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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
21 - 40 of 656 results
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Integration of Photovoltaic Technology to Decentralized Liquefied Natural Gas-Fueled Combined-Cooling-Heating-and-Power Plants
Authors: Alexandros Arsalis and Andreas N. AlexandrouIn this study a decentralized combined cooling-heating-and-power (CCHP) plant fueled with liquefied natural gas (LNG) is integrated with photovoltaic (PV) technology to reduce fuel consumption and improve the economics of the CCHP plant. In their previous publications the authors have investigated the potential of an LNG-fueled CCHP at different configurations and system capacities, where the inclusion of PV technology was not investigated in detail. In this study the penetration of PV technology is analyzed in detail to reveal possible benefits. The modular nature of PV technology allows an opportunity for investigating power generation at different configurations. Additionally this combination shows a potential for reducing emissions and suggests a new concept of integrating an intermittent source of energy, such as solar energy. The proposed system is based on a realistic gas turbine cycle, integrated with a cooling plant and a district energy network. The detailed analysis of this study shows the thresholds of the proposed system to become an ideal candidate for distributed generation applications, especially in locations which are distant from centralized power plants. Therefore apart from reducing transmission and distribution losses, waste heat could be recovered effectively to generate heating, or cooling (absorption refrigeration technology). The system considers fueling with LNG, which is a safe and transportable fuel option. The simulation results show a potential for further investigation of the proposed system, since its performance results in significant thermodynamic and environmental improvements. The system can be operated in two modes: (a) winter operation, where recovered heat is distributed to the district energy network, (b) summer operation, where recovered heat is used to drive an absorption chiller-based cooling plant to generate cooling, which is also distributed to the district energy network. The average primary energy ratio of the proposed system is near 90%, which shows a potential for operation at high efficiencies. The cost analysis shows that the payback period is within a reasonable time frame; approximately 4 years. The system is modeled based on theoretical and experimental, including data from manufacturers’ datasheets and other assumptions. Each component and/or subsystem is modeled separately and coupled to every adjacent component, as described in the system configuration. All details, including specific assumptions are provided in the study. The values for all system input parameters are given, followed by a description of all subsystem and/or component models, i.e. CCHP plant, heat exchangers, cooling plant and district energy network. The cost model is described in detail, with all necessary cost functions and their input values, and also to allow a more realistic analysis of the feasibility potential of the proposed system a rigorous cost model is formulated. The main economic parameters evaluated are: projected total lifecycle cost (LCC), investment cost, operating cost and PP. The system model is validated using two commercially available gas turbines as reference cases, which include measured data from their respective manufacturer. Therefore the model input values correspond to the values taken from the references. The results of the model validation are given in detail in the study. The calculated error between the system simulation and the manufacturers’ data is low (0 to about 5%). Thereby, it can be assumed that the proposed system is modeled within an acceptable level of accuracy. The proposed CCHP system can be applied using different operational strategies, which may be based on either thermal energy (heating/cooling) or electricity demand. However to allow complete utilization of the generated thermal energy, the system must be based on a thermal energy-led operation. Therefore if it is assumed that the system operates at a constant, full power capacity (which also allows maximum net electrical efficiency), all generated thermal energy is delivered to buildings. The system is grid-interconnected to allow import/export of electricity, while the buildings are equipped with vapor-compression heat pumps, which will be operated the thermal energy supplied from the CCHP system is insufficient. The heat pumps are operated with electricity generated from the CCHP system. In the case of a CCHP system it is important to choose the set of consumers (buildings) that will allow an efficient matching of the generated vectors of energy with demand. The reason is that for example in the case of heating mode, high heat is required during the evening and early morning hours in households (due to high occupancy and low ambient temperature), while high heat demand occurs during daytime working hours in weekdays. A proposed small-scale, decentralized CCHP system is considered as alternative to conventional large-scale centralized, electricity-only generating power plants. The system is designed, modeled and analyzed in terms of thermodynamics, including cost analysis and exergy analysis. The results of the system model simulation show the potential of the proposed system in terms of efficiency. The system performs efficiently, with a PER of near 90%, and therefore the proposed system may become a significant candidate in the energy market, since fuel consumption and CO2 emissions can be reduced. The considered fuel is LNG, and with the proposed design approach of its regasification, the cooling energy can be used to cool the feed air before compression, which results to a net electrical efficiency of almost 2%, which is an attractive system modification for areas with prolonged summer-like weather conditions. Overall, when the proposed system is compared to an equivalent conventional system, results show significant improvement in CO2 emissions reduction (almost 40%) and primary energy savings (more than 40%). The exergy analysis shows that there is a potential for improvement of the exergetic efficiency through design modifications. Exergy destruction is higher in the combustor, the cooling plant and the heat exchangers responsible for recovering waste heat (i.e. HEx2 and HEx3). In the case of the cooling plant and the heat exchangers, the irreversibility is due to the conversion of high quality waste heat to low quality useful heating (or cooling). This is an unavoidable result due to the purpose of the proposed system, although exergetic efficiency could improve with the replacement of the double-effect absorption chiller with a triple-effect one. Also, theoretically, net electrical efficiency (and also exergetic efficiency) can be improved with the introduction of a combined cycle configuration, which is however a more complex and costly, and thereby an unfavorable option for distributed generation applications. The only possible and feasible modification for the current system design could be the optimization of the combustion process, by preheating the reactants or minimizing the use of excess air, although this could result in an impractical (or inflexible) system configuration.
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High-Voltage DC Integration of Photovoltaic Power by Front-End Isolated Quasi-Z-Source Converter Modules in Series
By Yushan LiuConsidering dc characteristics of Photovoltaic (PV), a higher voltage dc integration of PV power is expected to inherit the PV power's natural dc property, replace the bulky line-frequency transformer as the central inverter, eliminate the dc-side low-frequency pulsating power as the cascade multilevel inverter, and reduce power loss in distribution and transmission. However, due to the PV panel insulation demand, the voltage of series connected PV panels is restricted to one kilovolt. To overcome that defect, a quasi-Z-source modular cascaded converter (qZS-MCC) is proposed by series connection of front-end isolated qZS half-bridge (HB) dc-dc converter submodules (SMs). The qZS-HB is able to handle PV voltage and power variations, dc-link voltage balance, and HV-side dc integration. Thus, there is no requirement to control the front-end isolation converter. It greatly reduces the complexity of control and implementation comparing to that without qZS network, where the front-end isolation converters of all SMs require separate control method and gate driving. Simulation investigations based on high-power qZS-HB SMs and experimental results on downscaled prototype validated the proposed solution, providing a promising approach for the future integration and transmission of high-power PV systems.
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Environmentally Powered Smart Sensor Nodes in a Mesh Network Topology for Air Quality Diagnostic
Authors: Alessio Galli, Farid Touati, Damiano Crescini and Adel Ben MnaouerBackground & Objective: Air pollution is a major problem that has been recognised throughout the world for hundreds of years. In the middle ages, the burning of coal in cities released increasing amounts of smoke and sulphur dioxide to the atmosphere. In the late 18th century, the Industrial Revolution, beginning in the UK, led to escalation in pollutant emissions based around the use of coal by both homes and industry.Pollutant emissions continued to grow through the 19th and early 20th centuries leading to poor Air Quality (AQ). In more recent times, pollution from motor vehicles has become the most recognised AQ issue. Present pollution monitoring is revealing that if we don't act swiftly then vehicle pollution could harm our environment and reduce the quality of life for future generations. The number of cars, both in Qatar and in most countries around the world, is currently steadily increasing, and a speed up in technological development is required to combat the pollution problem. Poor AQ has negative effects on the environment and thus on our wellbeing. Air pollution from transport vehicles includes emissions of carbon monoxide, particulates, nitrogen oxides and dioxide, hydrocarbons and so on. Whilst much attention has been directed towards poor outdoors AQ we sometimes forget that we spend up to 90% of our time indoors. Consequently, keeping the air which we breathe at home clean is crucial, particularly for vulnerable people including babies, children, pregnant women and the unborn babies, the elderly, and those suffering from respiratory or allergic diseases such as asthma. Although in the majority of homes the indoor AQ (IAQ) is fairly good, CO, SO2, NO2 etc… are just some of the indoor air pollutants which can give cause for concern. The level of indoor air pollutants depends on factors such as outdoor air pollutants, construction materials and interior finishing, poorly-designed air conditioning and ventilation systems, and households and furniture (via outgassing from fabrics, paints, pets, etc.). Over-ventilation, as often thought, does not solve the problem. Nevertheless, this illusory solution is not adequate in the hot climate of the Gulf region as it leads to unacceptable levels in power demand. Sustaining economic and social growth is impossible without a holistic environmental vision that places environmental preservation for Qatar's future generations at the forefront. The QNV2030 aim to strike a balance between developmental needs (human, society, economy) and the protection of its natural environment, whether land, sea or air. Echoing international initiatives, Qatar has recently undertaken relentless intensive steps in an attempt to address the problem of AQ. The QNV2030 associated Qatar National Development Strategy 2011-2016 (QNDS 2011-2016), through a set of well-defined recommendations, stresses on the need to address the issues of environment and air pollution. To meet these needs, in this extended abstract we present SERENO (SEnsor and REceiver Node), a renewable energy-harvested sensor node that intelligently monitors air quality continuously without human intervention. This paper discusses the challenges of designing an autonomous system powered by ambient energy harvesting. Preliminary results demonstrate that, the presented platform could effectively report and trace air quality levels in a sort of set and forget scenario using a mesh network topology to cover as large as possible area deploying from tens to thousand nodes. Methods: The advances in low power electronics and in electrochemical sensors have enabled the development of low cost and power efficient air quality monitoring systems (dedicated to specific target gas and analysis) suitable for even stringent environments and disruptive locations, where air quality assessment is required without human intervention. Environmental energy harvesting technologies has been developed to maximize wireless sensor systems' lifetime and minimize energy consumption by adopting ultra-low power electronics (i.e. ultra-low power controller, low-power AO and CMOS switches). The use of virtually no-power consumed sensors (e.g. electrochemical sensors connected to signal conditioning electronics with supply current around 1 uA) coupled with wireless communication, working on the principle duty cycling (i.e. the device remains in low power SLEEP mode for almost 100% of the time) helps in maximizing the power efficiency and lifetime of the system. It makes the system operative only to perform designated tasks i.e. sensor warm-up, sampling, data processing and wireless data transmission or communication. The top view diagram of the renewable energy harvested system for air quality monitoring named SERENO is given below. Figure 1 shows the 6 sensors operative on the PCB. The general description of the proposed system is described below.
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Cross-Flow Microfiltration of a High Strength Industrial Wastewater: Modelling of Membrane Fouling Mechanisms
Authors: Mutiu Kolade Amosa, Mohammed Saedi Jami and Ma'an Fahmi R. AlKhatibFreshwater has become the blue gold of the 21st century due to its continuous depletion resulting from expanding population, shifting climates, urbanization and industrialization, and waterways pollution. Water reclamation is an orthodox alternative drought-proof source of water, and utility of membrane technology seems indispensable to every effective reclamation and reuse program due to its excellent features. However, fouling is a limiting factor of membrane separations, and in order to control particulate fouling at the design stage and plant operation monitoring, tools utilized in evaluating the particulate content of feed-water in predicting membrane fouling are vital. Subsequent to an adsorption process, a downstream cross-flow microfiltration (MF) membrane process was carried out on the final discharge effluent of palm oil mill industry at constant transmembrane pressures (TMPs) of 40 kPa, 80 kPa, and 120 kPa for 60 min filtration time using MF membranes of 0.1 and 0.2 μm pore sizes. Darcy's law and Hermia's blockage models were fitted to the experimental data and it was observed that cake filtration could be best used to explain the fouling mechanisms of effluent on the membranes based on the R2 values generated for the two MF membranes at all TMPs, however, not without the complete, standard and intermediate blocking mechanisms contributing at the onset of the filtration process. This demonstrates that the fouling was as a result of gradual reversible cake deposition which could easily be removed by less onerous cleaning methods. This data could serve as requisite for future upscaling of membrane processes for characteristically similar effluents with the aim of achieving sustainable fluxes.
Introduction
In the past few years, membrane filtration has been applied in the treatment of wastewaters especially in situations where cleaner water quality are sought. The populous utility of the membrane technology is due to its ability to stand up to scrutiny in providing uniformly quality water. Many of the wastewater treatment processes developed so far span across the use of sole membranes or with the integration of other treatment technologies be it for upstream or downstream treatment depending on the quality of the wastewater and the quality of permeate being pursued. However, there has always been the problem of membrane pore blocking or fouling. This phenomenon usually lead to the reduction of permeate flux which is equivalent to productivity. These blocking phenomena are usually categorized into four mechanisms; complete blocking, intermediate blocking, standard blocking and cake filtration. In order to control particulate fouling at the design stage, as well as for monitoring during a plant operation, methods utilized in evaluating the particulate content of feed-water in predicting membrane fouling are essential. The fouling tendency, usually represented by silt density index (SDI) and modified fouling index (MFI), involve a constant-pressure membrane filtration tests, thus, the indices are calculated from the experimentally determined relationship between filtration time and cumulative permeate volumes (Boerlage et al., 2002; Huang et al., 2008). In both tests, feed-water is filtered through a 0.45 μm microfiltration membrane in a dead-end flow at constant pressure. In order to accurately measure and predict particulate fouling, it has been proposed that specific MFI be investigated with respect to specific membranes since MFI0.45 cannot represent all membrane types. This is due to the fact that principal factors such as retention of smaller particulates, proof of cake filtration, membrane pore size, surface morphology, and material must be considered in such investigations (Boerlage et al., 2002). In this study, an optimized adsorption process operation condition was applied to a high strength wastewater (final discharge effluent of the palm oil mill) to reduce the strength of the wastewater and cut down its fouling potential. Fouling mechanism on microfiltration membranes after the upstream adsorption process was characterized at different TMPs, and the results were analysed in suggesting the sustainability of the membrane productivity and cleaning procedure. The results of the study could be applied to any feedwater of similar physicochemical make up.
Methods
Subsequent to an upstream adsorption process, explained elsewhere (Amosa, 2015; Amosa et al., 2015a; Amosa et al., 2015b), with the aim of reducing the blocking tendency of the industrial effluent, a laboratory-based bench scale system using a cross-flow membrane filtration process was operated. The system was equipped with two polyethersulfone (PESU) microfiltration membranes of 0.1 and 0.2 μm pores, and operated at constant transmembrane pressures (TMP) of 40, 80 and 120 kPa similar to previous reports (Springer et al., 2013). Permeate volume V at varying filtration time t data were recorded at each TMP, and the flux-time plots were used to evaluate the fouling propensities of the feed-water. The fouling mechanism of the feed on the membrane was further evaluated using the Hermia's revised blocking filtration models (Hermia, 1982) for complete, standard, intermediate and cake filtration as respectively represented in Eq. 1.0, 2.0, 3.0, and 4.0 were applied in describing and quantifying the blocking mechanisms that controls the membrane filtration at each TMPs. [1.0] [2.0] [3.0] [4.0] where Ac, B, Ai and C represent respective model constants, while J is the flux (Iritani, 2013).
Results and Discussion
Figure 1. Cake filtration model fitted to the 0.1 μm MF membrane filtration data at 40 kPa Fig. 1 shows the domineering cake filtration with the highest coefficient of determination (other plots shown in attached file). With this, it will be intuitive that the intermediate blocking model should be the closest in stability to that of cake filtration model from the principle, and this will serve as a confirmation for the establishment of cake layer formation in the membrane filtration. The closest R2 value after the cake filtration appeared to be that of the intermediate blocking mechanism with a value of 0.9336. This indicates that intermediate blocking had a strength of impact close to that of the cake filtration. This is because, from principle, there exist a region where the intermediate blocking plays a role between the transition phase of the complete and standard blocking, and that of the cake filtration mechanism. The intermediate blocking plot suggests that the transition phase is between 12 and 36 minutes of filtration time which serves as the best straight line of the plot. The complete and standard blocking models are expected to be the dominant mechanism at the onset of the filtration experiment. It is evident from their plots that the two mechanisms dominated the onset of the filtration as they both exhibited their somewhat best straight lines between 0.3-1.2 L, and 1.4-2 L of filtered volumes. This can also be observed from flux-time plot for 0.1 μm MF membrane in Fig. 1. These results followed the cake filtration mechanism as reported in earlier filtration modelling investigations (Boerlage et al., 2003; Boerlage et al., 2002). Table 2 shows the stability of the 0.1 μm MF membrane at various TMPs assessed by the determination of coefficients (R2) of the filtration models. Table 2. Fitting of filtration models to 0.1 μm MF membrane TMP (kPa) R2 of Filtration models Complete Blocking Standard Blocking Intermediate Blocking Cake Filtration 40 0.8357 0.8864 0.9336 0.9835 80 0.7521 0.8022 0.8676 0.9194 120 0.8032 0.8466 0.8967 0.9388 Fig. 2. Cake filtration model fitted to the 0.2 μm MF membrane filtration data at 40 kPa Table 3 below shows the results of filtration models as fitted to the filtration experiments performed using the 0.2 μm MF membrane. Table 3. Fitting of filtration models to 0.2 μm MF membrane TMP (kPa) R2 of Filtration models Complete Blocking Standard Blocking Intermediate Blocking Cake Filtration 40 0.6801 0.7537 0.8605 0.9167 80 0.5578 0.6346 0.7943 0.8388 120 0.561 0.6746 0.886 0.909 Summarily from Tables 2 and 3, it was observed that the operation at TMP of 40 kPa gave the best fitting models overall, and it also showed that cake filtration was dominant in the mechanism describing the filtration process with highest R2 values of 0.9835 and 0.9167 for 0.1 and 0.2 μm MF membranes, respectively.
Conclusion
A general model of cross-flow microfiltration treatment of final discharge of palm oil mill was successfully studied to elucidate the fundamental mechanisms involved in flux decline and fouling of the membrane. The cake deposition resulting from particulates aggregation accounted for the major flux decline. The cake filtration model dominated all other fouling mechanisms in terms of R2 values for both MF membranes and this indicates that the fouling involved did not affect the pore structure of the membrane. Both MF membranes were much stable at the lowest TMP of 40 kPa which amounts to lower energy consumption of the process. However, the 0.1 μm MF membrane exhibited higher stability in terms of its higher R2 value of 0.9835 as against 0.2 μm MF with a R2 value of 0.9167. Furthermore, with cake layer formation, it could be predicted that steady state filtration will be sustainably attained at longer filtration times without complete blocking. Also, fouling due to cake layer formation is reversible, this gives an idea of cleaning methods that may be necessary during process design. This data could be utilized for upscaling design in predicting the fouling behaviour of such effluents when subjected to microfiltration process.
References
Amosa, M.K., 2015. Process optimization of manganese and H2S removals from palm oil mill effluent (POME) using enhanced empty fruit bunch (EFB)-based powdered activated carbon (PAC) produced from pyrolysis. Environmental Nanotechnology, Monitoring & Management In press.
Amosa, M.K., Jami, M.S., Alkhatib, M.F.R., 2015a. Electrostatic Biosorption of COD, Mn and H2S on EFB-Based Activated Carbon Produced through Steam Pyrolysis: An Analysis Based on Surface Chemistry, Equilibria and Kinetics. Waste Biomass Valor, 1-16.
Amosa, M.K., Jami, M.S., Alkhatib, M.F.R., Jimat, D.N., Muyibi, S.A., 2015b. A Two-Step Optimization and Statistical Analysis of COD Reduction from Biotreated POME Using Empty Fruit Bunch-Based Activated Carbon Produced from Pyrolysis. Water Qual Expo Health 7, 603-616.
Boerlage, S.F., Kennedy, M.D., Aniye, M.P., Abogrean, E., Tarawneh, Z.S., Schippers, J.C., 2003. The MFI-UF as a water quality test and monitor. J. Membr. Sci. 211, 271-289.
Boerlage, S.F., Kennedy, M.D., Dickson, M.R., El-Hodali, D.E., Schippers, J.C., 2002. The modified fouling index using ultrafiltration membranes (MFI-UF): characterisation, filtration mechanisms and proposed reference membrane. J. Membr. Sci. 197, 1-21.
Hermia, J., 1982. Constant pressure blocking filtration law application to powder-law non-Newtonian fluid. Trans. Inst. Chem. Eng. 60, 183–187.
Huang, H., Young, T.A., Jacangelo, J.G., 2008. Unified membrane fouling index for low pressure membrane filtration of natural waters: Principles and methodology. Environ. Sci. Technol. 42, 714-720.
Iritani, E., 2013. A Review on Modeling of Pore-Blocking Behaviors of Membranes During Pressurized Membrane Filtration. Drying Technol. 31, 146-162.
Springer, F., Laborie, S., Guigui, C., 2013. Removal of SiO2 nanoparticles from industry wastewaters and subsurface waters by ultrafiltration: Investigation of process efficiency, deposit properties and fouling mechanism. Sep. Purif. Technol. 108, 6-14.
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Determination of Pesticide Residues of Organochlorine in Some Local and Imported Foods in Qatar
More LessFresh fruit and vegetables are an important part of a healthy diet as they are a significant source of vitamins and minerals. However, fresh fruits and vegetables can also be a source of toxic substances such as pesticides. Pesticides are a several and diverse group of chemical compounds, which applied to crops at various stages of cultivation and during production and post-harvest treatment of agricultural commodities. Recently, the government of Qatar has attempted to encourage agricultural production. Despite a noticeable increase in agricultural production in Qatar, however, this increase does not fulfill the need of residents in Qatar. Therefore, Qatar imports large amounts of food products from other countries which are large agricultural producers. The lack of information regarding pesticide residues in food in Qatar implies the necessity to determinate their concentrations in food items. Organochlorine pesticides (also known as chlorinated hydrocarbons) are primarily insecticides with relatively low mammalian toxicity, fat soluble and normally persistent in the environment. Many chlorinated hydrocarbons have the ability to accumulate inside the body due to their lipophilic nature. The study was aimed to examine the occurrence of organochlorine pesticides residues in some local and imported vegetables and fruits in Qatar, as a prelude to assess the risks related to their consumption. In order to achieve this aim, the following specific objectives were carried out: (i) determine the amount of 10 organochlorine pesticides (Heptachlor, aldrin, dieldrin, Endrin, a-chlordane, g-chlordane, endosulfane I, methoxychlor, α-BHC and β-BHC) in seven mostly consumed vegetables and fruits in Qatar using Gas chromatography-electron capture detector (GC-ECD), (ii) screen the residues of pesticides in these vegetables and fruits using scan mode of Gas chromatography- mass spectrometry (GC-MS), and (iii) perform statistical analyses to data obtained. A total of 127 samples of most 7 consumed fresh vegetables and fruit from local and import production were analyzed. The samples included: 26 samples of fruits and 101 samples of vegetables. Samples were extracted within 24 hours and stored at 4°C until the analysis. The simple random sampling and stratified random sampling were used as sampling procedures for collecting the vegetables and fruits. For all vegetables and fruits except strawberries, simple random sampling was used. For strawberries sampling, the stratified random sampling procedure was used. The EPA Method 8081 was chosen as a reference method for the preparation and extraction method with some modification. Additionally, the Dionex Application Note 332 “Accelerated solvent extraction of pesticide residues in food products”, 2012, was used as extraction method for vegetables and fruits. The fresh fruits and vegetables samples were collected from farms and market a day before extraction. Each sample was divided in to two groups: washed sample with water and unwashed sample. No sample digestion was needed prior to extraction. A clean-up procedure is usually carried out to remove co-extracted compounds that may cause interference in the chromatographic determination or be detrimental to the analytical instrumentation. Following extraction, 5 g of anhydrous sodium sulfate were added to the collection vial to adsorb co-extracted water. The vial was shaken for 15 s and the water-free extract was decanted into a clean vial. Two solid phase extraction techniques were used (Florisil and Silica Gel). The EPA method 3620C- Florisil Cleanup and Method 3630C- Silica Gel Cleanup were used as reference methods for cleaning the samples. All samples were cleaned up using 2 g Florisil Clean-Prep Cartridge. However, some interferants that are not removed by Florisil Cartridge would be removed by a second cleanup technique which was Silica Gel cleanup. For the Quality Control and Quality Assurance measures (QC/QA), the Limit of detection and limit of quantitation were calculated for all analytes. The LOD and LOQ were calculated using 10 samples of the lowest concentration of spike (10 ppb). The evaluation of the recoveries of studied pesticides were done by adding known concentration of an internal standard (Decachlorobiphenyl) to about 10% of total number of samples. The range from 93.6% to 106.6% was the percent recoveries in spiked samples. Residues of 10 OCPs (Heptachlor, aldrin, dieldrin, Endrin, a-chlordane, g-chlordane, endosulfane I, methoxychlor, α-BHC and β-BHC) were identified using GC/ECD. The GC/ECD analyses were performed on an Agilent 6890 N equipped with a splitless injector and a 7683 autoinjector. The analysis by GC/MS was carried out on an Agilent 7890A MSD 5973 equipped with a split/splitless Inlet and a 7683B autoinjector. Separations were conducted using an HP-1 30 m 0.25 mm 0.25 μm column for GC/ECD and Rxi-5SILMS 30 m 0.25 mm 0.25 μm column for the GC/MS. The GC/MS data were acquired and processed with a wiley7n.1 and NIST98 Libraries. The most frequently detected OCPs in the samples were heptachlor, g-chlordane and a-chlordane. Two statistical analysis tests were used to determine significance (pair-difference t-test and analysis of variance (ANOVA)). In most of the comparisons between the washed and unwashed samples, no-significant differences were observed (P > 0.05). Here, there is a dire require for controlling program for residues of pesticides in food products. Since florisil and silica were used for cleanup, heavy matrix interferences were observed in most of the samples, consisting primarily of fatty acids. Thus the detection and identification of trace levels of pesticides in this complex profile can be very time-consuming and laborious. The level of pesticide residues contamination may be considered a potential public health problem, since pesticides are characterized by various degrees of toxicity to non-target species, including human beings. The results underscore the need for regular monitoring of large samples to determine the pesticide residues, especially for the imported samples. This research can be implemented as a regular monitoring for the presence of OCPs in fruits and vegetables. Also the results of this research can be used as reference for future work. Future studies should consider the processing factors other than washing with tap water in order to account for the reduction or removal of pesticides such as: washing (with acetic acid, sodium chloride and soap) and peeling. Also as a recommendation, we need to look to other types of food that are sold in Qatar and may contain pesticides residues, such as grains and dates. Future studies also should look to the presence of other type of pesticides such as organophosphorous and carbamates compounds.
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Durability and Microstructure of Cement Composites Containing Qatar's Municipal Wastes
Authors: D. Deniz Genc Tokgoz, N. Gozde Ozerkan, Osama Kowita and S. Joseph AntonyQatar produces more than 2.5 million tons of municipal waste per year with an average waste generation rate of 1.8 kg/day/capita which is one of the highest rates in the world. The rapid growth of municipal solid waste has become one of the serious environmental problem that Qatar is facing with. Qatar's municipal waste is composed of organic and recyclables materials. Municipal solid waste incineration has been performed in Qatar since 2011. By incineration of wastes, not only the volume and weight of wastes are reduced but also energy is generated. Prior to incineration of municipal wastes, recyclables are separated from the waste and the remaining waste is incinerated at a minimum temperature of 850oC. Bottom ash and fly ash are produced as a result of incineration process. These by-products may contain heavy metals and pose a thread to the environment hence needs treatment and/or special disposal. Approximately 60 tonnes of fly ash is generated daily from municipal waste incineration in Qatar and this ash called as municipal solid waste incineration (MSWI) fly ash. This MSWI fly ash is stabilised with cement and then disposed into special landfill. However, cementitious property of MSWI fly ash due to similar mineralogical composition with cement and its finer particle size may favor its potential utilisation in cement based materials. As aforementioned before, 40% of municipal waste of Qatar is composed of recyclables of which 14% is plastic. The major portion of plastic wastes, about 90% of total, are composed of light density polyethylene (LDPE) and high density polyethylene (HDPE) wastes. Therefore, there is a huge potential for recycling of PE wastes in Qatar considering the shortage of raw materials i.e. natural aggregate for construction industry. The scarcity of available land for disposal of municipal wastes and limited natural resources of raw materials for construction industry has opened new research areas for proper disposal and recycling of municipal wastes. Therefore, in this research work, municipal solid waste incineration (MSWI) fly ash and municipal polymeric wastes were used as secondary raw materials for the preparation of cement based composites. MSWI fly ash was utilised as partial replacement of cement by 10% by weight. Polyetyhlene wastes in granular form were utilised as partial replacement of natural aggregate by 10% by volume. Portland cement, silica fume (10% by weight) and MSWI FA (10% by weight) at constant rates were used as binder in all cement-based composites. Three different cement based composites were fabricated by partial substition of natural aggregate with LDPE and HDPE wastes at 0 and 10% by volume. The mixture without PE waste substitution was called as the reference mixture, with LDPE waste was called as Mix 1 and with HDPE waste was called as Mix 2. Besides mechanical performance, durability of fabricated cement composites containing municipal wastes was investigated to determine if their utilisation has positive contribution or adverse impact. The durability properties were examined by performing drying shrinkage and expansion under sulfate exposure tests. Scanning electron microscopy coupled with EDX were used to determine the degradation products of sulfate exposure. In terms of mechanical strength, samples containing PE wastes showed lower strength at early ages due to weaker bonding between LDPE/HDPE and the cement matrix. At later ages, strength improvement was observed and comparable strength values for Mix 1 and Mix 2 were measured with respect to the reference. The effect of utilisation of municipal wastes on the dimensional stability of cement composites was evaluated by measuring the variation of length change at 4, 11, 18, 25, 126 and 168 days of air drying. This test showed that incorporation of PE wastes (Mix 1 and Mix 2) reduced the drying shrinkage and provided better dimensional stability compared to the reference. Sulfate attack is known as one of the most deleterious effects on cement based composites due to the formation of expansive degradation products. To investigate the sulfate resistance of fabricated composites, the length change at 1 week, 2 weeks, 3 weeks, 4 weeks, 8 weeks, 13 weeks, 15 weeks, 4 months and 6 months of sulfate exposure was measured. Both the reference and samples containing PE wastes did not show any visual deterioration except a white and soft layer formed on top of all samples. The length change indicated that composites containing PE wastes experienced reduction in expansion compared to the reference and hence considered as more durable for external sulfate attack. More voids and pores were present in PE incorporated samples, therefore sulfate degradation products probably filled these pores and resulted in lower expansion compared to the reference. There was no significant difference between the mechanical performance and durability of cement composites containing LDPE and HDPE. The microstructure and composition of sulfate degradation products were investigated by SEM-EDX. The decalcification of the C-S-H phase were detected in each sample. Gypsum, calcite and thaumasite were identified as the major deterioration related products, while ettringite was found at trace level. This laboratory study showed that MSWI fly ash and PE wastes can be utilised together to produce durable cement based materials with a lower carbon footprint. Keywords: Municipal solid waste incineration, sulfate attack, thaumasite, ettringite, shrinkage, expansion
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The computational design of Pb free and stable hybrid materials for solar cells
More LessFadwa El Mellouhi1, Akinlolu Akande2, Sergey Rashkeev1, Mohamed El-Amine Madjet1, Golib Berdiyorov2, Carlo Motta2, Stefano Sanvito2 and Sabre Kais1, Fahhad Alharbi1
1Qatar Environment and Energy Research Institute, Hamad Bin Khalifa University, Qatar Foundation, Doha, Qatar
2School of Physics and CRANN, Trinity College Dublin, Ireland
In the past four years, the solar cell field has experienced an unprecedented meteoritic emergence of a new family of solar cell technologies; namely, perovskites solar cells (PSC) using (CH3NH3)PbI3 as absorber. [1] However, two main challenges prevent deploying PSC technology: the presence of the toxic element lead (Pb) and their structural instability.
The CRANN-QEERI initiative for Solar Energy Harvesting Materials (CRAQSolar project) aims at establishing a new research protocol for the rational and rapid design of advanced materials for solar energy harvesting. This will drastically accelerate the time necessary for materials discovery and will allow us to produce a new generation of photovoltaic compounds displaying high efficiency, ease of manufacturability, longevity and low costs. Our research protocol is based on the rational design of new compounds by means of state-of-the-art high-throughput electronic structure theory, followed by synthesis, processing and characterization. In particular we will target both chemical synthesis and liquid phase processing, two protocols, which guarantee handling of materials at low temperature and low costs. The grand objective of CRAQSolar is that of revolutionizing such cycle and to provide a way for producing a significant pallet of new promising compounds for further optimization. In particular the project has two targets:
Objective 1: Developing new hybrid organic/inorganic perovskites (HOIPs) with robust solar harvesting efficiency but also useful thermal and mechanical stability. These should be synthesized/processed chemically and have mobility superior to their all-organic counterparts.
Objective 2: Developing a range of compounds made of 2D materials (such as MoS2, TiS2, GaS, etc.) with strong light absorption properties and long-living excitons. These will be processed from the liquid phase so that solar cells devices may be produced by ink-jet printing.
We conducted extensive density functional theory (DFT) calculations on the prototypical light absorbing perovskite, CH3NH3PbI3, in its cubic phase, by taking into consideration the experimentally reported evidence of the fast rotation of CH3NH3 at room temperature. This compound has the standard AMX3 perovskite structure, where the cation position, A, is taken by methyl-ammonium, CH3NH3.
Ground-state total energies and forces were computed using DFT calculations with the FHI-aims all-electron quantum chemistry code [2]. These were used to optimize the crystal geometry, without the use of constraints. The GGA in the Perdew-Burke-Ernzerhof (PBE) parameterization was employed. Long-range van der Waals interactions have been taken into account via the Tkatchenko and Scheffler (TS) scheme [3]. The reciprocal space integration was performed over an 8 × 8 × 8 Monkhorst-Pack grid after performing convergence tests on the energy and forces.
Our pioneering work for this class of material consisted of lifting the limitation imposed in previous studies on the orientation of the organic molecule. This means that we did not limit our analysis to CH3NH3 oriented along the (100) or the (111) direction, for which the high Oh symmetry is maintained, but we also explore cases where the symmetry was lowered. Our main conclusion was that such symmetry lowering has profound consequences on the electronic structure namely that the bandgap changes from direct to indirect depending on the orientation of the CH3NH3 group.[4] Crucially such symmetry-lowering configurations represent local minima in the free energy surface of the crystal and they are stabilized by van der Waals (vdW) interactions. These are the key ingredients not only for obtaining accurate lattice parameters but also for the internal geometry. Our calculations then return a picture of the CH3NH3PbI3 as a “dynamical” bandgap semiconductor, in which the exact position of the conduction band minimum depends on the particular spatial arrangement of the molecules. Importantly our results are robust against bandgap corrections and spin-orbit interaction, and deliver an absorption spectrum in good agreement with experimental data near absorption edge.
These preliminary studies suggest that better efficiency might be achieved by seeking novel molecules maybe combined with different halides in order to enhance the symmetry breaking in these compounds. Our finding thus offers a design strategy to increase the efficiency of hybrid halide perovskites. This also lays a foundation in screening and designing alternative nontoxic lead-free materials.
The two classes of compounds selected for CRAQSolar's exploration encompass some among the most promising materials for developing a solar energy harvesting technology. In particular, since both can be grown and processed chemically from the liquid phase, they offer the possibility of achieving high energy-conversion efficiency, while maintaining low fabrication costs. Furthermore, these are families of compounds comprising a vast number of members with highly tunable properties, so that they are the ideal platform for a large-scale search.
Our efforts to design lead free family of hybrid materials demonstrate that the design of hybrid materials containing organic cations might require careful considerations among them the size of the cell used during the screening process. Our strategy will be presented as well as some resulting promising compounds.
Acknowledgement
Computational resources are provided by research computing at Texas A&M University at Qatar and the Swiss Super Computing Center(CSCS). This work is supported by the Qatar National Research Fund (QNRF) through the National Priorities Research Program (NPRP 8-090-2-047)
References
[1] M. Peplow, “The perovskite revolution [news],” Spectrum, IEEE, vol. 51, no. 7, pp. 16–17, 2014.
[2] V. Blum, R. Gehrke, F. Hanke, P. Havu, V. Havu, X. Ren, K. Reuter and M. Scheffler, Ab initio molecular simulations with numeric atom-centered orbitals, Comp. Phys. Comm. 180, 2175 (2009).
[3] A. Tkatchenko and M. Scheffler, Accurate molecular van der Waals interactions from ground-state electron density and free-atom reference data, Phys. Rev. Lett. 102, 073005 (2009).
[4] C. Motta, F. El Mellouhi, S. Kais, N. Tabet, F. Alharbi, and S. Sanvito, Revealing the role of organic cations in hybrid halide perovskites CH3NH3PbI3, Nature Communications 6, Article number:7026 (2015) (doi:10.1038/ncomms8026)
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Fabrication of Selective Sensors for Hg 2+ Traces in Water Using Graphene Decorated with Metal Nanoclusters
Authors: Ahmad I. Ayesh, Zainab Karam, Falah Awwad and Mohammed A. MeetaniMercury metal is released into water by different sources including sewage industrial waste, thus, it can enter human food chain. It is considered one of the most harmful pollutant of heavy metals since it is non-biodegradable, and it can enter to human body by different means including direct consumption (for example, through drinking water), absorption through skin, and by respiratory system. Exposure to mercury cause severe effects on human health such as brain damage, kidney failure, damage in the nervous system, birth defects, chromosome breakage, and paralysis [1, 2]. The United Nation Environment Program (UNEP) assessed the annual released quantity of mercury to 4400-7500 tons [3]. In addition, the International World Health Organization regulated the maximum allowed amount of mercury ions (Hg2+) in drinking water to 6 ppb [4]. Nevertheless, previous studies estimated the allowed amount of inorganic Hg2+ in water to 0.5 ppb [5]. Therefore, the development of sensitive, selective, reliable, and cost effective Hg2+ sensors is needed for medical diagnostic, quality control of food industry, as well as water and environment quality monitoring. In this work, we present novel conductometric sensors based on graphene and Au nanoclusters that are highly selective to Hg2+ ions. Electrical electrodes were deposited on the surface of graphene by thermal evaporation. Au nanoclusters were produced by sputtering and inert gas condensation technique inside an ultra-high vacuum chamber, and they were self-assembled on the surface of graphene. To the best of our knowledge, the sensors reported here are the first conductometric sensors based on graphene and Au nanoclusters that are utilized for detection of Hg2+ traces in water. These sensors were exceedingly sensitive to Hg2+ ions, therefore, they have potential to be applied for practical life applications. Gold nanoclusters were produced by the sputtering and inert gas condensation technique inside an ultra-high vacuum system. The system consists of three main chambers (source, mass filter, and deposition chambers) that were pumped initially to a base pressure of 10-8 mbar using two turbo pumps. A gold target of purity 99.99% (Testbourne ltd, UK) was fixed on a water-cooled magnetron sputter head. Plasma was generated inside the source chamber using argon (Ar) inert gas, and it was used to sputter Au from its target through dc discharge type. The supplied Ar gas was also utilized to condense the sputtered material forming nanoclusters, and to create pressure gradient between the source and deposition chambers that enables the formed nanoclusters to travel to the deposition chamber. Each Hg2+ sensor was fabricated using (1 cm × 1 cm) commercial graphene layer on SiO2/doped-Si substrate (thickness of SiO2 is 285 nm, and Si is p-type with resistivity of 0.001-0.005 ohm.cm). Interdigitated parallel Au electrodes (with electrode separation of 100 μm) were fabricated by thermal evaporation using a Torr International evaporator through a shadow mask on the surface of graphene [6]. Two batches of sensors were tested in this work: i) sensors based on graphene only, and ii) sensors based on graphene and percolating films of Au nanoclusters, each has a thickness of 5 nm. For nanocluster deposition, each graphene sample was fixed on a cryostat finger. Nanocluster deposition rate was initially measured using a quartz crystal monitor (QCM) facing nanocluster beam and was fixed on a motorized linear translator. Next, the QCM was removed away from the sample, thus, nanoclusters were deposited on graphene surface. Sensitivity measurements were performed using Hg2+ solutions with different concentrations (0.05, 0.1, 0.3, 0.6, 3, 6, 20, 40, and 60 ppb). The selectivity was tested using 0.6 ppb solutions of the following ions: Cr2+, Cd2+, Cu2+, Co2+, Fe2+, Zn2+, and K+. The selectivity results of the sensor reveal that the fabricated sensors are selective to Hg2+ ions, and the selectivity is evidently enhanced for sensors with Au nanoclusters. The sensitivity of sensors decorated with Au nanoclusters to Hg2+ ions is higher than that for sensors made of graphene only, which could be assigned to the high binding affinity of Au nanoclusters to Hg2+ ions [7, 8]. This can be explained qualitatively bearing in mind previous studies that investigated the binding energy of the metal ions (under consideration in this work) with either graphene or Au nanoclusters. Upon investigating the binding energy of metal ions with graphene, it was reported that Hg2+ ions have the highest binding energy to graphene compared to other ions (Cr2+, Cd2+, Cu2+, Co2+, Fe3+, Zn2+, and K+), which exhibit slightly lower binding energy to graphene and thus their sensitivity signals are very comparative [8]. The sensitivity of Au nanostructures to Hg2+ ions was found to be large due to their high binding energy [7]. In addition, the binding energy of Hg2+ ions to Au nanostructures is evidently higher than that to the other metal ions investigated in this work [9], which makes the graphene-Au sensor selective to Hg2+ ions. The sensing mechanism of the graphene-based sensors can be summarized as follows: exposure of the graphene sensor to Hg2+ ions decreases electron concentration in the n-type graphene, thus, the conductance of the sensor decreases. Decoration of graphene with Au nanoclusters creates electron scattering centers that increase electron diffusive scattering which decreases electrical conductance. Adsorption of Hg2+ ions on Au nanoclusters causes further decrease in the conductance, which implies the increase in the sensitivity and selectivity of the sensor. In conclusion, the sensitivity of the present sensors is below the minimum allowed limit of Hg2+ in drinking water set by the World Health Organization and that set by the United States Environmental Protection Agency. These sensors are small in size and easy to carry outdoor and have low power requirements, thus, they have a potential to be used for practical field applications.
References
[1] W. Chemnasiri, F.E. Hernandez. Gold nanorod-based mercury sensor using functionalized glass substrates, Sensors and Actuators B: Chemical 173 (2012) 322-328.
[2] Y. Li, H. Huang, Y. Li, X. Su. Highly sensitive fluorescent sensor for mercury (II) ion based on layer-by-layer self-assembled films fabricated with water-soluble fluorescent conjugated polymer, Sensors and Actuators B: Chemical 188 (2013) 772-777.
[3] B. Wang, S. Zhuo, L. Chen, Y. Zhang. Fluorescent graphene quantum dot nanoprobes for the sensitive and selective detection of mercury ions, Spectrochimica Acta Part A: Molecular and Biomolecular Spectroscopy 131 (2014) 384-387.
[4] WHO. Guidelines for drinking-water quality. Fourth edition ed., World Health Organization, 2011.
[5] E. U.S. Drinking Water Contaminants. http://water.epa.gov/drink/contaminants/index.cfm#list, 2011.
[6] A.I. Ayesh. Electronic transport in Pd nanocluster devices, Applied Physics Letters 98 (2011) 133108.
[7] Z. Liu, P.C. Searson. Single Nanoporous Gold Nanowire Sensors, The Journal of Physical Chemistry B 110 (2006) 4318-4322.
[8] C. Yu, Y. Guo, H. Liu, N. Yan, Z. Xu, G. Yu, Y. Fang, Y. Liu. Ultrasensitive and selective sensing of heavy metal ions with modified graphene, Chemical Communications 49 (2013) 6492-6494.
[9] S.A. Siddiqui, N. Bouarissa, T. Rasheed, M.S. Al-Assiri. Quantum chemical study of the interaction of elemental Hg with small neutral, anionic and cationic Aun (n = 1-6) clusters, Materials Research Bulletin 48 (2013) 995–1002.
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Detection and Location of Subsurface Voids Using Seismic Transmission Data
More LessKarst is ubiquitous on the peninsula of Qatar, including depressions, sinkholes, and caves. Faulting and fractures play a major role in the development of karst, where fluids find pathways through limestone and dissolve the host rock. The resulting fissures may grow larger as more surface water is funneled through to form cavities or karst. Sinkholes may also form, when cavern roofs collapse, and it is this last characteristic that is of concern to rapidly growing metropolitan areas, that expand in heretofore unexplored regions. Qatar has seen a recent boom in construction, including the planning and development of complete new sub-sections of metropolitan areas. Before planning and construction can commence, the development areas need to be investigated to determine their suitability for the planned project. Of particular concern are ubiquitous karst features that are prone to collapse, particularly when surface loading is increased due to the construction of new buildings. In this paper, we present the results of a study to demonstrate a variety of seismic techniques to detect the presence of a karst analog in form of a vertical water-collection shaft located on the campus of Qatar University, Doha, Qatar. Seismic waves are well suited for karst detection and characterization. Voids represent high-contrast seismic objects that exhibit strong responses due to incident seismic waves. However, the complex geometry of karst, including shape and size, makes their imaging nontrivial. While karst detection can be reduced to the simple problem of detecting an anomaly, karst characterization can be complicated by the 3D nature of the problem of unknown scale, where irregular surfaces can generate diffracted waves of different kind. In our current paper we build upon previous results (Gritto et al, 2015) and employ a variety of seismic techniques to demonstrate the detection and characterization of a vertical water collection shaft analyzing the phase, amplitude and spectral information of seismic waves that have been scattered by the object. The experiment consisted of seismic transmission and reflection surveys, using a 10 kg sledge hammer as a source and three-component 10 Hz geophones to record the data. We used the reduction in seismic wave amplitudes and the delay in phase arrival times in the geometrical shadow of the vertical shaft to independently detect and locate the object in space. Additionally, we use narrow band-pass filtered data combining two orthogonal transmission surveys to detect and locate the object. Our analysis showed that ambient noise recordings may generate data with sufficient signal-to-noise ratio to successfully detect and locate subsurface voids. This is a result of the low intrinsic attenuation of seismic waves by the limestone and dolomite rocks that are ubiquitous throughout Qatar. Being able to use ambient noise recordings would eliminate the need to employ active seismic sources that are time consuming and more expensive to operate.
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Effects of Combined Calcium Hypochlorite and Chlorine Dioxide on Drinking Water Quality in Qatar and Disinfection by Products Formation
Authors: Elsamoul H. Mohamed, Joseph A. Cotruvo, Mustafa M Osman and Hassan I. NimirChlorite, chlorate, bromate and trihalomethane's (THMs) are included in WHO guidelines for drinking water quality. This study examined dosing different chlorine concentrations as calcium hypochlorite (Ca(ClO)2) to water containing chlorine dioxide to evaluate the control of water quality in storage and the distribution system in Qatar with emphasis on chlorite, chlorate, bromate, pH and other parameters. Seven water samples were collected from the Ras Laffan-Q Power desalination plant outlet in amber bottles having a chlorine dioxide concentration of 0.3 mg/l in 1 liter. The bottles were spiked with Ca(ClO)2 in sequence to give concentration of 0.2, 0.4, 0.6, 0.8, 1.0, and 1.2 mg/l as free chlorine. The mixtures were stored for 7 days at 25°C in the dark then heated to 45°C for two days more, and analyzed daily for physical and chemical parameters. A total of 312 sub-samples were analyzed for chlorite, chlorate, bromate, bromide, chloride, nitrate, nitrite, sulfate, THMs, temperature, pH, electrical conductivity, and chlorine and chlorine dioxide residuals. Chlorite concentration reductions were observed from the first day forward as 59, 65, 68, 94, 100, and 100%, and 17.4, 22.1, 39.2, 63.9, 66.0, 68.9% (from 0.157 to 0.049 mg/l) respectively based on observed means for seven days the commensurate respective chlorate concentrations increases were 196, 344, 516, 602, 703, 787% (from 0.035 to 0.313 mg/l) based on observed mean values for seven days. These data were statistically analyzed by multivariate regression. There were no significant changes in THMs concentrations and the reductions in chlorite and increases in chlorate concentration are chlorine dosage dependent. No bromate formation was observed. Chlorine dioxide levels decrease as the free chlorine residual levels increased. This study demonstrates that hypochlorite/chlorine can be used as an operational tool to control the chlorite levels, and slow the disappearance of the chlorine dioxide over time during distribution, that is usually faster than chlorine disappearance. The original chlorine dioxide dosage will determine the ultimate chlorate concentration, which must also be managed.
References
EPA guidance manual Alternative Disinfectants and Oxidants EPA 815-R-99-014, April 1999. 9-1 and 9-25.
WHO, Guidelines for drinking-water quality, fourth edition. 2011(1)179,180, 325 and 326.
E. Marco. Aieta, Paul V. Roberts; Kinetics of the reaction between molecular chlorine and chlorite in aqueous solution Environ. Sci. Technol., 1986.
Daniel P. Hautman and David J. Munch. EPA - Method 300.1. Determination of inorganic anions in drinking water by ion chromatography Revision (1.0) 1997.
J.W. Eichelberger, J.W. Munch, and T.A.Bellar EPA Method-524.2. Measurement of Purgeable Organic Compounds In water by capillary column gas chromatography/mass spectrometry, (Revision 4) 1992.
Charles Z. Steinbergs, Removal of By-products of Chlorine and Chlorine Dioxide at a Hemodialysis Center 1986. Katherine Alfredo, The Potential Regulatory implications of Chlorate (AWWA), March 2014.
C.J. Volk, R. Hofmann, C. Chauret, G.A. Gagnon, G. Ranger, and R.C. Andrews, Implementation of chlorine dioxide disinfection: Effects of the treatment change on drinking water quality in a full-scale distribution system 2002.
Mary Ann H. Franson, Standard methods for the examination of water and waste water 2005 (21st, Edition) 4-67 and 4-79.
Ron Hofmann, Robert C. Andrews, and Georges Ranger, Water Quality and Disinfection Impact of ClO2 Contamination by free Chlorine: A Case Study (NRC Canada) 2004.
Mj Bekink and DJ Nozaic, Assessment of Chlorine Dioxide Proprietary Product for Water and Wastewater Disinfection May 2012.
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Hydrogen Production via Ethanol Decomposition over Bimetallic Catalyst
By Anchu AshokBimetallic catalyst shows distinct physical and chemical properties differ from its monometallic catalyst due to the high synergy between the monometals. Bimetals of transition metals shows different applications in the field of catalysis, batteries and solar energy conversion etc. CuCo bimetallic catalysts are excellent candidate for the applications in the field of heterogeneous catalysis, solid state sensor, energy storage devices, and lithium-ion batteries. With the increase in fuel cell application, need of H2 source also rises. H2 can be extracted from the hydrogen rich precursors of light alcohol such as methanol and ethanol that can be produced from corn stover, starch containing materials and other biomass byproducts. Ethanol is low toxic and easy handling renewable source for H2 production for fuel cell applications and the production of ethanol is environmentally sustainable. Transition metal possess high C-C cleavage bond which is an indispensable property in ethanol conversion. Steam reforming, partial oxidation, dehydrogenation and decomposition are the main routes for the hydrogen generation from ethanol. Out of these, decomposition technique is a low temperature process and suitable for small scale fuel cell applications e.g. charging cell phones, computers etc. We follow decomposition route for H2 production along with other necessary byproducts. Bimetallic CuCo catalyst shows good performance during ethanol decomposition for hydrogen production in the temperature range of 50°C-400°C. Various physical and chemical techniques (such as thermal method, precipitation methods, pyrolysis process, sonochemical method, polyol method, microwave irradiation, sol-gel process, combustion method etc.) have been reported for the synthesis of different morphological structures of bimetallic nanoparticles In this work we are following combustion synthesis method to prepare cobalt catalysts which have been reported to be active for ethanol-hydrogen production. This work focuses primarily on understanding the reaction mechanism leading to various products using in situ DRIFTS studies. Combustion synthesis was opted for synthesis due to various advantages such as low energy requirement, single step, fast and economic synthesis process as it does not require expensive equipment. In Solution Combustion Synthesis (SCS) the precursors were mixed to form a homogenous solution and heated it over the hotplate heater to initiate the combustion process which resulted in the synthesis of nanoparticles with uniform properties. Typically, it consist a redox reaction of the homogeneous mixture of metal nitrate (oxidizing agent) and oxygen containing fuels (reducing agent) such as glycine, urea, glucose, citric acid etc. The reaction between NH3 and HNO3 released during decomposition of glycine and metal nitrate respectively produces the energy required for single step combustion synthesis. At higher value of φ, the reactive medium generates H2 rich reducing environment to convert metal oxide to metallic form Bimetallic CuCo were synthesized from the aqueous solution of cobalt nitrate (Co(NO3)2·6H2O), copper nitrate (Cu(NO3)2·6H2O) and glycine (C2H5NO2) in solution combustion synthesis (SCS) method using a fuel to oxidizer ratio of φ 0.5, 1, 1.75 and 2.5. The amount of precursors was calculated based on the synthesis of 1.5 g product in the output. These precursors were mixed in 75 ml of water and stir continuously for 1 hr to form a homogenous mixture. The solution was heated over a hot plate heater until all the water got evaporated. Once it reaches the ignition temperature, the combustion reaction started locally at one point and then spread inside the beaker. The resulted powder was grinded using a mortar and pestle to get a uniform powder to be used for catalytic investigations. Synthesized particles were characterized using XRD, SEM and TEM. Ethanol decomposition over bimetallic CuCo were conducted using in situ diffuse reflectance infrared fourier transform spectroscopy (DRIFT) study under N2 flow at different temperatures (50, 100, 200, 300, 400°C). Temperature-time profile of CuCo shows an increase in combustion temperature with increase in fuel ratio with maximum temperature at φ = 1 (stoichiometric ratio) and after that it decreases. The XRD shows the presence of copper-cobalt component in their oxidized states. Theoretical studies shows increase in particle size with maximum flame temperature. Crystalline size calculation using Scherrer formula shows the same trend in particle size calculation as in Table 1. SEM of as-synthesized nanoparticles of cobalt oxide at different molar ratios from 0.5 to 2.5 in SCS mode shows the nanoparticles of high porosity that are randomly distributes as well as agglomerated. Mostly this high porosity is due to the escaping of excess gases during combustion process. Also the EDS results are in consistent with the XRD results showing higher amount of oxide in the synthesized CuCo compound. TEM image in Fig. 1 also shows agglomeration that is common in solution combustion mode with non-uniform sized particles. Copper-cobalt oxide synthesized using combustion technique has been reduced to pure nanocrystal by passing hydrogen in the reaction chamber at 300°C. An FTIR spectrum at 50 and 100°C shows the presence of adsorbed ethanol and ethoxy species over the reduced catalyst. IR band at 3669 cm− 1 indicates the presence of OH from adsorbed ethanol on the catalyst surface. At higher temperature the molecularly adsorbed ethoxy species is converted into acetate species along with the presence of carbonate species. After increasing the temperature from 200°C the intensity CO2 band at 2335-2367 cm− 1 is evident. At this temperature the acetate species are dehydrogenated to acetaldehyde and other intermediate species. Strong acetate band of 1760 cm− 1 above 200°C could be due to the transformation of acetaldehyde formed by the dehydrogenation of ethanol to either ethyl acetate or acetic acid though the nucleophilic reaction of ethoxy or hydroxyl species with the surface aldehyde. The presence of IR band between 2830-2695 cm− 1 shows the presence of aldehyde group in the decomposition reaction. At higher temperature, the presence of carbonate species is evident with the carbonate layer formation from SEM and TEM images. This carbon layer at higher temperature hinders the action of catalyst in ethanol decomposition reaction.
Acknowledgement
This publication was made possible by JSREP grant (JSREP-05-004-2-002) from the Qatar national research fund (a member of Qatar foundation). The statements made herein are solely the responsibility of the author(s). The authors also wish to acknowledge the technical services granted by Central Laboratory Unit (CLU) and Gas Processing Centre (GPC) at Qatar University along with QU internal grant (QUUG-CENG-CHE-14/15-9) to support this research
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Remote Sensing for a Sustainable Coastal Management
Authors: Dries Raymaekers, Els Knaeps and Ruben Van De KerchoveOur coastal ecosystems are extremely vulnerable and encounter pressures from natural hazards, climate change and coastal development leading to e.g. habitat loss, coastal erosion and pollution. Remote sensing can contribute to a sustainable coastal management and development by providing area wide information on i) the status and evolution of the coastal vegetation, coral reefs and ii) near real time and historic information on the water quality. These remotely sensed data will significantly contribute to our knowledge of the coastal zone and will complement more traditional field measurements and modelling efforts. In particular the recently launched sensors such as Sentinel-2 and Landsat-8, with a spatial resolution of 10 and 30 m respectively, allow for a factor 10 improvement in spatial detail. This means that remote sensing can now be used to monitor small scale coastal features such as harbors, ports, coral reefs and smaller patches of vegetation (e.g. mangroves) in a recurrent way (thanks to the high revisiting time of those satellites) and at no cost (thanks to the open data policy). New and high end image processing tools are being developed to process these new remote sensing data towards usable end products. These include tools for the detection of clouds, the removal of atmospheric absorption and scattering, the classification of the image in a number of pre-defined classes (e.g. vegetation species, coral associations,…) and the retrieval of bio-geophysical parameters (e.g. water quality parameter concentrations such as chlorophyll-a, suspended sediments; biomass estimation of aquatic and terrestrial vegetation; evaluation of structural indicators of vegetation (e.g. Leaf Area Index)). Here we present a complete end-to-end chain for the processing of Sentinel-2 and Landsat-8 data. This chain consists of all the necessary tools to convert raw Sentinel-2 and Landsat-8 imagery into ready-to-use maps and deliverables for end users. In detail, this comprises state-of-the-art tools and algorithms to i) automatically download and preprocess the imagery (including cloud detection and atmospheric correction) and ii) automatically convert these processed imagery into end products. Regarding the preprocessing tools, first the cloud detection and atmospheric correction module, OPERA, will be explained. The cloud detection algorithm builts further on the Automated Cloud-Cover Assessment (ACCA) algorithm(Irish, 2000). This algorithm uses a set of thresholds on different bands and band ratios. Here, the orginal ACCA is extended including tresholds on the ‘Coastal Aerosol’ and the ‘Cirrus’ band and provides improved cloud estimates particularly over water. The second preprocessing module OPERA is a scene-generic atmospheric correction, which means it can correct for atmospheric effects in scenes with land, coastal water and inland waters. OPERA is based on the atmospheric radiative transfer model Modtran5. It calculates the absorption and scattering in the atmosphere, the scattering effects at the air-water interface and neighbouring effects. Inputs for Modtran5, such as the aerosol optical thinkness, are estimated from the image itself. Applying OPERA on an uncorrected Sentinel-2 and Landsat-8 image removes all the unwanted effects and derives the ground reflectance for each pixel in the image. After atmospheric correction the resulting surface reflectances are further processed into end products providing information on the different aspects of the coastal ecosystem: water quality, coastal vegetation and coral reefs. To obtain information on water quality, the water pixels are processed to derive the concentrations of suspended sediment and chlorophyll-a. The suspended sediment can be retrieved because there is a clear relationship between its concentration and the reflectance of the pixel. In general, an increase in suspended sediment will result in an increase in water reflectance. This increase is particularly evident in the red, near infrared and short wave infrared spectral bands. The exact relationship is however different for each spectral band. For shorter wavelengths, like for instance the red band, the relationship will be linear for low concentrations (up to 50 mg L− 1), and then starts to saturate. This saturation will occur at higher concentrations for longer wavelength. This has led to the development of multiwavelength switching algorithms, where shorter wavelengths are used for low concentrations and longer wavelengths are used for higher concentrations. Short wave infrared bands can be used for the most extreme cases, where total suspended sediment reaches more than 500 mg L− 1. It should be noted that the suspended sediment concentrations refer to surface concentrations because of the limited penentration depth. Chlorophyll-a can be determined based on its specifc absorption characteristics in the red and NIR. The concentration of Chlorophyll-a can be accurately retrieved from airborne and satellite data in marine, lacustrine and transitional waters using site specific NIR-red-based reflectance ratios. The technique is based on a statistical relationship between the water quality variable of interest and the remote sensing signals. This approach is easily implemented with existing in situ data, and often produce reliable results for the areas and datasets from which they are derived. The concentration of Chlorophyll-a can then be used as an indicator of trophic status and to detect (harmful) algae blooms in coastal waters. Land pixels can be further classified according their land cover/land use. This allows to differentiate between several classes such as urban areas, bare soil, cropland and different vegetation types. Once classified into general broad classes, we further zoom in on those classes which are of particular interest for a substainable coastal management. One of those classes are for instance mangrove forests which are hugely valuable, both ecologically and economically, but are also highly threatened by clearing and rising sea levels. Here we present tools and methods to look at the mangrove extent, their species composition and the temporal changes in both. To classify the extent of mangroves at each time-step, all Landsat and Sentinel-2 channels are considered. A combination of an object-based approach to classify mangroves is applied. Using detailed knowledge on the biophysical properties of mangroves and changes over time, obtained from remote sensing, the histories of human-induced events and processes can be quantified.
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On the Development of a Stochastic Model to Mitigate Greenhouse Gas Emissions in Building and Transportation Sectors
Authors: Somayeh Asadi and Ebrahim KaranEnergy-related activities are a major contributor of greenhouse gas (GHG) emissions. A growing body of knowledge clearly depicts the links between human activities and climate change. Over the last century the burning of fossil fuels such as coal and oil and other human activities has released carbon dioxide (CO2) emissions and other heat-trapping GHG emissions into the atmosphere and thus increased the concentration of atmospheric CO2 emissions. The main human activities that emit CO2 emissions are (1) the combustion of fossil fuels to generate electricity, accounting for about 37% of total U.S. CO2 emissions and 31% of total U.S. GHG emissions in 2013, (2) the combustion of fossil fuels such as gasoline and diesel to transport people and goods, accounting for about 31% of total U.S. CO2 emissions and 26% of total U.S. GHG emissions in 2013, and (3) industrial processes such as the production and consumption of minerals and chemicals, accounting for about 15% of total U.S. CO2 emissions and 12% of total U.S. GHG emissions in 2013. This is why the adoption of hybrid and all-electric vehicles (EVs) instead of conventional gasoline powered vehicles with renewable source of power has been identified as the most effective GHG emissions mitigation strategy. This strategy not only saves considerable amounts of transportation-related CO2, but also reduces the demand for electricity in buildings, which is mainly supplied by coal-fired generation. Since solar energy is the only source of renewable energy that can be applied at a small scale (e.g. directly to the roof decking or solar window), this paper focuses only on the mitigation strategies in which EVs are powered by solar energy. One reason mitigation strategies are having difficulty delivering the desired outcome sought by policy makers is that many factors that affect the success or scale of GHG emissions reductions are uncertain and complex. Vehicle's specification (e.g. battery capacity, weight, and optimal energy use), road type and driving behavior (e.g. average speed), and environmental conditions (e.g. temperature and sunlight) are among the many factors affecting either energy consumption or generation and characterized by a significant degree of uncertainty. Thus, urban community planners and policy makers are confounded with huge amounts of unknown parameters, in which they wish to find the best solution from all feasible solutions (e.g. the largest GHG emissions reduction that a mitigation strategy can achieve) in the presence of uncertainty. The objective of this paper is to develop a stochastic mathematical model for energy consumption and mitigation strategy analysis that maximizes GHG emissions reductions based on the current demand trend and market prices. In this model, we consider EV and solar system costs, as well as the human activities (e.g. time spent in the building, time spent driving, and distance traveled) and environmental impacts (e.g. temperature, humidity, and sunlight) under uncertain conditions. What makes this study different from previous energy management or GHG emissions mitigation research is its focus on small-scale energy system and its validation process. Although mitigation actions through large-scale changes in energy system (e.g. new renewable energy power plant) will undoubtedly result in the largest GHG emissions reductions, but they also require major changes in the generation part of the energy sector and definitely need more investment. One the other hand, small-scale GHG emissions mitigation actions (e.g. EVs powered by solar energy) can be accomplished by local communities and characterized by a short decision making cycle, need much less investment, and also eliminate electricity losses in transmission and distribution systems. These all make small-scale GHG emissions mitigation strategies more practical and feasible. Another principal problem with prior energy management or GHG emissions mitigation research is that optimization models have not been validated with real data. In contrast, the proposed optimization approach is validated by comparing the estimated values of the optimal decision and actual values as realizations of the uncertain elements become known. Problem Statement The use of hybrid or EVs alone does not necessarily reduce the transportation's GHG emissions and it depends on the energy source. A conventional gasoline powered vehicle with 30 miles per gallon (mpg) fuel efficiency emits about 0.65 pounds CO2 per mile driven. In contrast, an EV with an average energy use of 3 mile per kWh emits about 0.71 pounds CO2 per mile driven when coal-fired electricity is used, and it emits 0.40 pounds CO2 per mile driven when natural gas-fired electricity is used. In order to optimize the mitigation strategies in which EVs are powered by solar energy (EV + solar power strategy), both energy supply (electricity generation) and demand (electricity consumption) sides must be considered. Research Methodology There are three primary solar systems: off-grid, grid-tied, and hybrid. Off-grid solar systems feed the extra energy the solar panels produce into batteries, while grid-tied solar systems send excess power to the electrical grid. Both off-grid and grid-tied systems yield the same amount of CO2 emissions reduction when the solar panels produce enough power for charging EV's batteries. When the solar panels are not producing the power required for charging an EV (e.g. during cloudy weather or night), however, grid-tied systems use electricity from the grid but off-grid systems use electricity stored in batteries. Depending on the electrical grid energy source in this case, a mitigation strategy using grid-tied systems may add a significant amount of CO2 to the atmosphere. Hybrid solar systems offer the flexibility of using a battery backup and being connected to the grid. Therefore, the outcome of a mitigation strategy using hybrid systems depends largely on the power generation capacity of the solar system. The area of solar panels, the solar cell efficiency and temperature coefficient, irradiance of input light, and temperature are the main factors affecting the capacity of a solar system. In the present problem, the decisions variables are the type of EV, which determines the optimal EV's energy use, the capacity of the solar system in the case of grid-tied system as well as the solar system storage capacity in the case of off-grid and hybrid system. Under a pre-specified budget constraint, the objective is to find these decision variables in such way to maximize GHG emissions reductions. The present model starts the optimization process by identifying the energy source of electricity generation. The electrical grid energy source is determined by the electricity demand at time t, Load t, and the electric power plants generating capacity, PPCj. The time index t takes integer values between 1 and N, where N is the time horizon of the analysis and the units of time measurement are hours. For instance, Load30 indicates the electricity demand on day 2, 6 AM. Smaller time horizons for the analysis and the prediction require less computation efforts but they are less accurate. To obtain a perfect reference for the best possible GHG emissions mitigation strategy, we solve a stochastic optimization problem with a prediction horizon of 1 hour over a year, thus N is 1 × 365 × 24 = 8760 hours. The power plant index j indicates the respective set of the renewable (j = 1), nuclear- (j = 2), natural-gas (j = 3), coal- (j = 4), and oil-fired (j = 5) power plant. Load t is a probabilistic variable because it is unknown at the time the decision should be made; however, PPCj is a deterministic variable and is known for the analysis region. It is assumed that the supply level is sufficient to meet peak demand. The CO2 emissions at time t are then calculated for each type of solar system. For a grid-tied system, the CO2 emissions (measured in lb or kg) are calculated which may be positive or negative. A Negative value indicates a reduction in the CO2 emissions. When an EV is charging at time t, the energy generated by solar panel will be used in transportation sector. However, when an EV is not charging, all the energy will be used in the building. For an off-grid system, the factor that can seriously affect the CO2 emissions is the solar battery's state of charge. This factor is a function of the solar system storage capacity, and the charging duration, which starts at the last prediction horizon, and ends at time t. Once the solar batteries are fully charged, the extra energy the solar panels produce will be used only in the building. Since off-grid solar systems are not connected to the electrical grid, the energy produced by the system can meet at most the building's demand (DB) and the rest is wasted. This happens when the solar batteries are fully charged and the system is producing more energy than building's load. In the off-grid system, the EV is charged using the electricity stored in batteries. When the energy required to fully charging the EV exceeds the electricity stored in batteries, the EV will be charging using both the batteries and the electrical grid. In contrast to an off-grid solar system, no extra power is wasted in hybrid systems because they can send excess power to the electrical grid. In order to reduce more GHG emissions, the energy generated by solar panel must preferably be used to charge EV's vehicle batteries. For a grid-tied system, this happens when the EV is charging right when the solar system is producing energy. Off-grid and hybrid solar systems offer the flexibility of using a battery backup to charge the EV even when the solar system is not producing enough energy, for example during cloudy weather or night. Thus, it is assumed that the power from the solar system is first used to charge the batteries and then excess power is used in the building or fed into the electrical grid. In order to estimate the electricity generated by solar system, the distributions of stochastic variables such as solar irradiance and temperature are obtained from the weather records over the last 20 years from 1994 to 2014. Also, a database of 46 solar panels from 15 manufacturers is used to obtain solar cell efficiency and temperature coefficient. The average efficiency of 15.86% and temperature coefficient of -0.44 %/°C are used in the analysis. In order to estimate the electricity demand at a given time, the distributions of hourly load are obtained from the operable electric generating plants with a combined rated capacity of 1 MW or more over the last 18 years from 1996 to 2014. The Energy Information Administration (EIA) was the primary sources of hourly load data. Results and Conclusions Results show that among three primary solar systems (i.e. off-grid, grid-tied, and hybrid), a hybrid system consists of 7 modules of solar panels with 6 kWh storage capacity was found to be the best solution. Hybrid solar systems overcome the disadvantage of off-grid solar systems by sending the excess power to the electrical grid and reduce more CO2 emissions than grid-tied solar systems by using the electricity stored in batteries in transportation sector instead of buildings. The presented model is also capable of estimating CO2 emissions reductions from mitigation strategies in which EVs are powered by solar energy. With this capability, urban community planners and policy makers will know how long it will take for their strategy to meet GHG emissions reduction targets. The stochastic optimization problem was solved with a prediction horizon of an hour over a month. Then, CO2 emissions reductions estimated by the presented stochastic model were compared with actual data collected on an hourly basis for the analysis period of one month (720 hours). The results showed an accuracy of about 4% when the EV is powered by a grid-tied or hybrid solar system. When applied to an EV + off-grid solar power strategy, the stochastic model estimated CO2 emissions reductions 11% lower than the actual reductions. Overall, the presented stochastic model had better performance than deterministic methods for different types of solar systems.
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Using GIS to Quantify Change in the Groundwater Levels in Qatar Between 1980 & 2009
Authors: Yasir Elginaid Mohieldeen and Anan Al-MarriSince early 2000s Qatar has been relying heavily on desalinated water from the Arabian Gulf as the main source of fresh water. In the case of natural disasters in the Gulf such as the red-tide phenomenon, or man-made disasters such as oil-spills, Qatar would not be able to desalinate water even for days never mind the months that some disasters would bring about. Qatar is very vulnerable to such disasters, and at present does not have the strategic reserves of fresh water. The current reserve capacity is for only two days. Two days is definitely not enough. For example, in the case of the oil spill in the Gulf of Mexico it took 36 days to clean the water before it could be usable. Another example is the 2008–2009 red-tide natural disaster that lasted for more than eight months and forced the closure of desalination plants in the region for weeks.
In addition the groundwater systems in Qatar are heavily exploited mainly for irrigation purposes. The over-abstraction has resulted in the deterioration of water quantity and quality (due to seawater intrusion). Therefore, groundwater in its current state would be unusable in the event of water shortages caused by disasters in the Arabian Gulf. Large scale artificial aquifer recharge plans have been proposed in order to provide strategic reserve in emergencies. The goal of this plan would be restore the 1980s groundwater levels, through artificial recharging.
GIS is used in this study to map change in the levels of the groundwater between 1980 and 2009, using potentiometric surface data, in order to identify potential recharge zones/areas. Such information is key in any aquifer recharge project that aims to restore the aquifers and use them as strategic water reserve in the event of water shortage emergencies. This study focuses on the upper aquifer in Qatar - the Al Damman aquifer.
The environment of Qatar is desertic with no surface water and very little rainfall. In 2014 the average natural water resources from rainfall was less than 29 cubic meters per year per capita (m3/y/ca), compared to the global average of 6,000 m3/y/ca, and a water poverty line of 1,000 m3/y/ca. However, Qatar per capita water consumption is among the highest in the World, reaching more than 500 liters per person per day, whereas the global average is about 160 liters per person per day. This high per capita consumption in Qatar is attributed to rapid urbanization and changes of living standards since the early 1980s. Qatar's Gross Domestic Product (GDP) has increased from 23.5 billion USD in 2003 to 211.8 billion USD in 2014. This economic boom that has put tremendous pressure on the groundwater resources, as population increased. This pressure was caused by the rapidly increased farming activities embarked upon in order to meet the food demand of the rapidly rising population. Another reason for the increase in farms is a consequence of it reflecting the social status of its owner. Qatar's population increased almost five times from 0.37 Million to 1.74 Million between 1986 and 2010, and six times between 1986 and 2014. Groundwater withdrawal by irrigators has occurred. Figure 7 shows abstraction for irrigation increasing from 100.3 Mm3/yr in 1983 to 248.73 Mm3/yr in 2009. The groundwater abstraction rate highly exceeds the natural replenishment rate of 58 Mm3/yr from rainfall, hence groundwater levels drop.
In 2009, about 99.9% of the total potable water, produced by the Qatari water company (KAHRAMAA), was desalinated while only 0.1% was from groundwater. Desalinated water production has increased four-fold between 2003 and 2011 (from 0.44 to 1.48 million m3/day).
To identify change in groundwater level two potentiometric iso-maps of the Al Dammam aquifer for the years 1980 map were acquired in a hardcopy format. The two maps were first converted from hardcopy format to digital format by scanning, in order to enable manipulation in the GIS system. The two scanned digital images were then geo-referenced to the Qatar National Grid 1995 (QNG 1995) coordinate system, using known ground control points and ArcGIS system. Then the images were digitized by tracing the potentiometric contours/isolines in each map, converting them into vector lines. Potentiometric values were assigned to their respective vector lines. The line-or vector -is then converted to point data. Interpolation techniques enabled the generation of a continuous surface (raster) to be able to compare the cell values of the same location of the two data sets.
Spatial interpolation techniques were used to create continuous raster surfaces in order to compare the two datasets from 1980 and 2009. Two main groups of surface interpolation techniques are available in the GIS environment: deterministic; and geo-statistical. Deterministic interpolation techniques create surfaces from measured points, based on either the extent of similarity or the degree of smoothing. While geo-statistical interpolation techniques utilize the statistical properties of the measured points. Geo-statistical techniques quantify the spatial autocorrelation among measured points and account for the spatial configuration of the sample points around the predicted locations.
Based on the nature of the data available for this study and its spatial distribution geo-statistical interpolation was preferred over deterministic techniques. The Ordinary Kriging method of geo-statistical interpolation was chosen as it provides accurate interpolation with minimum standard error. Two potentiometric raster surfaces for 1980 and 2009 were interpolated. The 1980 surface was then subtracted from the 2009 surface in order to calculate the change in groundwater level between the two years.
Two potentiometric raster surfaces for 1980 and 2009 were interpolated. The 1980 surface was then subtracted from the 2009 surface in order to calculate the change in groundwater level between the two years. The difference map shows areas where groundwater level dropped between 1980 in 2009.
To help better interpret the results, the map was overlaid over a 2013 Landsat 8 satellite image, from the Enhanced Thematic Mapper Plus (ETM+). The overlay showed major level increase in and around Doha, is clearly caused by: seepage from unlined treated sewage water dumping lagoon at Abu Nakhlaa- south-west Doha; and leakage from water distribution network in Doha. Some increase also identified in south Qatar due to pivot-irrigation systems using recycled treated water.
Areas with groundwater falls in level by 4 meters and more were considered as having high artificial injection potential. The 4 meter drop was selected to avoid possible Land-Surface Deformation (LSD) by having enough space for the recharge. A few centimeters of LSD could have serious consequences for high rise buildings in Doha City, Such deformation causes cracks and damage to these buildings if the ground moves. LSD also damages water and sewage network pipe-joints and fittings, exacerbating the water-leakage problem in Doha, resulting in the water-table rises in the city. The rising water table in Doha has become a serious issue as it impedes the digging of foundations. Expensive de-watering procedures are required and special coating for the foundations which add to the construction costs. Furthermore, water leakage implies more desalinated water needs to be produced in order to substitute for the lost waters, and hence more vulnerability to disasters in the Arabian Gulf.
Some central areas, despite the high potential recharge volumes, are suggested to be excluded from the recharge, to avoid raising the groundwater levels in Doha City. In Qatar, groundwater flows radially outwards from recharge areas, centered over the higher Qatar Anticline land that plunges to the north and to the south with a surface expression of a broad shallow dome. The water discharges into the adjacent low-lying land along the coast and the Arabian Gulf. Recharging these areas will increase the flow towards Doha, down the groundwater gradient.
Another reason for excluding these central areas is that the area has a large number of sink-holes. These karst features are produced by the dissolution of subsurface gypsum beds during humid and wet periods in the Pliocene and Pleistocene period. Filling these gypsum formations with freshwater is very likely to cause re-dissolution, and hence the collapse of ground surface.
The results present essential information that could be further refined through field work and groundwater survey. Further modeling of the groundwater movement and dynamics using monitoring wells data will also be completed.
Soil permeability and soil types analysis in the area are need to carry out the analysis of the recharge areas.
It is also recommended that an interferometry study, using polaromteric RADAR surveys, be completed before, during and after the artificial recharge in order to monitor possible land surface deformation.
GIS proved to be a very effective tool in assessing disaster preparedness, management, and prevention as it helped in determining the potential recharge areas that could be used for strategic water reserve.
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A Solid-State Transformer as Enabling Technology for Microgrids for Integration into the Power Distribution System: An Overview
More LessIn the present architecture of the electric power grids, energy is generated in large-scale that is remotely located from consumers and transmitted using passive high-voltage transmission networks to substations. The electric power is then delivered to consumers via medium and low-voltage distribution systems. Line frequency transformers (LFTs) enable high-efficiency and long-distance power transmission by stepping up the voltage on the transmission side. On the distribution side, the voltage is stepped down for industrial, commercial, and residential consumers. Furthermore, the traditional electric power system is characterized by hierarchical control structures with minimal feedback, limited energy storage, and passive loads. In recent years, the electric power system has been facing increasing stress due to fundamental changes in demand growth, technology change, and consumer preference. There has been a paradigm shift from centralized generation and control to distributed generation, storage and local control; in particular, there has been a global growth of investments in Renewable Energy Sources (RES) such as wind and solar. These RES generate fluctuating electric power and therefore they require Energy Storage Systems (ESS) to enable a time-shift between energy production and consumption. The high penetration of RES and other Distributed Generation (DG) types such as fuel cells (FCs) and Micro-Turbines (MTs) impose significant challenges on the operation of power system and coordination of supply and demand in real time. At the same time, the power system will need to react to events for which it was not designed for. Microgrids (MGs), being controllable small scale power networks, have become popular in distributed systems by facilitating an effective and smooth integration of distributed energy resources, loads, and energy storage devices into existing power systems. They help reduce expenditure by reducing network congestion, line losses and line costs and thereby higher energy efficiency. Power electronics converters are used in microgrids to control the routing of electricity and also provide flexible distributed generation sources interfaces to the distribution network to ensure stable and secure operation of the grid. These power converters rely on the type of microgrid (AC or DC), as well as on other features of the devices (voltage levels, power flow direction, etc.). In addition, they usually include a transformer in order to obtain galvanic isolation. The solid state transformer (SST), which is also called Electronic Power Transformer (EPT), Active Power Electronics Transformer (APET) and Intelligent TRansformer (ITR), has been proposed to replace the traditional line frequency distribution transformers. The basic operation of the SST is first to change the 50Hz AC voltage to high frequency (normally in the range of several to tens of kilohertz), then this high frequency voltage is stepped up/down by a high frequency transformer with significantly decreased volume and weight, and finally shaped back into the desired 50Hz voltage to feed the load. The SST is a power electronics circuit that provides a flexible method for interfacing microgrids with the existing Medium-Voltage (MV) power distribution system. It achieves voltage transformation via a high-frequency isolated transformer, therefore the mass and volume of the system can be reduced. Current and voltage are independently controlled via power semiconductor devices which enables grid support functions not present in the traditional LFT, including voltage and power factor regulation, fault isolation and limitation, filtering harmonic, reactive power compensation, power flow control and voltage and load disturbance rejection. However, at the present time, the commercial success of SSTs has been limited. Efforts have been made to design and implement SSTs with satisfactory performance, as well as explore its use at the distribution system level. The SST can functionally replace the traditional LFT and some power electronics converters, thus indicating a potentially more integrated and compact system. Although the concept of the SST can be seen straight forward, its implementation is a challenge. The SST combines the high voltage, high power, and high frequency operation, which make its design and operation a real challenge. To implement the SST, different power devices can be combined with different circuit topologies in different configurations. In addition, different core materials and transformer structures may be considered to build the high frequency transformer with different phase connections. Furthermore, due to power rating limitation of the semiconductor devices and magnetic components, SST topologies may have several SST cells connected in series or in parallel. Numerous degrees of freedom for the SST modularization are available, which lead to a vast amount of possible arrangements depending on the different levels of modularization in the three modularization axes: degree of power conversion partitioning; degree of phase modularity and number of levels or series/parallel connected cells. Since the level of modularity in each of these different directions is independent, these three axes can be considered to be orthogonal to each other and each element represents a specific design with a certain degree of modularization in each of the axes. The SST can be used as an enabling tool for interfacing microgrids (AC and DC) to medium voltage distribution network. For a SST-based microgrid, the performance of the microgrid mainly depends on the control algorithms of the SSTs. Generally, there are three SST control levels: system level, equipment level, and switch level. For a well-designed SST, the equipment level and firing level control strategies are well defined. However, the system level control strategy can be changed to fit different applications. In order to operate a microgrid properly and reliably, SST- based power control strategies should be developed to accommodate the modes of operation: grid-connected mode and standalone mode. That is why, the development of a controller that manages active and reactive power flow between the DC microgrid, the AC microgrid and the main distribution network is one of the most important research topic for the SST. Furthermore, investigating the effect of grid faults on the stability and performance of the SST is another hot research topic in the same area. Also, the SST can be used in different applications, such as: oil and gas and electric transportation applications. To give an overview of the SST, this work will present a review of the different levels of modularization, all possible control algorithms for the different control levels. Furthermore, stability and reliability analysis for grid connected SST will be reviewed. Finally, all possible application of the SST will be presented.
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Simulating Yields for Selected Vegetables in Qatar Using Crop, Climate, Soil and Management Information to Improve the Country's Food Security
Qatar produces only about 8 to 10 percent of food consumed in the country. Domestic production of perishable commodities, primarily vegetables, will be increased by using a combination of hi-tech water-efficient field and greenhouse production systems. Improving the decision making in the various stages of production faces a number of challenges mainly related to adverse climatic conditions, quality of soils, scarcity of irrigation water, and market constraints. This paper highlights preliminary results in assessing climate, soil and crop management constraints in Qatar. Components of the research framework include assessing the yield potential of selected crops through simulation modelling using historical climate and soils data. AquaCrop, a model developed by FAO, has been used in this study to simulate yields of squash for different planting cycles of 110 days in Doha over the 30 year period from 1985 to 2014. The mean simulated yield for January to March planting dates (22nd of each month) was 23 t/ha with a narrow range of only 21 to 24 t/ha, while the simulated yields were highly variable for April, May and June planting dates. The mean yield for April was 17 t/ha (lowest 4 t/ha, highest 24 t/ha). The mean yield for May and June plantings was 7 t/ha with a range of 1 to 20 t/ha. These results compare well with the recent data collected from Al Sulaiteen Agricultural and Industrial Complex site (SAIC) in Doha. The relatively lower yield with greater variability during April to June months is associated with higher evaporative demand and higher temperatures during the crop growth period. The model is used to estimate yields for other crops including cucumber and tomatoes. Comparison of the simulated crop yields with actual field data is underway. Further and more detailed analysis of the AquaCrop model is required.
This analysis will help improve the overall food security in the state of Qatar by assisting the decision making process in the various stages of production of selected perishable food crops. Yield potential for selected crops were simulated for conditions where water and nutrients are not limiting. However the simulated results can be used to estimate the optimum amount (and timing of application) of water and nutrients required to achieve the desired production.
The findings of this paper will contribute towards achieving the goals of our research project “Improving Food Security in Qatar: Assessing Alternative Cropping Systems Feasibility and Productivity in Variable Climates, Soil and Marketing Environments” (NPRP6-064-4-001) funded by Qatar National Research Fund (QNRF- a member of Qatar Foundation) through its National Research Priority Program.
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Vulnerability Assessment of Groundwater Aquifers in Qatar
More LessQatar peninsula is an arid country with limited water resources. With little rainfall of approximately 80 mm per year and no surface water, aquifers are the only source of natural water in Qatar. The groundwater aquifer receives around 50 million m3 per year as natural recharge, whereas annual groundwater abstraction is more than 220 million m3, mainly used for agriculture. Groundwater occurs in a form of fresh lenses mainly in the northern part of the country, sitting atop of brackish and saline groundwater. Seawater has progressively intruded inland over the last decades because of over-pumping. As a result, the water table has dramatically dropped to unprecedented levels and salinity increased, in addition to other adverse environmental impacts. Because of its karstic nature, Qatar aquifer is prone to different sources of adverse environmental impacts. The concept of aquifer vulnerability is based on the idea that some areas above an aquifer provide more resistant to contamination than others (Vrba and Zaporozec 1994). Mapping groundwater vulnerability using hydrogeological settings gives a clear understanding of natural variation from one point to another within an aquifer. Vulnerability mapping is a powerful tool that can be used for groundwater protection and land management. In this study, vulnerability map was created based on hydrogeological parameters, land use and natural groundwater quality. All maps have been prepared and manipulated within Geographical Information System (GIS). The final vulnerability map was obtained as a sum of different rated maps using Raster Calculator. Two different approaches were used to create vulnerability maps (a) DRASTIC approach, which depends on general hydrogeological settings, and (b) EPIK approach, which focuses on karst hydrogeology. DRASTIC approach uses seven rated maps of: depth to water table, recharge, aquifer media, soil media, topography, vadose zone and hydraulic conductivity to calculate a weighted index map of vulnerability (Aller et al., 1987). EPIK approach is based on (1) epikarst, (2) protection cover, (3) infiltration rate and (4) karstic network. Depth to water table varies from a few meters near the coast to tens of meters further inland and recharge occur mainly in the many land depressions that spread all over the country. These land depressions vary in diameter from a few meters to more than two kilometers. These depressions were formed as a result of land collapse due to cavities underneath. The cavities are the result of dissolution of limestone over thousands of years. In all cases, these depressions have a high weight in vulnerability assessment. Soil may provide some sort of aquifer protection depending on its type and thickness. The dominant soil in Qatar is lithosol, which is composed of rocky soil and provide no protection. Some loamy sand exists in farm lands, which is normally derived by rainfall runoff and provide some protection cover. Aquifer media comprises limestone with dolomite, chalk and clay of variable thicknesses. Three main layers of limestone occur in Qatar. These layers are from top to bottom (1) Dam and Dammam Formation, (2) Rus Formation and (3) Umm Alraduma Formation. Results of aquifer tests show aquifer is highly heterogeneous, which is typical in karst environment with high variation of hydraulic conductivity values. A thick layer of gypsum occurs within the middle layer of limestone (Rus) in the southern part of the country and has a great implication on water quality. This layer is soluble in water, which deteriorates the groundwater quality. All the previously discussed hydrogeological settings have been used to create vulnerability maps in Qatar. While DRASTIC laid more weight on coastal sediments, as they appear to be highly vulnerable in the final map, EPIK approach laid more weights on karst formations in the middle of the country. DRASTIC approach shows high vulnerability areas occur along the coastline and in land depressions Results of both approaches show the high vulnerable areas are those were land depressions occur.
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Bioelectrochemical CO2 Reduction to Acetic Acid and Ethanol: Improved Microbial Electrosynthesis Using Gas Diffusion Electrodes
Authors: Deepak Pant, Suman Bajracharya, Gunda Mohanakrishna and Karolien VanbroekhovenMicrobial Electrosynthesis (MES) comprises electro-reduction of carbon dioxide (CO2) to multi-carbon organic compounds by chemolithotrophs using electrons from a cathode. Reduction of CO2 to chemicals through microbial electrocatalysis was investigated by using a mixed culture of acetogenic and carboxydotrophic bacteria forming a microbial biofilm supported on a carbon based electrode, as biocathode, in a two chamber reactor. The biofilm was developed after a start-up phase with fructose and later on, growing on bicarbonate as substrate at sufficiently negative cathode potential (hydrogen evolution) in a couple of subsequent fed-batch operations. CO2 reduction could occur via direct electron transfer from the electrode or indirectly via mediators or via hydrogen at more reductive potential. Predominantly, Acetic acid was produced along with other volatile fatty acids (VFAs) while applying − 1.1 V/Ag/AgCl cathode potential, along with hydrogen evolution. At the initial stage of fed-batch operation, higher carbon recovery up to 60% was observed from bicarbonate (dissolved CO2) to acetic acid while after accumulation of acetate, the recovery rate went down to 12% as acetate degradation/conversion started or other unmeasured products formed. Maximum acetate production rate achieved during the operation was 40 g m− 2 day− 1 corresponding to coulumbic efficiency of 41%. Microbial analysis of catholyte at the end of the experiment showed that the bacterial community was dominated by Cellulomonas, Stappia and Pseudomonas spp. These results suggest that the mixed culture enriched with acetogenic bacteria can catalyze the electro-reduction of CO2 into a number of chemicals like VFAs through direct or indirect electron transfer mechanisms. While using gaseous CO2 as carbon source, the dissolution and mass transfer of CO2 to the biocatalyst limit the biological reduction process. In addition, the bacterial attachment and retention of reducing equivalent specially hydrogen also restrict the process at the cathode. In order to deal with these issues, a gas diffusion cathode (GDC) (VITO Core™) and a flow-through porous carbon felt cathode were separately tested in MES for CO2 reduction. In principal, the porous activated carbon with hydrophobic binder layer in GDC creates a three-phase interface that makes CO2 and reducing equivalents available to the bacteria. Flow-through graphite felt cathode retains the suspended biomass and electrochemically produced hydrogen when the catholyte is forced to flow through it. An enriched inoculum of acetogenic bacteria, isolated from wastewater sludge was used as biocatalyst. The cathode potentials were maintained at − 0.9 to − 1.1 V vs Ag/AgCl to facilitate CO2 reduction also via the hydrogen evolved at the cathode. On average, CO2 reduction to acetate was achieved with the production rate ∼35 to 43 mg/L/d supplying 20% (v/v) CO2 gas mixture in both the reactors. In the reactors without GDCs or modified cathode, CO2 reduction was never steady for a long period of operation. Acetate was the primary product of CO2 reduction but ethanol and butyrate were also produced concurrently at pH lower than 6. The highest acetate production rate reached in GDC reactor was ∼550 mg/L/d supplying 80% (v/v) CO2 mixture over the GDC. In conclusion, gas diffusion and flow-through cathodes were useful to develop stable CO2 reducing biocathodes and also to operate in continuous mode. Keywords: Microbial electrosynthesis, CO2 reduction, Gas diffusion cathode, Flow-through biocathode, Biocathode, Autotrophic Bioproduction.
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Impacts of PV Adoption in Qatar on Natural Gas Exports and Carbon Dioxide Emission Reduction
Authors: Antonio P. Sanfilippo and Larry PedersonQatar seeks to generate 2% of its electricity from solar power by 2020 (Bryden et al., 2013, REN 2015), and 20% by either 2024 (PV Insider, 2014) or 2030 (REN, 2015). Since electricity is produced almost entirely from natural gas in Qatar, these renewable energy targets introduce the prospect of natural gas savings that can be made use to increase trade and/or reduce carbon emissions. Electricity production in Qatar has been growing at a very fast pace since the mid-nineties. An estimated 7.3 millions of tons of oil equivalent (Mtoe) of natural gas were used in 2013 to produce 34.7 terawatt-hours (TWh), double the amount in 2007 and over five times as compared to 1997 (Table 1).
Table 1: Electricity production with associate natural gas (NG) use in Qatar 1971–2013. Source for electricity data: http://www.iea.org. Gas usage calculated as the estimated average efficiency for power plants using natural gas in the US for the period 2003–2013 (40.84%) estimated by the U.S. Energy Information Administration (http://www.eia.gov/electricity/annual/html/epa_08_01.html). Year – TWh produced in Qatar – NG used (Mtoe)1971 0.285 0.0601972 0.358 0.0751973 0.380 0.0801974 0.413 0.0871975 0.513 0.1081976 0.717 0.1511977 0.835 0.1761978 1.196 0.2521979 1.877 0.3951980 2.351 0.4951981 2.700 0.5691982 2.998 0.6311983 3.194 0.6731984 3.507 0.7381985 3.918 0.8251986 4.249 0.8951987 4.329 0.9121988 4.592 0.9671989 4.624 0.9741990 4.818 1.0141991 4.643 0.9781992 5.153 1.0851993 5.522 1.1631994 5.815 1.2241995 5.976 1.2581996 6.575 1.3841997 6.869 1.4461998 8.122 1.7101999 8.584 1.8072000 9.134 1.9232001 9.951 2.0952002 10.940 2.3042003 12.012 2.5292004 13.233 2.7862005 14.396 3.0312006 17.080 3.5962007 19.462 4.0982008 21.616 4.5512009 24.158 5.0872010 28.144 5.9262011 30.730 6.4702012 34.787 7.3252013 34.668 7.300
Ten-year forward projections, with cap limits of 200 Mtoe on yearly natural gas production, indicate that electricity production will peak at 48.4 TWh in 2021, with an associated natural gas use of 10.2 Mtoe (Table 2). Cap limits on natural gas production are necessary to prevent early depletion of natural gas reserves in Qatar, which have been estimated at 138 year at current output rates (QNB 2015).
Table 2: Ten-year projections (2014–2024) for electricity production and associated natural gas (NG) use in Qatar (Sanfilippo & Pedersen, in preparation). These projections assume that yearly NG production will not grow beyond 200 Mtoe. Year – Energy production (TWh) – NG needed for energy production (Mtoe) 2013 34.67 7.32014* 32.55 6.92015* 23.30 4.92016* 24.48 5.22017* 23.06 4.92018* 31.96 6.72019* 43.97 9.32020* 48.04 10.12021* 48.41 10.22022* 47.97 10.12023* 45.96 9.72024* 43.61 9.2.
The foreseen use of solar power to generate of electricity could yield a natural gas surplus of 0.2 Mtoe in 2020 and up to 1.8 Mtoe by 2024 or 2030, to reach 3.9 Mtoe thereafter, assuming a PV market peak of 43% in electricity generation – over 3.35% of Qatar total natural gas exports in 2013. This surplus could be repurposed for natural gas trade, and countries in the Far East stand as the most natural trading partners. Exports to Japan, Korea & China accounted for 41% of Qatar's NG world trade in 2013 (http://www.iea.org). Japan and Korea have historically been some of the greatest importers of natural gas from Qatar, and China is quickly emerging as a strong trading partner due to its growing need for energy. China's share in Total Primary Energy Supply (TPES) worldwide has grown from 7% in 1971 to 22% in 2013 (http://www.iea.org). China is now the world largest energy consumer with a 5% lead over the United States, the country that topped the list with 29% share of the world TPES in 1971. China's natural gas imports from Qatar rose from 0.5 to 8.8 Mtoe in only 5 years, from 2009 to 2013. Moreover, China is quickly becoming a major trading partner for Qatar. For the period 2009–2014, the trade between the two nations grew at a Compound Annual Growth Rate (CAGR) of 35.38%, as compared to 28.92% for the period 2003–2008 (http://data.imf.org). Across the same periods, Qatar's trade shows a sharp CAGR decline with both Japan (2009–2014 CAGR: 12.6 vs. 2003–2008 CAGR: 25.37%) and Korea (2009–2014 CAGR: 33.12 vs. 2003–2008 CAGR: 22.1%). Considering these market trends, China appears the most likely candidate partner for additional natural gas trade from Qatar. While the recent turbulence in Asian markets signals a slowdown in China's economy, it is unlikely that China's position as the world largest energy consumer will change in the years to come. Moreover, foreign natural gas is playing an increasingly important role in Chinese energy market (Higashi 2009). Despite plans by the Chinese government to expand domestic production, the internal Chinese natural gas market remains unbalanced (Li et al., 2014). The development and implementation of a new strategic roadmap are needed to manage the local production, marketing and transportation of gas efficiently. These changes may take decades to come to fruition, during which reliance on natural gas imports is bound to grow. In terms of carbon emissions, the amount of CO2 equivalent to the prospected 3.9 Mtoe of natural gas replaced by solar energy (see above) is 9,053,724 US tons, assuming the IEA estimate that each million British thermal units (MBtu) of energy generated by natural gas generate 117 pounds of CO2 emissions (http://www.eia.gov/tools/faqs/faq.cfm?id = 73&t = 11).
References
Bryden, J. Riahi, l., Zissler, R., (2013). MENA: Renewables Status Report. United Arab Emirates Ministry of Foreign Affairs, REN 21. International Renewable Energy Agency (IRENA).
Higashi, N. (2009). Natural gas in China. IEA Energy Markets and Security Working Papers.
Li, Z., Zhang, Q., Farfan Reyes, S., Wang, Z., (2014) Natural Gas Development strategy modeling in China. 4th International Association for Energy Economics Asian Conference, Beijing, China, September 19–21, 2014.
PV Insider, (2014). PV in MENA: Turning Policy into Projects. Retrieved on Nov 1, 2015 from http://www.pv-insider.com/menasol/pdf/policyintoplants.pdf. QNB, (2015).
QNB Economic Commentary, 21 June, 2015. REN21, (2015).
Renewables 2015 Global Status Report. http://www.ren21.net/status-of-renewables/global-status-report/. Sanfilippo, A. & Pederson, L., (in preparation).
Impacts of PV Adoption in Qatar on Natural Gas Exports to the Far East. In Lester, L. & Efird, B. (eds.) Energy Relations and Policy Making in Asia: The benefits of mutual interdependence, Palgrave Macmillan.
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Highly Efficient Artificial Photosynthesis of Formate from CO2 and Water on Heterojunction Copper Iron Oxide Catalysts
Authors: Hyunwoong Park, Unseock Kang, Dong Suk Han and Ahmed Abdel-WahabSolar CO2 recycling has received wide attention primarily to address global CO2 emission and to convert CO2 and water to value-added chemicals. Despite a long research history over the past four decades, the technology remains in an early stage, with low CO2 conversion efficiency and selectivity. CO2 is highly stable and has limited solubility in water, and its reduction requires multiple proton-coupled electron transfers, resulting in a range of carbon intermediates (C1–C3) as well as a larger amount of H2 over CO2 conversion products. For the realization of solar CO2 recycling, the system of interest should be operated sustainably, which requires the development of not only energy-efficient and cost-effective materials but also stand-alone, complete reaction processes (CO2 reduction and water oxidation) operating for long periods without any external bias. A range of semiconductors (mostly p-types) have been studied for CO2 conversion, including GaP, InP, GaAs, Si, Cu2O, and CuFeO2, all of which have narrow bandgaps (Eg) and sufficient Fermi levels (EF) capable of reducing CO2. Although promising, these aterials inherently require potential biases to drive the CO2 reduction reaction and compete with other metallic electrodes, whereas complete reactions (CO2 reduction and water oxidation) have been rarely demonstrated due to large overpotentials. Photocathode-photoanode couples have been demonstrated to operate, yet the syntheses of materials are complicated and the energy conversion efficiency is low. We have searched for high-efficiency, low-cost, and scalable p-type materials and found that CuFeO2 and CuO mixed materials meet all requirements. To our surprise, this material converted CO2 to formate with selectivity greater than 90% over 1 week and simultaneously produced molecular oxygen via water oxidation when simply wired to an inert anode (Pt foil) without any external bias under circum-neutral pH. The solar-to-formate (STF) energy efficiency was in the range of 0.7–1.2%, which is the highest reported value and comparable to the efficiency of photosynthesis occurring in most plants. For comparison, CuFeO2, CuO, and even Cu2O were fabricated; however, their efficiencies for formate production were much lower, and no oxygen was evolved.
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