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Coulson and Richardson's chemical engineering. Volume 3A, Chemical and biochemical reactors and reaction engineering /

Coulson and Richardson's Chemical Engineering: Volume 3A: Chemical and Biochemical Reactors and Reaction Engineering, Fourth Edition, covers reactor design, flow modelling, gas-liquid and gas-solid reactions and reactors.

Detalles Bibliográficos
Clasificación:Libro Electrónico
Otros Autores: Ravi, R. (Editor ), Vinu, R. (Editor ), Gummadi, Sathyanarayana N. (Editor ), Coulson, J. M. (John Metcalfe)
Formato: Electrónico eBook
Idioma:Inglés
Publicado: Kidlington, Oxford, United Kingdom : Butterworth-Heinemann is an imprint of Elsevier, [2017]
Edición:Fourth edition.
Temas:
Acceso en línea:Texto completo

MARC

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245 0 0 |a Coulson and Richardson's chemical engineering.  |n Volume 3A,  |p Chemical and biochemical reactors and reaction engineering /  |c edited by R. Ravi, R. Vinu, S.N. Gummadi. 
246 3 0 |a Chemical and biochemical reactors and reaction engineering 
250 |a Fourth edition. 
264 1 |a Kidlington, Oxford, United Kingdom :  |b Butterworth-Heinemann is an imprint of Elsevier,  |c [2017] 
300 |a 1 online resource 
336 |a text  |b txt  |2 rdacontent 
337 |a computer  |b c  |2 rdamedia 
338 |a online resource  |b cr  |2 rdacarrier 
500 |a Includes index. 
505 0 |a Front Cover; Coulson and Richardson's Chemical Engineering; Coulson and Richardson's Chemical Engineering: Volume 3A: Chemical and Biochemical Reactors and Reaction Engineering; Copyright; Contents; List of Contributors; Preface; 1 -- Reactor Design-General Principles; 1.1 Basic Objectives in Design of a Reactor; 1.1.1 By-products and Their Economic Importance; 1.1.2 Preliminary Appraisal of a Reactor Project; 1.2 Classification of Reactors and Choice of Reactor Type; 1.2.1 Homogeneous and Heterogeneous Reactors; 1.2.2 Batch Reactors and Continuous Reactors 
505 8 |a 1.2.3 Variations in Contacting Pattern-Semibatch Operation1.2.4 Influence of Heat of Reaction on Reactor Type; 1.2.4.1 Adiabatic Reactors; 1.2.4.2 Reactors With Heat Transfer; 1.2.4.3 Autothermal Reactor Operation; 1.3 Choice of Process Conditions; 1.3.1 Chemical Equilibria and Chemical Kinetics; 1.3.2 Calculation of Equilibrium Conversion; 1.3.3 Ultimate Choice of Reactor Conditions; 1.4 Material and Energy Balances; 1.4.1 Material Balance and the Concept of Rate of Generation of a Species; 1.4.2 Energy Balance; 1.5 Chemical Kinetics and Rate Equations 
505 8 |a 1.5.1 Definition of Order of Reaction and Rate Constant1.5.2 Influence of Temperature: Activation Energy; 1.5.3 Rate Equations and Reaction Mechanism; 1.5.4 Reversible Reactions; 1.5.5 Experimental Determination of Kinetic Constants; 1.6 Batch Reactors; 1.6.1 Calculation of Reaction Time: Basic Design Equation; 1.6.2 Reaction Time-Isothermal Operation; 1.6.3 Maximum Production Rate; 1.6.4 Reaction Time-Nonisothermal Operation; 1.6.5 Adiabatic Operation; 1.6.6 Kinetics From Batch Reactor Data; 1.6.6.1 Differential Method; 1.6.6.2 Integral Method 
505 8 |a 1.6.6.3 Differential Versus Integral Method: Comparison1.6.6.4 Fractional Life Method; 1.6.6.5 Kinetics of Gas-Phase Reactions From Pressure Measurements; 1.7 Tubular Flow Reactors; 1.7.1 Basic Design Equations for a Tubular Reactor; 1.7.2 Tubular Reactors-Nonisothermal Operation; 1.7.3 Pressure Drop in Tubular Reactors; 1.7.4 Kinetic Data From Tubular Reactors; 1.8 Continuous Stirred Tank Reactors; 1.8.1 Assumption of Ideal Mixing: Residence Time; 1.8.2 Design Equations for Continuous Stirred Tank Reactors; 1.8.3 Graphical Methods; 1.8.4 Autothermal Operation 
505 8 |a 1.8.5 Kinetic Data From Continuous Stirred Tank Reactors1.9 Comparison of Batch, Tubular, and Stirred Tank Reactors for a Single Reaction: Reactor Output; 1.9.1 Batch Reactor and Tubular Plug Flow Reactor; 1.9.2 Continuous Stirred Tank Reactor; 1.9.2.1 One Tank; 1.9.2.2 Two Tanks; 1.9.3 Comparison of Reactors; 1.10 Comparison of Batch, Tubular, and Stirred Tank Reactors for Multiple Reactions: Reactor Yield; 1.10.1 Types of Multiple Reactions; 1.10.2 Yield and Selectivity; 1.10.3 Reactor Type and Backmixing; 1.10.4 Reactions in Parallel; 1.10.4.1 Requirements for High Yield 
588 0 |a Online resource; title from digital title page (viewed on September 06, 2018). 
504 |a Includes bibliographical references and index. 
520 |a Coulson and Richardson's Chemical Engineering: Volume 3A: Chemical and Biochemical Reactors and Reaction Engineering, Fourth Edition, covers reactor design, flow modelling, gas-liquid and gas-solid reactions and reactors. 
590 |a Knovel  |b ACADEMIC - Chemistry & Chemical Engineering 
650 0 |a Chemical engineering. 
650 0 |a Bioreactors. 
650 2 |a Chemical Engineering 
650 2 |a Bioreactors 
650 6 |a Génie chimique. 
650 6 |a Bioréacteurs. 
650 7 |a chemical engineering.  |2 aat 
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650 7 |a Chemical engineering.  |2 fast  |0 (OCoLC)fst00852893 
700 1 |a Ravi, R.,  |e editor. 
700 1 |a Vinu, R.,  |e editor 
700 1 |a Gummadi, Sathyanarayana N.,  |e editor. 
700 1 |a Coulson, J. M.  |q (John Metcalfe).  |t Chemical engineering. 
776 0 8 |i Print version:  |z 0081010966  |z 9780081010969  |w (OCoLC)975468211 
856 4 0 |u https://appknovel.uam.elogim.com/kn/resources/kpCRCEVAC1/toc  |z Texto completo 
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