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Qatar Foundation Annual Research Conference Proceedings Volume 2018 Issue 1
- Conference date: 19-20 Mar 2018
- Location: Qatar National Convention Center (QNCC), Doha, Qatar
- Volume number: 2018
- Published: 12 March 2018
61 - 80 of 142 results
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Immobilized Nanosize ZrMetal Organic Frameworks ZrMOFs: Highly Active Reusable Catalysts for Cross Coupling Reactions
More LessFunctionalized Zr-based metal-organic frameworks (UiO-66-fun) have emerged as promising class of porous functional materials with very large specific surface area, ultrahigh porosity and chemical tunability as well as high stability in water and humid environments, which results in desirable properties for several catalytic applications.1–3 These high stable materials were selected as supporting molecular MOF catalysts. We have applied a simple and highly efficient method for synthetic post-functionalization of new and readily recoverable molecular catalysts that combines the catalytic active transition-metal complexes with the architecture of nano-size MOF and their application for cross coupling reactions. In the catalytic process, substituted aryl halides and arylboronic acids converted into corresponding biaryls through C-C bond forming process in a milder condition (Chart 1). In the tested catalysis reactions, functionalized nano-size UiO-66-fun catalysts can be recovered by simple filtration/centrifugation in air and reusable without significant loss of catalytic activity and while framework structures are maintained stable. The detailed post-functionalization and catalysis results will be presented. References: Kim, M.; Cahill, J. F.; Fei, H.; Prather, K. A.; Cohen, S. M. J. Am. Chem. Soc. 2012, 134, 18082.Bosch, M.; Yuan, S.; Rutledge, W. Zhou, H.-C. Acc. Chem. Res. 2017, ASAP, DOI: 10.1021/acs.accounts.6b00457. Pascanu, V.; Yao, Q.; Bermejo Gomez, A.; Gustafsson, M.; Yun, Y.; Wan, W.; Samain, L.; Zou, X.; Martin-Matute, B. Chem. - Eur. J. 2013, 19, 17483. Acknowledgment: Support of this research by the NPRP award (NPRP 9-377-1-080) from the Qatar National Research Fund.
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Environmental Assessment of RO Intakes Applicable for Qatar and the GCC Region
Authors: Hamish R Mackey, Abdulrahman Al-Kaabi and Sami G. AlGhamdiThe State of Qatar and the Gulf Cooperation Council (GCC) region are located in a hyper-arid area with no rivers, over-abstracted groundwater supply and limited rainfall. Consequently, with the discovery of oil and gas and the associated economic prosperity, the State of Qatar and the GCC region have relied on desalination of seawater from the Arabian Gulf. As of 2013, the GCC region held a 70% share of total global desalination capacity.Multi-Stage Flash (MSF) desalination technology has been the source of water supply in the State of Qatar and the GCC region for the past few decades due to the low cost of energy in these countries and the problems historically faced by Reverse Osmosis (RO) membrane processes in dealing wih the high salinity of the Arabian Gulf. MSF is a thermal process that distills water through stages based on high temperature and changing pressures. The systems suffer from high energy requirements and low recovery rates resulting in significant discharge of brine with elevated temperature to the ambient receiving water. RO on the other hand relies on applying a positive pressure to pass permeate through a fine polymer filter material against the osmotic pressure gradient. RO is widely adopted worldwide due to its lower energy consumption and increased product recovery. With recent developments the technology can cover the high salinity of the Arabian Gulf (40,000 mg/L to 55,000 mg/L total dissolved solids). Nevertheless, RO systems require extensive pretreatment to ensure the integrity of the membrane and to prevent blocking of the fine pores. This makes the process susceptible to surface water quality fluctuations such as during algal blooms and therefore its application in Qatar is still challenging due to the shallow and enclosed nature of the Arabian Gulf.Subsurface intake processes for RO have the potential to reduce the effects of fluctuations in source water quality and reduce the energy intensity of the process, since they provide natural filtration of the source water and simplify the extensive pretreatment requirements necessary to protect the RO membranes. However, significant tradeoffs occur by using subsurface intakes. For instance, intake pumping may be increased to overcome the additional headloss through the intake media while the construction phase also involves increased civil works. This research investigates the environmental impacts associated with the operation phase of RO systems using both open intake and beach well intake systems theoretically located in the State of Qatar, since operational phase impacts typically comprise most of the environmental loads in cradle-to-grave assessments.The study utilizes Life Cycle Assessment (LCA) methodology to assess a wide range of effects from the systems. The ReCiPe lifecycle impact indicator approach is utilized with mid-point impact indicators including climate change, marine eutrophication, terrestial acidification, photochemical oxidant formation, particulate matter formation, marine ecotoxicity, water depletion, mineral resource depletion and fossil fuel depletion. The RO system, its pretreatment and intake will be sized and modelled for a desalinated water output of 100,000 m3/d using a combination of fundamental process equations and commercially available software. The results will show a clear direction from an environmental perspective on which type of intake system Qatar should consider if implementing seawater RO as a preferred desalination technique.
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Coral bleaching in extreme environments: speciesspecific thermal tolerance limits
Increasing seawater temperatures are being measured worldwide, causing coral bleaching events during which the symbiosis between the coral host and its symbiotic zooxanthellae is disrupted, and a global decline in reef corals. In the Arabian Gulf where water temperatures are naturally extreme with summer maxima at 35°C and above and winter minima at 18°C and below, seawater temperature anomalies are repeatedly recorded in the summer. While Arabian Gulf corals have naturally evolved to survive at temperatures that would cause bleaching and mortality to most corals elsewhere, an increasing number of mortality events have been recorded in the Gulf (Qatar, Saudi Arabia, and the UAE) in the last decades, resulting in a substantial loss of biodiversity and coral cover, mostly in inshore environments. Efforts are being deployed locally to conserve remaining habitats and attempt the restoration of lost habitats, but to be successful, efforts need to incorporate regional species-specific traits such as the susceptibility and resistance to future bleaching. We here assess the tolerance and sensitivity of three ecologically important species from the Arabian Gulf, Acropora downingi, Porites lutea, and Dipsastraea pallida, sampled in Qatari offshore reefs in the mid-winter, by exposing them to heat stress in enclosed aquaria. Colonies were assigned to control aquaria maintained at 25°C, aquaria to be raised to 30°C, or aquaria to be raised to 36°C. After an acclimatization period, the 30°C and the 35°C aquaria were raised to their target temperature at a maximum rate of 1°C per day. During the warming period and for another three weeks, we monitored the photosynthetic activity of their symbiotic zooxanthellae twice a week with a diving-PAM fluorometer while checking for signs of bleaching. We found that the photosynthetic activity was not affected in any of the three species when the temperature was raised from 25°C to 30°C. At 34°C, the photosynthetic activity in A. downingi started declining. Once the temperature reached the 35°C target, all A. downingi colonies bleached, expelling their zooxanthellae, and died three days later. The photosynthetic activity in P. lutea and D. pallida started declining once the temperature reached 35°C and continued declining for an additional three weeks, after which P. lutea died and D. pallida recovered. The high tolerance of P. lutea and especially of D. pallida is promising for the survival of the two reef-builders in coming years, despite increasing seawater temperatures caused by climate change. However, the branching Acropora coral is not expected to respond well to any further increase of temperature, as reflected in its major regional decline in the past decades. Due to its high sensitivity, Acropora might also not be a good candidate in coral restoration projects, as it showed a high sensitivity to bleaching and the inability to survive bleaching events. However, aquarium conditions not being able to fully reflect natural conditions on the reef, further work would need to be conducted directly on the reef to determine whether other factors might be involved in assisting resistance to bleaching, survival under bleaching conditions, or recovery following bleaching. In any case, P. lutea and D. pallida would be excellent candidates in coral restoration projects, having showed a lower sensitivity to bleaching and the ability to survive for several weeks under thermal stress, therefore showing potential for a long-term survival even under warming conditions.
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Developing an ecofriendly approach to reduce the use of biocides for preventing Microbial Induced Corrosion
By Saad RasoolSulfate Reducing Bacteria (SRB) cause significant damage to marine oil pipelines necessitating the use of biocides for reducing the Microbial Induced Corrosion (MIC) and potential for great environmental harm. Currently, oil companies pump frequent batches of biocides to these under water pipelines without proper quantification of the bacterial population. This is primarily because the existing method for quantifying the bacterial population in a sample is not very effecient, as it can take up to 2 weeks to obtain the results. Our team has focused on developing an eco-friendly approach to limit the use of these biocides, which are used for targeting the SRB. SRB require high salt and low oxygen so first we genetically engineered a strain of bacteria that would report the osmolarity in oil pipelines, thus act as a biosensor for salt concentrations. The ratio of salinity in the seawater flowing in versus the seawater flowing out of the well will be used to estimate SRB populations in the pipelines, thus limiting the amount of biocides added in times of high Microbial counts.
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CFD Analysis of Falling Film Wettability in MED Desalination plants
Authors: Furqan Tahir, Abdelnasser Mabrouk and Muammer KocIn Gulf Cooperation Council (GCC) countries, 56% of the market is captured by thermal based desalination (both MED and MSF), while in Qatar 91% is based on thermal desalination. Among the thermal desalination technologies, Multi Effect Desalination (MED) operates at lower specific power consumption and is considered more energy-efficient than the Multistage Flash (MSF) distillation. The lower energy consumption of MED plants is due to high overall heat transfer coefficient and low pumping power. The most common problem in MED evaporators is fouling of tubes, which reduces heat transfer and performance. Horizontal falling film evaporators are the most common evaporator type used in MED; in which liquid film is maintained outside the tube and part of it evaporates producing vapors. Improperly maintained liquid film leads to fouling i.e. formation of salts on the surface of tubes, which affects heat transfer properties of the surface. So in order to minimize fouling, tubes should be completely wet; especially column based on second row in triangular pitch configuration and bottom row tubes, which receive lesser mass flux. Wettability study of falling film evaporator in 3-D domain is carried out using commercial CFD tool i.e. Ansys fluent v18.0. A column of three tubes having OD 19.05 mm, vertical pitch of 24.7 mm and 20 mm section is considered in this study. Brine inlet has an opening of 1 mm × 1 mm and mass flux (Wetting rate Γ) is varied from 0.03 kg/m-s to 0.2 kg/m-s. This mass flux variation include all flow regimes namely droplet, column and sheet modes. For multiphase flow, volume of fluid (VOF) model is selected, as this model is used where two phases are separated in the flow regime. Wall adhesion model is incorporated for film and tube contact. Conservation of mass, momentum and energy equations were solved in a transient manner via SIMPLE algorithm for pressure-velocity coupling. All equations were discretized in 2nd order and residual for convergence criteria was set to 10-6 for better accuracy. The time step was taken 5 × 10-6 s, to ensure that the global courant number is below 0.25 and iterations for each time step were 40. Initially mesh dependency check was carried out and then the model was validated against available data in the literature. CFD results show that at lower mass flux i.e. 0.03 kg/m-s, tubes are not completely wet and there are dry patches, which are more susceptible to fouling. As the mass flux is increased flow regime changes from droplet to column and then to sheet mode. Increasing mass flux diminishes dry patches problem but also at higher mass flux, film is detached from tube surface causing lower portion of tube to remain dry. There is no fixed critical value for flow regime transformation as it depends on many factors like tube Outer Diameter (O.D.), tube pitch, nozzle type, nozzle diameter and solution properties etc. Moreover, the effect of surface roughness was also taken into consideration and it was concluded that more roughness results in better film stability and enhanced wettability.
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Shallow Aquifer upper ∼120 m Rocks of Qatar: Depositional and Diagenetic Controls on Water Storage Capacity and Hydraulic Conductivity
More LessCarbonates and evaporites of Paleogene-age form the shallow-aquifer rocks that mantle most of Qatar, including the Paleocene and Lower Eocene Umm er Radhuma, and the Middle Eocene Rus and Dammam Formations. Nearly complete 10-cm-diameter rock cores have been recovered from boreholes in central and northern Qatar to depths of greater than 120 m. A 40-m section of exposed Rus and Dammam Formation from a cave in central Qatar (Misfer Cave) was also described. Assessment of aquifer quality in these rocks was undertaken through core and thin-section description, quantitative mineralogical determination (X-ray diffraction), as well as core-plug porosity, permeability, and pore-throat (mercury-injection capillary pressure) measurements.
Our work shows that the rocks from central Qatar can be separated into four depositional intervals: 1) m-scale fining-upward cycles of fossiliferous open-marine deposits with clay-rich caps (Umm er Radhuma), 2) fine-grained stromatolite-bearing, restricted shallow-marine deposits (uppermost Umm er Radhuma), 3) m-scale bedded marginal-marine gypsum deposits intercalated with thin shallow marine carbonate and clay deposits and capped by rooted and microcodium-bearing surfaces (Rus Formation), and 4) open-marine carbonates overprinted by karst processes (Dammam). Aquifer storage capacity and hydraulic conductivity are mostly a function of diagenetic features, and in spite of the lack of any evidence of significant burial, the diagenesis of these rocks is complex. The Umm er Radhuma and the Rus carbonates are almost completely dolomitized, whereas the Dammam is only partially dolomitized, with the amount of dolomitization varying both laterally and vertically. Best aquifer quality in central Qatar, based both on core plug data and well spinner tests, can be found in coarsely-dolomitized intervals that lack clay (lower Umm er Radhuma). Finer and clay-bearing dolomitized rocks have storage but lower hydraulic conductivity (upper Umm er Radhuma). Both gypsum-rich rocks and depositional limestones (which are generally mud-bearing) have lower porosity and permeability (Rus and Dammam). In central Qatar the effect of karst overprinting is variable, generally leading to lower matrix porosity and permeability due to clay translocation from above, but large vugs are also observed at exposure surfaces.
The borehole in northern Qatar was located within a karst collapse feature (doline) that is characterized by internal drainage. Based on satellite images, the collapse feature, likely reflecting the presence of deeper karst is approximately 1 km in width. Sediment tentatively interpreted as a cave deposit, and composed mainly of dolomite silt, has been observed in this core at depths of greater than 60 m below the surface. This fine-grained material intercalates with courser breccias that are interpreted as collapsed country rock. The impact of karstification on country rock matrix properties (porosity and permeability) is still to be determined. Whereas the rocks from northern Qatar are still under investigation, they are distinct from the central Qatar equivalents in that they lack any bedded evaporites. This leads to the prediction that the shallow aquifer in northern Qatar will be less compartmentalized than in central Qatar. The elemental makeup of waters from different stratigraphic intervals in both boreholes are being compared to help understand how the central and north shallow Qatar aquifers contrast.
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Developing a Framework for a Dynamic Modeling Tool to Support RiskBased Decision Making in the Petrochemical Industry
Authors: Rym Kanes, Clementina Ramirez-Marengo, Ali Sheharyar, Othmane Bouhali, Luc Vechot and Emilio AlvarezProcess Safety in the oil and gas industry is managed through a robust process safety management system that involves the assessment of the risks associated with a facility, throughout its lifecycle. Typical approaches for risk assessment of an accident scenario includes: the identification of hazards, the estimation of the frequency, the analysis of possible consequences, and the evaluation of the risk against a company's tolerance criteria. While current quantitative risk assessment methods (e.g.: Layer of protection analysis (LOPA), Bow Tie analysis (BT), etc.) have brought significant improvements in the management of major hazards, they tend to provide static values of risk at a given time (snapshot at the time of the assessment). In reality however, risk levels tend to fluctuate throughout the lifecycle of a process, due to several time-variant risk factors, which include: equipment aging (which impacts their reliability), variations in the integrity and vulnerability of safety barriers, plant activities (e.g.: maintenance, shut-down), health and efficiency of the process safety management system, process safety incidents or near misses, etc. Thus, to that effect, risk is dynamic in nature and risk assessment approaches should allow for continuous updating of risk values over time. Over the last decade, the petrochemical industry has put significant efforts in developing process safety indicators (PSIs) to continuously measure the health and efficiency of process safety management systems. This has increased the sources of information that are used to assess risks in real-time. Hence, there is an opportunity to leverage PSIs along with equipment/safety barrier performance data to estimate the quantitative measure of risk levels in a process facility on a time-variant basis. ExxonMobil Research Qatar (EMRQ) partnered with the Mary Kay O'Connor Process Safety Center – Qatar (MKOPSC-Q) to attempt development of a tool that uses Bayesian Belief Networks (BN) to capture any potential increase of risk levels in real-time as a result of pre-identified risk factors and reliability data of equipment and safety barriers. The tool is referred to as PULSE, which stands for Process Unit Life Safety Evaluation, and is intended to be used to support existing decision making practices. The work involves a phased approach that first included the development of a methodology to establish the framework for the tool. Then, implementation and testing of the framework was attempted using BN algorithms. The most recent phase involves application of the tool to maintenance and inspection planning. In this context, the work presented here demonstrates the feasibility of using PULSE to quantify changes in risk level for a process unit based on a case study from literature. Furthermore, the different aspects of PULSE development are described. These aspects include: translation of the Bow Tie into a BN, modification of the BN to include reliability data, and insertion of equipment failure incidents into the BN to perform dynamic modeling. The outcomes of the dynamic modeling with real time insertion of equipment failure evidence are discussed. Also, the application of dynamic modeling to support risk-based decision making with regards to inspection and maintenance planning is included.
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NASICON based Na4MnV PO4 3/MWCNTs Cathode Materials for Naion Batteries with Improved Electrochemical Performance
Lithium ion batteries (LIBs) have completely captured the portable electronics and electric vehicle market due to their tempting performance. However, due to limited reserves of lithium, the price for lithium is constantly increasing which necessitates to trace out some decent alternative to lithium ion batteries. In this regard, sodium ion batteries are considered one of the best substitutes for lithium ion batteries due to inherited properties of sodium metal like abundance of resources across the globe, ease of availability, economy and environmentally friendly nature. Moreover, sodium ion batteries follow the similar electrochemical principles as the lithium ion batteries which indicates that knowledge and understanding of principles of lithium ion batteries can be utilized for the development of smart sodium ion batteries. In this work NASICON (Na+ super ionic conductor) based Na4MnV (PO4) 3 was synthesized using the sol - gel technique. As prepared Na4MnV (PO4)3 demonstrates an active redox couple at around 3.6 V and 3.2 V during oxidation and reduction process respectively. The pristine Na4MnV(PO4)3 shows good initial discharge capacity ∼ 138 mAh g-1 at 0.05C. However, it shows rapid discharge capacity fading with increasing discharge rate (138 mAh/g at 0.05C and 15 mAh/g at 2C) and poor cycling performance (68.0% of the initial capacity was retained after 40 cycles) with increasing discharge rate. To improve the electrochemical performance of the developed material, Na4MnV (PO4)3/MWCNTS (MWCNTs = 1 & 3wt. %) were synthesized. The initial discharge capacity of these materials at 0.05C was found to be similar to pristine Na4MnV(PO4)3, however, the addition of MWCNTs has resulted in significant improvement in the discharge capacity at high c-rate which can be mainly attributed to the enhanced electronic conductivity of the pristine material. Apart from higher capacity at high c-rates, the addition of MWCNTs has also improved the cyclability of the pristine Na4MnV(PO4)3. A capacity retention of 99.0 % and 98.00% of the initial discharge capacity after 40 cycles is noticed for Na4MnV(PO4)3/1wt.%MWCNTs and Na4MnV(PO4)3/3wt.%MWCNTs respectively. The improved performance of Na4MnV (PO4) 3/MWCNTs cathode materails make them attractive for energystorage applications.
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Gas Driven Fracture during Gas Production using HeleShaw Cell
Authors: Riyadh Al-Raoush, Zaher Jarrar, Khalid Alshibli and Jongwon JungMethane hydrate is considered a potential energy source, with worldwide reserves on the order of 500–10,000 Gt of carbon. The production of Methane from hydratebearing sediments requires hydrate dissociation for releasing mobile methane gas in sediments prior to gas production operation. Existence of even a small fraction of fines can greatly decrease the permeability of sandy sediments, which will affect the gas recovery process. Fines can migrate through or clog the pores of sandy sediments depending on geometric constraints such as the ratio of the size of the pore throat to the size of the fine particle. In multiphase flow, clogging of fines at the pores causes a change in pressure gradient which affects the flow of gas through the pores and might induce gas driven fracture. In the literature, there is a major knowledge gap that needs to be resolved to develop technical and economically viable methane production strategies from gas hydrate reservoirs. A comprehensive understanding of the underlying physical processes such as fines migration, clogging, and gas-driven fracture during gas production in hydrate bearing sediments is needed. Effects of fines migration and clogging on gas flow path and gas driven fracture were studied for Carbon Dioxide (CO2). This was achieved by conducting multiphase flow experiments on brine saturated sand-kaolinite mixtures using 2D Hele-Shaw cell; a common analogous model that has been used to investigate particle displacement process in sediments and has the unique advantage in allowing real-time visualization. The cell consists of two transparent acrylic sheets that are separated by a small gap. The gap between the two sheets is maintained using filter sheets that have a thickness of 1/16 in. (1.6 mm) at the boundaries. Fluids flow radially between the sheets through a port in the middle of the bottom sheet. Multiphase flow experiments are conducted on samples of brine saturated uniform F75 sand mixed with kaolinite at different percentages by weight (0% to 20%). Pressure volume actuator (flow pump) is used to inject brine into the sample for saturation. Following saturation, CO2 is applied to the cell at a constant pressure (2 kPa, 5 kPa, and 10 kPa). Variation of gas pressure is monitored using a pressure sensor that is attached near the port of the cell. The injection processes are recorder using a high resolution digital camera mounted above the cell. Gas pressure was found to increase with increasing fines content, which indicates the clogging of pores by kaolinite particles. Particle image velocimetry (PIV) analysis was conducted using PIVLAB code on MatLab. Velocity vector field and density plots of velocity field were generated to track particles displacements. Particles near the fracture tip were moving at the highest velocity. The results showed three different regimes of gas flow through sediments. For low concentration of fines, the gas percolates through the pores with no major host particles displacement. For a high concentration of fines, major particle displacement occurs and gas driven fractures are created. Gas solely flows through those generated cracks with no observed percolation. Finally, a combination of the two regimes takes place for intermediate fines content.
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Groundwater pollution by petroleumderived contaminants in coastal semiarid environment
More LessA common source of contamination of soil and groundwater in arid and (semi)-arid coastal regions are accidental spills of petroleum products, such as crude oil, gasoline, and diesel fuel. Groundwater pollution by petroleum hydrocarbons is a serious pollution problem that poses hazards to water resources and living organisms including humans. After release to the sub surface, hydrocarbons move downward through the aerobic vadose zone under the force of gravity. Eventually, they reach the groundwater table, where oil overlay promotes the development of anaerobic conditions. The oil phase that occurs as floating product on the water table and as residuum on soil grains provides a continued source supplying hydrocarbons to the groundwater. Accumulations of residual hydrocarbons at or near the water table may undergo smearing due to variations in water table elevation driven by, for example, seasonal changes in recharge and discharge or by tidal forcing in coastal environments. In subsurface environments contaminated by petroleum products, the geochemical conditions near the water table, in particular, the oxygen availability, moisture content, salinity, pH, nutrient concentrations and temperature, are important determinants of biogeochemical processes. Among these variables, the interplay of moisture content, oxygen availability and temperature are critical for understanding the biodegradation of petroleum hydrocarbons in arid and (semi)-arid coastal soil environments. In addition, the fate and transport of hydrocarbons in groundwater also depend on the redox conditions, soil mineralogy and microbial community structure, as well as the availability of suitable electron acceptors and nutrients. We hypothesize that the transition zone between the vadose zone and the groundwater system represents a hot spot for the degradation of petroleum hydrocarbons. This transition zone, however, is a dynamic biogeochemical environment, whose functioning is closely linked to the amplitude and frequency of water table fluctuations. We propose to determine the role of water table fluctuations on the coupled hydrological and biogeochemical processes that affect the degradation and partitioning of petroleum hydrocarbons, under conditions relevant to aquifers. Coastal areas in this regard can function as zones of contaminant mass transfers between aquifers and surface water bodies, but also as excellent spots of in situ bioremediation of contaminated soil and groundwater thanks to coupled hydrological and biogeochemical processes. The main objectives of this project are to: 1) quantify the level of sorption and biodegradation of multi-component hydrocarbons in soil and groundwater; 2) quantify the rates of hydrocarbon biodegradation under oscillating aerobic and sulfate reducing conditions in groundwater contaminated with petroleum hydrocarbons; 3) determine the oxygen dynamics in the vadose zone and groundwater affected by hydrocarbon dispersion under variable water table fluctuation regimes; 4) assess the rates and mechanisms of biogeochemical reactions regulating groundwater nutrient turnover during hydrocarbon spill and its movement under conditions of groundwater table fluctuations; and 5) develop a reactive transport model for groundwater pollution by petroleum hydrocarbons. In this project, we combine the acquisition of integrated physical, chemical and microbial data using uniquely designed process-oriented experimental approaches. The results of this project will significantly add to the quantitative knowledge on the effects of water table fluctuations on the release and degradation of petroleum-derived hydrocarbon contaminants in soil environments that experience both arid conditions and tidally-driven water table fluctuations. The expected results of the research will inform groundwater management and protection in arid and (semi)-arid coastal environments. To quantify the level of sorption and biodegradation of petroleum hydrocarbons in subsurface soils and groundwater (Objective 1), we conducted a series of controlled-laboratory batch experiments under variable salinity, temperature and water chemistry conditions. The soil samples were collected from the eastern coast of Qatar which is close to the North Gas and Al-Shaheen Oil Fields. The initial physical characterization of soil samples showed sand classification with the texture class of sabkhas soil. The results of soil-phase chemical characterization suggested that the dominant minerals of the soil are calcite, dolomite and gypsum and the concentrations of chloride and sodium were found to be high with a chloride-to-sodium ratio of ∼1.6.We used volatile benzene and naphthalene hydrocarbons to determine the sorption and biodegradation rates. The results of sorption experiments showed that naphthalene was adsorbed to the soil more than benzene where the initial aqueous concentrations of benzene and naphthalene were reduced at equilibrium due to sorption by approximately 10% and 75%, respectively. This difference was attributed to the organic carbon-water partitioning coefficient which is higher for naphthalene. We developed a sorption kinetics model to define the sorption isotherm of benzene and naphthalene hydrocarbons for the specific coastal soil collected from Qatar site. The model assumes the two sites sorption to the soil, one site in local equilibrium and the other site on first-order kinetic sorption, and the best fits were found for the Langmuir sorption isotherm type for the used hydrocarbons and soil in this project. In this presentation, we present the results of sorption and biodegradation batch experiments as well as the design of a unique dynamic soil column experiment to understand the dynamic responses of the fate, transport and degradation of hydrocarbons and the soil biogeochemical processes to the relatively abrupt changes in hydrogeochemical and climatic conditions.
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Fines migration and clogging behavior in methane hydratebearing sediments
Authors: Jongwon Jung, Shuang Cao, Riyadh Al-Raoush and Khalid AlshibliThe structure of natural hydrate-bearing sediments that exist offshore or onshore is a combination of coarse-grained sediments and fine-grained particles. During gas production from hydrate-bearing sediments, fine particles may migrate with the flowing fluids within pore space and cause clogging of the pore space of the porous media. Therefore, fine particles play a significant role during methane production from hydrate-bearing sediments as it impact the overall sediment formation performance and production efficiency. The migration of fine particles and its impact on clogging have been investigated in a single-phase flow, but it has not been clearly understood in a multi-phase flow. This research focuses on the study of fines migration and clogging behavior during single and multi-phase flow which can be implicated in gas production from hydrates bearing sediments. Microfluidic pore models that mimic porous media with different pore throat sizes were fabricated and utilized to study fines migration and clogging behavior in porous media. Artificial particles and natural fine particles were selected to represent fine particles. The impact of flow rate, pore-fluid types, particle concentration, and pore-throat to fine particle size ratio was investigated. Fine particles used in this research include polystyrene latex particles, silica, and kaolinite. Pore-fluids used in this study include deionized (DI) water, and sodium chloride (NaCl) brine (2M concentration). The particle concentrations covered from 0.1% to 10%. And the pore-throat widths were fabricated from 40 μm to 100 μm. Single-phase flow experiments were conducted to show that the concentration of fine particles required to form clogging in pores increased as flow rate decreased. The results obtained using polystyrene latex particles provide the insight at a relatively higher flow rate (50 μl/min) than literature studies that fine particles with 2% concentration can migrate in the pore throat without bridge or clogging at the various pore throat and fine particle size ratios (o/d = 2.6∼36.4). Furthermore, silica presents higher critical clogging concentration (0.5% in brine) compared with kaolinite (0.2% in brine) when the pore-throat width equal to 60 μm due to the larger pore throat and fine particle size ratio. On the other hand, the findings show that clogging easily occurred at a lower pore-throat to fine particle size ratio even with a few number of fine particles. In addition, pore-fluid type directly influences the tendency of fine's to form clusters which in turn impacts the clogging behavior. For instance, silica fines clogging easier occurs in brine solution compare within deionized water due to larger cluster size in brine, while kaolinite shows an opposite result which means the kaolinite has higher clogging possibility in deionized water compared within brine solution. On the other hand, findings of multi-phase flow experiments show that fine particles accumulate along the liquid-gas interface and migrate together, which in turn cause bridging or clogging to occur easily in pores. These observations imply that a multi-phase flow during gas production could easily form clogging in pores, in which the flow permeability of porous media decreases even though clogging has not occurred in the same conditions with a single-phase flow. Thus, the permeability of porous media in engineering applications should be estimated by considering relatively easy clogging in pores in a multiphase flow compared to a single-phase flow. Findings of this research show the vital impact of pore-fluids and fluid-fluid interphase on fine particles migration and clogging in porous media. It provides a better understanding of the fines migration and clogging mechanisms. In addition, the results indicate the need to understand the types of fines and fluids in reservoir before evaluating if there will be a clogging potential during gas production from hydrates bearing sediments.
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Invitro conservation of some rare and threatened desert plants in Qatar
Authors: Talaat Ahmed and Mohammed AlsafranBackground A range of natural factors, invasive animals and human activity have been severely affecting stability of the ecosystem, resulting in the annihilation of plants habitats and so plant endangerment or even extinction. In Qatar, urgent action needs to be taken to stop decline of desert plant species as well as an effective strategy should be applied to reverse and save these wild endangered plants. Otherwise, they will be faced with the danger of their extinction in near future. Therefore, it is very important to have knowledge of protection measures, such as replanting and propagating through tissue culture technology, to protect the biodiversity in Qatar. Plant in-vitro culture systems have been used as an alternative approach to propagate and conserve a large number of rare and endangered plant species that show difficulties to be propagated using conventional methods of propagation. It was reported that standard culture environment could be effectively employed for short-term in-vitro conservation of different plant germplasm, through increasing intervals between subcultures especially in slow growing plant species. Objectives In the current study, conservation of rare and endangered desert plants using in-vitro culture were developed. Generally, these plants are not easy to be propagated by classical horticultural methods. Different techniques including micro-propagation, in vitro seed germination, and regeneration from callus were applied to propagate and conserve three endangered plant species in Qatar; Leptadenia pyrotechnica, Glossonema varians and Prosopis cineraria. Methods Collection of endangered plant species Location of the endangered plant species were identified and the plant parts- seeds, stem, shoots, roots, nodal cuttings or whole plant- depending on its type and availability, were collected. Surface sterilization of the collected material The plant materials were washed with tap water to remove dust and debris, then were soaked in 70% ethanol for 1–2 min, then were treated with sodium hypochlorite or Clorox for 10–20 min followed by rinsing 3–5 times with sterilized distilled water under aseptic conditions. In-vitro plants formation Organ culture using nodal sections of the plants were cultured on hormone-free MS medium (0.5X) for in vitro plants formation. For seeds were cultured on medium containing gibberellic acid (GA3) for efficient seeds germination. In this way, in vitro plants were established and multiplied to produce large number of healthy clones. In case seeds or nodal cuttings are not available, other plant parts like leaf or root were used as explants to initiate callus tissues. Results Seeds of Leptadenia pyrotechnica were collected, surface sterilized and germinated under aseptic condition using 0.5X MS media. In-vitro employing tissue culture via callus and shoot induction using different growth regulators was explored. Seedlings from in-vitro germination of the seed were used as explants. The results revealed that the highest callus production was obtained using 2.0 mg/L BAP. In addition, 0.5 mg/L and 2.0 mg/L NAA were good for callus initiation, compared to other hormones. Seedlings of Glossonema varians were collected were used as an explant for callus induction. Several plant growth regulator were used to initiate callus including 2, 4, D, NAA and BAP and their combinations. The results showed that the best plant growth regulators to induce callus were 1.5 mg/l IBA and 2 mg/l BAP. Prosopis cineraria, is a famous tree in Qatar. It is not easy to be propagated by classical horticultural methods. Seed dormancy was broken by scratching via sand paper. Several plant growth regulator were used to initiate callus including 2, 4, D, NAA and BAP and their combinations. The results showed that the best plant growth regulators to induce callus were both 2.0 mg/l 2, 4, D and 1.5 mg/l IBA. The obtained callus will be treated to regenerate new plantlets. Adventitious shoots and roots formation will be induced and a large number of in vitro plants will be produced. The in-vitro grown clones will be hardened (acclimatized) for greenhouse and later field conditions. The in-vitro plants will be removed from the cultures; medium will be removed by washing with running water and sown in pots. The pots will be covered with plastic sheets to keep high humidity and gradual removal of the plastic will harden the plants for greenhouse.Conclusions Recently, in-vitro culture technique of desert plants has received importance because it can be used for the fast propagation and ex situ conservation of endangered plants. The success of micro-propagation and in vitro conservation of the selected endangered plants depends on the best choice of the explants, the efficiency of the sterilization method and correct plant growth regulator. The best in-vitro conservation of the selected plant species is in MS media with the following plant hormones 2, 4, D, NAA. IBA and BAP.
Acknowledgements «This study was made possible by UREP grant # UREP19-209-1-037 from the Qatar national research fund (a member of Qatar foundation). The statements made herein are solely the responsibility of the author(s).»
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CuI and CuSCN as Hole Transport Materials for Perovskite Solar Cells
CuI and CuSCN as Hole Transport Materials for Perovskite Solar Cells Vinod E. Madhavan1*, Ahmer Ali Bozdar Baloch1, Afsal Manekkathodi1, Dhanasekaran Thirunvukkaarasu1, I. Zimmermann2, C. Roldán- Carmona2, G. Grancini2, M. Buffiere1, Mohammad Khaja Nazeeruddin2, A. Belaidi1 and Nouar Tabet1 1 Qatar Environment and Energy Research Institute, Hamad Bin Khalifa University, Qatar Foundation, P. O. Box 5825, Doha, Qatar 2 Group for Molecular Engineering of Functional Materials, Institute of Chemical Sciences and Engineering, Ecole Polytechnique Fédérale de Lausanne, CH-1951 Sion, Switzerland *[email protected]. ABSTRACT: Perovskite based solar cell is an important area of research for solar energy harvesting and for green energy revolution. The materials used for a thin film solar cell are considerably less with respect to the prevailing silicon based solar cells. There is an interest in copper based inorganic materials, especially copper iodide (CuI) and copper thiocyanate (CuSCN) as hole transport materials (HTMs) in perovskite solar cells (PSCs) for efficient, inexpensive and stable energy harvesting. Copper based films exhibit higher conductivity and wider-band-gap. The existing organic HTMs are expensive and have low hole mobility. The reported high power conversion efficiency (PCE) of CuI and CuSCN based perovskite solar cells are 6% and 20.3% respectively [Christians et al. J. Am. Chem. Soc., 2014, N Arora et al. Science 2017]. The perovskite solar cells based on inorganic CuI and CuSCN can be more stable and cost-effective with respect to spiro-OMeTAD HTM. We present our work on mixed perovskite in the form of (FAPbI3)0.85(MAPbBr3)0.15 in combination with CuI and CuSCN HTMs that lead to efficiencies 5.16% and 15.43% respectively in an n-i-p architecture under full sun illumination. The CuI based device displayed a short-circuit current density (Jsc) of 8.98 mA/cm2, Voc of 898.57 mV and fill factor (FF) of 0.64. Under similar conditions, the device with CuSCN, showed a significant increase in the Jsc (8.95 mA/cm2 to 20.86 mA/cm2) and Voc (from 898.57 mV to 1060 mV) (Figure1). A reference cell with standard spiro-OMeTAD HTM showed a PCE of 19.65% (with Voc of 1180 mV and Jsc of 22.70 mA/cm2). The high Jsc when using CuSCN with respect to CuI is mainly due to the effective charge extraction between the perovskite and CuSCN. However there is a strong quenching in the photoluminescence measurements in both CuI and CuSCN cases, which suggests that excellent hole injection is taking place from the perovskite active layer into the CuI and CuSCN hole transport materials (Figure 2). It is worth noting that CuI based perovskite devices showed a PCE of 6% with excellent photocurrent stability and 2 orders higher electrical conductivity that lead to higher fill factors [Christians et al. J. Am. Chem. Soc., 2014]. Impedance spectroscopy measurements revealed high recombination rate in CuI devices [Huangfu et al, Applied Surface Science 2015]. This could explain the low Voc and Jsc despite the quenching of the photoluminescence spectrum in the presence of CuI and CuSCN. Further studies are in progress in-order to find out the origin of the recombination and how to remediate them. Various device structure models (p-i-n and n-i-p geometry) with copper based HTMs are simulated with SCAPS software to find out the efficient structures with minimum losses. The results shows that the CuSCN based cells are more promising and can be used to prepare high efficiency perovskite solar cells. References J.A. Christians, R.CM. Fung, P.V. Kamat, J. Am. Chem. Soc. 2014, 136, 2, 758–764 pp. N. Arora, M. I. Dar, A. Hinderhofer, N. Pellet, F. Schreiber, S.M. Zakeeruddin, M. Grätzel, Science 2017,10.1126/science.aam5655. M. Huangfu, Y. Shen, G. Zhu, K. Xu and M. Cao*,F. Gu and L. Wang, Appl. Surf. Sci. 2015, 357-B, 2234–2240pp.
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Distribution Identification Isolation and Culturing of Cyanobacteria Found in Qatari Microbial Mats and its Applicability for Treatment of Industrial Wastewater
More LessA significant global environmental opportunity of today is finding beneficial reuse for industrial and domestic wastewater through appropriate treatment, redistribution and application. Although industrial wastewater may present various challenges in terms of exotic or hard to treat constituents, finding effective and efficient treatment options and subsequent reuse opportunities will be beneficial for many facets of the environment, especially in regions of the world where water scarcity is an issue. Numerous remediation methods have been developed to purify wastewater. Most of these are physiochemical in nature, which are often not effective to implement on a large scale and can be expensive. This research explores an environmentally natural approach using biological processes (microbial activity) to achieve the degradation of petroleum hydrocarbons. The objective of this study was to study microbes native to Qatar, in particular those found within microbial mats that are found in various areas around the country. The steps taken were to first estimate the area of microbial mats using GIS, identify the microbial species within these regionally specific mats, isolate and culture cyanobacteria from these mats and explore the applicability of using these organisms for treatment of industrial wastewater.
Microbial mat samples were collected from three geographical areas around Qatar, namely Ras Abrouq, Al Zubara and Khor Al Adaid. The collected microbial mats were firstly enriched in cultured medium. Different strains of cyanobacteria were isolated from these enriched mats and were cultured using solid media ASN-III and MN. Single strains of cyanobacteria were then sub cultured in BG-II liquid medium and were used to test the biodegradability of a test set of hydrocarbons (benzene, toluene and hexadecane). The optical densities of the cyanobacteria were measured using a spectrophotometer and the rate of biodegradation of the hydrocarbons were found using a Gas Chromatography Mass Spectrophotometer (GCMS).
Results show that most of the microbial mats identified in Qatar are found on the Dukhan coastline area. Another important area of mats is found at Khor Al Adaid (Inland Sea) located in the southeastern portion of the state. Different species of cyanobacteria were identified from these mats. The most common species identified from mats at Al Zubara were Oscillatoria, Phormidium, Microcolous, Lyngbya, and Spirulina. Those from Khor Al Adaid were Plectonema, Synechococcus, Phormeduim, Lyugbya, Oscillatoria, and Trichodesmium. Those from Ras Abrouq consisted mostly of Microcolous, Lyngbya, Pseudanabena, Oscillatoria, Phormidium, Spirulina, Gloeocapsa, and Aphanothecechroococcus.
Two species of the cyanobacteria, Oscillatoria and unicellular Cyanococcus, were successfully cultured and sub cultured in BG-II medium and used for biodegradation studies with hydrocarbons. Initial results suggest these species are capable of degrading hydrocarbons, but further studies are required to determine to what extent.
For future research, the duration of incubation of microbes with the chemicals of interest for degradation could be increased to help confirm capability. Furthermore, mixtures of different species of cyanobacteria could be used to understand if populations play a role in achieving effective biodegradation of hydrocarbons. This work is also being expanded to explore other microbes found around Qatar and testing their applicability to be effective “biodegraders”. All this research may be beneficial with our larger goal of finding more effective, efficient and environmentally natural approaches to treating industrial wastewater.
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Yeast Volatile Organic Compounds Inhibit Ochratoxin Biosynthesis By Aspergillus Carbonarius and a Ochraceus
Authors: Zahoor Ul Hassan, Maria Farbo, Pietro Urgeghe, Angela Marcello, Samir Jaoua and Quirico MigheliOchratoxin A (OTA) has hepatotoxic, teratogenic, nephrotoxic and carcinogenic effect in mammals and it is classified as a group 2B carcinogen by the World Health Organization. The European Union has set the maximum OTA level at 2 mg/kg in wine, grape juice, and other grape products, and at 3 mg/kg for all products derived from cereal, including cereal products and cereal grains for human consumption. Some species of Aspergillus are the main source of OTA in warm and tropical regions, and in particular Aspergillus carbonarius (Bainier) Thom is considered one of the most relevant OTA producers in food and feed. Inhibiting the growth of OTA-producing fungi on sensitive commodities is by far the most reliable method to prevent OTA contamination of food and feed. Aim of this study was to evaluate the biocontrol ability of selected yeast strains against OTA producing Aspergillus carbonarius and Aspergillus ochraceus. In a previous report, two non-fermenting (Cyberlindnera jadinii 273 and Candida friedrichii 778) and two low-fermenting (Candida intermedia 235 and Lachancea thermotolerans 751) yeast strains have shown a significant antagonistic behaviour against a virulent strain of A. carbonarius on grape berries as well as in in vitro experiments, while the filtrated and autoclaved culture broth of the yeast strains had no significant effect on pathogen growth.This biological effect was at least partly due to the release of volatile organic compounds (VOCs), since growth inhibition was observed without contact between yeast and Aspergillus spp.. Aspergillus colonies exposed to yeast VOCs did not sporulate, and were characterized by a white mycelium; the colony border was undefined, with elongated and scattered hyphae compared to unexposed control. Single hyphal tips and mycelium fragments were then transferred on PDA and after 5 days of growth at 25°C, typical dark sporulating colonies were evident, suggesting that the anti-sporulating effect is reversible. Aiming to further characterise the effect of VOCs produced by biocontrol yeast strains, we observed that, beside vegetative growth and sporulation, the volatile compounds significantly reduced the production of OTA by both A. carbonarius and A. ochraceus isolates. Exposure to yeast VOCs also affected gene expression in A. carbonarius, as confirmed by downregulation of polyketide synthase, non-ribosomal peptide synthase, and the regulatory genes laeA and veA. The main compound of yeast VOCs was 2-phenylethanol, as detected by Headspace-Solid Phase Microextraction-Gas Chromatography-Tandem Mass Spectrometry (HS-SPME-GC-MS) analysis. Yeast VOCs represent a promising tool for the containment of growth and development of mycotoxigenic fungi, and a valuable aid to guarantee food safety and quality. Further studies will aim at testing single purified VOCs in order to identify the most effective compounds responsible for the inhibition of fungal growth and OTA production by Aspergillus spp. in preventive food safety strategies.
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Evaluating the potential of using truck appointment systems to decrease reefer energy consumption at container terminals
More LessIn the recent decades there has been an unprecedented globalization of trade. One of the most important factors that made this possible is the containerization of the supply chain. As a consequence container terminals have become essential for todays globalized economy. The trend of containerization has further extended to the cold supply chain through the use of reefers (refrigerated containers), resulting in a tremendous increase in the trade of food and other perishable goods. In case of import dependent countries like Qatar the cold supply chain has become essential for food security. The number of reefers at container terminals has substantially grown and as a consequence their energy use. In average ports, the largest part of energy is consumed by crane operations and cooling of reefers. In case of ports that are dedicated to export/import of foods the cooling of reefers becomes the largest component of terminal energy consumption. This is especially the case in countries with extreme temperatures like Qatar. Although there has been a substantial amount of research dedicated to optimizing operational procedures of cranes at container terminals with a focus on minimizing energy use, similar approaches have not been explored in case of reefers and the related cold supply chain. In this work we focused on the potential of exploiting a terminal truck appointment system (TAS) to this goal. The main objective of the TAS is to minimize the waiting times at the port gates and to maximize the utilization of container yard equipment. It is important to note that previous research has shown that the information from the TAS can be used to optimize the crane operations. The majority of the existing research on TAS systems has been dedicated to evaluating the potential benefits that such systems can bring to a port in the sense of truck turn times. The concept of including reefer related information into a TAS adds a new dimension to the problem. This is due to the fact that the energy use of a reefer container is directly related to its dwelling time. The idea is to minimize the stay of reefers at the port. To be more precise the objective is to minimize the time since a reefer is unloaded to the port until a truck takes it out of the port. In practice this means that we wish to get the trucks that import the reefers to come to the port as soon as possible. This type of work adds a new type of objective where there is a higher priority related to trucks importing reefers. It is possible to develop a mixed integer program to assist in designing optimal methods for TAS related issues it is often not the best choice. The problem is that due to the high level of unpredictability in the movement of trucks inside and outside of the port the evaluation of a TAS system in this way is often not adequate. Due to this fact, the evaluation of such systems is frequently done using discrete event simulations (DES). In the existing literature the schedule for trucks is fixed, and further analysis is done to evaluate the effect of missed appointments and the percentage of «walk-in» trucks. The DES is only used for the truck arrivals to the port and related use of resources (Entrance Gate, Yard, Exit Gate, etc.). In the proposed research we extend the DES to also include dynamic appointment scheduling. To be more precise, we analyze how requests arrive and how appointments are given. This is important in the context of reefers since we want to give then higher priority, in the sense of leaving appointment slots open for truckers that transport them out of the port, which would otherwise be booked. The proposed DES is used to evaluate several strategies for appointments systems for both minimizing turn times of trucks and the dwelling times of containers. We show that some strategies can notably decrease the energy used for reefer cooling while maintaining short truck turn times.
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Performance of Antisoiling Coatings for Enhancement of PV Panel Performance in Doha
Authors: Maulid Mohamed Kivambe, Benjamin Figgis and Nouar TabetSevere temperature, humidity and dust characteristic of the desert region are major challenges in power generation efficiency of photovoltaic (PV) systems in the gulf region. Soiling can lead to daily average energy loss of up to 4% [1], necessitating frequent cleaning which adds to the cost. One of the solutions to the problem is to use anti-soil coatings, where hydrophilic or hydrophobic coatings with spectral characteristics suitable for PV applications are added to the outer layer of PV glass. However, it has been shown that the effectiveness of the coatings in reducing accumulation of dust in PV panels is dependent on climatic conditions [2-4]. Since coatings add to the cost of solar panels, it is imperative that the coatings are tested for suitability at the intended location or similar weather conditions prior to large scale application. In this work, anti-soil coatings on PV glass were tested outdoor in order to assess the effectiveness of the coatings as remedy for PV performance degradation upon exposure to environmental conditions of the Gulf region. Industrial anti-dust coatings on solar glass and uncoated solar glass; sample size ∼2.5 cm × 2.5 cm, were tested outdoor at Qatar Foundation's solar test facility (STF) in Doha. The coatings were hydrophobic (contact angle pre-exposure 83-90 degrees), while uncoated samples were hydrophilic (contact angle pre-exposure 34 -47 degrees). Measurements were taken pre-exposure (as received) and periodically upon exposure. The measurements were repeated after cleaning, which includes 3 day rain (Rain Clean), wash with free-running deionized (DI) water (DI-Clean), and wash with DI water with scrubbing (DI+S). The main test parameter of interest was radiant energy transmission properties. The impact of wind and humidity on energy transmission and the morphology and composition of the dust particles on samples were also analyzed. The following is a summary of the findings. Performance degradation due to dust is very high. Energy transmission loss of up to 37% was recorded during 13 weeks (week 8-week 20) of exposure, without dust storms (Fig. 1, 2).The advantage of coatings (over uncoated samples) is only marginal. Example, the average periodic energy transmission during week 8 –week 20 is < 1.5% higher for coated samples. Therefore, the tested anti-soil coatings seem not to offer significant remedy to performance degradation due to dust in Qatar. Patterned glass has better transmittance than plain glass, irrespective of coating type. Example, the average periodic energy transmission during week 8 –week 20 of exposure is ∼6% higher for patterned glass. The highest impact of dust in energy transmission is in the wave length range below 500 nm. This appears to be due to the high concentration of small (submicron) dust particles (see SEM images in Fig. 3).Cleaning recovers transmission to pre-exposure levels, except for shorter wavelengths (below 500 nm). This may suggest that smaller dust particles are difficult to remove. In-addition, presence of surface contaminants (non-dust-related) may require aggressive cleaning to remove.Dry wind appears to give a cleaning effect. Example, during W10 –W11, (Fig. 1) a period of fast winds (>2.5 m/s) and low humidity ( < 27%), energy transmission improved (instead of decreasing or remaining un-changed) for most of the samples. The morphology (Fig. 3) and compositions of dust on samples (Fig. 4) appear to be the constituents of the desert dust [5, 6]. However, dust particles exceptionally rich in Carbon (>30%), Iron (2%), Aluminium (>;4%) and Sulfur (>5%) have been observed. These may suggest existence of contribution from environmental activities such as transport and construction [7]. Dust particles with elevated amounts of Chlorine (3%) and Sodium (4%) have also been observed. These may indicate a contribution of salts from the sea [6, 7]. References [1] S. Semaoui, A. H. Arab, E. K. Boudjelthia, S. Bacha, and H. Zeraia, «Dust Effect on Optical Transmittance of Photovoltaic Module Glazing in a Desert Region,» Energy Procedia, vol. 74, pp. 1347-1357, 8// 2015. [2] Z. Abrams, P. Gonsalves, B. Brophy, and J. Posbic, «Field and Lab Verification of Hydrophobic Anti-Reflective and Anti-Soiling Coatings on Photovoltaic Glass,» Proceedings of the 29th EUPVSEC, pp. 2759-2764, 2014. [3] E. Klimm, T. Lorenz, and K. Weiss, «Can anti-soiling coating on solar glass influence the degree of performance loss over time of PV modules drastically?,» the 28th EUPVSEC, 2011. [4] E. Klimm, L. Ost, B. Spiegelhalter, and K. A. Weiss, «Tests of functional coatings on glass adapted to extreme - arid and maritime - climatic conditions for solar energy systems,» in Photovoltaic Specialist Conference (PVSC), 2015 IEEE 42nd, 2015, pp. 1-5. [5] T. Sarver, A. Al-Qaraghuli, and L. L. Kazmerski, «A comprehensive review of the impact of dust on the use of solar energy: History, investigations, results, literature, and mitigation approaches,» Renewable and Sustainable Energy Reviews, vol. 22, pp. 698-733, 6// 2013. [6] B. S. Yilbas, H. Ali, M. M. Khaled, N. Al-Aqeeli, N. Abu-Dheir, and K. K. Varanasi, «Influence of dust and mud on the optical, chemical, and mechanical properties of a pv protective glass,» Scientific Reports, vol. 5, p. 15833, 10/30/online 2015. [7] H. K. Elminir, A. E. Ghitas, R. H. Hamid, F. El-Hussainy, M. M. Beheary, and K. M. Abdel-Moneim, «Effect of dust on the transparent cover of solar collectors,» Energy Conversion and Management, vol. 47, pp. 3192-3203, 11// 2006.
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Experiment supported 2D COMSOL modeling of Fischer Tropsch Synthesis using Nonconventional media and Nonconventional catalyst
More LessFischer Tropsch Synthesis (FTS) is an exothermic chemical reaction in which synthesis gas (or ‘syngas’- a mixture of H2 and CO) is converted into hydrocarbons or value-added chemicals. In this process, a catalyst (typically cobalt based or Iron based) is used in a Fixed Bed (FB) or Slurry Bed (SB) reactor for the conversion process. Qatar hosts both the technologies in its world's largest Gas to Liquid (GTL) facilities (Shell Pearl GTL and Sasol Oryx GTL). Although both the technologies have been commercially implemented in a large scale, further process intensification by radial scale-up has been a challenging task due to certain process limitation associated with transport characteristics of both the beds. In particular, the FB technology has issues related to hotspot formation owing to exothermicity of the FTS process which is significantly better in its SB counterpart. Our efforts in the current study are invested to understand the FB performance when it is radially scaled-up to a higher reactor geometry, and to possibly mitigate the effect of hotspot formation. In particular, the objective of this work is to utilize the merits of nonconventional Supercritical Fluids FTS (SCF-FTS) to consolidate the benefits of both the beds (FB and SB) to address the challenges related to hotspot formation. For this, we have developed a multi-dimensional computational fluid dynamics (CFD) model in COMSOL® to facilitate a high-resolution understanding of both the SCF-FTS and conventional Gas Phase (GP)-FTS from the perspective of bed thermal management. As an extension to our previous modeling efforts in development of 1-D and 2-D FB-FTS model [1-2], we are currently involved in development of a multiscale 2D model to investigate the pore characteristics using both the modes of operation. Comprehensive experimental investigations were carried out at different operating conditions to support the modeling efforts. A conventional cobalt catalyst with inferior thermal conductivity was investigated in both GP-FTS and SCF-FTS. Later, a novel Micro-fibrous Entrapped Cobalt Catalyst (MFECC) with superior thermal conductivity was investigated in both GP-FTS and SCF-FTS. Conventional catalyst operated SCF-FTS conditions gave a very high value (0.90) than its GP-FTS. The MFECC catalytic bed on the other hand when operated in SCF-FTS conditions gave a slightly lower value (0.86), but six-fold % CO conversion than in GP-FTS. MFECC catalytic bed also exhibited higher C5+ selectivity & higher catalyst activity in SCF-FTS. In order to closely understand the intricate difference in thermal performance shown by the MFECC bed compared to conventional FB, we have performed a detailed CFD calculation. Results of the MFECC bed have shown to provide orders of magnitude improvement in bed thermal conductivity and proved its capability to control hotspot formation. In particular, the results of conventional FB at 20 bar and at a gas hourly space velocity of 5000 1/h in a reactor tube of 0.59 inch ID shows hotspot formation of about at the centerline. On the other hand, the temperature rise in MFECC bed for same operating condition was only. Further, a very recent outcome of this work enabled us to investigate the potential of scaling-up the radial geometry of the MFECC reactor to a 4” ID reactor to improve its throughput while maintaining temperature homogeneity in the reactor bed [2]. The proposed study is a part of a broader project involving both experimental and modeling studies, and is performed at multiple stages to enable mitigation of challenges related to reactor scale up, and runaway hotspot formation in a fixed bed FT reaction. References [1] M.M. Ghouri et al., Computers & Chemical Eng. 2016, 91, 38-48 [2] M.S. Challiwala et al., AIChE Journal, (Under Review)
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Density functional theory study of dry reforming of methane on nickel and nickel based bimetallic catalysts
More LessDry reforming of methane (DRM) reaction utilizes CO2, a major greenhouse gas to convert natural gas (mainly composed of methane) to synthesis gas, an important feedstock which could further be converted into valuable chemicals and cleaner fuel. This reaction presents a clear incentive in terms of its positive impact on the global environment and thus it has gained increasing attention in the last couple of decades. The superior catalytic activity of Nickel based catalysts and also their relatively lower costs make them the most promising catalyst for this reaction. However, these catalysts also deactivate rapidly owing to their high susceptibility to coke formation and filamentous carbon deposition. This severe catalyst deactivation is one of the major drawbacks that is obstructing the widespread commercialization of DRM. Several alternative catalysts have been explored for this reaction, including noble metals such as Rh and Ru. Even though these metals are found to be more reactive, as well as more resistant to carbon deposition, their high cost generally hinders their use [1]. One of the techniques that has been proposed to suppress the coke formation on the nickel surface is the substitution of single foreign transition metal atom which could modify the electronic structure [2]. In the current work, we present our exhaustive work on the solid state density functional theory (DFT) model results to study the wide network of elementary reactions comprising the DRM reaction on various facets of pure nickel catalyst, such as Ni(111) and Ni(100) surfaces. Calculations were performed using rev-PBE as exchange-correlation functional within the generalized gradient approximation (GGA) as implemented in the software VASP. Adsorption energies were calculated for all the DRM reaction intermediate species and then subsequently the activation barriers were calculated for all the elementary reactions in the DRM cycle. The catalytic activity of these pure nickel surfaces in terms of DRM reaction rate are then compared to the rates obtained on the single overlayer deposited nickel (X/Ni) surfaces where X is a transition metal such as Cu, Rh and Pd. Electronic structure analysis of various pure as well as overlayer modified surfaces is performed in terms of the d-band theory of catalysis. Our results indicate that the catalyst stability is greatly improved by a transition metal overlayer deposition on nickel surface. The carbon adsorption energy on a catalyst surface could be a good thermodynamic descriptor for estimating the coking tendency of this particular surface. One of the ways proposed in the literature to improve the coking resistance of a catalyst is to weaken the carbon adsorption energy. From a thermodynamic point of view, the decrease in the carbon adsorption energy on a catalyst surface would lower the surface coverage of carbon. This leads to a lower affinity for carbon deposition and an improvement of the coke reasistance of the catalyst. Our initial results indicate that the most stable adsorption energies of carbon on pure nickel surfaces are of the order of − 7.5 and − 8.96 eV respectively for the (111) AND (100) surfaces. Whereas, for the copper modified (111) and (100), the similar adsorption energies are of the order of − 5.62 and − 7.12 eV. This clearly shows that the copper modified nickel surface show an improved resistance for coking tendency and have lower affinity for carbon deposition.
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Polyelectrolyte membrane PEM and fuelcell catalyst studies using a miniaturized PEM fuel cell test fixture
Authors: Stephen Creager, Saheed Bukola and Rhett SmithAdvances in catalyst and electrolyte materials for hydrogen fuel cells are driving performance gains and cost reductions that are helping to bring hydrogen fuel-cell technology to market. Research on new materials is always a combination of synthesis and characterization, where characterization must eventually include incorporation of materials into an operating fuel cell. It is at this stage that research on leading-edge new materials often stalls, because conventional fuel-cell tests require relatively large amounts of material, e.g. several grams of a new catalyst and tens to hundreds of grams of ionomer, corresponding to many tens of square centimeters of membrane area, are required to run a comprehensive set of tests as is necessary to assure reproducibility and examine behavioral trends. These amounts of material are often not available in early-stage synthetic work, which means that characterization uses other approximate approaches, e.g. rotating disk electrode (RDE) voltammetry to study catalyst activity, with true fuel-cell testing often being delayed until syntheses may be scaled up. This situation is unfortunate because approximate tests often do not adequately screen materials. It would be desirable to run preliminary fuel-cell tests at an early stage to gain a better idea of materials properties before making decisions regarding which materials to scale up. This contribution will present our recent work building and using a miniature PEM fuel-cell test fixture that uses only very small amounts of material to conduct a true solvent-free fuel-cell test. The cell is fabricated from a conventional compression-style fitting and uses 5/8 inch diameter graphite or metal rods for gas delivery and for making electric contact with the electrodes. Membrane-electrode assemblies (MEAs) are made from 3/4-inch diameter PEM disks, typically cut from Nafion ionomer membrane, onto which carbon-cloth-based electrodes are bonded by hot pressing. Electrode diameters range from 1/8 to 3/8 inch. The presentation will include recent published work demonstrating reproducibility and select MEA characterization data, including in-situ voltammetry to assess electrochemically active surface area (ECSA) of catalysts and polarization curve measurements that are easily obtained using conventional linear sweep voltammetry with a conventional laboratory potentiostat. This situation is in contrast to conventional fuel-cell testing that requires specialized instrumentation with passage of very large currents, e.g. tens of amperes. Very recent work using the cells in hydrogen pump configuration will also be presented. This configuration is particularly useful for measuring resistances to proton transport through ionomers in the direction through the membrane plane, in contrast to most measurements which focus on in-plane resistance, because it is easier to measure. Very recent work on the synthesis and properties of new tetra-aryl-phosphonium (TAP) alkaline ionomers which are expected have high alkaline stability and to be good hydroxide-ion conductors, and on the effect of single graphene layers embedded in Nafion membranes on proton and other ion conduction through the Nafion membranes, will also be presented.
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