WATER PURIFICATION BY ION EXCHANGE Fronlispiece. Polystyrene sulphonic acid calion exchange bead (Magnijicalion 10 x, reduced 5/9ths on reproduction) WATER PURIFICATION BY ION EXCHANGE T. V. ARDEN, D.Se., Ph.D., F.R.I.C., C.Eng., M.I.M.M., P.A.I.W.E. Chcmical Director, The Permutit Company Ltd. NEW YORK PLENUM PRESS LONDON BUTTERWORTHS Published in the U.S.A. by PLENUM PRESS a division of PLENUM PUBLISHING CORPORATION 227 West 17th Street, New York, N.Y. 10011 First published by Butterworth and Co. (Publishers) Ltd. ISBN 978-1-4684-9038-1 ISBN 978-1-4684-9036-7 (eBook) DOT 10.1007/978-1-4684-9036-7 © Butterworth and Co. (Publishers) Ltd. 1968 Softcover reprint of the hardcover 1s t edition 1968 Suggested U.D.C. No. 541.183.12:628.16 Suggested additional No. 661.183.12 Libra~y qfCongress Catalogue Card Number 68-54310 CONTENTS PREFACE VII 1. INDUSTRIAL W ATERS Hard Water . Soft Water . Units . Typical Waters and Their Uses' Laundering, Wool Scouring, Bottle Washing, etc .. Chemi cal Pracessing, Metal finishing, etc .. Boiler Feed Water. 2. THE ION EXCHANGE PROCESS 13 Intraduction . The Development of Ion Exchange Resins. 3. EQlJILIBRIA AND KINETICS, AS APPLIED TO WATER TREATMENT 26 General Cation Exchange' Hydragen Ion Exchange, Sulphonic Resin· Hydrogen Ion Exchange, Carboxylic Resins . General Anion Exchange' Hydroxide Ion Exchange, Strang Base Resins . Acid Absorption, \Veak Base Resins . Kinetics. 4. UNIT WATER TREATMENT PROCESSES 49 Water Softening by Sodium Exchange· Alkalinity Removal with Carboxylic Resins . Sulphonic Resins . Hydrogen Ion Exchange . Acid Absorption by Weak Base Resins . Acid Absorption by Strang Base Resins . Mixed Beds 5. COMBINATION PROCESSES 80 1. Weak Acid Cation. Sodium Exchange Cation. Degas (WAC-Na-DG) 2. Strong Acid Cation. Weak Base Anion. Degas (SAC-WBA-DG) 3. Strong Acid Cation. Degas. Strong Base Anion (SAC-DG-SBA) 4. Strong Acid Cation. Weak Base Anion. Degas. Mixed Bed (SAC-WBA-DG-MB) 5. Strang Acid Cation. Degas. Strang Base Anion Mixed Bed (SAC-DG-SBA-MB) 6. Weak Acid Cation. Degas. Mixed Bed (WAC-DG-MB) 7. Weak Acid Cation. Strang Acid Cation. Degas. Anion. Mixed Bed (WAC-SAC-Degas-(WBA)-MB) (SBA2) (SBAI) 8. Strang Acid Cation. Weak Base Anion. Mixed bed. Mixed Bed (SAC-WBA-MB-MB) 9. Strong Acid Cation. Degas. Weak Base Anion. Strang Base Anion (SAC-DG-WBA-SBA) v CONTENTS 6. ORGANIC POISONING OF ANION EXCHANGE RES INS 90 The Problem' Organic Matter in Water . Poisoning of Resins . Cleaning Poisoned Resins . The Effect of Resin Structure . Non poisoning Resins . The Protection of Mixed Beds . Prevention of Poisoning, Summary 7. EQUIPMENT AND SPECIAL PROCESSES 113 Standard Resin Columns . Counterftow Units . Continuous Ion Exchange . Advantages of Continuous Ion Exchange . Special Problems of Continuous Ion Exchange . Types of Continuous Plant . Condensate Polishing for High Pressure Boilers . Brackish Water Desalination by Ion Exchange· Electrodialysis 8. INDUSTRIAL APPLICATIONS 150 The Treatment of Water-Soluble Organic Compounds . Recovery of Water and By-products from Industrial Wastes . Chromium Plating, Recovery of Water . Anodizing, Recovery of Water and Chromic Acid· Gold Plating, Recovery of Gold· Photographic Solutions, Recovery of Silver . Reactivition of Metal Finishing Solutions . Recovery of Metals by Complex Anion Formation . Elution Chromatography . Ion Exchange as a Manufacturing Process . Liquid Liquid Ion Exchange INDEX 181 VI PREFACE This book is an attempt to fill a gap in the existing literature on ion exchange. The many excellent works already available are of three main types, general introductions to the subject, specialist discussions of analytical and laboratory techniques, and advanced theoretical treatises. In practice, in spite of the vast number of processes which have been developed for la bora tory use, 99 per cent of all ion exchange resins produced in the world are used in water treatment, or closely allied applications. This book is intended as a general survey of the principles governing the practical uses of ion exchange resins, for the benefit of students encountering the subject for the first time, and for the chemists and engineers in many branches of industry whose work brings them into contact with water treatment, but who do not have the time to study more advanced volumes of basic theory. The background presented has been simplified to the maximum extent found possible without falsification, and an attempt has been made to relate each aspect of theory to its practical consequences in full scale water treatment. Mathematical methods have been avoided and pictorial or graphical presentation methods used wherever possible. As the book is concerned with general principles, rather than details of any particular research work, references to original papers and patents have been omitted except in the cases of special processes, which have a single clearly defined origin. The bibliography, included at the end, consists of books and review papers covering the various sections of this book, and giving the detailed original references which may be useful at a later stage of study. The practice, adopted in several earlier works, of including tables of equivalent resins produced by different manufacturers, has not been followed. The total number of resins now available is so large that a comprehensive table would be a massive item. Moreover, as knowledge in the field has increased in recent years, differences between individual resins previously classified as equivalent to each other have become increasingly important. Whenever a type of resin is described, a few examples are given of individual resins commonly used in Great Britain, but the lists are not intended to be comprehensive. Moreover, even in these cases, it must be emphasized that the classification is purely the result of my own studies of the res ins concerned. The manufacturers VlJ PREFACE of ion exchange resins rarely publish their exact structures, or manufacturing methods, and the attribution of structures to named resins should be considered, not as statements of fact, but as per sonal deductions from the analysis and general properties of the materials mentioned. The tables and graphs of operating results are quoted, with thanks, from the records of The Permutit Company Limited. They apply in principle to all other resins in the same general categories, but should not be taken to apply quantitatively to any one. Readers requiring the detailed operating characteristics of individual ion exchange resins can obtain the figures from the information sheets issued by all the major manufacturers; and it is hoped that a knowledge of the general principles set out here will facilitate understanding and comparison of the manufacturers' literature. Certain conventions of the water treatment industry have been followed. The hydrogen ion is written as H+, hydration being ignored. The terms 'silica', or 'SiOz' are used, in the absence of any more accurate general words, to refer to the various silicon containing anions present in water. The word 'absorb' and its derivatives are given their most generally understood meaning, that of uptake by permeation. No particular thermodynamic mechanism is implied. Grateful thanks are due to Dr. T. R. E. Kressman, Mr. J. Pilot and Mr. B. A. Sard, whose comments on the original typescript induced a proper sense of humility, and helped to eliminate the more glaring errors. V11l CHAPTER 1 INDUSTRIAL WATERS The water used by industry for boiler feed or process purposes may be taken from public supplies, or abstracted directly from wells, lakes or rivers. In Great Britain, town mains water will have been treated to render it largely clear and colourless, free from odour, and bacteriologically sterile. I t is thus directly suitable for many industrial purposes such as cooling, and in cases where ion exchange treatment is used, town mains water can normally be fed directly into the columns. Many large industrial users abstract water from natural sources for their own use. Where these are deep wells, the water is normally clear, colourless, and directly treatable by ion exchange; but in cases where water is taken directly from rivers or lakes, clarification by the classical methods of coagulation and filtration is normally necessary. These techniques are fully described elsewhere, and for the purposes of this book, the starting point of all industrial ion exchange processes is a supply of clear water, free from suspended and colloidal matter. HARD WATER The range of minerals contained in most natural waters is quite limited. The cations present are normally calcium, magnesium and sodium, while the anions are mainly chloride, sulphate and bicarbonate, with lower concentrations of nitrate, phosphate and silica. There are also traces of organic matter. For the majority of natural waters, analysis of the ions mentioned above will give the total dissolved so lids in the water. Waters occurring in regions of unusual rock formation may differ considerably from this pattern, but the principles which are to be discussed apply equally to waters of unusual composition. I t is customary to refer to waters as 'hard' or 'soft'. The former are waters containing appreciable concentrations (over 50 p. p.m.) of calcium and magnesium, which in Great Britain have normally been derived from the leaching of limestone or dolomitic rocks, by water containing free carbon dioxide. Significant concentrations of bicarbonate are therefore also present. Calcium may be derived INDUSTRIAL WATERS from other types of rock, for example gypsum, CaS04.2H20, in which case the principle ions present will be calcium and sulphate. 1t is a common convention in the water treatment industry to refer to ions in solution in terms of certain hypothetical combina tions. Thus calcium, magnesium and bicarbonate ions, when present together in solution, are grouped under the term 'temporary hardness', because on heating, all are substantially removed by precipitation of the corresponding insoluble carbonates, with loss of carbon dioxide into the atmosphere. Calcium and magnesium co-existing with sulphate or chloride are known as 'permanent hardness', since the solutions are stable to heat at normal pressure. These imaginary combinations have no real significance, but the two terms are convenient forms of abbreviation, and will be used in this book in places where they cannot give rise to misunderstanding. SOFT WATER While the meaning of hardness is gene rally understood, the term 'soft water' is often subject to confusion. Soft waters are those which contain less than about 20 p.p.m. Ca2+ and Mg2+, and in many areas of Great Britain, such as the hilly regions of Wales and Scotland, these soft waters have very low total dissolved solids: indeed, the total of all ions may be below 50 p.p.m. As a result, it is not uncommon to find among non-technical water users in industry, a belief that all soft waters, including those artificially softened, have a low mineral content. The misconception that ion exchange softening gives results equivalent to those of distillation is still not unknown; and it is a fairly common experience for a water treatment contractor to be asked to supply a softener, when abrief study of the proposed use of the water shows that complete de mineralizing, that is, removal of aH dissolved salts, is required. A water may, therefore, be soft, while still containing consider able concentrations of dissolved salts. WeH waters in low-lying areas near to the sea are often of this type, owing to ingress of sea water through porous rock. Waters containing a preponderance of sodium bicarbonate are also not uncommon in some countries. EquaHy, a water containing low total solids consisting largely of calcium salts, which is soft by ordinary standards, will be hard from the point of view of ion exchange reactions, since the cation resin on exhaustion will be almost fuHy loaded with calcium. For the purpose of this book, the concept of hardness will be separated from that of total mineral content. The terms 'hard' and 'soft' will be used to indicate the presence or absence of calcium and magnesium 2
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