Of Operation and Control Ion-Exchange Processes For

Total Page:16

File Type:pdf, Size:1020Kb

Of Operation and Control Ion-Exchange Processes For TECHNICAL REPORTS SERIES No. 78 Operation and Control Of Ion-Exchange Processes for Treatment of Radioactive Wastes INTERNATIONAL ATOMIC ENERGY AGENCY,VIENNA, 1967 OPERATION AND CONTROL OF ION-EXCHANGE PROCESSES FOR TREATMENT OF RADIOACTIVE WASTES The following States are Members of the International Atomic Energy Agency: AFGHANISTAN GERMANY, FEDERAL NIGERIA ALBANIA REPUBLIC OF NORWAY ALGERIA GHANA PAKISTAN ARGENTINA GREECE PANAMA AUSTRALIA GUATEMALA PARAGUAY AUSTRIA HAITI PERU BELGIUM HOLY SEE PHILIPPINES BOLIVIA HUNGARY POLAND BRAZIL ICELAND PORTUGAL BULGARIA INDIA ROMANIA BURMA INDONESIA SAUDI ARABIA BYELORUSSIAN SOVIET IRAN SENEGAL SOCIALIST REPUBLIC IRAQ SIERRA LEONE CAMBODIA ISRAEL SINGAPORE CAMEROON ITALY SOUTH AFRICA CANADA IVORY COAST SPAIN CEYLON JAMAICA SUDAN CHILE JAPAN SWEDEN CHINA JORDAN SWITZERLAND COLOMBIA KENYA SYRIAN ARAB REPUBLIC CONGO, DEMOCRATIC KOREA, REPUBLIC OF THAILAND REPUBLIC OF KUWAIT TUNISIA COSTA RICA LEBANON TURKEY CUBA LIBERIA UKRAINIAN SOVIET SOCIALIST CYPRUS LIBYA REPUBLIC CZECHOSLOVAK SOCIALIST LUXEMBOURG UNION OF SOVIET SOCIALIST REPUBLIC MADAGASCAR REPUBLICS DENMARK MALI UNITED ARAB REPUBLIC DOMINICAN REPUBLIC MEXICO UNITED KINGDOM OF GREAT ECUADOR MONACO BRITAIN AND NORTHERN IRELAND EL SALVADOR MOROCCO UNITED STATES OF AMERICA ETHIOPIA NETHERLANDS URUGUAY FINLAND NEW ZEALAND VENEZUELA FRANCE NICARAGUA VIET-NAM GABON YUGOSLAVIA The Agency's Statute was approved on 26 October 1956 by the Conference on the Statute of the IAEA held at United Nations Headquarters, New York; it entered into force on 29 July 1957, The Headquarters of the Agency are situated in Vienna. Its principal objective is "to accelerate and enlarge the contribution of atomic energy to peace, health and prosperity throughout the world". © IAEA, 1967 Permission to reproduce or translate the information contained in this publication may be obtained by writing to the International Atomic Energy Agency, Kamtner Ring 11, A-1010 Vienna I, Austria. Printed by the IAEA in Austria December 1967 TECHNICAL REPORTS SERIES No. 78 OPERATION AND CONTROL OF ION-EXCHANGE PROCESSES FOR TREATMENT OF RADIOACTIVE WASTES INTERNATIONAL ATOMIC ENERGY AGENCY VIENNA, 1967 OPERATION AND CONTROL OF ION-EXCHANGE PROCESSES FOR TREATMENT OF RADIOACTIVE WASTES (Technical Reports Series, No.78) ABSTRACT. A manual dealing with the application of ion-exchange materials to the treatment of radioactive wastes and reviewing the facilities currently using this method. This book is one of three commissioned by the IAEA on the three principal methods of concentrating radioactive wastes and was prepared by Mr. L.A. Emelity. Contents: Introduction; Historical review related to removal of radioactivity; Principles of ion exchange; Ion-exchange materials; Limitations of ion exchangers; Application of ion exchange to waste processing; Operational procedures and experiences; Costs of treatment by ion exchange; Appendix I - Producers of ex- change materials; Appendix II - Conversions; Appendix III - Regeneration data: specific gravity - concen- tration; Appendix IV - Glossary; Tables; References; Bibliography. Available in English only. (147 pp., 16x24 cm, paper-bound, 31 figures) (1967) Price: USÍ3.00; £1.1.2 OPERATION AND CONTROL OF ION-EXCHANGE PROCESSES FOR TREATMENT OF RADIOACTIVE WASTES IAEA, VIENNA, 1967 STI/DOC/10/78 FOREWORD When facilities are planned for handling radioactive materials, one of the many problems that arise involves the disposal of large-volume low- level wastes. The problem can be tackled by either of two methods: either to 'concentrate and contain' or to 'dilute and disperse'. The choice of method will be guided by the physical, economical, psychological and political environment. The designers of most major installations in the world have chosen to concentrate and contain the wastes, and the three principal techniques of concentration are chemical precipitation, evaporation and ion exchange. Though these techniques are well-established in the chemical processing industry, information on their application to the treatment of radioactive wastes is not readily available. To improve this situation and to give developing Member States some guidance on the solution of this waste-treatment problem, the International Atomic Energy Agency has commissioned books on the three techniques. This particular manual deals with ion exchange and has been compiled by Mr. L.A. Emelity, of Los Alamos Scientific Laboratory, University of California, Los Alamos, New Mexico, USA. Although it is assumed that the basic process is familiar to the reader, history and theory are very briefly mentioned. Ion-exchange materials, their applicationto the treatment of radioactive wastes, and a review of facilities at present using this method are the principal topics. CONTENTS I. INTRODUCTION 1 II. HISTORICAL REVIEW RELATED TO REMOVAL OF RADIOACTIVITY 4 II—1. Reactor systems 4 II—2. Miscellaneous radioactive wastes 5 III. PRINCIPLES OF ION EXCHANGE 8 III—1. General 8 III-2. Characteristics of ion-exchange materials 9 III—2. 1. Ion-exchange capacity 10 III-2.2. Sorption equilibria 10 III—2. 2.1. General 10 III-2.2.2. Donnan membrane equilibrium 11 III-2.3. Swelling equilibrium 12 III-2.4. Ion-exchange equilibrium: selectivity 13 III-2.5. Kinetics 15 III-3. Electrodialysis - Ion-exchange membranes 16 IV. ION-EXCHANGE MATERIALS 19 IV-1. General 19 IV-2. Structure of ion exchangers 19 IV-2.1. General 19 IV-2. 2. Natural inorganic and organic materials 20 IV-2. 3. Synthetic inorganic and organic materials 22 IV-3. Synthesis of ion exchangers 26 IV-3.1. Inorganic ion exchangers 26 IV-3. 2. Organic ion exchangers 27 IV-3.2.1. Condensation polymers 27 IV-3. 2. 2. Addition polymers 29 IV-3.3. Ion-exchange membranes 31 V. LIMITATIONS OF ION EXCHANGERS 32 V-l. Limitations applicable to all ion exchangers 32 V-2. Limitations applicable to natural organic exchangers 33 V-3. Limitations applicable to natural inorganic exchangers 33 V-4. Limitations applicable to synthetic organic exchangers 34 V-5. Limitations applicable to synthetic inorganic exchangers 36 V-5.1. Limitations: synthetic zeolites 36 V-5.2. Limitations: inorganic chemical compounds 36 V-6. Limitations applicable to ion-exchange membranes 37 VI. APPLICATION OF ION EXCHANGE TO WASTE PROCESSING . 38 VI-1. General 38 VI-2. Processing of reactor waters 39 VI-3. Processing of radioactive wastes 40 VI-3.1. General 40 VI-3.2. Treatment methods: batch operation 41 VI-3.3. Treatment methods: column operation 41 VI-4. Design considerations in treatment of reactor waters 46 VI~5. Design considerations in treatment of general laboratory and plant wastes 55 VI~6. Shielding requirements 60 VII. OPERATIONAL PROCEDURES AND EXPERIENCES 64 VII-1. General 64 VII-2. Operational procedures and experiences: treatment of reactor waters 64 VII-3. Experiences in treatment of general plant and laboratory wastes 66 VII-4. Transport of radioactive materials 76 VIII. COSTS OF TREATMENT BY ION EXCHANGE 78 VIII-1. General 78 VIII-2. Capital costs 79 VIII-3. Operating costs 80 APPENDICES I-IV I. PRODUCERS OF EXCHANGE MATERIALS 85 II. CONVERSIONS 86 III. REGENERATION DATA: SPECIFIC GRAVITY - CONCENTRATION 95 IV. GLOSSARY 97 TABLES I-XXVII I. Main components of the radioactivity of reactor coolant water circuits 99 II. Early reactors utilizing ion-exchange demineralization 100 III. Distribution coefficient of caesium on Decalso as a function of sodium concentration 101 IV. Approximate ion-exchange selectivity coefficients 102 V. Relative affinities of ions for a strong-acid resin with varying percentages of crosslinking 103 VI. Comparison of observed selectivity coefficients with values calculated by Myers & Boyd 104 VII. Dependence of ion-exchange rate on experimental control . 105 VIII. Relative ion-exchange rates 106 IX. Variation of resin capacity and moisture content with degree of crosslinking 107 X. Synthetic cation exchangers 108 XI. Natural cation exchangers 116 XII. Synthetic anion exchangers 118 XIII. Mixed bed ion-exchange resins 125 XIV. Ion-exchange membranes 126 XV. Coolant purification in certain early USA power reactors ... 128 XVI. Ion-exchange capacity at varying régénérant levels 129 XVII. Effect of feed rate and temperature on pressure drop 129 XVIII. Resin depth - Ion-exchange column 130 XIX. Principal radionuclides in general waste solutions 131 XX. Exchangers in use for separation of specific radionuclides 132 XXI. Research reactors using ion-exchange water treatment 133 XXII. Ion-exchange treatment of power reactor waters 134 XXIII. Ion exchange in waste treatment at nuclear energy establishments 135 XXIV. Classification of nuclides for transport purposes 136 XXV. Average prices of common engineering materials, October 1966, USA 137 XXVI. Unit operating cost: waste treatment by ion exchange 138 XXVII. Annual operating costs: waste treatment by ion exchange ... 139 REFERENCES 141 BIBLIOGRAPHY 144 I. INTRODUCTION With the rapidly expanding study and use of nuclear energy by an in- creasing number of nations, the problems of control of the radioactive waste products become more acute. Technological advances adapting nuclear physics discoveries to practical applications have followed such discoveries by only brief intervals; quantities and varieties of radioactive wastes have increased at a rate in excess of the development of control technology. Under the pressure of exceedingly limited time, the major effort in attacking the problem has been directed toward adaptation of known techniques in chemical processing and water and wastewater
Recommended publications
  • Secondary Alkane Sulfonate (SAS) (CAS 68037-49-0)
    Human & Environmental Risk Assessment on ingredients of household cleaning products - Version 1 – April 2005 Secondary Alkane Sulfonate (SAS) (CAS 68037-49-0) All rights reserved. No part of this publication may be used, reproduced, copied, stored or transmitted in any form or by any means, electronic, mechanical, photocopying, recording or otherwise without the prior written permission of the HERA Substance Team or the involved company. The content of this document has been prepared and reviewed by experts on behalf of HERA with all possible care and from the available scientific information. It is provided for information only. Much of the original underlying data which has helped to develop the risk assessment is in the ownership of individual companies. HERA cannot accept any responsibility or liability and does not provide a warranty for any use or interpretation of the material contained in this publication. 1. Executive Summary General Secondary Alkane Sulfonate (SAS) is an anionic surfactant, also called paraffine sulfonate. It was synthesized for the first time in 1940 and has been used as surfactant since the 1960ies. SAS is one of the major anionic surfactants used in the market of dishwashing, laundry and cleaning products. The European consumption of SAS in detergent application covered by HERA was about 66.000 tons/year in 2001. Environment This Environmental Risk Assessment of SAS is based on the methodology of the EU Technical Guidance Document for Risk Assessment of Chemicals (TGD Exposure Scenario) and the HERA Exposure Scenario. SAS is removed readily in sewage treatment plants (STP) mostly by biodegradation (ca. 83%) and by sorption to sewage sludge (ca.
    [Show full text]
  • Nuclear Power Plant Organization and Staffing for Lessons Learned
    IAEA-TECDOC-1052 minium XA9848504 Nuclear power plant organization staffingand for improved performance: lessons learned INTERNATIONAL ATOMIC ENERGY AGENCY fl/U Lr\^ The originating Section of this publication in the IAEA was: Nuclear Power Engineering Section International Atomic Energy Agency Wagramer Strasse5 P.O. Box 100 A-1400 Vienna, Austria NUCLEAR POWER PLANT ORGANIZATION AND STAFFING FOR IMPROVED PERFORMANCE: LESSONS LEARNED IAEA, VIENNA, 1998 IAEA-TECDOC-1052 ISSN 1011-4289 ©IAEA, 1998 Printe IAEe th AustriAn y i d b a November 1998 The IAEA does not normally maintain stocks of reports in this series. However, microfiche copies of these reports can be obtained from INIS Clearinghouse International Atomic Energy Agency Wagramerstrasse5 0 10 P.Ox Bo . A-1400 Vienna, Austria Orders shoul accompaniee db prepaymeny db f Austriao t n Schillings 100, fore for e chequa th f mth IAEmf o n i n o i r eAo microfiche service coupons which may be ordered separately from the INIS Clearinghouse. FOREWORD Experience from well operated nuclear power plants (NPPs) aroun worle dth d indicates that an organizational structure that effectively supports plant operation s i essentias n i l economically achieving high level f safet so operationa d yan l performance same th t e A .time , in many Member States, energy market e beinar s g opene o competitiont d n i s i t I . consideration of this new competitive energy market that this publication focuses on organization and staffing of NPPs to improve efficiency and effectiveness. This publication is primarily intended for senior NPP and utility managers.
    [Show full text]
  • 038 12 Conduct of Operations
    TMI-1 UFSAR CHAPTER 12 – CONDUCT OF OPERATIONS TABLE OF CONTENTS SECTION TITLE 12.0 CONDUCT OF OPERATIONS 12.1 ORGANIZATIONAL STRUCTURE 12.1.1 OFFSITE ORGANIZATION 12.1.2 OPERATING ORGANIZATION 12.1.2.1 PLANT DIVISION 12.1.2.1.1 OPERATIONS DEPARTMENT 12.1.2.1.2 MAINTENANCE DEPARTMENT 12.1.2.1.3 WORK MANAGEMENT DEPARTMENT 12.1.2.1.4 RADIOLOGICAL HEALTH AND SAFETY DEPARTMENT 12.1.2.1.5 CHEMISTRY DEPARTMENT 12.1.2.2 SECURITY DEPARTMENT 12.1.2.3 SITE ENGINEERING DEPARTMENT 12.1.2.3.1 PLANT ENGINEERING SECTION 12.1.2.3.2 DESIGN ENGINEERING SECTION 12.1.2.3.3 PROGRAMS SECTION 12.1.2.4 TRAINING DEPARTMENT 12.1.2.5 BUSINESS OPERATIONS DEPARTMENT 12.1.2.6 REGULATORY ASSURANCE DEPARTMENT 12.1.2.7 MANAGER – HUMAN RESOURCES 12.1.2.8 PROJECT MANAGEMENT DEPARTMENT 12.1.3 QUALIFICATION OF NUCLEAR PLANT PERSONNEL 12.1.4 SAFETY REVIEWS 12.2 TRAINING 12.2.1 TRAINING PROGRAMS 12.2.2 TECHNICAL TRAINING 12.2.2.1 MAINTENANCE TRAINING 12.2.2.2 RADIOLOGICAL CONTROLS/CHEMISTRY TRAINING PROGRAMS 12.2.3 OPERATIONS TRAINING 12.2.3.1 REPLACEMENT OPERATOR TRAINING PROGRAM (AO/CRO/SRO) 12.2.3.2 LICENSED OPERATOR REQUALIFICATION TRAINING PROGRAM (CRO/SRO) 12.2.3.3 SHIFT TECHNICAL ADVISOR (STA) TRAINING PROGRAM 12.2.3.4 AUXILIARY OPERATOR (AO) REQUALIFICATION TRAINING PROGRAM 12.2.4 TRAINING SUPPORT 12.2.4.1 GENERAL EMPLOYEE TRAINING PROGRAMS 12.2.4.2 FIRE PROTECTION TRAINING PROGRAM 12.2.4.3 EMERGENCY PREPAREDNESS TRAINING PROGRAMS 12.2.4.4 NOT USED 12.2.5 ENGINEERING SUPPORT PERSONNEL (ESP)TRAINING PROGRAM 12.2.6 TRAINING RECORDS CHAPTER 12 12-i REV.
    [Show full text]
  • Upgrading Water Treatment Plants
    Upgrading Water Treatment Plants E. G. Wagner and R. G. Pinheiro ISBN 0-419-26050-1 (pbk) 0-419-26040-4 Published on behalf of the WORLD HEALTH ORGANIZATION London and New York First published 2001 by Spon Press 11 New Fetter Lane, London EC4P 4EE Simultaneously published in the USA and Canada by Spon Press 29 West 35th Street, New York, NY 10001 Spon Press is an imprint of the Taylor & Francis Group © 2001 World Health Organization The authors alone are responsible for the views expressed in this publication. Printed and bound in Great Britain by TJ International Ltd, Padstow, Cornwall All rights reserved. No part of this book may be reprinted or reproduced or utilised in any form or by any electronic, mechanical, or other means, now known or hereafter invented, including photocopying and recording, or in any information storage or retrieval system, without permission in writing from the publishers. The publisher makes no representation, express or implied, with regard to the accuracy of the information contained in this book and cannot accept any legal responsibility or liability for any errors or omissions that may be made. Publisher's Note This book has been prepared from camera-ready copy provided by the authors. British Library Cataloguing in Publication Data A catalogue record for this book is available from the British Library Library of Congress Cataloging in Publication Data A catalogue record has been requested Foreword The availability of safe water, and in particular safe drinking water, has been an area of concern to the World Health Organization for many years.
    [Show full text]
  • Configuration Management in Nuclear Power Plants
    IAEA-TECDOC-1335 Configuration management in nuclear power plants January 2003 The originating Section of this publication in the IAEA was: Nuclear Power Engineering Section International Atomic Energy Agency Wagramer Strasse 5 P.O. Box 100 A-1400 Vienna, Austria CONFIGURATION MANAGEMENT IN NUCLEAR POWER PLANTS IAEA, VIENNA, 2003 IAEA-TECDOC-1335 ISBN 92–0–100503–2 ISSN 1011–4289 © IAEA, 2003 Printed by the IAEA in Austria January 2003 FOREWORD Configuration management (CM) is the process of identifying and documenting the characteristics of a facility’s structures, systems and components of a facility, and of ensuring that changes to these characteristics are properly developed, assessed, approved, issued, implemented, verified, recorded and incorporated into the facility documentation. The need for a CM system is a result of the long term operation of any nuclear power plant. The main challenges are caused particularly by ageing plant technology, plant modifications, the application of new safety and operational requirements, and in general by human factors arising from migration of plant personnel and possible human failures. The IAEA Incident Reporting System (IRS) shows that on average 25% of recorded events could be caused by configuration errors or deficiencies. CM processes correctly applied ensure that the construction, operation, maintenance and testing of a physical facility are in accordance with design requirements as expressed in the design documentation. An important objective of a configuration management program is to ensure that accurate information consistent with the physical and operational characteristics of the power plant is available in a timely manner for making safe, knowledgeable, and cost effective decisions with confidence.
    [Show full text]
  • INTRODUCTION to PFAS November 8, 2019
    INTRODUCTION TO PFAS November 8, 2019 trcsolutions.com | PFAS in the News https://pfasproject.com trcsolutions.com 2 Today’s Topics • PFAS Naming Conventions • Physical/Chemical Properties of PFAS • Sources of PFAS and Potentially- affected Sites • Replacement PFAS Chemistry • AFFF • Toxicology 3 PFAS Naming Conventions 4 Acronyms • PFC = Per-fluorinated chemical PFCA • PFAS = Per- and Poly-fluoroalkyl substances Perfluoroalkyl Substances PFAA • PFAA = Perfluoroalkyl acids PFSA • PFOA = Perfluorooctanoic acid (perfluorooctanoate) • PFOS = Perfluorooctane sulfonic acid (perfluorooctane sulfonate) • PFCA = Perfluorocarboxylic acids • PFSA = Perfluorosulfonic acids trcsolutions.com 5 Perfluorinated Compounds (PFCs) PFCs: Do not use this acronym anymore! • PFCs previously used to describe greenhouse gases • PFCs do not include polyfluorinated compounds 6 Quick Chemistry Lesson #1 • Remember: PFAS are Per and Polyfluoroalkyl substances • Per-fluoroalkyl substances: fully fluorinated alkyl tail • Perfluoroalkane carboxylates (or carboxylic acids): PFCAs FFF F F F O COOH = Head F C C C C (PFOA) C C C C OH F PFAAs F FFFFFF Alkyl tail, fully fluorinated • Perfluoroalkane sulfonates (or sulfonic acids): PFSAs FFF F F F F F F C C C C (PFOS) C C C C SO3H SO3H= Head F F FFFFFF 7 Quick Chemistry Lesson #2 • Remember: PFAS are Per and Polyfluoroalkyl substances • Poly-fluoroalkyl substances: non-fluorine atom (typically hydrogen or oxygen) attached to at least one carbon atom in the alkane chain Fluorotelomer Alcohol (8:2 FTOH) FFF F F F F F HH C C C
    [Show full text]
  • Facilities Operations Manual
    U.S. Department of Justice Federal Bureau of Prisons P R O G R A M S T A T E M E N T OPI: ADM/FAC NUMBER: 4200.11 DATE: April 12, 2016 Facilities Operations Manual /s/ Approved: Thomas R. Kane Acting Director, Federal Bureau of Prisons 1. PURPOSE AND SCOPE Since the Manual’s last edition, operations have been changed and new policies developed to improve organizational efficiency. This edition incorporates individual duties of Facilities Management staff, makes changes reflecting new laws and regulations, and consolidates Bureau directives regarding physical plant maintenance and operations. a. Summary of Changes Policy Rescinded P4200.10 Facilities Operations Manual (1/24/2006) This Program Statement incorporates changes in the areas listed below: ■ Rewrite of Chapter 1, Facilities Administration and Organization ■ Rewrite of Chapter 2, Work Programming, Scheduling and Reporting ■ Rewrite of Chapter 3, Buildings and Facilities Projects ■ Rewrite of Chapter 4, Architect-Engineer Services ■ Rewrite of Chapter 5, Preventive Maintenance/Inspections ■ Rewrite, renaming, and renumbering of Chapter 6, Automated Systems and Document Control ■ Rewrite and renaming of Chapter 7, Life Safety/Fire Protection ■ Rewrite and renaming of Chapter 8, Environmental ■ Rewrite of Chapter 9, Telecommunication Systems and Electronic Equipment ■ Rewrite and renaming of Chapter 10, Vehicle Fleet ■ Rewrite of Chapter 11, Mechanical Systems and Power Plant Operations ■ Rewrite of Chapter 12, Electrical Systems ■ Rewrite of Chapter 13, Physical Plant Review Program ■ Rewrite of Chapter 14, Plumbing Systems ■ Rewrite of Chapter 15, Accessibility ■ Rewrite, renaming, and renumbering of Chapter 16, Energy/Water Conservation and Greenhouse Gas ■ Rewrite of Chapter 17, Historic Preservation b.
    [Show full text]
  • Fundamentals of Nuclear Power
    Fundamentals of Nuclear Power Juan S. Giraldo Douglas J. Gotham David G. Nderitu Paul V. Preckel Darla J. Mize State Utility Forecasting Group December 2012 Table of Contents List of Figures .................................................................................................................................. iii List of Tables ................................................................................................................................... iv Acronyms and Abbreviations ........................................................................................................... v Glossary ........................................................................................................................................... vi Foreword ........................................................................................................................................ vii 1. Overview ............................................................................................................................. 1 1.1 Current state of nuclear power generation in the U.S. ......................................... 1 1.2 Nuclear power around the world ........................................................................... 4 2. Nuclear Energy .................................................................................................................... 9 2.1 How nuclear power plants generate electricity ..................................................... 9 2.2 Radioactive decay .................................................................................................
    [Show full text]
  • Why Nature Chose Selenium Hans J
    Reviews pubs.acs.org/acschemicalbiology Why Nature Chose Selenium Hans J. Reich*, ‡ and Robert J. Hondal*,† † University of Vermont, Department of Biochemistry, 89 Beaumont Ave, Given Laboratory, Room B413, Burlington, Vermont 05405, United States ‡ University of WisconsinMadison, Department of Chemistry, 1101 University Avenue, Madison, Wisconsin 53706, United States ABSTRACT: The authors were asked by the Editors of ACS Chemical Biology to write an article titled “Why Nature Chose Selenium” for the occasion of the upcoming bicentennial of the discovery of selenium by the Swedish chemist Jöns Jacob Berzelius in 1817 and styled after the famous work of Frank Westheimer on the biological chemistry of phosphate [Westheimer, F. H. (1987) Why Nature Chose Phosphates, Science 235, 1173−1178]. This work gives a history of the important discoveries of the biological processes that selenium participates in, and a point-by-point comparison of the chemistry of selenium with the atom it replaces in biology, sulfur. This analysis shows that redox chemistry is the largest chemical difference between the two chalcogens. This difference is very large for both one-electron and two-electron redox reactions. Much of this difference is due to the inability of selenium to form π bonds of all types. The outer valence electrons of selenium are also more loosely held than those of sulfur. As a result, selenium is a better nucleophile and will react with reactive oxygen species faster than sulfur, but the resulting lack of π-bond character in the Se−O bond means that the Se-oxide can be much more readily reduced in comparison to S-oxides.
    [Show full text]
  • A Method for the Production of Sulfate Or Sulfonate Esters
    (19) *EP002851362B1* (11) EP 2 851 362 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) Int Cl.: of the grant of the patent: C07C 303/24 (2006.01) C07C 303/28 (2006.01) (2006.01) (2006.01) 27.11.2019 Bulletin 2019/48 C07C 305/06 C07C 305/08 C07C 305/20 (2006.01) C07C 305/24 (2006.01) (2006.01) (21) Application number: 13185032.3 C07C 309/73 (22) Date of filing: 18.09.2013 (54) A method for the production of sulfate or sulfonate esters Verfahren zur Herstellung von Sulfat oder Sulfonatestern Procédé pour la production d’esters de sulfate ou de sulfonate (84) Designated Contracting States: (56) References cited: AL AT BE BG CH CY CZ DE DK EE ES FI FR GB • DENIZ GUNES ET AL: "ALIPHATIC THIOETHERS GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO BY S-ALKYLATION OF THIOLS VIA TRIALKYL PL PT RO RS SE SI SK SM TR BORATES", PHOSPHORUS, SULFUR AND SILICON AND THE RELATED ELEMENTS, (43) Date of publication of application: TAYLOR & FRANCIS INC, US, vol. 185, no. 8, 1 25.03.2015 Bulletin 2015/13 January 2010 (2010-01-01), pages 1685-1690, XP008165903, ISSN: 1042-6507, DOI: (73) Proprietor: Ulusal Bor Arastirma Enstitusu 10.1080/10426500903213563 [retrieved on 06520 Ankara (TR) 2010-08-02] • OKI ET AL: "Solvothermal synthesis of carbon (72) Inventors: nanotube-B2O3 nanocomposite using tributyl • Bicak, Niyazi borate as boron oxide source", INORGANIC 34469 Istanbul (TR) CHEMISTRY COMMUNICATIONS, ELSEVIER, • Gunes, Deniz AMSTERDAM, NL, vol.
    [Show full text]
  • Isolation of Organic Selenium Compounds from Antarctic Krill After Enzymatic Hydrolysis and Bifunctional Chromatography
    Isolation of Organic Selenium Compounds from Antarctic Krill after Enzymatic Hydrolysis and Bifunctional Chromatography Von der Fakultät Maschinenbau der Helmut-Schmidt-Universität / Universität der Bundeswehr Hamburg zur Erlangung des akademischen Grades einer Doktor-Ingenieurin genehmigte DISSERTATION vorgelegt von M. Sc. Mariana Siwek aus Bukarest Hamburg 2007 Gutachter: Prof. Dr.-Ing. Bernd Niemeyer Helmut-Schmidt-Universität / Universität der Bundeswehr Hamburg Prof. Dr. Volker Kasche Technische Universität Hamburg-Harburg Tag der Disputation: 07. Dezember 2007 Acknowledgement My sincere thanks to Prof. Bernd Niemeyer and Prof. Volker Kasche for giving me this great opportunity to perform my PhD thesis at the Department of Biotechnology II (now Institute of Technical Biocatalysis) of the Hamburg University of Technology and for offering me during this time their helpful support and guidance. I acknowledge with thanks and deepest appreciation Dr. Boris Galunsky for his precious scientific guidance and for his invaluable advice over these years. I would also like to thank my colleagues from my department and also Dr. Jan Bergmann and his colleagues from the GKSS Institute of Coastal Research in Geesthacht for their help, advice and experience. And last but not least, many thanks go to my family and my friends who always supported and believed in me. Their constant encouragement and understanding motivated me and essentially contributed to the accomplishment of this work. I II TABLE OF CONTENTS 1. INTRODUCTION...............................................................................................
    [Show full text]
  • Functional Group Manipulation Usin Organoselenium Reagents
    22 Reich Accounts of Chemical Research (25), bound covalently or by physical forces to the possibilities. One is that cosynthetase alters the con- enzyme system, is then converted into uro’gen-I11 (1) formation of the deaminase-bilane complex to direct by an intramolecular rearrangement which directly cyclization of 25 at C-16. There are indication^",^^ that affects only ring D and the two carbons which become deaminase associates with cosynthetase, and it has been C-15 and C-20. The nature of the intermediate between ~uggested”~,~~that cosynthetase acts as a “specifier the bilane and uro’gen-111 remains to be established, protein” in the way lactoalbumiri works during the and this leads to the concluding section. biosynthesis of lactose. The other possibility is that the Prospect. In the presence of deaminase alone, and bilane (25) is the product from deaminase but is then also nonenzymically, the cyclization of bilane (25) occurs the substrate for cosynthetase which brings about ring at C-19 to produce 26, leading to uro’gen-I (11). We closure with rearrangement to produce uro’gen-I11 suggest that in the presence of cosynthetase cyclization specifically. occurs at C-16 rather than at (2-19 (Scheme XIII). The Work is in hand on these aspects and on the problem postulated attack at C-16 would produce the spiro of the structure of the intermediate5’ between the bilane intermediate 27; the labeling arising from 25b and 25c and uro‘gen-111. It will be good to have the answers to is shown. Fragmentation and cyclization again as il- the few remaining questions.
    [Show full text]