Physico-Chemical Pre-Treatment for Drinking Water Sdosooo28

Total Page:16

File Type:pdf, Size:1020Kb

Physico-Chemical Pre-Treatment for Drinking Water Sdosooo28 PHYSICO-CHEMICAL PRE-TREATMENT FOR DRINKING WATER SDOSOOO28 A Thesis Submitted In Fullfillment Of The Requirement For The Degree Of Doctor Of Philosophy In Chemistry By Wissal Ahmed Mahmoud Hassanien B.Sc. & Ed. Chemistry, U of K M.Sc. Chemistry, U of K Department of Chemistry Faculty of Education University of Khartoum August 2004 r-1 °- * > > ° O s 0 c 0 JJ>TJ A f f „ o DEDICATION To my Father and mother with love and respect To my Brothers and sisters ACKNOWLEDGEMENTS I would like to express my sincere thanks and deep gratitude to Professor Mohmed Ali Hussien for his supervision, indispensable help. My thanks also to Dr. Ibrahim Mohmed Ahmed for his supervision, encouragement, and invaluable advice throughout this work. Special thanks are due to Central Laboratory staff, Almogran, Khartoum State Water Corporation, for providing facilities Thanks are extended to Dr. Mubarak Dirar, Physics department, University of Sudan for Technology and Science, for laboratory facilities Thanks are also extended to the Microbiology Lab staff, Sudanese Standards and Metrology Organization, especially Professor Mona Alajab for their valuable collaboration in the bacteriological field. Thanks to Abd Alrazig Mohmed Abd Albagi, physics department, University of Khartoum for his help and advice in experimental design. My thanks also are due to the sustained encouragement of my family. To all who contributed, in a way or another, towards the completion of this work lam greatly indebted. Abstract The objective of this work is to attempt to improve the quality of town water by application of alternating current, direct current and magnetic field to raw water as pre-treatment to enhance the coagulation and flocculation. The research focuses particularly on development in water treatment processes. The design and operation for these processes and the evaluation thereof have been mentioned. Treatment generally requires application of electric current AC or DC (0.1- 1.0A) for residence current time 2-12 minutes, or application of magnetic field (20 -400 mT). The measurement of turbidity of raw water before and after treatment was done to obtain the efficiency of turbidity removal. Total suspended solids (TSS) of raw water were determined before and after treatment to obtain the efficiency of TSS removal. Total bacteria count was determined using standard plate count method. Most probable number (MPN) technique was used to determine the number of coliform organisms that were present in water to obtain the efficiency of water purification. Electric susceptibility was determined for raw water and water treated by magnetic field and by electric current to show the effect of these parameter on polarization which in turn affect the stability of colloids. The results obtain revealed that treatment by AC electric current gave turbidity removal efficiency in the range 40-81%, and TSS in the range 37-61%. Treatment by DC electric current gave turbidity removal efficiency in the range 17-76 % and TSS 9-57 %. Coagulation of natural colloids and other material suspended in water is faster in water impacted by an electric current. When alum and polymer was used as coagulant together with AC electric current, clarification rate was greater by 1.8-2.4 times in Damira 2001; 1.5- 3.3 times by poly aluminum chloride together with AC electric current; 2.4-4.5 times by alum and poly diallyl dimethyl ammonium chloride together with DC electric current in Damira 2002 . The effect of the magnetic field on the removal of both turbidity and total suspended solids does not follow a regular pattern. Whereas coagulation is faster in water impacted by magnetic field together with alum and polymer, clarification rate was greater 1.5- 4.8 times than in the absence of the field. in Electric currents have been shown to be capable of disinfecting drinking water and reducing the numbers of bacteria in the raw water. The mortality efficiency of total bacteria count was 57-83% and of total coliform was 58-93% when exposed to electric current for an extended residence current times between 2 to 11 minutes. The mortality efficiency of total bacteria count was 60-85%, and of total coliform was 53-95% when exposed to current between 0.16-0.60A at constant current time. The results obtained from physical and chemical analysis of raw water and water treated by AC, DC electric curreni and magnetic field revealed that there was small changes in pH, total dissolved solids, conductivity and temperature of water after treatment, whereas turbidity, total suspended solids, and hardness of water were decreased after treatment. Chemical analysis of separated water sludge revealed that the quantity of SiO., by mass percent was higher in sample treated by electric current due to precipitation of soluble silica and decomposition of carbonates. Analysis for the elements of the separated water sludge by Atomic Absorption Spectroscopy revealed that the concentration of the elements was reduced due to decomposition of the sludge complexes by electric effect. Analysis of the separated water sludge by XRD, indicated that, there was no significant change in the structure of the clay mineral before and after treatment by AC, DC electric current. Measurement of the electric susceptibility of magnetized water is directly proportional to the intensity of the applied magnetic field. The electric susceptibility of electrified water was decreased upon increasing electric current due to the increase in the number of paraelectric particles that align themselves in the direction of the field and thus decreases the electric susceptibility. IV 44>) A+c&aJl .(^Luu ^ 400-20) t<?-aUii- Jl^. .AjjljjiJ! SJLJI iliUi 40 (j^JI ^ sjl£*JI yi jl ;«:US J .lijUl ^WJ^11 ^JUJI U .%61-37 ti^JI ^ AJKII ^ULJ U^l\ AJA tt\j\ '^liSj t% 81- s.i.^ti ji^ji 4j|j| s^uSj 4 %76-17 CJAJI ^ ijl£*JI <ll j UUS ol .%57-9 < .(2001 ij^S) %2.4-1.8 <+** AJJ ,«-• f.jjijJ)l\ JJJJK ii»l»j ^IU-a]l «.U1! JJJjlll JJI ^lij L_uiJLi jJUJI frU] ij* 4.5-2.4 V-ij Ajjy L«S ij* 3.3-1.5 .(2002 -.j^)^iL*ll ^>ft£ll jLull V r-j^ ^ V < *-« 6Jjl Jj hj L&ilJ J\ %83-57 OH Cjljx. l JL SAJ ^WJ^ J^ V^ ^ %93-58 ow Ajj i %85- 60 u« c j\ Ju IJJSSJI ^iSlI JAJI ^J- UUS U .<1JSJ 11 -2 0.6-0.16 OJJ CJljy ^L.j^ jUU W^>i Jic %95-53 OJJ iJ KK-.1I ^S J *UI t> Jj.niJ l#iJUl i_i«ljll ^U^l JJ^ V <ii j^ 4ju.,ill AjciVl ^jja. jU>J (^jJall sJ—'jl' J.'^' jL^aij ^11 ^JJ^J LA- JLa-JI aLajl ^4 Lu VI Contents Particulars Page No. Chapter One : Introduction .1 The Characteristics of Water (1) .2 Physical Characteristics of Water (1) .3 Chemical Characteristics of Water (2) .4 Biological Characteristics of Water (3) .5 Water Quality (6) .6 Bacteriological Water Quality (9) .7 Water Treatment (11) .8 Electrical Water Treatment (13) .9 Magnetic Water Treatment (17) .10 Chemical Water Treatment (20) .11 Biological Water Treatment (28) .12 Water Disinfection (29) The Objectives (32) Chapter Two: Experimental 2.1 Samples Collection (33) 2.2 Materials and Instrumentation (33) 2.3 Electrical Treatment of Water Using AC /Damira 2001 (34) 2.4 Effect of Electrical Treatment on Hardness of Water (35) 2.5 Effect of Electrical Treatment on Water Temperature, (35) Conductivity, and Total Dissolved Solids. 2.6 Effect of Electrical Current AC on Water Coagulation/ (36) Damira 2001. 2.7 Effect of Alum Addition on Raw Water Turbidity (36) 2.8 Electrical Treatment Using 0.35A/ Damira 2002 (37) 2.9 Effect of Electrical Current on Water Coagulation/ (37) Damira 2002 2.10 Electrical Water Treatment Using DC Electric Current (37) 2.11 Effect of Electric Current DC on Water Coagulation (38) 2.12 Magnetic Water Treatment (general procedure) (39) 2.13 Variation of Turbidity Against Magnetic Field and (40) Precipitation Times 2.14 Effect of Electric Current on The Mortality of Bacteria in (40) Raw Water 2.15 Physical and Chemical Analysis of Raw and Treated Water. (43) vii 2.16 Chemical Analysis of The Separated Water Sludge Before (43) and After Treatment by Electric Current. 2.17 Determination of Electric Susceptibility of Raw and (46) Treated Water By Magnetic Field. 2.18 Determination of Electric Susceptibility of Raw and (46) Treated Water By Electric Current. Chapter Three : Results and Discussion - Water Turbidity, Total Suspended Solids When Applying (47) Various AC/ Damira 2001. - Water Turbidity for Current Duration 5 Minutes (50) - Effect of Electric Current on Water Hardness (57) - Effect of Electric Current on Conductivity and TDS (57) - Effect of Polymer and Alum Together with AC on Turbidity (58) Removal /Damira 2001 - Effect of Alum on Water Turbidity (61) - Water Turbidity, TSS, When Applying Various (62) AC / Damira 2002 - Water Turbidity, TSS, for Current Duration 3and 4 minutes. (69) - Effect of Polymer and Alum Together with AC on Turbidity (72) Removal Damira 2002 - Water Turbidity, TSS, When Applying Various DC/ Damira (76) 2002 - Water Turbidity, TSS for Current Duration 3.4, and 5 minutes. (84) - Effect of Polymer and Alum Together with DC on Turbidity (89) Removal. - Water Turbidity, TSS When Applying Magnetic Field of (92) Varying Strength. - The Effect of Magnetic Field on Conductivity and TDS. (95) - Variation of Turbidity Against Magnetic Field and (100) Precipitation Times. - The Effect of Electric Current on The Mortality of Bacteria. (101) - The Effect of Residence Current Time on The Mortality of (120) Bacteria. - Kinetic With Respect to Bacteria. (125) - Physical and Chemical Analysis of Water. (136) - Chemical Analysis of Separated Water Sludge by Atomic (137) Absorption.
Recommended publications
  • Investigation of Fouling Mechanisms on Ion Exchange Membranes During Electrolytic Separations
    INVESTIGATION OF FOULING MECHANISMS ON ION EXCHANGE MEMBRANES DURING ELECTROLYTIC SEPARATIONS By Matthew James Edwards A thesis submitted to the faculty of The University of Mississippi in partial fulfillment of the requirements of the Sally McDonnell Barksdale Honors College. Oxford, MS 2019 Approved by: __________________________________ Advisor: Dr. Alexander M. Lopez _________________________________ Reader: Dr. Adam Smith __________________________________ Reader: Dr. John H. O’Haver i Ó 2019 Matthew James Edwards ALL RIGHTS RESERVED ii DEDICATION I would like to dedicate this Capstone Project to my parents, Michael and Nidia Edwards. Their support and commitment to my education has been unfailing for as long as I can remember. I am thankful for everything they have done. It is with their help that I am privileged to attend The University of Mississippi, and I will forever be grateful. iii ACKNOWLEDGEMENTS I would first like thank Dr. Alexander M. Lopez and The University of Mississippi Chemical Engineering Department for the opportunity to work on this research project. The guidance, patience, and willingness to work with and teach an undergraduate student has been beneficial and inspiring to me during my time here at Ole Miss. Second, I would like to thank Dr. Paul Scovazzo for providing guidance on how to write this thesis and for allowing me to use his lab and equipment as well. I would also like to thank all the graduate students of the Chemical Engineering Department, primarily Saloumeh Kolahchyan. The willingness to take the time to answer my questions, to guide me in how use all the equipment in the lab, and to show me how to follow lab protocols required for the completion of my thesis research.
    [Show full text]
  • State-Of-The-Art Water Treatment in Czech Power Sector
    membranes Article State-of-the-Art Water Treatment in Czech Power Sector: Industry-Proven Case Studies Showing Economic and Technical Benefits of Membrane and Other Novel Technologies for Each Particular Water Cycle Jaromír Marek Department of Chemistry, Faculty of Science, Humanities and Education, Technical University of Liberec, Studentská 1402/2, 461 17 Liberec, Czech Republic; [email protected]; Tel.: +420-732-277-183 Abstract: The article first summarizes case studies on the three basic types of treated water used in power plants and heating stations. Its main focus is Czechia as the representative of Eastern European countries. Water as the working medium in the power industry presents the three most common cycles—the first is make-up water for boilers, the second is cooling water and the third is represented by a specific type of water (e.g., liquid waste mixtures, primary and secondary circuits in nuclear power plants, turbine condensate, etc.). The water treatment technologies can be summarized into four main groups—(1) filtration (coagulation) and dosing chemicals, (2) ion exchange technology, (3) membrane processes and (4) a combination of the last two. The article shows the ideal industry-proven technology for each water cycle. Case studies revealed the economic, technical and environmental advantages/disadvantages of each technology. The percentage of Citation: Marek, J. State-of-the-Art technologies operated in energetics in Eastern Europe is briefly described. Although the work is Water Treatment in Czech Power conceived as an overview of water treatment in real operation, its novelty lies in a technological model Sector: Industry-Proven Case Studies of the treatment of turbine condensate, recycling of the cooling tower blowdown plus other liquid Showing Economic and Technical waste mixtures, and the rejection of colloidal substances from the secondary circuit in nuclear power Benefits of Membrane and Other plants.
    [Show full text]
  • Wastewater Treatment and Reuse in the Oil & Petrochem Industry
    Engineering Conferences International ECI Digital Archives Wastewater and Biosolids Treatment and Reuse: Proceedings Bridging Modeling and Experimental Studies Spring 6-13-2014 Wastewater treatment and reuse in the oil & petrochem industry – a case study Alberto Girardi Dregemont Follow this and additional works at: http://dc.engconfintl.org/wbtr_i Part of the Environmental Engineering Commons Recommended Citation Alberto Girardi, "Wastewater treatment and reuse in the oil & petrochem industry – a case study" in "Wastewater and Biosolids Treatment and Reuse: Bridging Modeling and Experimental Studies", Dr. Domenico Santoro, Trojan Technologies and Western University Eds, ECI Symposium Series, (2014). http://dc.engconfintl.org/wbtr_i/46 This Conference Proceeding is brought to you for free and open access by the Proceedings at ECI Digital Archives. It has been accepted for inclusion in Wastewater and Biosolids Treatment and Reuse: Bridging Modeling and Experimental Studies by an authorized administrator of ECI Digital Archives. For more information, please contact [email protected]. Wastewater Treatment and Reuse In Oil & Petrochemical Industry Otranto, June 2014 COMPANY PROFILE DEGREMONT, THE WATER TREATMENT SPECIALISTS 4 areas of 5 areas of expertise: activities: . Drinking water production . Design & Build plants . Operation & . Reverse osmosis desalination Services plants . Urban wastewater treatment . Equipment and reuse plants . BOT / PPP . Biosolid treatment systems . Industrial water production and wastewater treatment units plants 2 Wastewater Treatment and Reuse COMPANY PROFILE DEGREMONT, THE WATER TREATMENT SPECIALISTS In over For industrials: For local authorities: 70 . Energy . Drinking water countries, . Upstream oil and gas Degrémont offers . Desalination . Refining and solutions to local . Urban wastewater authorities and petrochemicals . Sludge and biosolids industries . Chemicals . Pharmaceutical, cosmetics, fine chemicals .
    [Show full text]
  • Advancing Electrodeionization with Conductive Ionomer Binders That
    www.nature.com/npjcleanwater ARTICLE OPEN Advancing electrodeionization with conductive ionomer binders that immobilize ion-exchange resin particles into porous wafer substrates ✉ ✉ Varada Menon Palakkal 1,3, Lauren Valentino 2,3, Qi Lei 1, Subarna Kole1, Yupo J. Lin 2 and Christopher G. Arges 1 Electrodeionization (EDI) is an electrically driven separations technology that employs ion-exchange membranes and resin particles. Deionization occurs under the influence of an applied electric field, facilitating continuous regeneration of the resins and supplementing ionic conductivity. While EDI is commercially used for ultrapure water production, material innovation is required for improving desalination performance and energy efficiency for treating alternative water supplies. This work reports a new class of ion-exchange resin-wafers (RWs) fabricated with ion-conductive binders that exhibit exceptional ionic conductivities—a3–5-fold improvement over conventional RWs that contain a non-ionic polyethylene binder. Incorporation into an EDI stack (RW-EDI) resulted in an increased desalination rate and reduced energy expenditure compared to the conventional RWs. The water-splitting phenomenon was also investigated in the RW in an external experimental setup in this work. Overall, this work demonstrates that ohmic resistances can be substantially curtailed with ionomer binder RWs at dilute salt concentrations. npj Clean Water (2020) 3:5 ; https://doi.org/10.1038/s41545-020-0052-z 1234567890():,; INTRODUCTION EDI stack is more thermodynamically efficient for removing ions in 10 Electrochemical separations, which primarily consist of electrodia- the more challenging dilute concentration regime. lysis (ED), electrodeionization (EDI), and membrane capacitive A drawback of conventional EDI is the utilization of loose resin deionization (MCDI/CDI),1 are a subset of technologies primarily beads that foster inconsistent process performance, stack leakage, used for deionization and other water treatment processes.
    [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]
  • Coal Fired Power Plant Water Chemistry Issues: Amine Selection at Supercritical Conditions and Sodium Leaching from Ion Exchange Mixed Beds
    COAL FIRED POWER PLANT WATER CHEMISTRY ISSUES: AMINE SELECTION AT SUPERCRITICAL CONDITIONS AND SODIUM LEACHING FROM ION EXCHANGE MIXED BEDS By JOONYONG LEE Bachelor of Science in Chemical Engineering Kangwon National University Chuncheon, South Korea 1995 Master of Science in Chemical Engineering Kangwon National University Chuncheon, South Korea 1997 Submitted to the Faculty of the Graduate College of the Oklahoma State University in partial fulfillment of the requirements for the Degree of DOCTOR OF PHILOSOPHY May, 2012 COAL FIRED POWER PLANT WATER CHEMISTRY ISSUES: AMINE SELECTION AT SUPERCRITICAL CONDITIONS AND SODIUM LEACHING FROM ION EXCHANGE MIXED BEDS Dissertation Approved: Dr. Gary L. Foutch Dissertation Adviser Dr. AJ Johannes Dr. Martin S. High Dr. Josh D. Ramsey Dr. Allen Apblett Outside Committee Member Dr. Sheryl A. Tucker Dean of the Graduate College ii TABLE OF CONTENTS Chapter Page I. INTRODUCTION ......................................................................................................1 1.1. Coal-Fired Power Plants ...................................................................................1 1.2. Ultrapure Water ................................................................................................3 1.3. Mixed-Bed Ion Exchange .................................................................................5 1.4. Objective ...........................................................................................................6 II. WATER CHEMISTRY IN POWER PLANTS ......................................................10
    [Show full text]
  • OEM Technical Manual for Electropure
    OEM Engineering Manual Electropure™ XL & EXL Series EDI Contains information for the successful system engineering, design, installation, operation, and maintenance of SnowPure’s “Electropure™ XL and EXL” EDI products by an OEM pure water system integrator. Pictured: EXL - 750 750 High Flow Industrial EDI Manual: Version 3.5 (A4) Module Updated: February 2018 SNOWPURE, LLC, 2005-2018 VERSION 3.5 (XL+EXL) –FEBRUARY 2018 PAGE 1 Worldwide HQ (Headquarters): SnowPure Water Technologies San Clemente, CA 92672, USA Tel: +1.949.240.2188 [email protected] www.snowpure.com SnowPure Global Sales Offices: China Sales Office Electropure Environmental Technology (Shanghai) Co. Ltd. 伊乐科环保科技(上海)有限公司 Tel: +86.21.6167.1860 Email: [email protected] www.snowpure.com.cn Middle East Sales Office SnowPure Middle East Amman, Jordan Email: [email protected] International Distributors: Hong Kong (Authorized Distributor) SnowPure International (HK) Ltd. Hong Kong Tel: +1.858.692.0664 [email protected] Germany (Authorized Distributor) TES Water Treatment GmbH India (Authorized Distributor) Tel: +49.6205.2870.0 Evergreen Technologies Pvt. Ltd. [email protected] Tel: +91.2201.2461 [email protected] Sweden, Finland, Norway, Baltics (Authorized Distributor) Japan (Authorized Distributor) PWS Pure Water Scandinavia AB AMP Ionex / Mihama Tel: +46.23.797.990 エイエムピー・アイオネクス株式会社 / 美浜株式会社 [email protected] Tel: +81.3.4570.3820 [email protected] Switzerland, Austria, Czech Republic, Slovakia www.amp-ionex.com ROC Components AG Tel: +41.61.461.8303 Korea (Authorized Distributor) [email protected] Innomeditech, Inc. 주식회사 이노메디텍 Ukraine (Authorized Distributor) Tel: +82-31-80022500 Nerex PE [email protected] Tel: +38.44.223.5636 www.innomeditech.co.kr [email protected] SNOWPURE, LLC, 2005-2018 VERSION 3.5 (XL+EXL) –FEBRUARY 2018 PAGE 2 Table of Contents WORLDWIDE HQ (HEADQUARTERS): .............................................................................
    [Show full text]
  • Promoting Water-Splitting in Janus Bipolar Ion-Exchange Resin Wafers for Electrodeionization
    Molecular Systems Design & Engineering Promoting water-splitting in Janus bipolar ion-exchange resin wafers for electrodeionization Journal: Molecular Systems Design & Engineering Manuscript ID ME-ART-12-2019-000179.R1 Article Type: Paper Date Submitted by the 29-Feb-2020 Author: Complete List of Authors: Jordan, Matthew; Louisiana State University, Cain Department of Chemical Engineering Valentino, Lauren; Argonne National Laboratory, Applied Materials Division Nazyrynbekova, Nargiza; Louisiana State University, Cain Department of Chemical Engineering Palakkal, Varada Menon; Louisiana State University, Cain Department of Chemical Engineering Kole, Subarna; Louisiana State University, Cain Department of Chemical Engineering Bhattacharya, Deepra; Louisiana State University, Cain Department of Chemical Engineering Lin, Yupo; Argonne National Laboratory, Applied Materials Division Arges, Christopher; Louisiana State University, Cain Department of Chemical Engineering Page 1 of 35 Molecular Systems Design & Engineering Promoting water-splitting in Janus bipolar ion-exchange resin wafers for electrodeionization Matthew L. Jordana#, Lauren Valentinob#, Nargiza Nazyrynbekovaa, Varada Menon Palakkala, Subarna Kolea, Deepra Bhattacharyaa, Yupo J. Linb*, and Christopher G. Argesa* aCain Department of Chemical Engineering, Louisiana State University, Baton Rouge, LA 70803 bApplied Materials Division, Argonne National Laboratory, Lemont, IL 60439 #Contributed equally to this report *corresponding author: [email protected], [email protected] DESIGN, SYSTEM,
    [Show full text]
  • Water Treatment Based on Ion Exchange Membrane Permeable Combined with the Field Electrodeionization (EDI)
    Civil and Environmental Research www.iiste.org ISSN 2224-5790 (Paper) ISSN 2225-0514 (Online) Vol.6, No.12, 2014 Water Treatment Based on Ion Exchange Membrane Permeable Combined with The Field Electrodeionization (EDI) Sugito 1* Budi Prijo sembodo 2 1.Environmental Engineering of Univ. PGRI Adi Buana Surabaya, Indonesia. Jl. Ngagel Dadi III.B/37 Surabaya, Post code ; 60245-East Java_Indonesia 2.Electrical Engineering of Univ. PGRI Adi Buana Surabaya, Indonesia. Jl. Ngagel Dadi III.B/37 Surabaya, Post code ; 60245-East Java_Indonesia * Email correspondency : [email protected] The research is financed by the Directorate General of Higher Education, Ministry of Education and Culture, Indonesia through Grant Competition Research 2012-2014 Abstract Water treatment can be done by ; removal of cations / anions contained in the water used: ion exchange resin (ion exchanger), deionization, distillation membrane transfer, flash evaporation, and reverse osmosis. But the way that can be done separately, each has drawbacks. If done multiple, can simultaneously support for removal of cations anions process contained therein. Water treatment processing procedures in this study are ; filtration using polipropylena, absorption by Manganese zeolite treatment, then ion exchange resins using anion and cation resin, continued with treatment electrodeionization (EDI) using membrane permeable cation and anion permeable membrane, which is arranged in cross, where the anode electrode attached adjacent by cation permeable membrane, and vice versa. Water treatment by technology based filtration, absorption, and ion exchanger with permeable membrane combined with electrodeionization (EDI) field concluded that; removal of some of parameters are: Total Disolved Solid (TDS) 752 ppm, Turbidity 4.94 NTU scale, color 40 units PtCo, Iron 0.55 mg/L Fe, Total hardness 457.24 mg/L CaCO3, Chloride 500 ppm, Nitrate 0.82 ppm, Nitrite 0.49 mg/L NO2-N, Zinc 0.07 ppm, Sulfate 9.14 ppm, Sodium 575.46 ppm, Organic Substances 17.74 mg/L KMnO4, and Detergent 0:06 mg/L LAS.
    [Show full text]
  • Effects of the Operating Parameters on the Reverse Osmosis-Electrodeionization Performance in the Production of High Purity Water
    Korean J. Chem. Eng., 22(1), 108-114 (2005) Effects of the Operating Parameters on the Reverse Osmosis-Electrodeionization Performance in the Production of High Purity Water Jung-Hoon Song, Kyeong-Ho Yeon, Jaeweon Cho and Seung-Hyeon Moon† Department of Environmental Science and Engineering, Gwangju Institute of Science and Technology (GIST), 1 Oryong dong, Buk-gu, Gwangju 500-712, South Korea (Received 30 June 2004 • accepted 26 October 2004) Abstract−An RO-CEDI (Reverse osmosis-continuous electrodeionization) hybrid process was investigated to pro- duce high purity water. The RO system, with an effective membrane area of 1.1 m2, was operated using tap water with conductivity of 64 µs·cm−1, and the CEDI system experiments were carried out in a cell-pair stack consisting of 3 com- partments. During the parametric study of the RO-CEDI hybrid system, the optimal operating conditions were deter- mined based on the water purity. The electrical resistivity and water dissociation of the ion exchange resins and ion exchange membrane were verified as the key mechanisms of the CEDI system in the water purification. The produced water met the quality requirements as a make-up water in a nuclear power plant with a resistivity of 10-16.7 MΩ·cm. Key words: Continuous Electrodeionization, RO-CEDI Hybrid Process, Make-up Water, High Purity Water INTRODUCTION ments for the nuclear power plant. The RO-IX (Reverse osmosis-Ion exchange) process is now broad- EXPERIMENTAL ly used as the final water treatment step to produce high purity water in a nuclear power plant due to its high decontamination efficiency, 1.
    [Show full text]
  • Electrodeionization Apparatus and Process for Purifying a Liquid
    Europäisches Patentamt *EP000803474B1* (19) European Patent Office Office européen des brevets (11) EP 0 803 474 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) Int Cl.7: C02F 1/469, B01D 61/48, of the grant of the patent: B01D 61/52, B01J 47/08 02.04.2003 Bulletin 2003/14 (21) Application number: 97300606.7 (22) Date of filing: 30.01.1997 (54) Electrodeionization apparatus and process for purifying a liquid Vorrichtung und Verfahren zur Reinigung einer Flüssigkeit mittels Elektrodeionisation Appareil et procédé pour purifier un liquide par électrodéionisation (84) Designated Contracting States: • Moulin, Jacques AT BE CH DE DK ES FI FR GB GR IE IT LI LU MC 78 Plaisir (FR) NL PT SE Designated Extension States: (74) Representative: Greenwood, John David et al AL LT LV SI Graham Watt & Co. St. Botolph’s House (30) Priority: 26.04.1996 US 638040 7-9 St. Botolph’s Road Sevenoaks Kent TN13 3AJ (GB) (43) Date of publication of application: 29.10.1997 Bulletin 1997/44 (56) References cited: EP-A- 0 503 589 US-A- 3 291 713 (73) Proprietor: MILLIPORE CORPORATION US-A- 3 755 135 US-A- 4 226 688 Bedford Massachusetts 01730 (US) US-A- 5 308 466 (72) Inventors: • Denoncourt, Jeffrey P. Winchester, MA 01890 (US) Note: Within nine months from the publication of the mention of the grant of the European patent, any person may give notice to the European Patent Office of opposition to the European patent granted. Notice of opposition shall be filed in a written reasoned statement.
    [Show full text]
  • Waste Heat Driven Membrane Distillation for Industrial Wastewater Treatment
    kth royal institute of technology Doctoral Thesis in Energy Technology Waste Heat Driven Membrane Distillation for Industrial Wastewater Treatment IMTISAL-E-NOOR Stockholm, Sweden 2021 Waste Heat Driven Membrane Distillation for Industrial Wastewater Treatment IMTISAL-E-NOOR Doctoral Thesis 2021 Academic Dissertation which, with due permission of the KTH Royal Institute of Technology and Aalto University, is submitted for public defense on Monday the 1st March 2021, at 8:00 a.m. via Zoom in KTH Royal Institute of Technology, Sweden. Department of Energy Technology Department of Bioproducts and School of Industrial Engineering and Biosystems Management School of Chemical Engineering KTH Royal Institute of Technology Aalto University Stockholm, Sweden Espoo, Finland Imtisal-e-Noor, Doctoral Thesis-2021 Imtisal-e-Noor, Doctoral Thesis-2021 This doctoral dissertation is completed under Erasmus Mundus Joint Doctoral Programme, Environomical Pathways for Sustainable Energy Services (SELECT+) for the degree of Doctor of Philosophy from KTH Royal Institute of Technology, Sweden and degree of Doctor of Science (Technology) from Aalto University, Finland. © Imtisal-e-Noor Aalto University publication series DOCTORAL DISSERTATIONS 184/2020 ISBN (printed): 978-952-64-0131-7 ISBN (pdf): 978-952-64-0132-4 ISSN 1799-4934 ISSN 1799-4942 (electronic) TRITA-ITM-AVL 2021:2 ISBN: 978-91-7873-774-1 Printed by: Universitetsservice US-AB, Sweden, 2021 Imtisal-e-Noor, Doctoral Thesis-2021 Imtisal-e-Noor, Doctoral Thesis-2021 Supervising Professors and Thesis Advisers Prof. Andrew Martin, KTH Royal Institute of Technology, Sweden Prof. Olli Dahl, Aalto University, Finland Preliminary Examiners Prof. Wojciech Kujawski, Nicolaus Copernicus University, Poland Dr. Alessandra Criscuoli, Institute on Membrane Technology (CNR-ITM), Italy Opponent Prof.
    [Show full text]