Preliminary Field Test Results from a Photovoltaic Electrodialysis Brackish Water Desalination System in Rural India

Total Page:16

File Type:pdf, Size:1020Kb

Preliminary Field Test Results from a Photovoltaic Electrodialysis Brackish Water Desalination System in Rural India Preliminary Field Test Results From a Photovoltaic Electrodialysis Brackish Water Desalination System in Rural India The MIT Faculty has made this article openly available. Please share how this access benefits you. Your story matters. Citation He, Wei, Natasha C. Wright, Susan Amrose, Tonio Buonassisi, Ian Marius Peters, and Amos G. Winter. “Preliminary Field Test Results From a Photovoltaic Electrodialysis Brackish Water Desalination System in Rural India.” Proceedings of the ASME 2018 International Design Engineering Technical Conferences and Computers and Information in Engineering Conference, 26-29 August , 2018, Quebec City, Quebec, Canada, ASME, 2018. © 2018 ASME As Published http://dx.doi.org/10.1115/DETC2018-86183 Publisher American Society of Mechanical Engineers Version Final published version Citable link http://hdl.handle.net/1721.1/120050 Terms of Use Article is made available in accordance with the publisher's policy and may be subject to US copyright law. Please refer to the publisher's site for terms of use. Proceedings of the ASME 2018 International Design Engineering Technical Conferences and Computers and Information in Engineering Conference IDETC/CIE 2018 August 26-29, 2018, Quebec City, Quebec, Canada DETC2018-86183 PRELIMINARY FIELD TEST RESULTS FROM A PHOTOVOLTAIC ELECTRODIALYSIS BRACKISH WATER DESALINATION SYSTEM IN RURAL INDIA Wei He Natasha C. Wright Susan Amrose Massachusetts Institute of Massachusetts Institute of Massachusetts Institute of Technology Technology Technology Cambridge, MA, United States Cambridge, MA, United States Cambridge, MA, United States Tonio Buonassisi Ian Marius Peters Amos G. Winter, V Massachusetts Institute of Massachusetts Institute of Massachusetts Institute of Technology Technology Technology Cambridge, MA, United States Cambridge, MA, United States Cambridge, MA, United States ABSTRACT brackish water desalination has received renewed attention as a Brackish water desalination is crucial to meet basic drinking possible drinking water solution for India. water needs in rural India. Solar photovoltaic powered The most common desalination technology is reverse electrodialysis (PV-ED) has been justified as a more cost- osmosis (RO), with 60 – 90% of the market share depending on effective solution than the current dominant reverse osmosis location [5]. Tata Project Ltd. have installed and are maintaining approach for off-grid systems. This paper presents preliminary about 2,200 on-grid RO systems to meet daily drinking and results from an ongoing field pilot of a village-scale PV-ED cooking water needs across India, demonstrating that the system in Chelluru, which is a small village in South India. technology can operate in a village context. However, grid System performance is compared to predictions of a PV-ED electricity poses a number of challenges. In most villages, it is parametric model of local solar irradiance, ED system not reliable, usually providing electricity intermittently [6], and parameters, power systems parameters, water storage, and cost, also not prevalent. In 2011, only 55.3% of rural households used validating the model over a single-batch ED operation. An ~88% grid electricity for basic activities such as lighting [7]. On one “solar-to-treated water” conversion efficiency was achieved in a hand, brackish water desalination systems with oversized typical ED batch operation, using 2.47±0.27 kWh/m3 for production capability are designed to address poor grid quality, brackish desalination in the village. This paper also discusses the resulting in higher water cost. On the other hand, to compensate difficulties and local constraints encountered during the initial for poor grid access, diesel generators are often used, posing field testing and analyzes system performance in the context of additional environmental concerns. local constraints and availability. Including India, the rapid decrease in the cost of renewable energy generation [8] and the increased awareness of INTRODUCTION environmental sustainability have led many to explore This paper presents results from an ongoing field trial of a photovoltaic-RO (PV-RO) desalination in many countries which pilot village-scale solar powered electrodialysis brackish water have freshwater shortages [9, 10]. Thomson and Infield desalination system in rural India and preliminary validation of prototyped a 3 m3/day batteryless PV-RO system with a 2.4 kWp a systems-level model of energy flow. India is facing a severe PV panel in the UK, and its estimated lifecycle water cost was drinking water shortage. With a steadily increasing population £2.00/m3 [11]. Bilton et al. presented a generalized methodology that will reach an estimated 1.7 billion in 2050 [1], the water to evaluate the techno-economic feasibility of a small-scale PV- situation is expected to become even worse [2]. Groundwater RO system for desalinating water in a remote area [12]. They with salinities that exceed the acceptable salinity for drinking, concluded that a community-scale PV-RO system is more cost which is total dissolved salts (TDS) higher than 500 mg/L, effective than an equivalent diesel-based system and the underlies about 60% of India’s land area [3, 4]. As a result, transport of water in most remote locations [12]. 1 Copyright © 2018 ASME Downloaded From: https://proceedings.asmedigitalcollection.asme.org on 01/11/2019 Terms of Use: http://www.asme.org/about-asme/terms-of-use The abundance of solar irradiance in India and lack of grid data from 2010-2014, the average solar irradiance of Chelluru is access might suggest a straightforward PV-RO solution for about 5-6 kWh/m2/day. drinking water. However, Wright et al. found that the village- scale off-grid RO system is not the best option for brackish water THE PILOT PV-ED SYSTEM desalination in rural India [3]. For salinities commonly found in The objectives of the system design for Chelluru were to (1) rural India (TDS < 2000 mg/L), PV electrodialysis (PV-ED) minimize the system capital cost; and (2) maximize the water desalination has a much lower energy consumption, requiring recovery rate of brackish water desalination. The Chelluru less than 50% of the specific energy consumption (SEC) as RO system would also be an important case study to further improve to desalinate water to a final TDS of 350 mg/L [3]. This on the parametric design theory developed by Bian et al. [13], substantial reduction in energy consumption contributes to a and to help elucidate the technical, economic and social significant cost reduction in the off-grid power system. Bian et challenges of desalination in rural India. al. articulated a parametric theory between local solar irradiance, The PV-ED system in Chelluru was designed following the ED system parameters, power systems parameters including co-optimization methodology in [13], in which a cost- and number of batteries, and water storage, and was able to optimize performance-optimal PV-ED system using constant voltage and the capital system cost using the off-shelf components [13]. pumping power was designed using off-the-shelf components. Their preliminary analysis indicated a potential 42% cost The system design and operational parameters are listed in Table reduction compared to conventional design methods using 1. Solar irradiance data and temperature data of Chelluru from reasonable initial assumptions for a village-scale brackish water NSRDB for 2014 was used. desalination system in rural India [13]. Based on this optimized system design, an initial However, most of these studies are either theoretical studies configurable PV-ED system was built in Chelluru India in early or experimental studies in the lab. Very few systems are reported 2017. Figure 2 shows the installed system layout of the pilot PV- that have been tested in the field with actual brackish water ED system, demonstrating the ability of the system to reverse sources. To fill this significant gap, we installed and tested an operation through the ED stack and also the large amount of optimally designed PV-ED system in Chelluru, India, and product water storage acting as a buffer. This large buffer allows validated our system model to design co-optimal PV-ED systems the system to store water for cloudy days rather than increasing in India. The significance of the design model validation is to the number of batteries, reducing system cost. Figure 3 shows show the model’s ability to predict desalination behavior under the installed PV panels on the rooftop, the installed ED intermittent solar energy with battery storage, and the built membrane unit with piping, and the installed inverter and battery system’s ability to cost-optimally leverage these components to bank. meet the design goal of daily water production in a real-world A single hydraulic stage and single electrical stage ED condition. This paper describes the system design, validation of membrane unit was selected for the system design. The desired the energy flow model over a single ED batch, preliminary ED unit was modified from an available GE ED stack, model analysis of the system performance, and a discussion of lessons AQ3-1-2-50-35. As the original GE ED stack had two electrical learned during initial field testing. stages, the first electrical stage was not electrified and membranes were removed in the first stage to minimize the THE VILLAGE OF CHELLURU IN RURAL INDIA pressure loss. As a consequence, the modified ED stack had one Chelluru is an Indian village about 70km northeast of effective electrical stage and one “empty” electrical stage. In the Hyderabad with a population of approximately 2,000 people and future, the co-optimal system will use a single electrical stage a shortage of drinkable groundwater. The groundwater salinity is ED stack manufactured to the desired specifications. 1,300-1,500 mg/L, varying with the seasons. Currently, Chelluru’s drinking water needs are largely met by an on-grid Table 1 Chelluru PV-ED system design. RO brackish water desalination plant installed by Tata Projects Ltd., which has been used for eight years.
Recommended publications
  • Reverse Osmosis and Nanofiltration, Second Edition
    Reverse Osmosis and Nanofiltration AWWA MANUAL M46 Second Edition Science and Technology AWWA unites the entire water community by developing and distributing authoritative scientific and technological knowledge. Through its members, AWWA develops industry standards for products and processes that advance public health and safety. AWWA also provides quality improvement programs for water and wastewater utilities. Copyright © 2007 American Water Works Association. All Rights Reserved. Contents List of Figures, v List of Tables, ix Preface, xi Acknowledgments, xiii Chapter 1 Introduction . 1 Overview, 1 RO and NF Membrane Applications, 7 Membrane Materials and Configurations, 12 References, 18 Chapter 2 Process Design . 21 Source Water Supply, 21 Pretreatment, 26 Membrane Process Theory, 45 Rating RO and NF Elements, 51 Posttreatment, 59 References, 60 Chapter 3 Facility Design and Construction . 63 Raw Water Intake Facilities, 63 Discharge, 77 Suspended Solids and Silt Removal Facilities, 80 RO and NF Systems, 92 Hydraulic Turbochargers, 95 Posttreatment Systems, 101 Ancillary Equipment and Facilities, 107 Instrumentation and Control Systems, 110 Waste Stream Management Facilities, 116 Other Concentrate Management Alternatives, 135 Disposal Alternatives for Waste Pretreatment Filter Backwash Water, 138 General Treatment Plant Design Fundamentals, 139 Plant Site Location and Layout, 139 General Plant Layout Considerations, 139 Membrane System Layout Considerations, 140 Facility Construction and Equipment Installation, 144 General Guidelines for Equipment Installation, 144 Treatment Costs, 151 References, 162 iii Copyright © 2007 American Water Works Association. All Rights Reserved. Chapter 4 Operations and Maintenance . 165 Introduction, 165 Process Monitoring, 168 Biological Monitoring, 182 Chemical Cleaning, 183 Mechanical Integrity, 186 Instrumentation Calibration, 188 Safety, 190 Appendix A SI Equivalent Units Conversion Tables .
    [Show full text]
  • Thermal Desalination Using MEMS and Salinity-Gradient Solar Pond Technology
    Thermal Desalination using MEMS and Salinity-Gradient Solar Pond Technology University of Texas at El Paso El Paso, Texas Cooperative Agreement No. 98-FC-81-0047 Desalination Research and Development Program Report No. 80 August 2002 U.S. Department of the Interior Bureau of Reclamation Technical Service Center Water Treatment Engineering and Research Group Form Approved REPORT DOCUMENTATION PAGE OMB No. 0704-0188 Public reporting burden for this collection of information is estimated to average 1 hour per response, including the time for reviewing instructions, searching existing data sources, gathering and maintaining the data needed, and completing and reviewing the collection of information. Send comments regarding this burden estimate or any other aspect of this collection of information, including suggestions for reducing this burden to Washington Headquarters Services, Directorate for Information Operations and Reports, 1215 Jefferson Davis Highway, Suit 1204, Arlington VA 22202-4302, and to the Office of Management and Budget, Paperwork Reduction Report (0704-0188), Washington DC 20503. 1. AGENCY USE ONLY (Leave Blank) 2. REPORT DATE 3. REPORT TYPE AND DATES COVERED August 2002 4. TITLE AND SUBTITLE 5. FUNDING NUMBERS Thermal Desalination using MEMS and Salinity-Gradient Solar Pond Technology Agreement No. 98-FC-81-0047 6. AUTHOR(S) Huanmin Lu, John C. Walton, and Herbert Hein 7. PERFORMING ORGANIZATION NAME(S) AND ADDRESS(ES) 8. PERFORMING ORGANIZATION REPORT NUMBER University of Texas at El Paso El Paso, Texas 9. SPONSORING/MONITORING AGENCY NAME(S) AND ADDRESS(ES) 10. SPONSORING/MONITORING Bureau of Reclamation AGENCY REPORT NUMBER Desalination Research and Denver Federal Center Development Program Report No.
    [Show full text]
  • Commercial Thermal Technologies for Desalination of Water from Renewable Energies: a State of the Art Review
    Preprints (www.preprints.org) | NOT PEER-REVIEWED | Posted: 4 January 2021 doi:10.20944/preprints202101.0033.v1 Review Commercial Thermal Technologies for Desalination of Water from Renewable Energies: A State of the Art Review Jhon Feria-Díaz 1, 2, *, María López-Méndez 1, Juan Rodríguez-Miranda 3, Luis Sandoval-Herazo 1 and Felipe Correa-Mahecha 4 1 Instituto Tecnológico Superior de Misantla, Km 1.8 Carretera Lomas del Cojolite, 93821 Misantla, México; [email protected]; [email protected]; [email protected] 2 Universidad de Sucre, Cra. 28 #5-267, Sincelejo, Colombia; [email protected] 3 Universidad Distrital Francisco José de Caldas, Cra. 7 #40b-53, Bogotá, Colombia; [email protected] 4 Fundación Universidad de América, Avda Circunvalar No. 20-53, Bogotá, Colombia; [email protected] * Correspondence: [email protected] Abstract: Thermal desalination is yet a reliable technology in the treatment of brackish water and seawater; however, its demanding high energy requirements have lagged it compared to other non- thermal technologies such as reverse osmosis. This review provides an outline of the development and trends of the three most commercially used thermal or phase change technologies worldwide: Multi Effect Distillation (MED), Multi Stage Flash (MSF), and Vapor Compression Distillation (VCD). First, state of water stress suffered by regions with little fresh water availability and existing desalination technologies that could become an alternative solution are shown. The most recent studies published for each commercial thermal technology are presented, focusing on optimizing the desalination process, improving efficiencies, and reducing energy demands. Then, an overview of the use of renewable energy and its potential for integration into both commercial and non- commercial desalination systems is shown.
    [Show full text]
  • Chapter 9 Solar Desalination 1. Introduction
    CHAPTER 9 SOLAR DESALINATION John H. Lienhard,1,¤ Mohamed A. Antar,2 Amy Bilton,1 Julian Blanco,3 & Guillermo Zaragoza4 1 Center for Clean Water and Clean Energy, Room 3-162, Department of Mechanical Engineering, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Cambridge, Massachusetts 02139-4307, USA 2 Department of Mechanical Engineering, King Fahd University of Petroleum and Minerals, Dhahran, Saudi Arabia 3 Plataforma Solar de Almeria, Carretera de Senes s/n, 04200 Tabernas (Almeria), Spain 4 Visiting Professor of Electrical Engineering, King Saud University, Riyadh, Saudi Arabia ¤Address all correspondence to John H. Lienhard E-mail: [email protected] In many settings where freshwater resources or water supply infrastructure are inadequate, fossil energy costs may be high whereas solar energy is abundant. Further, in the industri- alized world, government policies increasingly emphasize the replacement of fossil energy by renewable, low-carbon energy, and so water scarce regions are considering solar-driven desalination systems as a supplement to existing freshwater supplies. Even in regions where petroleum resources are copious, solar-driven desalination is attractive as a means of con- serving fossil fuel resources and limiting the carbon footprint of desalination. Finally, in set- tings that are remote and ‘off-the-grid,” a solar driven desalination system may be more eco- nomical than alternatives such as trucked-in water or desalination driven by diesel-generated electricity. This article reviews various technologies that couple thermal or electrical solar energy to thermal or membrane based desalination systems. Basic principles of desalination are reviewed. Solar stills and humidification-dehumidification desalination systems are dis- cussed.
    [Show full text]
  • Wastewater Treatment by Electrodialysis System and Fouling Problems
    The Online Journal of Science and Technology - January 2016 Volume 6, Issue 1 WASTEWATER TREATMENT BY ELECTRODIALYSIS SYSTEM AND FOULING PROBLEMS Elif OZTEKIN, Sureyya ALTIN Bulent Ecevit University, Department of Environmental Engineering, Zonguldak-Turkey [email protected], VDOWÕQ#NDUDHOPDVHGXWU Abstract: Electrodialysis ED is a separation process commercially used on a large scale for production of drinking water from water bodies and treatment of industrial effluents (Ruiz and et al., 2007). ED system contains ion exchange membranes and ions are transported through ion selective membranes from one solution to another under the influence of electrical potential difference used as a driving force. ED has been widely used in the desalination process and recovery of useful matters from effluents. The performance of ED, depends on the operating conditions and device structures such as ion content of raw water, current density, flow rate, membrane properties, feed concentration, geometry of cell compartments (Chang and et al., 2009, Mohammadi and et al., 2004). The efficiency of ED systems consist in a large part on the properties of the ion exchange membranes. Fouling of ion exchange membranes is one of the common problems in ED processes (Lee and et al., 2009, Ruiz and et al., 2007). Fouling is basically caused by the precipitation of foulants such as organics, colloids and biomass on the membrane surface or inside the membrane and fouling problem reduces the transport of ions. The fouling problems are occasion to increase membrane resistance, loss in selectivity of the membranes and affect negatively to membrane performance (Lee and et al., 2002, Lindstrand and et al., 2000a, Lindstrand and et al., 2000b).
    [Show full text]
  • Demineralization Treatment Technologies for the Seawater Demineralization Feasibility Investigation
    Special Publication SJ2004-SP7 Demineralization Treatment Technologies for the Seawater Demineralization Feasibility Investigation Technical Memorandum B.7 Demineralization Treatment Technologies For the Seawater Demineralization Feasibility Investigation Contract #SE459AA by R. W. Beck, Inc. 800 North Magnolia Avenue, Suite 300 Orlando, Florida 32803-3274 FINAL St. Johns River Water Management District P.O. Box 1429 Highway 100 West Palatka, Florida December 31, 2002 Contents Contents 1.0 INTRODUCTION 1.1 General ............................................................................................................. 1 1.2 Purpose............................................................................................................. 1 1.3 Early Desalination Technologies.................................................................... 2 2.0 THERMAL DESALINATION PROCESSES.................................................... 3 2.1 History.............................................................................................................. 3 2.2 Multi-stage Flash Distillation ......................................................................... 4 2.3 Multi-effect Distillation................................................................................... 4 2.4 Vapor Compression......................................................................................... 5 2.5 Thermal Plant Performance Enhancements................................................. 5 3.0 MEMBRANE TECHNOLOGY..........................................................................
    [Show full text]
  • Application of Electrodialysis in Waste Water Treatment and Impact Of
    ne Scien ra ce b & m T Akhter and Habib, J Membr Sci Technol 2018, 8:2 e e M c h f n o DOI: 10.4172/2155-9589.1000182 o l l a o Journal of Membrane n g r y u ISSN: 2155-9589 o J Science & Technology Review Article Open Access Application of Electrodialysis in Waste Water Treatment and Impact of Fouling on Process Performance Mohsan Akhter, Ghulam Habib* and Sana Ullah Qamar Department of Chemical Engineering, National University of Science and Technology, Islamabad, Pakistan Abstract Electrodialysis (ED) is a new advanced separation process that is commonly utilized for producing drinking water from water bodies as well as for the treatment of industrial effluents. ED process is applied on commercial scale. Basically, an ED process consists of an ion exchange membrane and the diving force necessary for applicability of the process is electric potential. Due to the presence of electric potential ions from one solution after passing through ion selective membrane barrier are transferred to another solution. The main factors on which ED process performance depends on concentration of ion in raw water, flow rate, concentration of feed, current density, membrane properties and cell compartments geometry. Fouling which is produced by foulants including organics, colloids and biomass on the inside membrane internal structure or on the outside surface results in reduction of process separation efficiency and energy consumption is enhanced. Fouling increases the membrane resistance and selectivity of membrane is reduced by fouling. Therefore, some methods are proposed to reduce fouling in ED system such as pre-treatment of feed solution, zeta potential control, membrane properties modification and flowrate optimization.
    [Show full text]
  • Florida Brackish Water and Seawater Desalination: Challenges and Opportunities
    FWRJ Florida Brackish Water and Seawater Desalination: Challenges and Opportunities Christopher P. Hill lorida has historically been the pioneer in face water. As the population of Florida has desalination in the United States. As a grown and the availability of fresh groundwa - Christopher P. Hill, P.E., BCEE, is drinking matter of necessity, it was one of the first ter has diminished, there has been a move - F water technical leader with Brown and states to embrace desalinated groundwater as a ment towards alternative water supplies, Caldwell in Tampa. source of drinking water. Florida installed its including brackish groundwater, surface water, first desalination facility in 1969, which was a and seawater. small electrodialysis (ED) facility in Siesta Key. Today, Florida boasts more than 150 desalina - Desalination and In the mid-2000s, much of Florida was fac - tion facilities, with a combined capacity of more Water Supply Planning ing looming water shortages and the need for al - than 515 million gallons per day (mgd) and ac - ternative water supplies was imminent. As a counting for nearly 25 percent of Florida’s total Florida’s five water management districts result, many water providers maximized exist - water supply (Figure 1). are responsible for sustainable management of ing supplies and began developing alternative From groundwater to seawater, no state its water resources. Each of the districts devel - supplies. Now, in the midst of the national hous - has more operating desalination capacity. ops a regional water supply plan (RWSP) every ing and economic crises, many of these same Florida accounts for more than 50 percent of five years that evaluates the adequacy of exist - water suppliers find themselves flush with un - the U.S.
    [Show full text]
  • An Overview of Industrial Desalination Technologies ASME Industrial Demineralization (Desalination): Best Practices & Future Directions Workshop
    An Overview of Industrial Desalination Technologies ASME Industrial Demineralization (Desalination): Best Practices & Future Directions Workshop Washington, D.C. Shahid Chaudhry January 28-29, 2013 1 • The Challenge: Increasing Demand of Water & Energy Resources; Decreasing Supplies of Conventional Water & Energy Resources. Sustainable Management of Water & Energy Resources 2 • Eight Major Water Using Industries Oil & Gas Refining & Petrochemicals Power Generation Food and Beverage Pharmaceutical Microelectronics Pulp & Paper, and Mining GWI: Industrial Desalination & Water Reuse: Ultrapure water, challenging waste streams and improved efficiency, 3 Strategies: Water Conservation / Water Use Efficiency Unaccounted / Water Losses Water Recycling Desalination - Most Energy Intensive / Expensive Water? 4 • Desalination An Energy Intensive Process, An Integral Part of the Future Water Supply Portfolio Source Waters – Generally Four Types Brackish Ground Water, Surface Water, Municipal WW, Agricultural Runoff, Industrial Effluents, Sea Water, etc. Main Processes Categories: Thermal 4 - 6 kWh / m3 + Steam Heating of Contaminated Water under Vacuum Conditions to Create Pure Water Vapors) Membranes 1 - 6 kWh / m3 Energy Requirements - Function of: Plant Capacity, Feed Water Quality, Pretreatment, Desalination Process/Technology, and Level of Treatment Desalination Technology of Most Interest Today Reverse Osmosis 5 • Desalination Methods Distillation Multi-Stage Flash Distillation (MSF) Multiple-Effect Distillation (MED / ME) Vapor-Compression
    [Show full text]
  • Electrodialysis Reversal (EDR)
    GE Power & Water Water & Process Technologies Electrodialysis Reversal (EDR) What GE offers GE offers the broadest water and process technologies solutions portfolio—we focus on difficult-to-treat water and wastewater, and implementing water reuse solutions to provide customers with the quantity and quality of water they need for their applications. GE’s $2 billion-plus water division has 8,000 employees worldwide dedicated to solving every kind of water problem and making GE one of the most admired and respected companies operating today. With over 50 years of ED-EDR technology experience, we have the technical knowledge and process expertise to design solutions that are reliable and cost effective for your water purification needs. With 900+ EDR installations globally, GE offers a depth of experience for the design, manufacturing, installation, operation and maintenance of your EDR system. Customer Benefits • Simplified operation and lower capital costs with the GE carbon electrode • Up to 95% TDS reduction on brackish water • Up to 94% water recovery • Requires less pretreatment for suspended solids • High silica levels do not impact performance or water recovery • Handles high organic waters • Up to 0.5 mg/l continuous chlorine feed and capable of shock treatments New Developments in EDR Technology Carbon Electrode AR908 Membrane GE has developed a new electrode which will become the GE has developed a new caustic-stable ion exchange standard electrode for all new GE EDR systems and can also membrane for ED that allows for more aggressive CIP be used in upgrades to existing EDR systems. of EDR stacks. • The Carbon Electrode • AR908 membranes surface is coated allow EDR stacks to be with the same ion cleaned up to pH 13, to exchange resin that keep stacks clean while is contained in GE’s processing higher turbidity membranes.
    [Show full text]
  • Desalination Methods for Producing Drinking Water
    E-249 04-10 Desalination Methods for Producing Drinking Water *Justin K. Mechell and Bruce Lesikar s populations increase and sources of high- Source waters quality fresh drinking water decrease, many Several factors influence the selection of source Acommunities have considered using desalina- waters to feed desalination plants: the location of the tion processes to provide fresh water when other plant in relation to water sources available, the deliv- sources and treatment procedures are uneconomical ery destination of the treated water, the quality of or not environmentally responsible. the source water, the pretreatment options available, Desalination is any process that removes excess and the ecological impacts of the concentrate dis- salts and other minerals from water. In most desali- charge. nation processes, feed water is treated and two streams of water are produced: Seawater • Treated fresh water that has low concentra- Seawater is taken into a desalination plant ei- tions of salts and minerals ther from the water’s surface or from below the sea • Concentrate or brine, which has salt and floor. In the past, large-capacity seawater desalina- mineral concentrations higher than that of tion plants have used surface intakes on the open the feed water sea. The feed water for desalination processes can Although surface water intake can affect and be be seawater or brackish water. Brackish water con- affected by organisms in the ocean, the issues related tains more salt than does fresh water and less than to this method can be minimized or resolved by salt water. It is commonly found in estuaries, which proper intake design, operation, and maintenance of are the lower courses of rivers where they meet the technologies.
    [Show full text]
  • Nanophotonics-Enabled Solar Membrane Distillation for Off-Grid Water Purification
    Nanophotonics-enabled solar membrane distillation for off-grid water purification Pratiksha D. Dongarea,b,c,d,1, Alessandro Alabastria,b,d,1, Seth Pedersend,e, Katherine R. Zodrowd,e, Nathaniel J. Hogana,b,c, Oara Neumanna,b,d, Jinjian Wud,e, Tianxiao Wange, Akshay Deshmukhd,f, Menachem Elimelechd,f, Qilin Lid,e,2, Peter Nordlandera,b,d,g, and Naomi J. Halasa,b,d,g,h,2 aDepartment of Electrical and Computer Engineering, Rice University, Houston, TX 77005; bLaboratory for Nanophotonics, Rice University, Houston, TX 77005; cApplied Physics Graduate Program, Rice University, Houston, TX 77005; dNanosystems Engineering Research Center for Nanotechnology-Enabled Water Treatment (NEWT), Rice University, Houston, TX 77005; eDepartment of Civil and Environmental Engineering, Rice University, Houston, TX 77005; fDepartment of Chemical and Environmental Engineering, Yale University, New Haven, CT 06520-8286; gDepartment of Physics and Astronomy, Rice University, Houston, TX 77005; and hDepartment of Chemistry, Rice University, Houston, TX 77005 Contributed by Naomi J. Halas, May 16, 2017 (sent for review February 2, 2017; reviewed by Svetlana V. Boriskina and Amy Childress) With more than a billion people lacking accessible drinking water, there its flow through the module suffers these same inherent limitations is a critical need to convert nonpotable sources such as seawater to (17–21). Localized heating in the feed channel can be achieved by water suitable for human use. However, energy requirements of integrating MD into industrial processes (22) or by using a solar desalination plants account for half their operating costs, so alternative, absorber plate above the feed channel (23) to provide supplemen- lower energy approaches are equally critical.
    [Show full text]