Electrodialysis and Electrodialysis Reversal
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Supercapattery: Merit-Merge of Capacitive and Nernstian Charge Storage Mechanisms
Supercapattery: Merit-merge of capacitive and Nernstian charge storage mechanisms George Zheng Chen University of Nottingham Ningbo China, 199 Taikang East Road, Ningbo, 315100, Zhejiang, China. First published 2020 This work is made available under the terms of the Creative Commons Attribution 4.0 International License: http://creativecommons.org/licenses/by/4.0 The work is licenced to the University of Nottingham Ningbo China under the Global University Publication Licence: https://www.nottingham.edu.cn/en/library/documents/research- support/global-university-publications-licence-2.0.pdf Supercapattery: Merit-merge of capacitive and Nernstian charge storage mechanisms George Zheng Chen1,2 1 Department of Chemical and Environmental Engineering, Faculty of Engineering, University of Nottingham, University Park, Nottingham NG7 2RD, UK 2 Department of Chemical and Environmental Engineering, Faculty of Science and Engineering, University of Nottingham Ningbo China, University Park, Ningbo 315100, China Email: [email protected] Abstract Supercapattery is the generic name for hybrids of supercapacitor and rechargeable battery. Batteries store charge via Faradaic processes, involving reversible transfer of localised or zone-delocalised valence electrons. The former is governed by the Nernst equation. The latter leads to pseudocapacitance (or Faradaic capacitance) which may be differentiated from electric double layer capacitance with spectroscopic assistance such as electron spin resonance. Since capacitive storage is the basis of supercapacitors, the combination of capacitive and Nernstian mechanisms has dominated supercapattery research since 2018, covering nanostructured and compounded metal oxides and sulfides, water-in-salt and redox active electrolytes and bipolar stacks of multi-cells. The technical achievements so far, such as specific energy of 270 Wh/kg in aqueous electrolyte, and charging-discharging for over 5000 cycles, benchmark a challenging but promising future of supercapattery. -
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 . -
Industrial Experiment on Electrodialized Separation of Highly Concentrated Multicomponent Technological Solutions at Thermal Power Plants
E3S Web of Conferences 124, 01029 (2019) https://doi.org/10.1051/e3sconf/201912401029 SES-2019 Industrial experiment on electrodialized separation of highly concentrated multicomponent technological solutions at thermal power plants A. A. Filimonova1, N. D. Chichirova1, A. A. Chichirov1,*, and A. I. Minibaev1 1 Kazan State Power Engineering University, Kazan, Russia Abstract. The main sources of highly concentrated multicomponent technological solutions at thermal power plants (TPPs) are water treatment plants. Analysis of operation of the ion-exchange water treatment plant at the Nizhnekamsk Thermal Power Plant-1 showed that half of alkali supplied to regeneration of the anion-exchange alkali filters is not used, but is discharged for neutralization and then to wastewater. Due to the fact that the cost of alkali used in technological processes is quite high, it is economically feasible to process the alkaline waste with the alkali extraction and its reuse in the production cycle. The article presents the experimental results on the electro-membrane separation of alkaline waste regeneration solutions and wash water after anion-exchange filter regeneration. The revealed differences in the selectivity of various ion transfer through the electrodialysis apparatus membranes, depending on time and amount of transmitted electricity, allowed us to establish the possibility of obtaining an alkaline solution purified from impurities. 1 Introduction biotechnology, pharmaceuticals, water treatment at power plants, wastewater treatment [12–16]. Thermal power plants (TPPs) in Russia use The main advantage of electrochemical, and electrochemical methods of water treatment in a small especially electro-membrane methods, is that chemical volume and only as additional methods of water reactions and transformations are conducted using purification [1–4]. -
History of Transistors
TRANSISTOR MUSEUM™ HISTORY OF TRANSISTORS VOLUME 1 THE FIRST GERMANIUM HOBBYIST TRANSISTORS Special Collection of Historic Transistors Designed for the Historian, Engineer, Experimenter, Researcher and Hobbyist INCLUDED ARE CLASSIC EXAMPLES OF THESE 1950/60s GERMANIUM HOBBYIST TRANSISTORS 2N35 2N107 SURFACE BARRIER 2N170 CK78X A Publication of the Transistor Museum™ Copyright © 2009 by Jack Ward ABOUT THIS BOOK AND THE TRANSISTOR MUSEUM™ This book is the first of a series of History of Transistors publications developed by the Transistor Museum™. The History of Transistors Volume 1 documents The First Germanium Hobbyist Transistors, a subject that should be of great interest to the modern-day experimenter, engineer, historian, researcher and hobbyist. Included in the book are technical descriptions, historical commentary, circuits, and photographs of the famous germanium transistors that first appeared in the 1950s and have had a profound effect on the world of electronics ever since. Also included are working examples of some of the best remembered hobbyist transistors – 2N35, 2N107, Surface Barrier, 2N170, and CK78X. The web version of this book is available as a pdf at this url: http://www.semiconductormuseum.com/MuseumLibrary/HistoryOfTransistorsVolume1.pdf You can purchase a hardcopy version of the book, which also includes packaged examples of all five hobbyist transistors listed above, as well as additional storage/display envelopes for starting your own collection. You can visit the Transistor Museum™ Store for details on how to purchase this book as well as numerous other historic semiconductors and publications. http://www.semiconductormuseum.com/MuseumStore/MuseumStore_Index.htm The Transistor Museum™ is a virtual museum that has been developed to help preserve the history of the greatest invention of the 20TH century – the TRANSISTOR. -
Mass Transfer Phenomena During Electrodialysis of Multivalent Ions: Chemical Equilibria and Overlimiting Currents
applied sciences Article Mass Transfer Phenomena during Electrodialysis of Multivalent Ions: Chemical Equilibria and Overlimiting Currents Manuel César Martí-Calatayud * , Montserrat García-Gabaldón and Valentín Pérez-Herranz * IEC Group, Departament d’Enginyeria Quimica i Nuclear, Universitat Politècnica de València, Camí de Vera s/n, 46022 València, Spain; [email protected] * Correspondence: [email protected] (M.C.M.-C.); [email protected] (V.P.-H.); Tel.: +34-96-3877632 (V.P.-H.) Received: 26 July 2018; Accepted: 3 September 2018; Published: 6 September 2018 Featured Application: Selective ion transport through polymer electrolytes is crucial for environmental applications, especially in deionization of water for drinking and irrigation purposes and in effluents’ treatment. Ion transport through permselective membranes is relevant in emerging energy applications as well. Abstract: Electrodialysis is utilized for the deionization of saline streams, usually formed by strong electrolytes. Recently, interest in new applications involving the transport of weak electrolytes through ion-exchange membranes has increased. Clear examples of such applications are the recovery of valuable metal ions from industrial effluents, such as electronic wastes or mining industries. Weak electrolytes give rise to a variety of ions with different valence, charge sign and transport properties. Moreover, development of concentration polarization under the application of an electric field promotes changes in the chemical equilibrium, thus making more complex understanding of mass transfer phenomena in such systems. This investigation presents a set of experiments conducted with salts of multivalent metals with the aim to provide better understanding on the involved mass transfer phenomena. Chronopotentiometric experiments and current-voltage characteristics confirm that shifts in chemical equilibria can take place simultaneous to the activation of overlimiting mass transfer mechanisms, that is, electroconvection and water dissociation. -
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. -
Effects of Various Electrical Fields on Seed Germination Fredrick Warner Wheaton Iowa State University
Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1968 Effects of various electrical fields on seed germination Fredrick Warner Wheaton Iowa State University Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Agriculture Commons, and the Bioresource and Agricultural Engineering Commons Recommended Citation Wheaton, Fredrick Warner, "Effects of various electrical fields on seed germination " (1968). Retrospective Theses and Dissertations. 3521. https://lib.dr.iastate.edu/rtd/3521 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. This dissertation has been microfilmed exactly as received 69-4288 WHEATON, Fredrick Warner, 1942- EFFECTS OF VARIOUS ELECTRICAL FIELDS ON SEED GERMINATION. Iowa State University, Ph.D., 1968 Engineering, agricultural University Microfilms, Inc., Ann Arbor, Michigan EFFECTS OF VARIOUS ELECTRICAL FIELDS ON SEED GERMINATION by Fredrick Warner Wheaton A Dissertation Submitted to the Graduate Faculty in Partial Fulfillment of The Requirements for the Degree of DOCTOR OF PHILOSOPHY Major Subject: Agricultural Engineering Approved : Signature was redacted for privacy. Signature was redacted for privacy. Signature was -
Electrodialysis Principle
Setup of a 20 m3/h ED/RO plant to produce pure water from river water. A case study focusing on the electrodialysis process and the compatibility with RO pretreatment by Rudolf E. Brunner and Dr. Patrick Altmeier Ioncontract GmbH PCCell GmbH Znaimer Straße 34 Lebacher Straße 60 71263 Weil der Stadt 66265 Heusweiler [email protected] www.electrodialysis.de Electrodialysis principle • Anions move towards anode • Cations move towards cathode • Cation exchange membranes let cations through and block anions • Anion exchange membranes let anions go through and block cations • Electroneutrality 1 Electrodialysis Model Principle of electrodialysis is a stack of alternating cation and anion exchange membranes. Model: A tower block with alternating red and blue floors, filled with people Looking down, youmay see either blue or red floors. Electrodialysis Rules • Yellow: go up! Do not pass blue ceiling! • Green: go down! Do not pass red floor! 2 Apply Rules • All have moved until the blocking rule apply. • Result is: blocking rule apply in each second floor. • Note: We ignored the electroneutrality, for instance. An ED stack scheme 3 Continuous ED processing • A Diluate enter the cell, DC will be processed and Diluate Electrodialyzer out leave the cell as the finished product. Concen- trate out • The solute for the uptake of the ions enter the cell and leave it as the final concentrate. Electrode rinse Diluate • Electrode rinse will be in circulated (option: use of concentrate stream) Concen- trate in continuous mode Batch ED process DC • Each process solutionis Electrodialyzer hydraulical sealand cirulated often. • Ionic concentration shift slowly; each solution remain the same. -
Boron Removal from Dual-Staged Seawater Nanofiltration Permeate by Electrodialysis
Desalination and Water Treatment 10 (2009) 60–63 www.deswater.com October 1944-3994 / 1944-3986 © 2009 Desalination Publications. All rights reserved. doi: 10.5004/dwt.2009.782 Boron removal from dual-staged seawater nanofiltration permeate by electrodialysis Marian Turek*, Piotr Dydo, Barbara Bandura-Zalska Silesian University of Technology, Faculty of Chemistry, ul. B. Krzywoustego 6, 44–100 Gliwice, Poland Tel. +48 (32) 2372735; Fax +48 (32) 2372277; email: [email protected] Received 30 September 2008; accepted in revised form 10 July 2009 abstract The dual-staged nanofiltration to desalinate seawater is being proposed. The promising energy consumption, much lower than for RO seawater desalination, is reported. However, further reduc- tion in boron is needed. In the authors’ opinion, since the salinity of the second stage NF permeate is rather low, the easiest way to remove boron is to transfer it through an ion-exchange membrane (electrodialysis, ED). The relatively deep demineralization necessity is a shortcoming in the boron removal electrodialysis process, but ED seems to be privileged, since under these conditions boron (most likely borate) with its low mobility has to compete with small Cl– content only. In order to determine the applicability of the electrodialysis for boron removal from dual-staged nanofiltration the set of laboratory measurements was conducted. The simulated dual-staged nanofiltration per- 2+ 2+ + – 2– meate composition was as follows (mg/L): Mg — 0.2; Ca — 0.1; Na — 92; Cl — 117; SO4 — 0.2; B — 2.4. An ED unit, equipped with AMX and CMX Neosepta (Tokuyama Co.) membranes and 0.4 mm membrane-to-membrane distance, was applied. -
Recent Advances in Electrical Doping of 2D Semiconductor Materials: Methods, Analyses, and Applications
nanomaterials Review Recent Advances in Electrical Doping of 2D Semiconductor Materials: Methods, Analyses, and Applications Hocheon Yoo 1,2,† , Keun Heo 3,† , Md. Hasan Raza Ansari 1,2 and Seongjae Cho 1,2,* 1 Department of Electronic Engineering, Gachon University, 1342 Seongnamdaero, Sujeong-gu, Seongnam-si, Gyeonggi-do 13120, Korea; [email protected] (H.Y.); [email protected] (M.H.R.A.) 2 Graduate School of IT Convergence Engineering, Gachon University, 1342 Seongnamdaero, Sujeong-gu, Seongnam-si, Gyeonggi-do 13120, Korea 3 Department of Semiconductor Science & Technology, Jeonbuk National University, Jeonju-si, Jeollabuk-do 54896, Korea; [email protected] * Correspondence: [email protected] † These authors contributed equally to this work. Abstract: Two-dimensional materials have garnered interest from the perspectives of physics, materi- als, and applied electronics owing to their outstanding physical and chemical properties. Advances in exfoliation and synthesis technologies have enabled preparation and electrical characterization of various atomically thin films of semiconductor transition metal dichalcogenides (TMDs). Their two-dimensional structures and electromagnetic spectra coupled to bandgaps in the visible region indicate their suitability for digital electronics and optoelectronics. To further expand the potential applications of these two-dimensional semiconductor materials, technologies capable of precisely controlling the electrical properties of the material are essential. Doping has been traditionally used to effectively change the electrical and electronic properties of materials through relatively simple processes. To change the electrical properties, substances that can donate or remove electrons are Citation: Yoo, H.; Heo, K.; added. Doping of atomically thin two-dimensional semiconductor materials is similar to that used Ansari, M..H.R.; Cho, S. -
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). -
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..........................................................................