chemical reactor design - harriot (2003)

... 10016 tel: 21 2-6 9 6-9 000; fax: 21 2-6 8 5-4 540 Eastern Hemisphere Distribution Marcel Dekker AG Hutgasse 4, Postfach 812, CH-4001 Basel, Switzerland tel: 4 1-6 1-2 6 0-6 300; fax: 4 1-6 1-2 6 0-6 333 World Wide ... value of E. SCALEUP AND DESIGN PROCEDURES The design of large-scale chemical reactors is usually based on conversion and yield data from laboratory re...

Ngày tải lên: 01/04/2014, 10:31

... / 413 8.5 Polymerization Reactors / 413 8.6 Biochemical Reactors / 414 8.7 Slurry Reactors / 415 8.8 Microscale Reactors / 415 INDEX 417 xii CONTENTS PREFACE Chemical reactors are unquestionably ... catalyst. The three classical generic chemical reactors are the batch reactor, the continuous stirred-tank reactor (CSTR), and the plug flow tubular reactor (PFR). Each of these reactor...

Ngày tải lên: 01/04/2014, 10:24

... by Vðt batch Þ: 70 CHEMICAL REACTOR DESIGN, OPTIMIZATION, AND SCALEUP 15.1.1 Inert Tracer Experiments 540 15.1.2 Means and Moments 543 15.2 Residence Time Models 545 15.2.1 Ideal Reactors and Reactor Combinations ... needed for most practical problems in chemical reactor design, but sophisti- cated numerical techniques are rarely necessary given the speed of modern com- puters. Th...

Ngày tải lên: 01/04/2014, 10:31

... ln f i ( 2-5 6) Differentiating Equation 2-5 6 at constant temperature and compo- sition gives dµ i = RTd ln f i ( 2-5 7) Combining Equations 2-5 5 and 2-5 7 gives RTd f V dp ii T ln = [] ( 2-5 8) Subtracting ... greater demands on chemical engineers. Consequently, chemical reactor design methodologies must incorporate both control and hazard analysis. However, the desig...

Ngày tải lên: 01/04/2014, 10:25

... Towers 14.3.f Bubble Reactors 14.3.g Stirred Vessel Reactors E.rump/e 14.3.g-I Design ofu Liquid-Phase o-Xj.lene Oxidurion Reactor. A. Stirred rank reacror. B. Bubble reactor, 732 Acknowledgments ... A)&apos ;-& quot; mf3"(krnol .A)' -& quot; (kmol S )-& quot; (krnol s )-& quot; m:'" ;- " hr- mP3(m- "s" kg cokeikg cat. hr...

Ngày tải lên: 01/04/2014, 10:25

... I Reactor pressure Reactor temperature Gas composition (mole percent): butene-1 cis-butene-2 trans-butene-2 Run II Reactor pressure Reactor temperature Gas composition (mole percent): butene-1 cis-butene-2 trans-butQnQ-2 53.33 ... v ki in the fcth row and the ith column. -1 2 0 0 0 0-1 -1 1 1 -1 1 0-1 1 (2.9.6) 0 1 1-1 -1 1-2 000 Next, take the first...

Ngày tải lên: 01/04/2014, 10:25

... Using the Reaction Model 283 5.3.9 Design of the First-stage Reactor . . 285 5.3.10 Design of the Second-stage Reactor. 292 5.4 Hydrotreating Reactor Design Alan G. Bridge and E. Morse ... The process consists of first-stage azeotropic reactor and second-stage solvent reactor. The first-stage reactor is a batch type reactor with stirrer. This reactor is o...

Ngày tải lên: 01/04/2014, 10:29

Ngày tải lên: 01/04/2014, 10:30

... Mixed Reactors and in a Succession of Isothermal Plug Flow and Completely Mixed Reactors: Completely Macro-Mixed versus Completely Macro- and Micro- Mixed 12.7 Semi-Empirical Models for Reactors ... a First-Order Irreversible Reaction. Comparison with Conventional Design Models 14.3.7 Stirred Vessel Reactors 832 Example 14.3.7.A Design of a Liquid-Phase 837 o-Xylene Oxidation...

Ngày tải lên: 01/04/2014, 10:31

... stirred-tank reactor (CSTR), and (c) cascade of CSTRs. 1.2 CLASSIFICATION OF CHEMICAL REACTORS 5 Figure 1.3 Multiphase reactors: (a) packed-bed reactor, (b) moving-bed reactor, (c) flui- dized-bed reactor, ... Stirred-Tank Reactor (CSTR), 105 4.2.3 Plug-Flow Reactor (PFR), 106 4.3 Reaction-Based Design Equations, 107 4.3.1 Ideal Batch Reactor, 107 4.3.2 Plug-Flow Reactor, 109 4....

Ngày tải lên: 01/04/2014, 10:36