Water Desalination Concentrate Management and Piloting

Total Page:16

File Type:pdf, Size:1020Kb

Water Desalination Concentrate Management and Piloting WATER DESALINATION CONCENTRATE MANAGEMENT AND PILOTING SOUTH FLORIDA WATER MANAGEMENT DISTRICT DECEMBER 2009 Prepared By 1301 INTERNATIONAL PARKWAY • SUITE 550 • SUNRISE, FLORIDA 33323 • (954) 837- 0030 • FAX (954) 837- 0035 South Florida Water Management District Water Desalination Concentrate Management and Piloting TABLE OF CONTENTS Page EXECUTIVE SUMMARY ES.1 Purpose ......................................................................................................... viii ES.2 Background ................................................................................................... viii ES.3 Project Components ........................................................................................ ix ES.4 Results and Recommendation ........................................................................ ix 1.0 INTRODUCTION 1.1 Purpose ........................................................................................................... 1 1.2 Background ..................................................................................................... 1 1.3 Reverse Osmosis Technology ......................................................................... 3 2.0 SOURCE WATER AND CONCENTRATE DATA COLLECTION 2.1 Purpose ........................................................................................................... 7 2.2 Scope .............................................................................................................. 7 2.3 List of Water Treatment Facilities .................................................................... 8 2.4 Water Quality and Membrane Simulations ...................................................... 9 2.5 Water Quality Categories .............................................................................. 13 2.5.1 Category 1 - CaCO3, BaSO4, and SrSO4 ....................................... 13 2.5.2 Category 2 - CaSO4, CaCO3, BaSO4, and SrSO4 .......................... 13 2.5.3 Category 3 - CaSO4, CaCO3, BaSO4, and SrSO4 (Unique RO Feed) ........................................................................................ 15 2.5.4 Category 4 - Surface Water/Seawater ............................................ 15 2.6 Representative Facility for Each Water Quality Category .............................. 15 2.7 Summary ....................................................................................................... 16 3.0 CHARACTERIZATION OF THE EXISTING PLANT TREATMENT SCHEMES 3.1 Purpose ......................................................................................................... 18 3.2 Scope ............................................................................................................ 18 3.3 Facility Process Analysis ............................................................................... 18 3.3.1 City of North Miami Beach, Norwood-Oeffler Water Treatment Plant ............................................................................................... 20 3.3.2 City of Deerfield Beach, West Water Treatment Plant ..................... 21 3.3.3 City of Hollywood Water Treatment Plant ........................................ 25 3.3.4 Marathon Seawater Desalination Facility ........................................ 25 3.4 Technology Feasibility Evaluation ................................................................. 28 3.4.1 Dual Reverse Osmosis with Intermediate Chemical Precipitation .................................................................................... 28 3.4.2 Thermal Evaporation (Brine Concentration) and Evaporation Pond ............................................................................................... 31 3.4.3 Thermal Evaporation (Brine Concentration) and Brine Crystallization ................................................................................. 35 i pw://Carollo/Documents/Client/FL/SFWMD/8178A00/Deliverables/Final Report.doc 3.4.4 Salt Extraction and Recovery .......................................................... 38 3.5 Comparison of the Concentrate Minimization Technologies and Pilot Study Recommendation .......................................................................................... 41 3.6 Summary ....................................................................................................... 43 4.0 EXAMINATION OF TECHNICAL, PERMITTING, AND IMPLEMENTATION FACTORS 4.1 Purpose ......................................................................................................... 44 4.2 Scope ............................................................................................................ 44 4.3 Background ................................................................................................... 44 4.4 Approach ....................................................................................................... 44 4.5 Regulations for Disposal of Reverse Osmosis Concentrate ........................... 45 4.5.1 Hazardous Waste ........................................................................... 46 4.5.2 Regulations Affecting Concentrate Disposal in the District .............. 48 4.6 Concentrate Disposal Systems...................................................................... 58 4.6.1 City of Deerfield Beach WTP .......................................................... 58 4.6.2 City of North Miami Beach WTP...................................................... 58 4.6.3 Florida Keys Aqueduct Authority Marathon Seawater Desalination Facility ........................................................................ 59 4.6.4 City of Hollywood Water Treatment Plant ........................................ 59 4.7 Effects of Increased Recovery ....................................................................... 60 4.7.1 Effect of Increased Recovery on RO Concentrate Water Quality ............................................................................................ 60 4.7.2 Predicted Solid Waste Composition ................................................ 63 4.7.3 Potential Effect of Concentrate Treatment on Waste Stream Disposal .......................................................................................... 63 4.8 Concentrate Minimization Technologies ........................................................ 67 4.8.1 Dual Reverse Osmosis with Intermediate Chemical Precipitation .................................................................................... 67 4.8.2 Thermal Evaporation and Brine Crystallizer .................................... 68 4.8.3 Thermal Evaporation and Evaporation Pond ................................... 68 4.8.4 Salt Extraction and Recovery .......................................................... 69 4.9 Summary ....................................................................................................... 69 5.0 ESTIMATION OF THE COSTS AND BENEFITS OF IMPLEMENTING THE RECOMMENDED IMPROVEMENTS 5.1 Purpose ......................................................................................................... 72 5.2 Scope ............................................................................................................ 72 5.3 Approach ....................................................................................................... 72 5.4 Treatment Alternatives .................................................................................. 73 5.5 Flows for Cost Opinions ................................................................................ 73 5.6 Assumptions for Cost Opinions ..................................................................... 77 5.6.1 Common Assumptions .................................................................... 77 5.6.2 Other Assumptions for Concentrate Treatment Operations ............. 79 5.7 Cost Opinions ................................................................................................ 81 5.7.1 North Miami Beach WTP ................................................................ 81 5.7.2 Hollywood WTP .............................................................................. 85 5.7.3 Deerfield Beach WTP ..................................................................... 89 5.7.4 Cost Comparison and Conclusions ................................................. 93 6.0 PILOT STUDY 6.1 Purpose ......................................................................................................... 94 ii pw://Carollo/Documents/Client/FL/SFWMD/8178A00/Deliverables/Final Report.doc 6.2 Background ................................................................................................... 94 6.3 Objectives ..................................................................................................... 95 6.4 Materials and Methods .................................................................................. 95 6.4.1 Bench Scale Tests .......................................................................... 95 6.4.2 Pilot Unit Process Description ......................................................... 95 6.4.3 Pilot Operation ................................................................................ 99 6.4.4 Schedule ....................................................................................... 101 6.4.5 Sampling and Analysis .................................................................. 101 6.4.6 Roles and Responsibilities ............................................................ 104 6.5 Results and Discussion ..............................................................................
Recommended publications
  • Water Treatment and Reverse Osmosis Systems
    Pure Aqua, Inc.® Water© 2012 TreatmentPure Aqua ,and Inc. ReverseAll Right sOsmosis Reserve dSystems. Worldwide Experience Superior Technology About the Company Pure Aqua is a company with a strong philosophy and drive to develop and apply solutions to the world’s water treatment challenges. We believe that both our technology and experience will help resolve the growing shortage of clean water worldwide. Capabilities and Expertise As an ISO 9001:2008 certified company with over a decade of experience, Pure Aqua has secured its position as a leading manufacturer of reverse osmosis systems worldwide. Goals and Motivations Our goal is to provide environmentally sustainable systems and equipment that produce high quality water. We provide packaged systems and technical support for water treatment plants, industrial wastewater reuse, and brackish and seawater reverse osmosis plants. Having strong working relationships with Thus, we ensure our technological our suppliers gives us the capability to contribution to water preservation by provide cost effective and competitive supplying the means and making it highly water and wastewater treatment systems accessible. for a wide range of applications. Seawater Reverse Osmosis Systems System Overview Designed to convert seawater to potable water, desalination systems use high quality reverse osmosis seawater membranes. The process separates dissolved salts by only allowing pure water to pass through the membrane fabric. System Capacities Pure Aqua desalination systems are designed to provide high
    [Show full text]
  • 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]
  • Circle Reverse Osmosis System
    CIRCLE REVERSE OSMOSIS SYSTEM KEY FEATURES Water Saving Technology – Patented technology eliminates backpressure The RC100 conforms to common in conventional RO systems making the Circle up to 10 times more NSF/ANSI 42, 53 and efficient than existing products. 58 for the reduction of Saves You Money – Conventional RO systems waste up to 24 gallons of Aesthetic Chlorine, Taste water per every 1 gallon of filtered water produced. The Circle only wastes and Odor, Cyst, VOCs, an average of 2.1 gallons of water per 1 gallon of filtered water produced, Fluoride, Pentavalent Arsenic, Barium, Radium 226/228, Cadmium, Hexavalent saving you water and money over the life of the product!. Chromium, Trivalent Chromium, Lead, RO Filter Auto Flushing – Significantly extends life of RO filter. Copper, Selenium and TDS as verified Chrome Faucet Included – With integrated LED filter change indicator. and substantiated by test data. The RC100 conforms to NSF/ANSI 372 for Space Saving Compact Design – Integrated rapid refill tank means more low lead compliance. space under the sink. SPECIFICATIONS Product Name H2O+ Circle Reverse Osmosis Water Filtration System Model / SKU RC100 Installation Undercounter Sediment Filter, Pre-Carbon Plus Filter, Post Carbon Block Filter (RF-20): 6 months Filters & Lifespan RO Membrane Filter (RF-40): 24 months Tank Capacity 6 Liters (refills fully in less than one hour) Dimensions 9.25” (W) x 16.5” (H) x 13.75” (D) Net weight 14.6 lbs Min/Max Operating Pressure 40 psi – 120 psi (275Kpa – 827Kpa) Min/Max Water Feed Temp 41º F – 95º F (5º C – 35º C) Faucet Flow Rate 0.26 – 0.37 gallons per minute (gpm) at incoming water pressure of 20–100 psi Rated Service Flow 0.07 gallons per minute (gpm) Warranty One Year Warranty PO Box 470085, San Francisco CA, 94147–0085 brondell.com 888-542-3355.
    [Show full text]
  • Ion Exchange and Disposal Issues Associated with the Brine Waste Stream
    FWRJ Ion Exchange and Disposal Issues Associated With the Brine Waste Stream Julie Karleskint, Daniel Schmidt, Robert Anderson, Jayson Page, and A.J. Berndt he City of Arcadia recently completed from the local water supply authority, it was Julie Karleskint, P.E., is a senior construction of a new 1.5-mil-gal-per- determined that ion exchange would be the associate with Hazen and Sawyer in Tday (mgd) water treatment plant most cost-effective option for construction. A Sarasota. Daniel Schmidt, P.E., is a (WTP) using ion exchange technology to re- reduction in capacity was also provided since senior associate with Hazen and Sawyer place its 3-mgd lime softening WTP. The lime the City’s water supply source, groundwater in Tampa. Robert Anderson, P.E., is a plant had reached the end of its serviceable life from the intermediate aquifer, was limited senior associate with Hazen and Sawyer and the treatment of groundwater for the re- based on current pumping limitations and in Orlando. Jayson Page, P.E., is a moval of radionuclides, hardness, sulfides, or- permitted capacity. senior associate with Hazen and Sawyer ganic carbon, and fluoride was desired in The groundwater is supplied from six order to provide safe drinking water to the wells, approximately 350 ft deep and located in Coral Gables. A.J. Berndt is the utility community. After evaluating several treatment within a 1-mi radius of the plant. A summary director for the City of Arcadia. technologies, including lime treatment, of the water quality from the wellfield is shown nanofiltration, ion exchange, and purchases in Table 1.
    [Show full text]
  • Refinery Wastewater Management Using Multiple Angle Oil-Water Separators
    REFINERY WASTEWATER MANAGEMENT USING MULTIPLE ANGLE OIL-WATER SEPARATORS Kirby S. Mohr, P.E. Mohr Separations Research, Inc. 1278 FM 407 Suite 109 Lewisville, TX 75077 Phone: 918-299-9290 Cell: 918-269-8710 John N. Veenstra, Ph.D., P.E., Oklahoma State University Dee Ann Sanders, Ph.D., P.E. Oklahoma State University A paper presented at the International Petroleum Environment Conference in Albuquerque, New Mexico, 1998 ABSTRACT In this work, an overview of oil-water separation, as used in the petroleum refining industries, is presented along with case studies. Discussions include: impact of solids, legal aspects, and differing types of systems currently in use, along with their advantages and disadvantages. Performance information on separators is presented with an emphasis on new multiple angle coalescing plate technology for refinery wastewater management. Several studies are presented including a large (20,000 US GPM flow rate) system recently installed at a major US refinery. The separator was constructed by converting two existing API separators into four separators, and adding multiple angle coalescing plates to increase throughput and efficiency. A year of operating experience with this system indicates good performance and few problems. Other examples provide information on separators installed in the United States and other countries. Keywords: Oil-water separator, multiple angle, coalescence, refinery, wastewater management, petroleum, coalescing plate technology BACKGROUND AND INTRODUCTION Oil has been refined for various uses for at least 1000 years. An Arab handbook written by Al-Razi, in approximately 865 A.D., describes distillation of “naft” (naphtha) for use in lamps and thus the beginning of oil refining (Forbes).
    [Show full text]
  • Leachate Generated by an Oil - and - Gas
    ISSN: 0078-1576 ~ ~ o ~ ~ o ::r: f­ a:: o z z Leachate Generated by an Oil - and - Gas UJ ~ Brine Pond Site in North Dakota (/) 0..­ zl"­ 0.0o· by LLJz ~~ Edwa rd C. Mu rphy a:: "1: Alan E. Kehew !Xl Cll (/) Gerald H. Groenewold (/)111 William A. Beal ~:J <':>0 I CIl QC: z~ «CIl I 0 -Jill O::e z>­ «~ >-; !Xl(/) Q­ UJ~ ~"­ «~ a::­w2 Zt:) LLJ <.:>~ UJ~ ~/11 «0 ::r: U L.... f«L. LLJO -Jz III L. ell ..c MISCELLANEOUS SERIES 71 +'"o NORTH DAKOTAGEOLOGICALSURVEY 1J Sidney B. Anderson, c Acting State Geologist /11 1988 Reprinted from the January-February 1988, Volume 26, Number 1 issue of Ground Water Leachate Generated by an Oil-and-Gas Brine Pond Site in North Dakota by Edward C. Murphya, Alan E. Kehewb, Gerald H. Groenewoldc , and William A. Beal d ABSTRACT INTRODUCTION Two unlined ponds were used for holding and Brines typically are produced along with evaporation of brines produced with oil and gas at a well crude oil at oil-well sites. These brines are recog­ site in north-centra! North Dakota. The brine-evaporation nized as the major source of potential environ­ ponds were in use from 1959 up to the late 1970s when mental contamination associated with oil produc­ they were backfilled and leveled. Continued salt-water migration at this site since closure has decreased crop yields tion (Knox and Canter, 1980). The issue of how to in surrounding fields and has killed trees in a shelterbel t properly dispose of oil-field brines has been con­ within an area of approximately 10 acres.
    [Show full text]
  • Reverse Osmosis As a Pretreatment of Ion Exchange Equipment at PSE
    Copyright Warning & Restrictions The copyright law of the United States (Title 17, United States Code) governs the making of photocopies or other reproductions of copyrighted material. Under certain conditions specified in the law, libraries and archives are authorized to furnish a photocopy or other reproduction. One of these specified conditions is that the photocopy or reproduction is not to be “used for any purpose other than private study, scholarship, or research.” If a, user makes a request for, or later uses, a photocopy or reproduction for purposes in excess of “fair use” that user may be liable for copyright infringement, This institution reserves the right to refuse to accept a copying order if, in its judgment, fulfillment of the order would involve violation of copyright law. Please Note: The author retains the copyright while the New Jersey Institute of Technology reserves the right to distribute this thesis or dissertation Printing note: If you do not wish to print this page, then select “Pages from: first page # to: last page #” on the print dialog screen The Van Houten library has removed some of the personal information and all signatures from the approval page and biographical sketches of theses and dissertations in order to protect the identity of NJIT graduates and faculty. ABSTRACT REVERSE OSMOSIS AS A PRETREATMENT FOR ION EXCHANGE AT PSE&G'S HUDSON GENERATING STATION by Steven Leon Public Service Electric and Gas Company's Hudson Generating Station has historically had problems providing sufficient high quality water for its two once through, supercritical design boilers. The station requires over 60 million gallons annually to compensate for system losses.
    [Show full text]
  • Selective Salt Recovery from Reverse Osmosis Concentrate Using Inter-Stage Ion Exchange Joshua E
    University of New Mexico UNM Digital Repository Civil Engineering ETDs Engineering ETDs 7-3-2012 Selective salt recovery from reverse osmosis concentrate using inter-stage ion exchange Joshua E. Goldman Follow this and additional works at: https://digitalrepository.unm.edu/ce_etds Recommended Citation Goldman, Joshua E.. "Selective salt recovery from reverse osmosis concentrate using inter-stage ion exchange." (2012). https://digitalrepository.unm.edu/ce_etds/8 This Dissertation is brought to you for free and open access by the Engineering ETDs at UNM Digital Repository. It has been accepted for inclusion in Civil Engineering ETDs by an authorized administrator of UNM Digital Repository. For more information, please contact [email protected]. Joshua E. Goldman Candidate CIVIL ENGINEERING Department This dissertation is approved, and it is acceptable in quality and form for publication: Approved by the Dissertation Committee: Dr. Kerry J. Howe , Chairperson Dr. Bruce M. Thomson Dr. Stephen E. Cabaniss Dr. Jerry Lowry i Selective Salt Recovery from Reverse Osmosis Concentrate Using Inter-stage Ion Exchange BY Joshua E. Goldman B.A., Anthropology, State University of New York at Stony Brook, 2000 M.S, Environmental Science, University of South Florida, 2007 DISSERTATION Submitted in Partial Fulfillment of the Requirements for the Degree of Doctor of Philosophy Engineering The University of New Mexico Albuquerque, New Mexico May, 2012 ii DEDICATION This dissertation is dedicated to the loving memory of my grandmother, Henriette Stein. iii ACKNOWLEDGMENTS This project was funded by the WateReuse Research Foundation. Resins were donated by ResinTech and Purolite. Francis Boodoo of ResinTech provided technical consultation for the pilot design.
    [Show full text]
  • Appendix A: Distillation and Reverse Osmosis Brine NOD, Phase I
    This document is part of Appendix A and includes Distillation and Reverse Osmosis Brine: Nature of Discharge for the “Phase I Final Rule and Technical Development Document of Uniform National Discharge Standards (UNDS),” published in April 1999. The reference number is EPA-842-R-99-001. Phase I Final Rule and Technical Development Document of Uniform National Discharge Standards (UNDS) Distillation and Reverse Osmosis Brine: Nature of Discharge April 1999 NATURE OF DISCHARGE REPORT Distillation and Reverse Osmosis Brine 1.0 INTRODUCTION The National Defense Authorization Act of 1996 amended Section 312 of the Federal Water Pollution Control Act (also known as the Clean Water Act (CWA)) to require that the Secretary of Defense and the Administrator of the Environmental Protection Agency (EPA) develop uniform national discharge standards (UNDS) for vessels of the Armed Forces for “...discharges, other than sewage, incidental to normal operation of a vessel of the Armed Forces, ...” [Section 312(n)(1)]. UNDS is being developed in three phases. The first phase (which this report supports), will determine which discharges will be required to be controlled by marine pollution control devices (MPCDs)—either equipment or management practices. The second phase will develop MPCD performance standards. The final phase will determine the design, construction, installation, and use of MPCDs. A nature of discharge (NOD) report has been prepared for each of the discharges that has been identified as a candidate for regulation under UNDS. The NOD reports were developed based on information obtained from the technical community within the Navy and other branches of the Armed Forces with vessels potentially subject to UNDS, from information available in existing technical reports and documentation, and, when required, from data obtained from discharge samples that were collected under the UNDS program.
    [Show full text]
  • Reverse Osmosis Brochure
    REVERSE OSMOSIS RO Storage Tanks High Purity Water Storage REVERSE OSMOSIS Amtrol invented the pre-pressurized water storage tank over 50 years ago and they are still considered the standard of the industry. These tanks feature a polypropylene liner and butyl diaphragm to prevent water from making contact with the metal tank for cleaner, fresher, better tasting water. All Amtrol RO tanks are manufactured in the USA at our ISO 9001:2008 registered facilities. REVERSE OSMOSIS Tanks • Provide water storage in reverse osmosis water systems. Polypropylene liner and butyl rubber diaphragm • Meet the most demanding specifications for are locked together with potable water. Amtrol’s unique hoop ring • Reliable diaphragm vs. bladder design. and groove design. • Individually tested for safety. ® Durable steel tank for • Available with Pro-Access stainless steel extra-long life. system connection. Typical Installation Cold Hot Drain Line Water Water Line Line Recirculation Line RO Water Membrane Feed Reverse Osmosis Water Storage Tank Pre Post Filter Filter Specifications and Tank Selection A Under Sink Models System Tank A B Tank Shipping Model Connection1 Tank Stand Model Volume Diameter Height Precharge Weight Number NPTM Color Type (Gallons) (Inches) (Inches) (psi) (lbs.) B (Inches) RO-2 140-32 2.0 8 13 ¼ Blue 5 Plastic 5 RO-2 140-653 2.0 8 13 ¼ Blue 20 Plastic 5 Standard RO-3 140S723 3.2 9 15 ¼ White 5 Plastic 7 RO-3 140S725 3.2 9 14 ¼ White 5 3 Bumps 7 A RO-4 141S343 4.4 11 15 ¼ Blue 5 Plastic 9 RO-4 141S344 4.4 11 15 ¼ White 5 Plastic 9 RO-4 141S351 4.4 11 15 ¼ White 5 3 Bumps/Plastic 9 B RO-4 141S352 4.4 11 15 ¼ Blue 5 3 Bumps/Plastic 9 RO-10 143-132 10.0 15 18 ¾ Blue 5 Plastic 20 1 Stainless Steel System Connection.
    [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]
  • Treatment of Concentrate
    Desalination and Water Purification Research and Development Program Report No. 155 Treatment of Concentrate U.S. Department of the Interior Bureau of Reclamation May 2009 REPORT DOCUMENTATION PAGE Form Approved 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 this 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 Department of Defense, Washington Headquarters Services, Directorate for Information Operations and Reports (0704-0188), 1215 Jefferson Davis Highway, Suite 1204, Arlington, VA 22202-4302. Respondents should be aware that notwithstanding any other provision of law, no person shall be subject to any penalty for failing to comply with a collection of information if it does not display a currently valid OMB control number. PLEASE DO NOT RETURN YOUR FORM TO THE ABOVE ADDRESS. T T T T T 1.T REPORT DATE (DD-MM-YYYY) 2. REPORT TYPE 3. DATES COVERED (From - To) March 9, 2008 Final 2002–2008 4.T TITLE AND SUBTITLE 5a. CONTRACT NUMBER Treatment of Concentrate Agreement 04-FC-81-1050 5b. GRANT NUMBER 5c. PROGRAM ELEMENT NUMBER 6. AUTHOR(S) 5d. PROJECT NUMBER Mike Mickley, P.E., Ph.D. 5e. TASK NUMBER Task F 5f. WORK UNIT NUMBER 7. PERFORMING ORGANIZATION NAME(S) AND ADDRESS(ES) 8. PERFORMING ORGANIZATION REPORT Mickley & Associates NUMBER 752 Gapter Road Boulder CO 80303 9.
    [Show full text]