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Calculations in Furnace Technology. Division of Materials Science and Technology PDF

277 Pages·1970·3.775 MB·English
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PERGAMON MATERIALS ADVISORY COMMITTEE DR. H.M. FINNISTON, F.R.S. Chairman DR. G. ARTHUR DR. J.E. BURKE PROFESSOR B. CHALMERS PROFESSOR A. CHARLESBY PROFESSOR R.W. DOUGLAS D.W. HOPKINS PROFESSOR W.S. OWEN PROFESSOR G.V. RAYNOR, F.R.S. PROFESSOR D.W. SAUNDERS LIEUT-COLONEL S.C. GUILLAN. Executive Member CALCULATIONS IN FURNACE TECHNOLOGY BY CLIVE DAVIES Ph.D. (B'ham), B.Sc. Hons. (Wales), A.I.M., A.M. Inst. F., A.R.I.C Swansea College of Technology 1966 P E R G A M ON PRESS OXFORD - LONDON · EDINBURGH · NEW YORK TORONTO - SYDNEY - PARIS · BRAUNSCHWEIG Pergamon Press Ltd., Headington Hill Hall, Oxford 4 & 5 Fitzroy Square, London W.l Pergamon Press (Scotland) Ltd., 2 & 3 Teviot Place, Edinburgh 1 Pergamon Press Inc., Maxwell House, Fairview Park, Elmsford, New York 10523 Pergamon of Canada Ltd., 207 Queen's Quay West, Toronto 1 Pergamon Press (Aust.) Pty. Ltd., 19a Boundary Street, Rushcutters Bay, N.S.W. 2011, Australia e Pergamon Press S.A.R.L., 24 rue des Écoles, Paris 5 Vieweg&Sohn GmbH, Burgplatz 1, Braunschweig Copyright © 1970 Clive Davies First edition 1970 All Rights Reserved. No part of this publication may be reproduced, stored in a retrieval system, or transmitted, in any form or by any means, electronic, mechanical, photo- copying, recording or otherwise, without the prior per- mission of Pergamon Press Ltd. Library of Congress Catalog Card No. 78-102400 Printed in Hungary This book is sold subject to the condition that it shall not, by way of trade, be lent, resold, hired out, or otherwise disposed of without the publisher's consent, in any form of binding or cover other than that in which it is published. 08 013365 7 (flexicover) 08 013366 5 (hard cover) To my wife Marion Preface THIS is intended as a course book for students taking exami- nations under the broad subject heading "Furnace Technol- ogy". It should be particularly useful to students of Metallurgy taking Furnace Technology at both part II and part IV of the Institution of Metallurgists examinations. It does, however, cover the requirements of a large number of professional, technical and university courses. For this reason, many of the worked examples have been given in detail. It has been the author's experience that such a treatment is very necessary and not an over-simplification. It is expected that students will be conversant with the ap- propriate subject-matter of the book, and will have studied, or will be studying, the more theoretical and practical aspects of the subject-matter. xi Acknowledgements GRATEFUL acknowledgement is made to the various publishers and authors who have permitted the use of their illustrations. Full references are given in the text. The author also acknowledges the assistance of the Institute of Fuel, the Institution of Metallurgists, the Institution of Heat- ing and Ventilating Engineers, the City and Guilds of London Institute, the Swansea Education Committee, and the Univer- sity of Wales, in granting permission for the use of past exami- nation questions. The author accepts full responsibility for any errors in reproduction of questions and for the solutions given. Since the change to SI units is imminent a number of the examples have been changed to what they would probably have been in this system of units. Finally, I would like to thank J. N. Harris and D. H. Davies for helpful suggestions, and D. W. Hopkins, without whose considerable help and encouragement this book might never have been completed. xiii Introduction FURNACE technology involves the detailed study of solid, liquid, gaseous, and nuclear fuels and electric heating as well as the design of furnaces and other heat utilization devices. In order to compare the economics of different sources of heat the effi- ciency of utilization processes must be determined. Furnaces and boilers using the same or different fuels may be compared one with another, or with the theoretical thermodynamic heat requirement for the operation. In order to arrive at efficiencies of utilization, various calculations have to be made. Thus, the available heat in fuels (calorific values), the rate of combustion, and the product of these two, calorific intensity, need to be determined in order to decide whether sufficient heat of the required level of intensity is theoretically available in the fuel to carry out the specified duty. In evaluating efficiencies, it is necessary to measure the quan- tity of fuel used, of air entering, and of flue gases leaving the plant, and the heat lost to the surroundings. In addition, the effect of insulation upon furnace structures must be calculated before it is actually installed. For example, in the open-hearth steel furnace, while heat conservation by roof insulation ap- pears desirable, any attempt to do so would raise the temperature of the "cold end" to such a value that the refractory would fail by deformation under the existing compression stresses. In all instances of furnace insulation there is an optimum beyond which the additional cost of lagging exceeds the value of the heat saved. When the design of furnaces is under consideration, it is necessary to calculate the size of flues, combustion space, and chimneys, and the rating of fans required to supply sufficient air for combustion. It is also necessary to calculate the pressure XV XVI INTRODUCTION losses that occur throughout the system. Temperatures and temperature differences must also be known as the basis for choice of materials and for installation of heat recovery de- vices. CHAPTER 1 Introductory 1.1. INTRODUCTION The fossil fuels—coal, oil, and gas—are at present the most important sources of energy, although atomic energy is likely to assume increasing importance. Atomic energy has to be con- verted into a usable form, generally electricity, and this, at present, involves normal modes of heat transference. The instrinsic value of any fuel as a source of heat is related to the heat which would be produced by combustion under iso- thermal and ideal gas conditions. Coal and oil are defined by the geologist as sedimentary rocks but they differ from all other sedimentary rocks by being organic (chemical) and it is the release of the heat of combus- tion of the organic material that provides us with a source of energy. In most coalfields there is a geological continuity from peat through brown coals to the anthracites. This change in rank can be measured by a number of parameters, perhaps the best function being the increase in carbon content of the vitrain macιrai, vitrain being one of the four banded constituents that can be observed by macroscopic examination of coals. Just as rocks contain minerals, so coals contain macιrais. No chemical formula can be applied to coal or oil; the for- mer is a complex organic molecule whose structure has not yet been elucidated, while oil is a complex mixture of many differ- ent organic molecules. However, both can be assigned elemen- tal formulae which indicate the percentages of carbon, hydro- gen, oxygen, nitrogen, sulphur, and other elements, and this in- formation is generally sufficient to assess the value of the pro- D : CIFT 2 1 2 CALCULATIONS IN FURNACE TECHNOLOGY duct as a fuel. In both cases it is necessary to consider the effect of any mineral matter which is present, before any calculations on the basis of elemental composition can be made, since in many cases the mineral matter can either interfere with the mechanical processes of combustion or have deleterious effects on the structure of the combustion chamber. 1.2. PRESENTATION OF ANALYSIS Solid fuels contain inorganic matter and are usually burned containing moisture, and the combustion engineer requires to know the composition and characteristics of the material being burned—the "as-fired" analysis. Sampling and analysis of fuels at this stage is generally inconvenient and expensive and it is necessary to devise a method of presentation which will enable allowances to be made for variations resulting from changes in sources of supply and from consequences of storage in the open. Analysis may be carried out on "air-dried" fuel, i.e. fuel in approximate equilibrium with the atmosphere at the prevailing temperature and humidity, or on the "dry basis", i.e. after heating to 105°C for at least one hour in vacuo, or in an atmos- phere of nitrogen. Solid fuel for industrial purposes is purchased against specified values for heating capacity, moisture and ash content, chemical composition in respect of certain elements, and physical condition relative to size. The mineral matter in coal as mined is not identical with the ash content as determined by combustion under standard conditions. But there is a com- paratively simple relationship : the King-Maries-Crossley for- mula (KMC) where mineral matter (MM) is given by : MM =1-13 ash +0-5 pyritic S + 08C0 —2-8 S 2 in ash + 2-8SO +0-5Cl. 4 Alternatively, the British Coal Utilization Research Associa- tion (BCURA) formula, which requires less data, may be used : MM = 1· 10 ash+0-53 total S + 0-74 C0 - 0-32. 2

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