| Preface to the First Edition |
| Preface to the Second Edition |
| Preface to the Student Edition |
| List of Symbols |
| Fundamentals of chemical reactor calculations / Chapter I： |
| Introduction / 1.1： |
| Material balance / 1.2 The material, energy and economic balance： |
| Energy balance |
| Economic balance |
| Heat of reaction / 1.3 Thermodynamic data: heat of reaction and chemical equilibrium： |
| Chemical equilibrium |
| Conversion rate, chemical reaction rate and chemical reaction rate equations / 1.4： |
| Influence of temperature on kinetics |
| Influence of concentration on kinetics |
| The degree of conversion / 1.5： |
| Relation between conversion and concentration expressions |
| Selectivity and yield / 1.6： |
| Selectivity and yield in a reactor section with recycle of non-converted reactant |
| Classification of chemical reactors / 1.7： |
| References |
| Model reactors: single reactions, isothermal single phase reactor calculations / Chapter II： |
| The well-mixed batch reactor / II.1： |
| The continuously operated ideal tubular reactor / II.2： |
| The continuously operated ideal tank reactor / II.3： |
| The cascade of tank reactors / 11.4： |
| The semi-continuous tank reactor / II.5： |
| The recycle reactor / II.6： |
| A comparison between the different model reactors / II.7： |
| Batch versus continuous operation |
| Tubular reactor versus tank reactor |
| Some examples of the influence of reactor design and operation on the economics of the process / II.8： |
| The use of one of the reactants in excess |
| Recirculation of unconverted reactant |
| Maximum production rate and optimum load with intermittent operation |
| Model reactors: multiple reactions, isothermal single phase reactors / Chapter III： |
| Fundamental concepts / III.1： |
| Differential selectivity and selectivity ratio |
| The reaction path |
| Parallel reactions / III.2： |
| Parallel reactions with equal order rate equations |
| Parallel reactions with differing reaction order rate equations |
| A cascade of tank reactors |
| The continuous cross flow reactor system / III.3： |
| Consecutive reactions / III.4： |
| First order consecutive reactions in a plug flow reactor |
| First order consecutive reactions in a tank reactor |
| General discussion |
| Combination reactions / III.5： |
| Graphical methods |
| Optimum yield in a cascade of tank reactors |
| Algebraic methods |
| Autocatalytic reactions / III.6： |
| Single biochemical reactions |
| Multiple autocatalytic reactions |
| Residence time distribution and mixing in continuous flow reactors / Chapter IV： |
| The residence time distribution (RTD) / IV.1： |
| The E and the F diagram |
| The application of the RTD in practice |
| Experimental determination of the residence time distribution / IV.2： |
| Input functions |
| Residence time distribution in a continuous plug flow and in a continuous ideally stirred tank reactor / IV.3： |
| Models for intermediate mixing / IV.4： |
| Model of a cascade of N equal ideally mixed tanks |
| The axially dispersed plug flow model |
| Conversion in reactors with intermediate mixing / IV.5： |
| Some data on the longitudinal dispersion in continuous flow systems / IV.6： |
| Flow through empty tubes |
| Packed beds |
| Fluidized beds |
| Mixing in gas-liquid reactors |
| Nature of the micromixing phenomena / Chapter V Influence of micromixing on chemical reactions： |
| Macro or gross overall mixing as characterized by the residence time distribution |
| The state of aggregation of the reacting fluid |
| The earliness of the mixing |
| Boundaries to micromixing phenomena / V.2： |
| The model tubular and tank reactors |
| Boundaries for micromixing for reactors with arbitrary RTDs |
| Intermediate degree of micromixing in continuous stirred tank rea / V.3： |
| Preface to the First Edition |
| Preface to the Second Edition |
| Preface to the Student Edition |
図書
