work efficiently in mitigating the corrosion. The final decision on whether to choose this inhibitor or the other should be merely based on a thorough economical analysis that includes your needs and takes into consideration your requirements.
Acknowledgement
“This report was made possible by a UREP award [UREP 17 – 133 – 2 - 034] from the Qatar National Research Fund (a member of The Qatar Foundation). The statements made herein are solely the responsibility of the author.”
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Experimental Investigation of Permeability and Fluid Loss Properties of Water Based Mud Under High Pressure-High Temperature Conditions
Authors: Ahmad Amra, Mahmood Amani, Rommel Yrac, Dawod Hjeij, Ahmed Abdelrauf and Jana MahfouzDrilling in deeper formations and in high pressure and high temperature (HPHT) environments is a new frontier for the oil industry. Fifty years ago, no one would have imagined drilling in more than 10,000 feet of water depth like we do today. However, more issues need to be researched, tested, and studied in order to maintain a good drilling efficiency as deeper depths are drilled. One of these issues is the great effect that drilling at HPHT conditions has on the behavior of drilling fluids. The goal of this research was to study fluid loss properties of water based mud and its effect on permeability under HPHT dynamic conditions utilizing advanced laboratory equipment that allows for wide ranges of pressure and temperature. Filtration tests were performed at both ambient and HPHT conditions. After several laboratory evaluations of fluid loss additives available in the market, Polysal HT was found to be the most effective in reducing the fluid loss of the water based mud for both static and dynamic tests at HPHT conditions. It is economically designed to be saturated in salt and other brine system. An additive that encapsulates particles with protective polymer coating as colloid. Drilling fluid stabilizer especially in drilling hydratable shale and a remarkable effectiveness in wide range make up water (high saline and high hardness). The fluid loss behavior of the mud and the characteristics of the filter cake produce dare the basic factors that need to be considered when determining mud treatment. A detailed workflow of experiments using equipment from OFITE HPHT Fluid Apparatus with differential pressure of 500 psi under 230 °F with 2.5” filter paper (30 minutes) as well as OFITE Permeable Plugging Tester with 1,200 psi differential pressure @ 230 °F using a ceramic disc were conducted. Also tests were conducted using the Low Temperature- Low Pressure API Filter Press at 100 psi @77 °F with 3.5” filter paper for the purpose of comparison. Drilling fluid behavior should be studied and researched in order to get better drilling efficiency and less fluid losses. This topic has been for years the subject of research and many laboratory studies. Most of these studies focused on the methods and parameters involved in the study of drilling fluid characteristics. Mud can act unexpectedly under HPHT conditions and testing its properties at these conditions produces results that differ from those obtained from testing under static conditions. Drilling fluids' interaction with the spacer fluid is also critical. Krueger found out that the API filter loss tests (standard and high pressure) shouldn't be considered accurate when testing for the losses in mud that has viscosity reducers under dynamic conditions. He also studied the quantities of dynamic fluid loss in water based muds when adding substances to the drilling fluid such as CMC, starch, polyacrylate, and viscosity reducers. He found that–in dynamic system-starch and viscosity reducers were the most useful additives. However, when using API fluid test, the results deduced that CMC, starch and polyacrylate were the most beneficial additives. So he deduced that industry was paying so much on the API filter loss test (standard or at high temperature high pressure) expecting it to be accurate, instead of focusing on the dynamic filtration tests (at HPHT) whose results were more accurate since their conditions were very similar to the reservoir conditions. This is an experimental study of the impact of having HPHT reservoirs on the drilling fluids loss. Three different cases will be studied at different conditions. An API Filtration and fluid loss equipment will be used in order to test the mud capacity to withhold its filtrates under the HTHP as well as from static to dynamic condition. Experiment #1 consist of low pressure, low temperature conditions. The second one is at HTHP using static model. Finally, the last experiment will also be at HTHP conditions but using a dynamic model. Fluid loss models (beyond the conventional such as viscosity, gel strength, yield point and so forth) will then be compiled. The Polysal HT, a modified starch that serve as the fluid loss control additive along with Bentonite and Polypac UL will generally do the job. Roodhart stated that the commonly used 30 minutes API filtration test was inadequate especially in dynamic conditions. Also, he concluded that the range for fluid data testing (1,000 psi [7-MPa] differential) was lacking and deficient. Shadravan and Amani investigated the HPHT challenges in drilling and completions. Lee et al. researched the rheological properties of an extreme HPHT drilling fluids. Amani et al. compared the rheological properties of oil based and water based drilling fluids under HPHT conditions. Shadravan et al. looked at the possibility of fluid loss in underbalanced situations. Bland et al. mentioned that there were many parameters that need to be taken into consideration while designing and monitoring drilling fluids for HPHT conditions. These parameters included pressure and temperature effects on hydraulic calculations (while drilling under HPHT conditions at large depths, mud is subjected to high pressures and temperatures for long period of time) and PVT behavior of the base fluid (where the usual conditions considered by industry in fluid PVT measurements ranged from 15 psi per 750 °F to 20,000 psi/350 °F, but this range was exceeded while drilling under HPHT conditions). In addition, drilling efficiency was affected greatly by HPHT conditions where the use of additives like barite to increase the mud weight for such conditions caused lower drilling efficiency where the percentage of dispersed solids increased. This has many disadvantages (like decreasing hydraulic and cutting efficiency) during drilling high compressive formations under HPHT conditions. Elkatatny and Nasr-El-Din studied the formation of filter cake under static and dynamic conditions. They deduced that the same filtrate quantity was formed during dynamic and static conditions. However, dynamic conditions' spurt volume exceeded that under static conditions and when the filtration process reached an end, the part of the filtrate near to the drilling fluid had zero porosity and permeability. Further results by the CT scan proved that ceramic disk properties (like permeability and porosity) varied significantly during filtration and this should be taken into account during filter cake calculation. Properties of water based drilling fluids under HPHT dynamic testing conditions that can be measured include spurt loss, quality of plugging, total fluid loss, and cake formation thickness. Crespo et al. looked at some fluid loss related problems such as formation fracture, lost circulation, and well-control problems as a result of surge and swab pressures for yield-power-law drilling fluids. As the results show, permeability is proportional to the flow rate per unit cross sectional area. This can be translated into pore throats in subsurface rock. Therefore, the greater the pore size through which the fluid is going to flow at a constant flow rate, the higher the capacity of the fluid to flow and therefore its permeability. It can be deduced that as the concentration of the Polysal HT increased, less and less filtrate was lost into the formations. Same results were obtained from the low temperature low pressure API test where smaller filtrate volume was obtained as the concentration of the used Polysal HT increased. Thus, water based mud under HTHP conditions undergoes many changes in its main parameters like spurt loss, fluid loss, and filter cake thickness. Fluid loss control additives are therefore required in order to handle these changes and maintain the required properties of the used drilling fluid where Polysal HT was the required additive in this case. Dynamic as well as static API filtration tests should be performed before choosing the best additive. Numerous trials has been set up to test the fluid loss effectivity of the mud used in drilling but a very limited resources targeted the HTHP course due to its collaborative safety and productivity concerns, they call it “Drilling in the Dark” (a time to time check of properties).
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Investigating Recycling Practices in Qatar's Hotel Industry – A Study Focusing on Food Waste Measurement and Reduction
More LessThe year of 2015 is set to be a milestone for sustainability as governments are increasingly called upon to adopt the UN Post-2015 Development Agenda. Tourism has the potential to contribute directly and indirectly to the Sustainable Development Goals. Particularly, Tourism is seen to be able to play a key role in adopting and implementing sustainable use and management of natural resources, through environment-friendly practices and solutions. Hotels and Food and Beverage business (F&B) are one of the most important components of the tourism sector. Large number of visitors and guests visit hotels and F&B businesses, and waste is automatically generated. Qatar's tourism sector is amongst the fastest growing globally, and the number of tourists that Qatar aims to attract by the year 2030 is projected to reach seven million. The growth in the sector equally means a similar (and natural) increase in the waste generated. Handling solid waste has remained one of the main problems that directly affect the environment. Mismanagement of waste endangers the health of populations especially ones residing near landfills. The problem this research identified was the lack of data and information much needed for policy recommendation addressing recycling of different materials including Food Waste in the hotel industry in Qatar. This study was primarily set up to achieve two folded goal. First, it aims at exploring the current practices within the Hotel Industry in Qatar regarding recycling of waste materials including food. Second, it examines the effect of awareness on Food Waste reduction. To achieve these goals, first, a survey questionnaire was designed to gather the information from a number of 111 hotels (including designated hotel-apartments). Second, an experiment was designed to measure the effect of awareness-cards on Food Waste reduction through comparing the findings from the control and the experiment groups. The survey was conducted during the months of June, July and August, 2015, while the Food Waste experiment took place during the month of Ramadan, 2015. Some of the findings related the two research objectives are presented in the following graphs:
The Graph above clearly indicates the average amount of food-waste (FW) generated per guest per day throughout the experiment period of 20 days. The first day of the experiment for the Control Group, i.e. without awareness cards, the average amount of food waste started at 0.6 Kgs per person (i.e. guest), but reduced through the experiment period. For the experiment group when awareness cards were provided on tables the food waste remained very consistent at around 0.2 Kgs per guest. The overall results showed overwhelmingly that awareness, once generated has an immediate, clear and positive influence on customer behaviour, and in this case reduced the average food waste. The experiment measured total food-waste during the 20 days within this restaurant at 1,335 Kgs. Several important points constituted the conclusion and recommendations drawn from the results and analysis of both efforts. The summary highlights the vital importance and need for investments across all aspects of material recycling, which should be encouraged at a government level, and extended to SMEs, to develop local businesses within the recycling sector in Qatar. More efficiency is also required between F&B organisers and charities, and great incentives should be put in place for those participating in recycling efforts, and conversely penalties should be implemented for those organisations not actively pursuing “reduction” strategies to waste. Food cost reduction, without impact on food quality or perceived value, could be conservatively reduced by about 50% through spreading awareness of the impacts of Food Waste on the environment.
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Influence of Sinusoidal Drive Speed Modulation on Rotor with Continuous Stator Contact
Authors: Abdullah Alzibdeh, Mohamed Y. Al-Qaradawi and Balakumar BalachandranTorsional vibrations experienced by drill strings can be detrimental to drilling operations. With a goal of understanding torsional vibrations experienced by drill strings and determining means to attenuate undesired vibrations, the authors have studied the effect of adding a sinusoidal modulation to a constant rotation speed of a drill string. A combination of modeling, analysis, and experiments is used to explore the influence of this rotation input modulation on the system response. The drill string is modeled as a modified Jeffcott rotor, which is described by a system with three degrees of freedom. Considering the case of forward whirling of a rotor in continuous contact with a stator, the equations of motion are reduced to a single degree-of-freedom nonlinear oscillator describing the torsional motions. In order to understand the fast time scale and slow time scale components of the motion, the method of direct partitions of motions is used to determine an approximate response to the nonlinear oscillator. The obtained results of the analysis illustrate that with the sinusoidal modulation of the rotor drive speed, the equivalent torsion stiffness can be enhanced and the character of the friction force at the contact can be made smooth. The analyses helps bring forth the stabilizing influence of the added sinusoidal input to the rotor drive speed. Over the considered parameter ranges, the numerical results obtained with the full three degree-of-freedom model and the reduced single degree-of-freedom model are found to be in agreement with each other. Furthermore, the results from these models are found to compare well with those obtained by using the method of direct partition of motions. Experiments with a laboratory scale drill-string arrangement are to be carried out to validate the analytical and numerical findings and further explore the effectiveness of the drive speed modulation on the rotor dynamics.
Introduction
Slender rotating structures are used in many engineering applications. Drill strings are long rotating slender structures, which are used in drilling operations. A schematic of a rotary drill rig is shown in Fig. 1 (e.g., Liao, Balachandran, Karkoub, and Abdel-Magid, 2011). Drill strings experience different types of vibrations (axial, torsional, and lateral vibrations) that may lead to detrimental failures of a drilling system. Drill-string vibrations have attracted the attention of many researchers, and many models have been developed to understand them. Since drill strings have a large length-to-diameter ratio, typically, the first torsional natural frequency and first lateral natural frequency are close to each other. This frequency proximity and the nature of the system allows for coupling and energy transfer between the associated vibration modes. Here, as a step towards developing further understanding, a drill string is modeled as an extended planar Jeffcott rotor with gravity acting normal to the rotor. Due to the planar motions, no gyroscopic effects are considered. The extended model, which was earlier considered in the work of Vlajic, Liu, Karki, and Balachandran (2014), is shown in Fig. 2. The model is described with three degrees of freedom (DOF), namely, x and y to account for lateral motions, and theta to account for torsional motion. A large number of research efforts have focused on controlling drill-string vibrations by using different feedback control algorithms, which need measurements along the drill string. In this work, the authors propose a different control approach to mitigate whirling motions during continuous rotor-stator contact. This can be compared to a situation of a drill string being in continuous contact with the borehole. The approach is open loop in implementation and this approach is based on adding a high frequency input to the drive speed of the drill string. Given the open-loop nature, the method does not depend on any measurements along the drill string or rotary table, which could be attractive for a practical stand point. Although the current focus is on motions of a rotor with continuous stator contact, it is planned to study stick-slip and non-contact cases in the future.
System Modeling, Studies, and Results
As previously mentioned, the drill string is modelled as a Jeffcott rotor with three DOF. Proceeding along the lines of the group's prior work (Vlajic, Liu, Karki, and Balachandran, 2014), after some approximations for the continuous rotor-stator contact case, the 3 DOF system is reduced to a single second-order nonlinear differential equation governing the torsional motion. In Fig. 3, for a representative case with a constant drive speed, the torsional state histories obtained for the full model and the reduced model are plotted. It is noted that the final state of the motion is captured quite well. To further analyze the response during forward whirling, the reduced-order model was nondimensionalized and an approximate solution was obtained by using the method of direct partitions. This method allows one to separate slow scale motions from fast scale motions. As discussed, in the group's prior work, this method can be useful to examine whirling motions. The results obtained by directly integrating the full model as well as the reduced-order model have been compared with that obtained by using the method of direct partitions of motions. It is seen that the perturbation analyses is able to provide an approximate solution that compares well with the numerical results obtained through direct integrations. Next, this analysis is used to examine the influence of the addition of secondary frequency component. It is seen that the addition of the secondary frequency, a high-frequency one, helps smooth out the friction coefficient variation with respect to the relative speed at contact. This is found to have a beneficial effect on the motion and helps suppress large-amplitude torsional motions. Stability analysis was also conducted to examine this effect.
Concluding Remarks
A study has been conducted to examine the influence of sinusoidal modulation of rotor drive speed in a system, wherein the rotor experiences continuous stator contact. A single degree of-freedom reduced model is developed to study the torsion response and it is found that the addition of a high frequency input can be beneficial in attenuating rotor motions. This is believed to be useful for developing open-loop control schemes for attenuating forward whirling motions of drill strings. Results obtained from a lab scale experimental arrangement will be used to examine the effect of this drive speed modulation further and they will be reported in the conference presentation. Future studies could build on the current effort to examine cases of backward whirling. Acknowledgment: The authors would like to gratefully acknowledge the support received from the Qatar National Research Fund for NPRP Project 7-083-2-041, to pursue this collaborative work between the University of Maryland, College Park, MD, USA and Qatar University, Doha, Qatar.
References
1. Liao, C.-M., Balachandran, B., Karkoub, M., and Abdel-Magid, Y., Drill-String Dynamics: Reduced-Order Models and Experimental Studies, ASME Journal of Vibration and Acoustics, Vol. 133, 2011, pp. 041008-1-041008-8.
2. Vlajic, N., Liu, X., Karki, H., and Balachandran, B., Torsion Oscillations of a Rotor with Continuous Stator Contact, International Journal of Mechanical Sciences, Vol. 83, pp. 65 − 75, 2014.
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Azolla as a Feedstock for Bio-Refinery: Cultivation, Conversion and Application
Azolla is one of the world's fastest growing aquatic macrophytes, with a doubling time of only 2-5 days (Taghi-Ganji et al., 2005). It can be found on the surface of wetlands, ditches, ponds and rivers, native to the tropics, subtropics, and warm temperate regions of Africa, Asia, and the Americas (Costa et al., 2009) (Figure. 1). It has been intensively studied during the last few years for its potential uses as a green manure in rice fields, as a feed supplement for aquatic and terrestrial animals, as a human food, as medicine, as water purifier, as a biofertilizer, control of weeds and mosquitoes, to eradicate different metals, or to remove nitrogenous compounds from the water and the reduction of ammonia volatilization which accompanies the application of chemical nitrogen fertilizer. (Gregory, et al., 1997; Lumpkin, et al., 1980; Sadeghi, et al., 2013). Several other studies have also verified Azolla's potential as a biogas and hydrogen fuel source (Peters, 1976; Newton 1976, Van Hove, 1989).
These beneficial uses urged researchers to call it “green gold mine”. Seven extant Azolla species (A. filiculoides, A. caroliniana, A. mexicana, A. pinnata, A. nilotica, A. microphylla, A. rubra) are reported) Armstrong, 1998). Among the Azolla species, A. filiculoides is the only fern which is found in Anzali wetland, northern Iran (Sadeghi et al., 2012a, b; Sadeghi et al., 2013). A. Filiculoides also grows in southern South America, and western North America to Alaska. Also, it is on the US noxious weed list. Azolla has already covered about 50 percent of the 20,000 hectare Anzali wetlands. The overgrowth of Azolla is now considered as a serious issue in this unique ecosystem. Now, this useful plant is a harmful weed in water because it forms dense surface mats, interfering with boating, fishing, blocking irrigation channels and waterways and recreational activities as well as degrading water quality by reducing oxygen levels. It has been an increasing effort to maximize the beneficial properties and find new applications for that. So, Thermochemical conversion was applied on this biomass. Thermochemical processes depend on the relationship between heat and chemical action as a means of extracting and creating products and energy. Pyrolysis, gasification, and liquefaction which is conducted at a temperature of several hundred degrees Celsius are categorized in thermochemical processes. Currently, there are two principal processes for bio-oil production from biomass: pyrolysis and hydrothermal liquefaction (HTL). Besides biocrude oil as a liquid fuel, a special type of biochar which can be considered as an attractive byproduct was produced in HTL process. This carbonaceous material, which has received less attention can be potentially used for the removal of heavy metals contamination from wastewater (Liua, et al., 2009). The Cu at higher concentrations is a potentially toxic metal in the environment, mainly as the soluble form Cu2+. Obtained biochar from HTL of Azolla was used for Cu removal. The major concern in (HTL) is the high temperature and consequently high pressure of the process which results in high capital cost of equipment. So the process pressure and temperature should be reduced, but at a lower temperature, bio-oil yield is not high enough to make HTL economical for sustainable fuel production. For this purpose, ethanol was used as a solvent instead of water. Also, lipid extraction from Azolla was studied with Soxhlet extraction; because of its simplicity in operation, potential for scale up and safety. As our knowledge, to date, no study has reported an evaluation of the Azolla bio-refinery and also thermochemical conversion of Azolla for producing advanced fuel. This research was conducted in two parts: 1) cultivation and 2) conversion. The purpose of cultivation was to find the optimum requirements to reach the highest growth rate of Azolla under laboratory conditions. The results will help us to manage growing of this aquatic fern and also conserve wetland. This study showed, Humidity and pH are the most significant variables for achieving maximum Azolla growth rate. In conversion part; an all-out attempt was made to maximize the beneficial properties of the Azolla-Anabaena association and to find its new applications. After cultivation and harvesting of Azolla, this biomass was investigated as a feedstock for thermochemical conversion process. Lipid extraction, hydrothermal treatment, hydrothermal liquefaction and pyrolysis process were scrutinized aimed at utilizing Azolla as a biodiesel, liquid fertilizer, biocrude oil, biochar. Also, after these processes, liquid and solid residual were separated and analyzed for future utilization as liquid fertilizer and absorbent for heavy metal removal, respectively. This harmful weed with its fast growth rate and high potential products can be quite useful plant and can be fed into biorefinaries so that its removal will also conserve wetland. An all-out attempt has been made to maximize the beneficial properties of Azolla and find new applications for it. Reaching the highest growth rate under laboratory conditions will be conducive for managing this fast growing fern. Humidity and pH are the most significant variables for achieving a maximum Azolla growth rate. The dry mass growth rate of Azolla was. The maximum growing rate was achieved at; temperature: 22 °C, light = 20 Lux, humidity: 75% and pH = 6.4 with 2.1 days considered as doubling time. Lipid extraction, hydrothermal treatment, hydrothermal liquefaction and pyrolysis process were exerted upon Azolla for producing biodiesel, liquid fertilizer, biocrude oil, and biochar. Hydrous harvested Azolla converted to bio-crude oil at hydrothermal condition and Heat value increased from − 0.86 to 31.0 MJ/kg (yield = 39%). Bio-crude oil derived from pyrolysis had yields 29% with HHV = 33.2 MJ/kg. Pre-treatment at 180 °C before hydrothermal liquefaction at 300 °C was produced highest bio oil quality. Lipid content in Azolla was about 11.7%, which includes 38.07%, 39.49% and 19.81% saturated, monounsaturated and polyunsaturated fatty acids, respectively. The nitrogen rich liquid was produced at hydrothermal treatment. This harmful weed of overgrowth rate can be fed into biorefinaries so that its removal will also conserve wetlands.
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Advanced Multiphase CFD Modelling to Understand Impact of Undersea Oil Spill
Authors: Krishnaswamy Nandakumar, Abhijit Rao and Kalliat T. ValsarajThe growing energy demand across the globe has resulted in an increase in the deep water oil exploration activities which in turn has increased the risk of occurrence of associated accidental oil releases. Oil and Gas offshore businesses are important to Qatar's economy. Further, the country is heavily dependent on its marine water resources for fulfilling its potable water needs through the desalination process. So, it is imperative to safeguard the marine environment during an unfavorable accidental oil release, which essentially would put entire ecosystem into peril. Development of reliable models can assist in predicting the extent of damage caused to the environment and can further help in deciding the mitigating strategies during such events. The current research focusses on exploring the of capabilities of Multiphase Computational Fluid Dynamics (CFD) models in simulating various transport processes associated with deep water oil spills. The accidental release of oil in deep oceans results in formation of the plume. The interaction of inertial oil mass with surrounding water results in the formation of droplets which rises in the water column due to buoyancy. Dispersant addition is one of the preferred methods of oil spill remediation which causes the lowering of interfacial tension at the oil/water interface and under the action of local turbulence, it enhances the droplet disintegration process. In deep spill scenarios, droplets spend large amounts of time in the water column, hence, the dissolution process of soluble hydrocarbons which otherwise is detrimental to aquatic life, becomes important. The objective of this work is to develop integrated numerical models which can effectively guide us in predicting the fate of oil mass in such scenarios and help us is estimating the overall impact of such accidents on the environment. Before taking a leap into full scale modelling, it is imperative to grasp a good understanding of above mentioned transport processes at a more fundamental scale. Hence, in the first phase of this project, single droplet dynamics in quiescent systems were studied. We primarily investigated the effect of surfactant (the chief component of a dispersant), on the dynamics of a crude oil droplet rising in a stagnant column. Laboratory scale experiments were performed and a multiphase CFD model based on Volume of fluid method was developed to capture the shape dynamics of the droplet rising in a surfactant laden environment. To capture the subsurface dissolution of hydrocarbons from oil droplet, a unique experiment was devised wherein a binary organic mixture, representing a pseudo oil droplet comprising of volatile and non-volatile hydrocarbons, was employed to study the effect of unsteady mass transport on the overall dynamics of the droplet. Based on the experimental observations, correlations were proposed to estimate the mass transfer rate at various stages of droplet motion. A CFD model capable of evaluating concentration fields of the transported species in both dispersed as well as continuous phases, was developed by coupling VOF approach with species transport model. The above models were also employed to study the jet breakup dynamics in the laminar regime. The next challenge was to extend the applicability of developed models to large scale scenarios. Turbulence is inherent to oceanic environment and hence incorporating it into existing models becomes important. In a real deep spill scenario, a swarm of bubbles and droplets often interact with each other in a turbulent environment and this leads to occurrence of a sequence of coalescence and disintegration processes. The information on size of droplets serves as an important parameter for the evaluation of approximate rise velocities and overall mass transfer rates in the system. Thus, a model capable of predicting droplet size distribution can be employed for determining the fate of droplets in the event of accidental subsea releases. In current work, this objective was achieved by integrating traditional multiphase CFD models and turbulence models, with a population balance (PB) approach. The developed model was validated against the experimental observations reported in Johansen et al (Marine Pollution Bulletin. 2013;73(1), 327–335). Through this work, we were able to demonstrate the capability of an integrated CFD+PB model in analyzing the effect of dispersed (oil) phase flow rates, the presence of dispersants and the presence of air (introduced along with the dispersed phase) on the overall size distribution of oil droplets.
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Tremendous Change in Economy of Qatar Through Economics‘s Tools
More LessAs about Qatar well known country among Gulf countries, depends on a single commodity of resources or we can say rentire state which is totally depends on natural resources as petrochemicals and gas. In the classical views of economics always use the diminishing law of return in production, which shows if production factor one or two are used in production, this will increase production but in decreasing rate. Which means if factors of production are not using equally, this problem may come in production of anything but other things should same as technology etc but somewhere its work still in life. Qatar has an unemployment problem in youth, which could be solved through Government interference in the policies for example: Qatar and other Gulf States are suffering from lack of economic growth of the country. But to solve these problems, the Government sets up a central planning authority which has been called by several names, such as the planning commission, planning ministry or planning board. What goods should be produces, how should they be produces, how should they be distributed among the population and how much should be invested to bring about economic growth are all decided but the central planning authority. This method of solving central problems through the use of economic planning has been adopted in socialist countries. In such economic system, the capital and property are collectively owned by society and work of production is organized by the government. In this system, private entrepreneurs have no right to undertake the work of production and consumers lose their freedom to choose and consume the goods of their choice. Government plays an active role in the solution of the various central problems, regarding production, distribution and investment. Regarding Qatar, this policy works in international market as consumers of Gas is in world–wide. So the government of Qatar control its Gas production as not demand for and supply of Gas but the price will determine its production (as international market will give the price of Gas) Government of Qatar and of Corse other GCC countries could control its economy through the interference of the Government of the country. As the adaptation of proper monetary policy (in which the policies regarding the supply of money, bank credit and the rate of interest are included), fiscal policy (which is concerned with the government expenditure and taxation policies) and direct controls such as industrial licensing policies, control on price, import and exports. The other economic tool could be used in production of a single commodity as LNG in Qatar. Production possibility Curve in economics explains how much production of gas should be optimum level of production. One of the major issues before the oil-rich Gulf States (Qatar) in recent decades has been the diversification of their economies from the oil to non-oil sectors. Their heavy dependence (from 70 to 90%) on the oil revenues has prompted these countries to formulate the policies so that other sources of income from the non-oil sector can be enhanced. But the question is how in these Gulf States have been successful in implementing these policies? Moreover, what are the major drawbacks in the diversification their economies in the present time? In this paper, an attempt has been made to understand the rationale behind the diversification of Arab Gulf economies dominated any single rent revenues. This has been discussed in the framework of their overall macro-economic development, taking into consideration the various factors of productions, so that a desired balanced growth can be maintained. The main focus of the paper is on the current initiatives taken these States towards the building of a non-oil economy. While highlighting the Arab Gulf State's economic diversification drive, the paper, particularly point out the varying degrees of seriousness and success because as this paper concludes, this economic diversification project cannot be conceived without taking into account the impact of fluctuation in oil prices in the global market as well as on the overall economic and political stability in the region.
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Enhanced Energy Extraction from a Solar Panel
Authors: Shahbaz Tabish, Atif Iqbal, Imtiaz Ashraf and Khaliqur RahmanDue the movement of the sun throughout the day, the insolation level incident on the fixed panel surface varies largely. The maximum level of insolation occurs only around noon. This leads to the panel to be under-utilised. To maximise the utilisation of the panel during the day, mechanical solar tracking is used. This method not only increases the utilisation of the, but increases the power being extracted from the panel. Solar tracking using one axis tracking increases the energy yield from the solar panel by 40 percent.
Extended Abstract
During the span of a day the sun's movement has been shown in figure 1. As the day passes by, the level of incident solar radiation (insolation) changes. This change takes place due to position of the sun. The angle at which the sun's rays fall on the photovoltaic panel affects the insolation level available for the panel to convert into electrical energy. For the fixed panel, the sun's rays are not normal to plane of the panel most of the time. This causes the panel to be under-utilised. To extract more energy from the same panel, solar tracking is required. This follows the sun's movement thereby increasing the insolation level throughout the day. This increase in the insolation level is due to the fact that the angle between the normal to the solar panel and incident light is to be kept minimum.
Figure 1: Sun's movement throughout the day
The principle of a single axis solar tracking has been shown in figure 2. The solar tracking can be accomplished by four methods: active tracking, passive tracking, chronological tracking and manual tracking [1]. Active trackers measure the light intensity from the sun using light sensors which give signal to the controller and driving mechanism. Passive trackers commonly make use of a low boiling point compressed gas. This gas is filled in two canisters each placed in east and west directions. The heating of the fluids cause the panel to tilt over to the side with more sunshine. These will have viscous dampers to prevent excessive motion in response to wind gusts [2]. A chronological tracker uses a rotation mechanism to counteract the effect of Earth's rotation. A simple rotation mechanism, turning at a constant speed of one revolution per day or 15 degrees per hour, is adequate for many purposes, such as keeping a photovoltaic panel pointing within a few degrees of the Sun. This can easily be achieved by the use of a stepper motor control.
Figure 2: Principle of single axis solar tracking
The data for the insolation level and temperature for the whole year have been obtained from the NASA website for Aligarh and Doha [3]. The simulations have been run assuming that there is no condition of partial shading. For the purpose of simulation of energy output during the day, five solar panels of 250 Wp were taken in parallel to give a total of 1.25 kWp of power under STC. The energy outputs for the months throughout the year were obtained for two conditions: first for the fixed panel condition, and second for the panel with continuous one-axis solar tracking. The results have been compared and shown for Aligarh and Doha in Figs. 3 and 4 respectively. In Fig. 5, the percentage increase in the energy output for each month has been shown for both the cities.
Figure 3: Daily energy yield from a 1.25 kWp solar array on a monthly basis in Aligarh
Figure 4: Daily energy yield from a 1.25 kWp solar array on a monthly basis in Doha
Figure 5: Increase in daily energy yield on a monthly basis
References
[1] B H Khan ‘Non-Conventional Energy Resources’ Tata McGraw Hill, 2009.
[2] Kamala J. and Alex J., 2014, ‘Solar Tracking for Maximum and Economic Energy Harvesting’, Int. J. of Engg. and Tech, Vol. 5(6), pp 5030–5037.
[3] NASA Surface meteorology and Solar Energy website: https://eosweb.larc.nasa.gov
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Isolation and Identification of Potentially Pathogenic Vibrio Species from Qatari Coastal Seawaters
The genus Vibrio accounts for a major group of marine and estuarine bacteria capable of causing diseases in various aquatic organisms including fishes, corals, shellfish's and shrimps. Infections with these organisms have profound environmental and economic consequences. In the present study, 52 isolates of Vibrio species were isolated from the water samples collected from 14 sites surrounding Qatar during the winter season. Using 16S rRNA gene sequence analysis and MALDI-TOF MS we identified 13 different luminous and non-luminous Vibrio species. V. alginolyticus (50%) was the predominant species followed by V. harveyi (11%), V. owensii (7%), V. nigripulchritudo (6%), V. rotiferianus (6%), V. mediterranei (6%), V. hepatarius (2%), V. shilonii (2%), V. maritimus (2%), V. coralliilyticus (2%), V. tubiashii (2%), V. parahaemolyticus (2%), and V. proteolyticus (2%). We were able to identify all (100%) isolates using 16S rRNA, (>94 percentage similarity) as compared to MALDI TOF-MS which could correctly identify only 60% isolates. Majority (70%) of the potentially pathogenic Vibrio's isolates of Vibrio's were recovered from the fishing ports of Qatar namely Al-Khor and Al-Wakra. The isolation of various pathogenic species of Vibrio's from the Qatari marine environment indicates the potential sanitary risk and stresses the need for further studies to prevent infections.
Acknowledgments:
This research was supported by the research grant (Grant NPRP 6-647-1-127) from the Qatar National Research Fund (a member of Qatar Foundation) to R. Fotedar (Ministry of Environment, Qatar), Thorsten Stoeck (L, Germany), Teun Boekhout (CBS- KNAW, The Netherlands) and Jack Fell (RSMAS,USA).
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Performance Analysis of Multiphase High Power Open End Drives Fed from Dual Matrix Converter
Authors: Khaliqur Rahman, Atif Iqbal, Nasir Al-Emadi and Rashid Al-AmmariIn this paper an open ended seven phase stator winding drive is considered for analysis that is to be fed from matrix converter controlled by space vector pulse width modulation scheme. Open-end winding variable speed drives with dual matrix converter supply have been extensively investigated for various applications in the past, based on a three-phase machine configuration. This topology is relatively simple for practical realization. It offers a higher number of switching states without the need for capacitor voltage balancing algorithms, when compared to the equivalent standard multi-level converter in single sided supply mode. This paper considers a seven-phase open-end winding topology. A relatively simple SVM algorithm, based on already developed seven-phase two level drive SVM method, is used for operation of both converters. The proposed modulation technique is straight forward to implement and is capable of generating pure sinusoidal output voltages, without any low-order harmonic components. The method offers superior harmonic performance when compared to seven-phase topology in single-sided supply mode. The developed scheme is verified by simulation, using a seven phase induction machine operated under V/f control. The proposed drive topology find application in high power ac drives such as in oil & gas industries, electric/hybrid electric vehicles, ship propulsion, traction etc. The simulation results support the proposed idea.
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Modeling Development of a Combined Methane Fixed Bed Reactor Reformer
The growing concern of many countries globally about the greenhouse gas emissions have emphasized interest towards dry reforming of methane (DRM). For an oil and gas based economy such as the state of Qatar, CO2 emission is a big challenge, as it has rendered Qatar as the highest CO2 emitting country per capita in the world. The potential of DRM process for integration in the existing infrastructure of Qatar is a key aspect of this research as a part of exceptional proposal granted to Dr. Nimir Elbashir by QNRF aimed at CO2 fixation. DRM is a heterogeneous chemical reaction in which the two greenhouse gases; CH4 and CO2 are converted to synthesis gas. Synthesis gas or ‘syngas’ is a precursor to a large variety of value added chemicals including hydrocarbons via Fischer-Tropsch Synthesis (FTS). In addition to CO2, steam can also be used to reform methane into syngas in a process known as steam reforming of methane (SRM). Steam Reforming of Methane (SRM) ΔH298 = 206 kJ/mol (1) Dry Reforming of Methane (DRM) ΔH298 = 247 kJ/mol (2) In addition to these two processes, there is also an exothermic reforming process, known as the partial oxidation of methane (POX), where methane is combusted to yield syngas. DRM process is beset by numerous major process limitations including its high endothermicity, high rate of catalyst deactivation (due to carbon formation) and low-quality syngas yield ratio (H2:CO⇐1:1). These challenges have posed severe obstruction towards widespread commercialization of this technique. A synergistic amalgamation of the reforming of methane as DRM+SRM, DRM+POX and DRM+SRM+POX have been recommended in the literature as a way to tackle the intrinsic limitations of the DRM process. In the current work, such combinations of methane reforming processes have been simulated thermodynamically using direct Gibbs free energy (GFE) minimization method. Energy valuations of various case scenarios have been carried out under varying operating conditions (temperature, presssure and feed mole ratios) assuming both ideal gas conditions and non ideal regimes using cubic equations of state (Peng Robinson (PR), Redlich Kwong (RK) and Soave Redlich Kwong). The main objective of the thermodynamics aspect of this study is to find optimized condition of reduced energy requirement and reduced carbon deposition while maintaining considerable CO2 fixation in a combined reforming process. In order to completely understand the system, a one-dimensional pseudo-homogeneous fixed bed reactor model which incorporates all the transport limitations (heat, mass and momentum) for combined SRM/DRM processes is developed. Reaction kinetics utilizing Langmuir-Hinshelwood Hougen-Watson (LHHW) type rate expressions published in the literature for SRM and DRM under analogous operating conditions have been used in the reactor bed model. These model results will be further validated against the experimental data published in literature. The kinetic conversion profiles are then compared with the thermodynamic results to systematically determine the regimes of kinetic deviation (from equilibrium) for the combined SRM/DRM system. This approach of carrying out both thermodynamic and reaction engineering analysis is advantageous in understanding the reforming process in a broader view and will also help in setting base for experimental investigations. These modeling results will be used as pre-experimental initial findings for the NPRP exceptional project aimed towards development of highly effective and coke resistant catalysts.
References
Pakhare, D. and J. Spivey, A review of dry (CO2) reforming of methane over noble metal catalysts. Chemical Society Reviews, 2014. 43(22): p. 7813-7837.
Song, C., Tri-reforming: a new process for reducing CO2 emissions. Chemical Innovation, 2001. 31: p. 21-26.
Jiang H, Li H, Zhang Y., Tri-reforming of methane to syngas over Ni/Al2O3—thermal distribution in the catalyst bed. Journal of Fuel Chemistry and Technology 2007. 35: p. 72-78.
Noureldin, M.M.B., N.O. Elbashir, and M.M. El-Halwagi, Optimization and Selection of Reforming Approaches for Syngas Generation from Natural/Shale Gas. Industrial & Engineering Chemistry Research, 2014. 53(5): p. 1841-1855.
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Analysis of Sand Bacteriophages Genome in Qatar
Authors: Umm-Kulthum Ismail Umlai, Annette Shoba Vincent and Valentin IlyinAbstract Objective: In this era of increasing antibiotic resistance (WHO)[1], we are running out of time as common bacterial infections are progressively rejecting drugs that would be standard for treatment. It is due to these reasons that research regarding bacteriophages, viruses that infect bacteria has seen a sudden revival. The Science Education Alliance- Phage Hunters Advancing Genomics and Evolutionary Science (SEA-PHAGES) headed by Dr. Graham Hatful from the Howard Hughes Medical Institute (HHMI)[2], University of Pittsburgh and Carnegie Mellon University has begun a nationwide initiative to discover, categorize and study the billions of bacteriophages that surround us. This initiative aims to create a thorough database containing genomic data for as many bacteriophages as possible. The study of these viruses is virtually new, and thus requires a significant effort; there is a novel, virtually untapped resource of genes and proteins that could greatly benefit our understanding of genomes and be used as treatments to bacterial infections that are resistant to antibiotics. Studying the bacteriophages is of great importance. The same protocols and procedures from the SEA-PHAGES program were applied to search for bacteriophages in Qatar within the sand and soil at Carnegie Mellon University Qatar. This is the first research of its kind to be carried out in Qatar and possibly at the Gulf region. Bacteriophages, which infect Arthrobacter.sp, were discovered in the sand from Al-Rayyan, Doha Qatar (Diversity of Bacteriophages in the ecology of Qatar). Following this, the viral plaques obtained were purified, isolated using a QIAamp MinElute Virus Kit[3] (Qiagen) and finally sequenced using Next Generation sequencing methods at Weil Cornell Medical University Qatar. Method: The sequenced DNA of phages were assembled using a Short Oligonucleotide Analysis Package- Denovo (SOAP-Denovo) software package. A program called Velvet has been also used in conjunction to ensure the best results were obtained using the optimal k-mer, providing the longest contig length. The longest length obtained was a contig of 12,380 at a k-mer of 59, along with a large number of smaller contigs. The largest 201 contigs have been annotated; gene nucleotide and protein sequences were collected, using the gene prediction software, GeneMarkS available online. Each of the genes from the contigs were then searched against the entire non redundant protein (NR) database of available annotated genes at the National Centre for Biotechnology Information (NCBI's) online database using Basic Local Alignment Search Tool (BLAST-p). They were also searched against non-submitted phage genomes collected at SEA-PHAGES. That result in about 558 annotated genes/proteins. All the proteins are being studied to understand better what the bacteriophage genome comprises of and how the proteins allow them to survive and infect bacteria in the sand collected from Al Rayyan in Doha. Results: So far three different bacteriophage contigs were found from the sequenced DNA, containing a total of 14 genes, most of which are derived from the Enterobacteriophage T7 cluster. However the individual genes displayed some variation from the original genes due to the small rate of mutations that naturally occurs with bacteriophages during replication. In addition to this, variations could be due to natural exchange of genetic information between viruses to form mosaic genomes. Thus each bacteriophage is unique due to this variation and each has proteins that can perform a slightly different function. One such gene was found had a 99% identity with Gene 3.5 from the Enterobacteriophage T7 family (phages that can infect Escherichia coli (E.coli) bacteria, which are commonly responsible for foodborne illnesses). This particular gene was searched against the PDB (protein database) from the same NCBI BLAST tool, to search for mutations. The query returned results of 100% identity with a (Chain L) T7 RNA Polymerase complexed with T7 lysozyme (interplay between an RNA polymerase and lysozyme). One particular bacteriophage contains a gene originating from a bacteriophage of the Yersinia species (phiA1122). This gene codes for a head-to-tail joining protein, which is a major component of a phage. This bacteriophage principally infects and neutralizes, Yersinia pestis, which is the causative agent of the Bubonic plague in humans[4] (Garcio.E). This particular gene must have been transferred during naturally occurring gene exchange between bacteriophages that infect the same organism simultaneously (Fleischmann, W) [5]. Discussion: The findings strongly suggest that Gene 3.5 has a function in breaking down the bacterial cell wall during infection. A further search on the Research Collaboratory for Structural Bioinformatics (RSCB) PDB was carried out to find a structural view of the protein. Upon studying the protein, it was found that the fragment containing the mutation is not seen in the crystal structure, which means it is a flexible loop. If this section of the protein moves in the crystal structure then it most probably moves in nature as well. This strongly suggests that the flexible mutated loop on the protein surface could affect of protein-protein interaction; and may result in slight changes in the mechanism (or temperature) by which the phage ligates or transfers genetic information from one phage to another. Future work: Future work aims to further study the Qatari bacteriophage genes and their proteins, their mutations and functions. Characterizing the remainder of the bacteriophage will allow us to better understand and annotate its genome. The relevance of these phages in a practical application could be in medical, industrial or agricultural uses. It could possibly have a role in treating E.coli infections or to prevent the contamination of such bacteria in the food industry. Further research could be done to sample more sand from various parts of Qatar (and various depths within the sand) to search for more bacteriophages. It is very likely that there are bacteriophages that could have more significant applications present within the sand. The same procedures could be followed to determine the functions and the nature of these phage genes.
References
[1] World Health Organization. 2015. Antimicrobial Resistance. Available at: http://www.who.int/mediacentre/factsheets/fs194/en/. Accessed on 13 November 2015.
[2] Howard Hughes Medical Institute. Science Education Alliance. Available at: http://www.hhmi.org/programs/science-education-alliance. Accessed on 13 November 2015.
[3] Qiagen.com. 2015. QIAamp MinElute Virus Kit. Available at: https://www.qiagen.com/us/shop/sample-technologies/combined-sample-technologies/preparation/qiaamp-minelute-virus-spin-kit/. Accessed on 13 November 2015.
[4] Garcio.E. 2003. The Genome Sequence of Yersinia pestis Bacteriophage φA1122 Reveals an Intimate History with the Coliphage T3 and T7 Genomes. Journal of Bacteriology. [Online]. Available at: http://jb.asm.org/content/185/17/5248.full. Accessed on 13 November 2015.
[5] Fleischmann. W.R. 1996. Chapter 43: Viral Genetics. Medical Microbiology 4th edition. Available at: http://www.ncbi.nlm.nih.gov/books/NBK8439/. Accessed on 13 November 2015.
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Chemical Characterization and Source Identification of Beached Oil from Two Areas Along the North-Western Coast of Qatar
Authors: Nasser Alkaabi, Mohammad Alghouti, Nabil Zouari, Theis Solling, Steffen Bach and Jan H. ChristensenOver the years there have been several reports of oil spills affecting particularly the northern coast of Qatar. In most cases, the source of oil spills is not identified. The spilled oils are very resistant to degradation and can affect the coastal ecosystem over many years. Even today, after 24 years, some of the oil that was spilled during the 1991 Gulf War can be found in sand, close to the Al Zubahra UNESCO site.
The Maersk Oil Research and Technology Center in Doha (MO-RTC) has established the Oil Fingerprint project in collaboration with the University of Qatar and the University of Copenhagen. One of the objectives of the collaboration is to identify the potential source and origin of oil spills based on their chemical composition.
A total of 38 samples were collected. During the sampling campaign it was discovered that the coast was contaminated with highly weathered oil that could originate from the Gulf War era but also with more fresh oil that most likely originates from recent oil spills in the Arabian Gulf. We therefore collected polluted soil samples and contaminated sediments from two main areas along the beach in North-western Qatar. The samples were analysed using gas chromatography – mass spectrometry in selected ion monitoring mode (GC-MS/SIM) and the oil composition was characterized. The likely source of the beached oil was identified by a comparison of diagnostic source ratios by comparing petroleum hydrocarbon fingerprints of steranes and hopanes of the spills against an oil database. The initial chemical fingerprinting based on selected ion chromatograms (SICs) of steranes (m/z 217) and hopanes (m/z 191), were remarkable similar as were the C29-/C30-Hopane ratios between sampling sites. However, a more detailed pixel-based analysis showed significant differences between samples.
The process also included an assessment of the physical and biological weathering effects on the oil spills. Petroleum biomarker patterns (steranes and hopanes) are identical for all 14 samples included in this pilot study. The only differences observed were in the relative concentration of LMW and HMW steranes. This could be due to real source oil differences, however, the general weathering patterns indicate that these differences are more likely due to extensive weathering of especially two samples (9-02, 3-02) but also 8-01 and 10-01 shows severe weathering effects. Analysis of alkyl-PAHs provided an overall evaporative weathering degree for the samples. Distinct differences in the isomer patterns were observed for 3- to 4-ring alkyl-PAHs and this cannot be immediately explained as biodegradation. The largest fraction of the samples seems to originate from the same source but other sources are clearly present. A more detailed analysis with normalization to Euclidean norms within six selected SICs revealed more source specific information. In conclusion, the results indicate at least 2-3 different sources on the basis of differences in PAH isomer patterns. This was confirmed by visual inspection of SICs of C1-C3 alkyl-substituted phenanthrene, dibenzothophene, chrysene and pyrene isomers. Apart from the finding that the spills originate from several sources, the evaporation profiles indicated that not all of the spills are crude oils but that some are also heavy fuels. This suggests ongoing bunker flush off the coast of Qatar.
These findings are of importance in further bioremediation processes in which, different approaches should be investigated to achieve high efficiency strategies if removal of oil pollutants from AlZubaraa area.
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Remarkable Thermal Stability of Nano-Crystalline Al-Mg-Li Alloys through the Addition of 1%Sr
Authors: Sara Iyad Ahmad and Khaled YoussefNanocrystalline metals -with grain sizes less than 100 nm- have proven to attain exceptional mechanical properties such as strengths that exceed those of coarse-grained and alloyed metals with grain size greater than 1 μm. As a result, such materials are to be acknowledged as the new class of high-performance engineering materials and to be implemented in various structural applications. The main reason behind the ultrahigh strength of this class of materials is mainly grain refinement, as in this mechanism, reducing grain size means introducing more grain boundaries. Grain boundaries act as barriers to the intra-grain dislocation motion, which is the main cause for the ductility of materials. Hence in its absence, the material is said to be strong and hard to deform. However, the strength associated with the new reduced grain size is associated with a penalty that leads to microstructural instabilities. This is because the atoms that lie in the grain boundary region are not as ordered and stabile as inside the grains. Hence those atoms are occupying unfavorable interfacial positions energetic wise, which means that they have high energy. As a result of the high volume fraction of grain boundaries, the system tends to pursue stabilization by seeking a configuration that shall allow for the lowest energy possible. The atomic system tends to eliminate the root of the problem which is the large number of grain boundaries and solve the problem by grain growth. Thus the removal of grain boundaries becomes the driving force to decreasing the system's energy. Hence an obstacle is yet to be overcome in order for those materials to be fully utilized to the maximum, as those nano-materials are prone to grain growth at lower temperatures than their conventional counterparts, which limits their service temperatures and expected lifetime. Grain growth can be slowed or even eliminated either thermodynamically, for example by adding solute atoms that segregate to the high energy sites in the grain boundaries, occupying it and lowering the free energy of the grain boundaries, or kinetically by the presence of second phase particles which results in grain boundary pinning, reducing the mobility of the grain boundaries and hence grain growth. This research aimed to studying the effect of adding 1% strontium (Sr) on stabilizing the grain boundaries of an aluminum-based alloy (Al-Mg-Li) which has a very low density yet a specific strength higher than that of steel. In order to achieve the goals of this research, a comparison must be made between the two samples of Al-5Mg-4Li and Al-5Mg-4Li-1Sr. Samples were prepared in a SPEX 8000 shaker mill and annealed at various temperatures up to 600 °C. To study the effect of Sr under various thermal conditions, both the as milled and annealed samples were analyzed using various experimental characterization methods such as X-Ray Diffraction (XRD) and Transmission Electron Microscopy (TEM) to perform a structural analysis and calculate the grain size of each sample. Using the Williamson-Hall model to calculate the average grain size for both samples based on the obtained XRD patterns, the results showed that for the as milled samples of Al-5Mg-4Li and Al-5Mg-4Li-1Sr, the average grain size was calculated to be 36.59 nm and 25.86 nm, respectively. The previous results were further proven when the TEM average grain size calculations gave similar results of 33 nm and 21 nm for the as-milled Al-5Mg-4Li and Al-5Mg-4Li-1Sr samples respectively. The thermal stability of the samples was proven when the grain size was measured after annealing at different temperatures for both Al-5Mg-4Li and Al-5Mg-4Li-1Sr samples. The average grain size was measured for Al-5Mg-4Li (annealed at 400 °C) and Al-5Mg-4Li-1Sr (annealed at 600 °C) to be 172.05 nm and 38.90 nm respectively. This shows that even at a higher temperature, the grain size for the sample that has Sr is much smaller and is still the nano-range. To verify the previous results of thermal stability, Vickers-hardness was measured for each sample after annealing as the mechanical properties of the thermally stabilized sample is expected to exceed those of the conventional sized sample. The plot of hardness variation of the nanocrystalline samples as a function of annealing temperatures showed that at room temperature, the hardness values for Al-5Mg-4Li and Al-5Mg-4Li-1Sr samples were 2.85 GPa and 3.24 GPa, respectively. With increasing annealing temperature, the hardness of Al-5Mg-4Li decreases gradually and reaches a low value of 0.8 GPa after annealing at 600 °C. In contrast, Al-5Mg-4Li-1Sr showed excellent thermal stabilization with increasing annealing temperature. Increasing the annealing temperature to 600 °C decreased the hardness value to 2.73 GPa. This hardness value is almost as high as the hardness of the as milled Al-5Mg-4Li (2.85 GPa) at room temperature. Since the XRD patterns did not show any traces of second phase particles, we suggest that the stabilization of the grain size and hence other mechanical properties such as hardness at high temperatures can be attributed to solute drag or the thermodynamic mechanism. Grain Growth does not only limit the nano-crystalline materials service temperatures, but also its unique technological applications as a consequence. Hence we anticipate that the results of this research will have implications in the development of thermally stabilized ultra-tough nanostructured materials for technological applications.
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Diatoms & Dinoflagellates Associated with Seagrasses, Algae and Mangrove
Authors: Mohanad Mushtaha, Yousef Ashraf Nasr and Abdullrahman Al-MuftahMarine environments sustain a variety of living organisms starting from microorganisms up to large macro-organisms. This support comes with the diversity of marine habitats that are created naturally to provide certain conditions for each single organism. However, Mangrove areas are one of many important places that are considered to be highly productive and could be suitable for planktonic life. Mangroves can be defined as salt tolerant plants that grow on the coasts and in shallow water. There are many types of plankton such as Diatoms & Dinoflagellate (Phytoplankton) that may be found in Mangrove areas (N. M. Nour El-Din & J. A. Al-Khayat, 2005). The presence of Diatoms & Dinoflagellate could be related to the occurrence of floating detritus in which Diatoms & Dinoflagellate can be found in association with them (Faust, M., & Gulledge, R. 1995). Moreover, Planktons can also be found attached to the seagrasses and Algae along the shallow shorelines. The presence of such planktonic type is affected by temperature and salinity so; such floating environments will be used to examine this effectiveness at shallow mangrove areas and along the coast area. Mangroves, Algae and seagrasses are found sometimes suspended in the water column and they start to move up and down due to the generation of Oxygen bubbles. (Faust, M. & Gulledge, R. 1995). Because of that, we will collect them only at the daytime. Thus, we will look at the species composition and how they will be affected by the variation of temperature and light in different seasons (summer (2015), spring and fall) and identifying any invasive species. Samples will be collected from three coastlines around Qatar (Al-Thakiera, Fwiret and Al-Wakra) and will be observed using light and electron microscope. The importance of this study is to show and identify benthic diatoms and dinoflagellates species and to have data about the harmful types because they affect fish stocks and water quality, in order to avoid having these two main problems on Qatari waters.
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Synthesis and Properties of Nanocrystalline BiTe-Base Thermoelectric Materials for Energy Applications
More LessThermoelectric (TE) is the science associated with converting the thermal energy into electricity based on the Seebeck effect. The attractive features of thermoelectric devices are their long life, low maintenance, highly reliable and they do not produce emissions harmful to the environment. Thermoelectric generators are used to provide electrical power in medical, military, and space applications where their desirable properties outweigh their relatively high cost and low operating efficiency. However, the widespread use of thermoelectric components is presently limited by the low figure-of-merit of presently known materials. Bismuth telluride Bi2Te3 (which has a peak ZT value of 1.1) is currently regarded as the state-of-the art TE material with high efficiency and is therefore attractive for energy harvesting processes. The objective of the work is to demonstrate a new route to the realization of highly efficient bulk Bi2Te3 structures at the nanoscale. Nanostructures provide a chance to disconnect the linkage between thermal and electrical transport by introducing some new scattering mechanisms. This will help in increasing figure of merit and then the efficiency. We present in this work novel versions of both p-type and n-type Bi2Te3 alloy materials with significantly enhanced figures of merit (ZT) between 25 °C and 125 °C.
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Improving Water and Nutrient Use Efficiency for Crop Production in Dry Lands via Soil Amendments and Remote Sensing Techniques
More LessThe soils of the Arabian Peninsula in general and GCC countries in specific are dominantly sandy (low nutrient and water holding capacity, high infiltration rate). These soils need high inputs for crop production. To be cost-effective in agriculture production these soils need careful consideration to enhance water and nutrient use efficiency and increase crop production. A number of organic and inorganic amendments have been used by various researchers in this regards. However, little has been done in this respect on UAE soils, and hence forms the focus of this study. The study aims to achieve this through soil improvement using soil amendments and assessing the efficiency through remote sensing techniques.
The green house and field trials were conducted simultaneously (January 2015) on Okra (Abelmoschus esculentus) at ICBA station using sandy soil which is dominant in the UAE and the GCC countries. Five inorganic amendments (Zeoplant, Zeoplant pellet, Meliorit, AustaHort and Palagonite) and one organic (locally produced compost) were used at different rates (0, 1.5, 3 and 4.5 kg/m2). Fresh water is used to offset the irrigation requirement of Okra equivalent to 100% and 75% ETc. The treatments were triplicated in a randomized complete block design.
Agronomic parameters (Germination, growth, flowering and fruiting) were recorded. Spectral signatures were collected in the range of 400 to 1100 nm using a hand held spectroradiometer with standardized viewing and radiation conditions for all treatments. Each parcel was monitored spectrally from the stage of being a bare parcel to the stage of 50% covered by vegetation.
Okra fruit is collected on a weekly basis and weight recorded. The SPAD meter is used in the field and greenhouse for the measurement of chlorophyll content during the growth stages.
The organic and inorganic amendments in general improved the water use efficiency as well as enhanced the biomass production to a significant extent compared to the treatment where amendments were not used. At 75% ETc the performance of amended soils was comparable to 100% ETc and fruit biomass production was similar. The use of the soil amendments can save up to 25% of the irrigation water in sandy soils.
These are preliminary results from sandy soil representing the main soil type in UAE. These amendments may behave differently in other types of soils hence further test are being started in Arabian Gulf University to test the same amendments on Bahraini soil.
Keywords
Water scarcity, Crop production, Sandy soils, Water and Nutrient Use Efficiency, Monitoring efficiency, UAE
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Textile-Reinforced Mortar (TRM) System as a Strengthening Technique on Reinforced Concrete Beams
Authors: Muhammad Shekaib Afzal, Usama Ebead and Kshitij ShresthaThere is considerable investment in construction industry in Qatar for civil infrastructures and taking into account the severe environmental conditions, they would entail for proper maintenance, repair and strengthening for safe, continuous, uninterrupted, and efficient functionality. Reinforced concrete (RC) structural members, which constitute majority of construction works in Qatar, can be easily deteriorated by the deleterious effect of seawater exposure in the form of humidity or direct splashing for sea-level and offshore structures. Such deterioration can also be due to the exposure to extreme high temperatures, severe humidity and high chloride. All such environmental effect can significantly reduce the life-span of RC structures by up to 10-15 years.
The cost of rehabilitation and strengthening is usually estimated in millions of dollars. Traditional methods of strengthening corrosion-damaged structures involve the replacement of the corroded bars and the substitution of deteriorated concrete layers with new concrete. Our study proposes an “optimum strengthening technique” for RC structures to mitigate the prevailing conditions of Qatar. This relatively new technique utilizes “textile-reinforced mortar (TRM)” to strengthen concrete beams. TRM systems consist of one or more layers of textiles made of carbon, glass, or Polyparaphenylene benzobisoxazole (PBO) grids that are sandwiched between layers of associated cementitious mortars. The cement-based mortar used in TRM acts as a barrier against chloride ions penetration thus protecting the main reinforcing bars from corrosion attack. Textiles' lightweight, high tensile strength, corrosion resistance, and ease of application make the strengthening system appealing. The potential of TRM for the repair and strengthening of concrete structures is not just the result of its physio-mechanical performance but also the ease and simplicity of installation that does not require any sophisticated equipment or retraining of the construction work. In addition, the compatibility between the mortar used and the concrete substrate is inherited since both materials have the cement as a common “base”. TRM systems, with their innovative features, ensure the endurance of the rehabilitation process and consequently the sustainability of the strengthened structure.
Recently in the last few years, several research works in the USA and Europe in the field of TRM strengthening technique have been reported for masonry and concrete structural members. Majority of these works is limited to single type of textile (either carbon, PBO or glass) and on limited types of reinforcement levels. The work presented here compares two different types of TRM systems in the same domain, performed on three different levels of reinforcement ratios representing flexural deficient, lightly reinforced and typical under-reinforced beams.
Experimental works were done to state the efficiency and effectiveness of textile reinforced mortar (TRM) in increasing the ductility and the flexural capacity of reinforced concrete (RC) beams. The aim of the experimental work was to investigate the parameters that contribute to the increase in the load carrying capacity of beams strengthened with TRM system. Eighteen medium-scale rectangular RC beam specimens, 2500 mm long, 150 mm wide and 260 mm deep, were prepared at three different reinforcement ratios of “ “ρ” _“s” ^“1” “ = 0.5%;” o “ρ” _“s” ^“2” “ = 0.72%;” f: “ρ” _“s” ^“1” “ = 0.5%; “ “ρ” _“s” ^“2” “ = 0.72%; “ “ρ” _“s” ^“3” “ = 1.27%.” The strengthened beams utilized two TRM types namely carbon and Polyparaphenylene benzobisoxazole (PBO) TRM systems respectively. The RC beam specimens were tested in flexure under four point loading until failure with a clear span of 2.2 m. The strengthening technique was applied to the soffit of the beam (flat type) altering the number of layers of textile. Three beams (of three different reinforcement ratios) without TRM strengthening were used as control specimens. Nine beams were externally reinforced by one (“ρ” _“T-c” ^“1” “ = 0.014%”), two (“ρ” _“T-c” ^“2” “ = 0.028%”) and three (“ρ” _“T-c” ^“3” “ = 0.041%”) layers of carbon TRM system. Six beams were strengthened with one (“ρ” _“T-PBO” ^“1” “ = 0.009%”) and two (“ρ” _“T-PBO” ^“2” “ = 0.018%”) layers of PBO TRM system.
From Based on the experimental observations, a reasonable gain in flexural strength and energy absorption was achieved for both the TRM systems. An increase of the initial stiffness was achieved for strengthened specimens; however, an apparent decrease in the overall ductility was observed with TRM strengthening. Results showed that the flexural capacity of strengthened beams increased to an average of 38% for carbon TRM system and an average of 26.7% for PBO TRM system over that of their control (un-strengthened) specimens. The highest increase in the load carrying capacity was 77.51% for a specimen having with the main reinforcement ratio of D12 (“ρ” _“s” ^“2” “ = 0.72%)” and was strengthened with carbon TRM system using three layers of carbon textile.
Ductility index (ΔI) and energy absorption (Ψ) values were also calculated in order to know the behavior of ductility and flexural capacity in each of the beam specimen. The term ductility index (ΔI) is defined as the ratio between the deflection at the ultimate load and that at yield load, representing its ability to stretch/deform under sustained load before fracture. During experimentation, it was observed that the average values of ductility indices of using carbon as strengthening material were 1.1 × , 1.2 × and 0.5 × for “ρ” _“s” ^“1” “ = 0.5%,” “ρ” _“s” ^“2” “ = 0.72% and “ “ρ” _“s” ^“3” “ = 1.27%” beam specimens respectively to that of their control specimen. Similarly the average values of ductility indices of using PBO as strengthening material were 2.42 × , 0.75 × and 0.56 × for “ρ” _“s” ^“1” “ = 0.5%,” “ρ” _“s” ^“2” “ = 0.72% and “ “ρ” _“s” ^“3” “ = 1.27%” specimens respectively to that of the control specimen. Also the term energy absorption (Ψ) is defined as the area under the load- deflection curve up to the ultimate load, representing the amount of energy absorbed by the specimen before complete failure. The average values of energy absorption for using carbon as strengthening material were 1.8 × , 1.2 × and 1.6 × for “ρ” _“s” ^“1” “ = 0.5%,” “ρ” _“s” ^“2” “ = 0.72% and “ “ρ” _“s” ^“3” “ = 1.27%” beam specimens respectively to that of the control specimen. Similarly the average values of energy absorption for using PBO as strengthening material were 2.0 × , 1.0 × and 1.5 × for “ρ” _“s” ^“1” “ = 0.5%,” “ρ” _“s” ^“2” “ = 0.72% and” “ρ” _“s” ^“3” “ = 1.27%” specimens respectively to that of the control specimen.
Therefore, both the adopted TRM systems performed exceptionally well within the scope of the work, with carbon TRM system showing a relatively higher increase in the capacity of strengthened specimens and PBO TRM systems exhibiting relatively more ductile failure with higher bond strength between the TRM surface and concrete substrate. Moreover, crack patterns for the strengthened beam showed effective distribution of cracks/damage over the length of beam as compared to severe and concentrated damage in the associated control un-strengthened beams. Further, during the experimentation, it was seen that the technique of applying the TRM system also considers the contractor's ease where the construction workers (although not very skilled) can easily implement the technique after being given simple demonstrations.
The study puts forth proper procedures and standards to the construction industry on the rehabilitation and strengthening of the existing concrete structures using innovative TRM strengthening technique. Successful implementation of the project will result in “state-of-the-art recommendations for design and construction specifications”, which will place Qatar and research at Qatar University in a leadership position not only limited to the Gulf region. Furthermore, this can potentially act as an “important initiation for the development of new industrial opportunities” in the country.
Keywords
Reinforced concrete beams, textile reinforced mortar, flexural strengthening, ductility index, energy absorption.
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The Effect of Chilled Water Supply Temperature on the Energy Efficiency of the Chiller System
Authors: Abdulwahab Alyousef and Abdulwahab BukshaishaA steady-state model for a centralized cooling system is developed and utilized to evaluate its energy efficiency. The numerical model resolves the energy equations for a cooling tower and a centralized water-cooled chiller simultaneously. It requires inputs that are readily available. The user-inputs are the ambient conditions, the cooling tower air flow rate, the condenser water flow rate, the evaporator water flow rate, the superheat and sub-cooling associated with the refrigeration cycle, and the full load design conditions. The model utilizes an empirical relationship for the compressor power as a function of load and temperature, and gives the user an option to select between a constant speed chiller and a variable speed chiller. The outputs include the chiller coefficient of performance, compressor input power and compressor isentropic efficiency. This talk will discuss the results of the assessment conducted of the effect of chilled water supply temperature on the performance and energy efficiency of the chiller system. The findings and recommendations on how to optimize chiller systems for best energy performance will also be presented.
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Comparative Analysis of Antifungal Activity of Total Phenolics from Different Date Palm Cultivars Against Five Phyto Pathogenic Fungi
Authors: Resna Nishad and Talaat AhmedIntroduction: Pathogen attacks impose natural selection on plants to evolve complex arrays of defensive strategies. Among the diverse defensive mechanisms evolved by plants to withstand pathogen attack, the ability to synthesize an arsenal of low-molecular weight volatile and non-volatile chemicals including phenolics helps them to prepare a robust defense response against pathogen entry. Systemic induction and accumulation of low molecular weight phenolics is observed in response to various diseases and thus are studied as markers for resistance to pathogens. Phenolics that exhibit anti-oxidant activity exert their inhibitory effects on pathogen colonization via protein precipitation and iron depletion.
Phytochemical analysis have been proved that date palm is rich source of phenol. Very little information is available on the inherent Date palm phenolic content that has been involved as resistance factors. All the studies are focused on phenolic content from date palm fruit and its property. Here we focusing on comparative analysis of phenolics from different cultivars leaf and how it affect the different pathogenic fungi. Material and Methods: We conducted a genome mining analysis of date palm whole genome available in the NCBI site, to detect the presents of enzyme involved in the secondary metabolite pathway. Analyzed the presents of receptor protein specific for the recognition of fungal pathogen.
Five date palm pathogens were isolated from the diseased date palm and surrounding soil from the date palm field located in northern region of Qatar. Leaf, shoot and root samples collected from the diseased date palm and rhizosphere soil collected from near the diseased date palm. Samples were stored at 40?C in aseptic condition until further use. Sterilized plant samples were plated in the potato dextrose agar (PDA) for the fungal isolation and the soil were plated on molten agar for fungal isolation. The plates were incubated at 250?C until single colony appeared. The isolated fungi were examined under microscope. Based on the microscopic and physical characteristics fungi were identified.
The pathogenicity were determined with detached leaf inoculation analysis and in vivo pathogenicity analysis with three date palm cultivar varieties. Detached leaf inoculation analysis performed in laboratory condition and the in vivo pathogenicity conducted in green house with controlled growth condition. The date palm varieties used in this current study are Khalas, Khneezi and Barhi. All the four pathogens, Fusarium solani, Fusarium oxysporum, Rhizectonia solani Fusarium sp and Ceratocystis radicicola were used for pathogenicity analysis.
Total phenolic were extracted from three date palm culvars through water extraction procedure. Extraction performed with different temperature range. Comparative analysis of antifungal property of total phenolics from different date palm cultivars such as Khalas, Khneezi and Barhi was carried out after optimizing extraction temperature. Antifungal activity is determined with disc diffusion analysis. 100 μl of extract impregnated filter disc (10 mm in diameter) placed on the PDA plate followed by fungal disc placed on the disc. Plates were incubated at 250?C and the fungal growth monitored. Experiment repeated in triplicate along with control. Results and conclusion: The genome mining analysis of date palm result revealed 45 enzyme sequences from shikimate pathway, which is a support for the active synthesis of phenolic content in date palm. Plant phenolics synthesize via shikimate-phenylpropanoid-flavonoid pathways and include phenolic acids, flavanoids, tannins and less common stilbenes and lignins. Presents of chitin elicitor receptor kinase in date palm indicate the phytopathogenic fungal detection ability of date palm.
From the isolated fungi, the date palm pathogenic fungi were screened and subcultured. Five pathogenic fungi were isolated, Fusarium solani, Fusarium oxysporum, Rhizectonia solani, Fusarium sp and Ceratocystis radicicola. Pathogenicity of all the five isolated fungi were confirmed by analyzing necrosis caused on the date palm leaf (Fig. 1). The frequency of necrotic lesion and disease susceptibility found more in Khneezi than Khalas and Barhi.
Water extraction procedure conducted at 400?C for 24 hrs were accepted as standardized phenolic extract for antifungal activity. Growths of the fungi were measured after 3 day and 5 days of incubation to determine the antifungal activity of phenolic extract (table 1). Phenolic extract from the Khalas showed more antagonistic activity against Rhizectonia solani whereas phenolic extract from Barhi showed more inhibitory activity against Fusarium solani, Fusarium oxysporum and Ceratocystis radicicola. In all the experiment Khneezi showed week inhibitory activity this supports our previous susceptibility study (not published) in that Khneezi showed more susceptible to C.radicicola. This result is an evident for the disease resistant activity of date palm phenolics.
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Sampling of Qatari Sand Microbes: Serious about B.cereus
Authors: Umm-Kulthum Umlai, Annette Shoba Vincent and Vincent IlyinObjective: A shortage of studies regarding the ecology of Qatar led to the sampling sand to determine the composition of microbes within the sand (below a certain size). This sampling began with a sand sample obtained from Al Rayyan, Doha Qatar. The sample was purified, and sequenced after isolating the DNA. A comprehensive analysis of the local Qatar sand sample shows a range of various microbes (which are smaller than 0.2 micrometer), which exist in the sand. Among these organisms was Bacillus cereus a bacterium from the Bacillus family that is most commonly responsible for mild food poisoning. The genes are being studied further to understand better what the sand microbial composition is like. Furthermore, it will help us better understand the genomes of these microbes and possibly how the proteins allow them to survive within the sand. Method: After obtaining the sequenced DNA, a Short Oligonucleotide Analysis Package- Denovo (SOAP-Denovo) system that helps assemble the genetic information into short reads called contigs was used. In addition to this, another program called Velvet was also used in conjunction to ensure the best results were obtained using the optimal k-mer, providing the longest contig length. The longest length obtained was a contig of 12,380 at a k-mer of 59. Subsequently, the results of the assembly program were assembled into nucleotide and protein sequences using the gene prediction software, GeneMarkS available online. Each of the genes from the contigs were then searched against the National Centre for Biotechnology Information (NCBI's) online database using Basic Local Alignment Search Tool (BLASTp) which utilizes certain algorithms to compare the protein input sequences in FASTA format to the entire non redundant protein database of available sequenced genes. This tool provided us with a possible list of the gene's (percentage) identity, along with the maximum and total scores, the query cover (percentage of sequence that matches that available for a particular organism's gene) and the E-value (the smaller the value the less the probability of the similarity occurring due to random chance) in order to assess the probability that the results are accurate. All this data was collected are currently being analyzed further. Results: It was found that the microbe majorly contributing to presence in the sand was Bacillus thuringensis with 50%, closely followed by Bacillus cereus with 40%, 5% Methylobacterium, 3% Enterobacteriophages, 2% other forms of Bacillus species and finally some traces of Streptococcus pneumonia as well as some other organisms. Bacillus thuringiensis or Bt is a common biological pesticide used in agriculture and is safe for human consumption; this bacterium is a common soil dwelling organism. Bacillus cereus on the other hand is less safe for human consumption as it produces harmful toxins that cause mild food poisoning and it is similarly a soil-dwelling microbe. Methylobacterium, are bacteria that are usually found in soil and are the natural flora found on the ground. Enterobacteriophages are bacteriophages that commonly infect E.coli. And finally Streptococcus pneumoniae are pathogenic bacteria that exist in the body but are the main causative agents of pneumonia in humans when they exceed a certain threshold or if the immune system is vulnerable. Discussion: The results showed that the microbes did not share 100% identity with their respective matches. There is a high chance that the small percentage differences (which ranged from 1-6%) could be due to mutations that enable the microbes to adapt to their environment's temperature. For example, some of the B.cereus genes that have undergone mutation are those that code for polysaccharide synthase (94% identity), histidinol dehydrogenase (99%), a capsular polysaccharide biosynthesis protein (99%), or a sodium/hydrogen exchanger (also 99%). Future work: In order to verify the presence of the organism in the sand, there will need to be more samples, and a repeat of the experiments. With repeated experiments, the organisms will not be filtered; the threshold for the size of microbes will be increased, allowing for a greater view of the composition of the sand samples in Qatar. This will allow us to gain a better picture of microbial life in the ecology of Qatar; especially in terms of the presence of pathogenic microbes.
The sand samples will be cultured and grown on blood agar plates and the microbes would be identified through morphological characteristics. A repeat of the DNA isolation and sequencing will be carried out to confirm the presence of the microbes such as B.cereus. Furthermore, PCR tests will have to be conducted using universal primers for 16sRNA of certain bacteria as a control, to check against the DNA extracted from the sand sample during the initial round of DNA sequencing. If any of the genes are the same as the B.cereus from the first time, it would be confirming its presence in the sand.
It would be possible also to design primers specific for B. cereus in order to develop a convenient method of testing for such organisms. This could be extremely useful for test in food since food poisoning is commonly caused by these easily detectable and curable microbe infections. This could help reduce the level of food poisoning in the country, which is quite a common occurrence in Qatar.
In future studies, more samples could be taken from various parts in Qatar, as well as at a range of different depths within the sand, to further increase our knowledge of the types of microbes present in the ecology.
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Experimental Investigation on Gasoline and Diesel Fuels Surrogates Designed Via Computation and Property Integration Methods
Authors: Nimir Elbashir, Saad Intikhab, Sawitree Kalakul, Hanif Ahmed Choudhury and Rafiqul GaniAutomotive researchers attempts to simulate combustion of fuels in order to improve engine performance.[1] Conventional fuels are difficult to represent in these simulations due to their complex composition. Surrogates that meet American Society of Testing and Materials (ASTM) standards are a good alternative to conventional fuels. This study aims at design and analyzing surrogate mixtures for both gasoline and diesel. Surrogates were designed through a computer aided model developed at the Technical University of Denmark.[2] The model architecture has four structures viz., (i) problem definition (ii) property model identification (iii) mixture blend design and (iv) model-based verification.
Surrogate diesel, comprised of five paraffinic compounds viz., n-dodecane, n-tetradecane, tetralin, cyclo-octaneand iso-cetane in different volumetric ratios. Surrogate gasoline comprised of six different chemicals viz. n-butane, n-heptane, iso-octane, 1-pentene, methyl cyclopentane and toluene in different volumetric ratios. Target physical properties of these fuel surrogates were measured using advanced analytical equipment and experimental techniques developed at Texas A&M University at Qatar.[3] Diesel surrogate was tested for the target properties employed in the model viz. density, viscosity, heat content, flash point, vapor pressure, pour point, cloud point and distillation curve. Butane present in the gasoline surrogate hampers handling and testing since it is extremely critical to prepare a homogeneous blend that comprises of both liquids and a permanent gas. Also, the conventional sampling technique was found to be ineffective to prevent loss of permanent gas in the surrogate. Therefore, a novel sampling methodology and advanced blending technique was developed to minimize loss of butane and volatile components such as 1-pentene. Detailed Hydrocarbon Analysis (DHA) for gasoline surrogate was carried out by Gas Chromatography (GC) according to ASTM D6730 to verify the efficacy of blending technique as well as sampling method. The composition analysis through DHA confirmed that the blending and sampling methodology was accurate with maximum relative standard deviation of approx. 5.82%. Subsequently gasoline surrogate was tested for density, viscosity, vapor pressure, heat content, distillation curve and compositional attributes.
The surrogate mixtures prepared in this study complied well with their respective ASTM standards for the properties measured. The work would further be continued to investigate the engine performance and emission characteristics for diesel surrogate. Engine performance will be evaluated in terms of Power/Torque and Theoretical Brake Specific Fuel Consumption (BSFC). Emissions of Carbon Monoxide (CO), Hydrocarbon (HC) and Nitrogen Oxides (NOx) will be determined. Results of this study provide a basis to further improving the computer aided models used to design the surrogates and for design of future generations of efficient fuels of different composition obtained from both conventional sources (petroleum) and non-conventional sources (e.g. from natural gas via gas-to-liquid (GTL), coal via coal-to-liquid (CTL) or biofuels). Also, the outcome of this study will be used to optimizing the design of fuel blends obtained from the aforementioned sources.
References
[1] Pitz, W. J., & Mueller, C. J. (2011). Recent progress in the development of diesel surrogate fuels. Progress in Energy and Combustion Science, 37(3), 330–350.
[2] Yunus, N. A., Gernaey, K. V., Woodley, J. M., & Gani, R. (2014). A systematic methodology for design of tailor-made blended products. Computer and Chemical Engineering, 66, 201–213.
[3] Elmalik, E.E., Raza, B., Warrag, S., Ramadhan, H., Alborzi, E., Elbashir, N.O. (2014). Role of Hydrocarbon Building Blocks on Gas-to-Liquid Derived Synthetic Jet Fuel Characteristics. Industrial & Engineering Chemistry Research, 53, 1856–1865.
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Study and Comparison of PFC Rectifiers: Quasi Z Source, Traditional Flyback
Authors: Sinan Asaad Sabeeh and Fahad AlhuwaishelThis study focuses on comparing the Traditional Flyback PFC (F-PFC), and the Quasi Z-Source PFC (QZS PFC) on range of (36–720W) and input Voltage of (130, 200, 230V) with an output Vdc of 36 Volts while operating in Continuous Conduction Mode. The study has confirmed that F-QZS PFC has better THD%, P.F, and lower output current and voltage ripple relative with the output power. In addition, the stress on each main element has been explored and it was confirmed that the F-QZS has robust measured voltage and current across the elements due to the effect of crossed capacitance topology in the F-QZS while the F-PFC suffers from high spikes. Finally, a very precise closed loop duty ratio control was developed to optimize the performance of the F-QZS PFC.
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Growth of Hybrid Perovskites (HP) Light Harvesting Layer and TiO 2 Electron Transport Material for Solar Cells Application
Hybrid Perovskites (HP) recently emerged as alternative light harvesting layer to fabricate high efficiency thin film solar cells. The perovskite based solar cells took advantage of the experience gained in the field of the dye sensitizes solar cells and the extremely thin absorber (ETA) solar cells. It is worth mentioning that the structure of the perovskite solar cell is very similar to a dye sensitized solar cell and ETA solar cell. These cells are composed of the transparent conducting layer (TCO), the electron transport material (ETM) the absorber, the hole transport material, and the back contact. Our work focuses on the deposition and characterization of two components of the perovskite based solar cell. These components are the ETM which is titanium dioxide layer (TiO2) in this case and the absorber material which is the perovskite layer. Dip coating technique was used to grow compact and pinhole free TiO2 films from a solution of Titanium alkoxide diluted in isopropanol. The dip coating technique is particularly attractive for thin film solar cell application due to its simplicity, low cost, and good quality of films. For a compact film, dipping was restricted to two dips and four dips. The films were structurally and morphologically characterized by X-ray diffraction and scanning electron microscope (SEM). XRD analysis showed the deposited TiO2 films have anatase structure. SEM results showed a full coverage of the films with less pinholes. The two step sequential physical vapour deposition was performed to grow HP thin films using thermal evaporation technique. Thin films of HP were deposited using thermal evaporator under high vacuum from two sources namely lead iodide and methylamine iodide. Firstly, Lead iodide was deposited which acts as a template for the crystallization of perovskite layers. Then methylamine iodide was deposited for the desired film. X-ray diffraction of the as deposited film showed the presence of mixed phases of lead iodide and perovskites. This indicates at room temperature methylamine iodide diffused deep enough in the lead iodide film to form the perovskite structure. Films were then annealed at 110 °C for 1 hour in nitrogen atmosphere for better crystallinity which is proven by the sharper and high pick intensities. Also, varying the ratio of both organic and inorganic sources did not influence the presence of lead iodide phases as confirmed by XRD. Further optimization are in progress to form single perovskite phase formation.
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