Design and Simulation of a Solar Energy System for Desalination of Brackish Water
Total Page:16
File Type:pdf, Size:1020Kb
Load more
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 . -
Dynamic Modeling of Multi Stage Flash (MSF) Desalination Plant
Dynamic Modeling of Multi Stage Flash (MSF) Desalination Plant by Hala Faisal Al-Fulaij Department of Chemical Engineering University College London Supervisors: Professor David Bogle Thesis submitted for the degree of Doctor of Philosophy (Ph.D.) at University College London (UCL) July 2011 I, Hala Faisal Al-Fulaij, confirm that the work presented in this thesis is my own. Where information has been derived from other sources, I confirm that this has been indicated in the thesis. Hala F. Al-Fulaij Acknowledgments i Acknowledgments This Ph.D. was carried out between March 2007 and January 2011 at the Chemical Engineering department, University College London (UCL). This work was supervised by Professor David Bogle (UCL) and Professor Hisham Ettouney (Kuwait University). I take this opportunity to thank both of my supervisors for general guidance throughout the project and their great help, support and insight. I also thank Professor Giorgio Micale and Doctor Andrea Cipollina from University of Palermo who expended their time and made significant contribution to my knowledge especially in the computer tools field. Also, I am grateful for the love and support of my family, especially my mother, father, husband and sisters. Their patience and encouragement have given me the strength to complete my thesis study. Finally I would like to dedicate this thesis to my lovely children (Rayan, Maryam, AbdulWahab and Najat) hoping them the most of health, success, and happiness. Abstract ii Abstract The world population is increasing at a very rapid rate while the natural water resources remain constant. During the past decades industrial desalination (reverse osmosis (RO) and multistage flash desalination (MSF)) became a viable, economical, and sustainable source of fresh water throughout the world. -
Characterization and Performance of Nanofiltration Membranes
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by Covenant University Repository Environ Chem Lett (2014) 12:241–255 DOI 10.1007/s10311-014-0457-3 REVIEW Characterization and performance of nanofiltration membranes Oluranti Agboola • Jannie Maree • Richard Mbaya Received: 16 October 2013 / Accepted: 17 January 2014 / Published online: 1 February 2014 Ó Springer International Publishing Switzerland 2014 Abstract The availability of clean water has become a nanofiltration membranes. We also present a new concept critical problems facing the society due to pollution by for membrane characterization by quantitative analysis of human activities. Most regions in the world have high phase images to elucidate the macro-molecular packing at demands for clean water. Supplies for freshwater are under the membrane surface. pressure. Water reuse is a potential solution for clean water scarcity. A pressure-driven membrane process such as Keywords Nanofiltration membranes Á Membrane nanofiltration has become the main component of advanced characterizations Á Pore size Á Surface morphology Á water reuse and desalination systems. High rejection and Performance evaluation Á ImageJ software water permeability of solutes are the major characteristics that make nanofiltration membranes economically feasible for water purification. Recent advances include the pre- Introduction diction of membrane performances under different oper- ating conditions. Here, we review the characterization of Nanofiltration process is one of the most important recent nanofiltration membranes by methods such as scanning developments in the process industries. It shows performance electron microscopy, thermal gravimetric analysis, attenu- characteristics, which fall in between that of ultrafiltration ated total reflection Fourier transform infrared spectros- and reverse osmosis membranes (Mohammed and Takriff copy, and atomic force microscopy. -
Nanofiltration (NF) Is a Pressure Driven Membrane Process
Nanofiltration Nanofiltration (NF) is a pressure driven membrane process. Hydraulic pressure is used to overcome the feed solution’s osmotic pressure and to induce diffusion of pure water (referred to as permeate) through a semi-permeable NF membrane. The residual feed stream (referred to as retentate, concentrate, or reject) is concentrated by the process, and depending on water quality, may be suitable for further water recovery in additional downstream unit processes; otherwise, the residual stream requires disposal. NF is designed to achieve high removal of divalent and multivalent ions (e.g., calcium, magnesium, sulfate, iron, arsenic, etc.), and is occasionally referred to as membrane softening. NF may achieve moderate to low removal of monovalent ions (e.g., sodium, potassium, chloride). NF is commonly employed to remove hardness from brackish groundwater to produce potable water. Water characterized by high concentrations of calcium or magnesium and monovalent salts may be treated with NF prior to a reverse osmosis. An illustration of the process is shown below. FEED NF PERMEATE CONCENTRATE Summary of technical assessment of NF Criteria Description/Rationale Status of technology Mature and robust technology for water softening and metals removal in various sectors of the industrial and municipal water treatment sectors. Has been employed for produced water treatment. Feed water quality bins Feed water total dissolved solids concentration applicability depends on feed solution composition and may range from 500 to 12,000 mg/L. Most useful for treatment of water with high concentrations of divalent ions (e.g., magnesium, calcium, barium, sulfate), multivalent metals ions (e.g., iron, manganese), and radionuclides. -
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. -
Forward Osmosis – a Brief Introduction
Forward Osmosis – A Brief Introduction This paper outlines some of the aspects of Forward Osmosis process and its derivatives, with regard to key issues, concepts and some applications. By Peter G. Nicoll Forward Osmosis (FO) over the past five years has generally it is apparent that they are increasingly becoming a topic of some attracted more attention, both academically and commercially, interest. National Geographic [1] in an article in April 2010 cited it with a number of companies raising finance on the back of its as one of the three most promising new desalination technologies potential. The process exploits the natural process of osmosis, and at the last IDA World Congress in Perth, Australia in 2011, which is how plants and trees take up water from the soil – a low six papers were published on this subject. In the Journal of energy, natural process. It works by having two solutions with Membrane Science the number of papers published has seen a different concentrations (or more correctly different osmotic very significant increase over the last three years (24 in 2012), pressures) separated by a selectively permeable membrane, in the showing the increasing level of academic interest. We have also case of the plants and trees their cell walls, and ‘pure’ water flows seen the emergence of a number of commercial organisations from less concentrated solution across the membrane to dilute with significant funding to develop and exploit the technology the more concentrated solution, leaving the salts behind. The clue such as, Hydration Technology Innovations Inc, Modern Water in the potential applications is that it is widely used in nature, plc, Oasys Water Inc, Statkraft AS and Trevi Systems Inc. -
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. -
Exploration of an Innovative Draw Solution for a Forward Osmosis- Membrane Distillation Desalination Process
University of Wollongong Research Online Faculty of Engineering and Information Faculty of Engineering and Information Sciences - Papers: Part B Sciences 2017 Exploration of an innovative draw solution for a forward osmosis- membrane distillation desalination process Nguyen Cong Nguyen Dalat University, National Taipei University of Technology Shiao-Shing Chen National Taipei University of Technology Shubham Jain VIT University Hau Thi Nguyen Dalat University, National Taipei University of Technology Saikat Sinha Ray National Taipei University of Technology See next page for additional authors Follow this and additional works at: https://ro.uow.edu.au/eispapers1 Part of the Engineering Commons, and the Science and Technology Studies Commons Recommended Citation Nguyen, Nguyen Cong; Chen, Shiao-Shing; Jain, Shubham; Nguyen, Hau Thi; Sinha Ray, Saikat; Ngo, Hao H.; Guo, Wenshan; Lam, Ngoc Tuan; and Duong, Hung, "Exploration of an innovative draw solution for a forward osmosis-membrane distillation desalination process" (2017). Faculty of Engineering and Information Sciences - Papers: Part B. 323. https://ro.uow.edu.au/eispapers1/323 Research Online is the open access institutional repository for the University of Wollongong. For further information contact the UOW Library: [email protected] Exploration of an innovative draw solution for a forward osmosis-membrane distillation desalination process Abstract Forward osmosis (FO) has emerged as a viable technology to alleviate the global water crisis. The greatest challenge facing the application of FO technology is the lack of an ideal draw solution with high water flux and low er verse salt flux. Hence, the objective of this study was to enhance FO by lowering reverse salt flux and maintaining high water flux; the method involved adding small concentrations of Al2(SO4)3 to a MgCl2 draw solution. -
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. -
Journal of Membrane Science 593 (2020) 117444
Journal of Membrane Science 593 (2020) 117444 Contents lists available at ScienceDirect Journal of Membrane Science journal homepage: www.elsevier.com/locate/memsci Nanofiltration membranes with hydrophobic microfiltration substrates for robust structure stability and high water permeation flux T ∗∗ ∗ Xi Zhanga,b, Chang Liua,b, Jing Yanga,b, , Cheng-Ye Zhua,b, Lin Zhangc, Zhi-Kang Xua,b, a MOE Key Laboratory of Macromolecular Synthesis and Functionalization, Hangzhou, 310027, China b Key Laboratory of Adsorption and Separation Materials & Technologies of Zhejiang Province, Department of Polymer Science and Engineering, Zhejiang University, Hangzhou, 310027, China c Key Laboratory of Biomass Chemical Engineering, College of Chemical and Biological Engineering, Zhejiang University, Hangzhou, 310027, China ARTICLE INFO ABSTRACT Keywords: Traditional nanofiltration membranes (NFMs) suffer from ultrafiltration substrates with low porosity, small pore Nanofiltration membrane size and relatively poor solvent stability. Herein, NFMs have been fabricated on a series of hydrophobic polymer Microfiltration substrate microfiltration substrates to address these issues. Polyphenol-based coatings of tannic acid/diethylenetriamine Surface wettability (TA/DETA) were co-deposited on the hydrophobic substrates to improve their surface wettability and to make Water permeation flux them appropriate for interfacial polymerization. The spreading behaviors of aqueous solutions, which are of Structure stability significant importance to the formation of defect-free polyamide layers, were directly visualized by laser con- focal microscopy. The influences of TA/DETA coatings on the interfacial polymerization were further demon- strated by both dynamic molecular simulation and nanofiltration performance evaluation. The as-prepared NFMs exhibit higher water permeation flux compared with traditional ones because of the large pore size and high porosity of the microfiltration substrates, as well as the relatively low cross-linking degree of polyamide layers. -
1 Selectrodialysis and Bipolar Membrane
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by UPCommons. Portal del coneixement obert de la UPC 1 SELECTRODIALYSIS AND BIPOLAR MEMBRANE ELECTRODIALYSIS 2 COMBINATION FOR INDUSTRIAL PROCESS BRINES TREATMENT: 3 MONOVALENT-DIVALENT IONS SEPARATION AND ACID AND BASE 4 PRODUCTION 5 6 Mònica Reig1,*, César Valderrama1, Oriol Gibert1,2, José Luis Cortina1,2 7 8 1Chemical Engineering Dept., UPC-Barcelona TECH, Av. Diagonal 647, 08028 Barcelona, Spain 9 2CETAQUA Carretera d'Esplugues, 75, 08940 Cornellà de Llobregat, Spain 10 *Corresponding author: Tel.:+34 93 4016997; E-mail address: [email protected] 11 12 13 ABSTRACT 14 Chemical industries generate large amounts of wastewater rich in different chemical 15 constituents. Amongst these, salts at high concentrations are of major concern, making 16 necessary the treatment of saline effluents before discharge. Because most of these rejected 17 streams comprise a combination of more than one salt at high concentration, it is reasonable 18 to try to separate and revalorize them to promote circular economy at industry site level. For 19 this reason, ion-exchange membranes based technologies were integrated in this study: 20 selectrodialysis (SED) and electrodialysis with bipolar membranes (EDBM). Different 21 process brines composed by Na2SO4 and NaCl at different concentrations were treated first by 22 SED to separate each salt, and then by EDBM to produce base (NaOH) and acids (HCl and 23 H2SO4) from each salt. The optimum of both electrolyte nature and concentration of the SED - 2- 24 stack streams was evaluated. Results indicated that it was possible to separate Cl and SO4 25 depending on the anionic membrane, initial electrolytes and concentrations of each stream. -
Emergence of Forward Osmosis and Pressure-Retarded Osmotic Processes for Drinking Water Treatment
FWRJ Emergence of Forward Osmosis and Pressure-Retarded Osmotic Processes for Drinking Water Treatment Steven J. Duranceau Description of Emerging Processes from a solution of a lower concentration to a so - lution with a higher concentration. These three Steven J. Duranceau is associate professor of Approximately 97 percent of the Earth’s technologies (RO, FO, and PRO) are common environmental engineering in the civil, water takes the form of salt water in oceans, seas, in that they use semi-permeable membranes to environmental, and construction engineering and lakes. Because of a worldwide water short - separate dissolved solutes from water. The semi- department at the University of Central age, a need exists for alternative desalination permeable membrane acts as a barrier that al - Florida in Orlando. technologies that can produce inexpensive, reli - lows small molecules such as water to pass able, and sustainable sources of water for the through, while rejecting larger molecules like world’s growing population, as well as to meet salts, organics, and proteins, as well as viruses, its industrial and agricultural needs. Green en - bacteria, and other pathogenic material. Both solution on the permeate side of the mem - ergy is available wherever one finds a river that FO and PRO exploit the osmotic pressure dif - brane is the driving force in the FO process. flows into a sea, equivalent to the energy con - ference that develops when a semi-permeable The flux direction of the permeating water in tained in a 900-ft-high waterfall[1]. Desalina - membrane separates two solutions of different FO, PRO, and RO is demonstrated in Figure tion technologies, such as reverse osmosis (RO) concentrations.