| PREFACE |
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xv | |
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1 | (32) |
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1.1 Definition of the Rate of Reaction, --r(A) |
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2 | (4) |
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1.2 The General Mole Balance Equation |
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6 | (2) |
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8 | (2) |
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1.4 Continuous-Flow Reactors |
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10 | (6) |
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1.4.1 Continuous-Stirred Tank Reactor |
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10 | (1) |
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11 | (3) |
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14 | (2) |
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16 | (9) |
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25 | (1) |
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25 | (6) |
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31 | (1) |
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31 | (2) |
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2 CONVERSION AND REACTOR SIZING |
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33 | (35) |
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2.1 Definition of Conversion |
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33 | (1) |
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34 | (6) |
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34 | (3) |
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37 | (3) |
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2.3 Applications of the Design Equations for Continuous-Flow Reactors |
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40 | (8) |
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48 | (8) |
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2.5 Some Further Definitions |
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56 | (3) |
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59 | (3) |
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62 | (4) |
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66 | (1) |
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67 | (1) |
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3 RATE LAWS AND STOICHIOMETRY |
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68 | (57) |
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68 | (15) |
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3.1.1 The Reaction Rate Constant |
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69 | (4) |
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73 | (2) |
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3.1.3 Elementary Rate Laws and Molecularity |
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75 | (2) |
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3.1.4 Reversible Reactions |
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77 | (4) |
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3.1.5 Nonelementary Rate Laws and Reactions |
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81 | (2) |
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3.2 Present Status of Our Approach to Reactor Sizing and Design |
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83 | (1) |
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84 | (21) |
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84 | (3) |
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3.3.2 Constant-Volume Reaction Systems |
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87 | (3) |
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90 | (2) |
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3.3.4 Volume Change with Reaction |
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92 | (3) |
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3.4 Expressing Concentrations in Terms Other Than Conversion |
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105 | (2) |
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3.5 Reactions with Phase Change |
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107 | (4) |
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111 | (3) |
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114 | (9) |
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123 | (1) |
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123 | (2) |
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4 ISOTHERMAL REACTOR DESIGN |
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125 | (98) |
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4.1 Design Structure for Isothermal Reactors |
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125 | (4) |
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4.2 Scale-Up of Liquid-Phase Batch Reactor Data to the Design of a CSTR |
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129 | (18) |
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129 | (8) |
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137 | (10) |
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147 | (6) |
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4.4 Pressure Drop in Reactors |
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153 | (21) |
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4.4.1 Pressure Drop and the Rate Law |
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153 | (1) |
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4.4.2 Flow Through a Packed Bed |
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154 | (14) |
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4.4.3 Spherical Packed-Bed Reactors |
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168 | (5) |
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4.4.4 Pressure Drop in Pipes |
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173 | (1) |
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4.5 Synthesizing a Chemical Plant |
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174 | (2) |
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4.6 Using C(A) (liquid) and F(A) (gas) in the Mole Balances and Rate Laws |
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176 | (11) |
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4.6.1 CSTRs, PFRs, PBRs, and Batch Reactors |
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177 | (5) |
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182 | (5) |
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4.7 Unsteady-State Operation of Reactors |
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187 | (13) |
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189 | (1) |
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190 | (7) |
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4.7.3 Reactive Distillation |
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197 | (3) |
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200 | (2) |
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202 | (2) |
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204 | (1) |
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205 | (14) |
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Journal Critique Problems |
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219 | (1) |
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Some Thoughts on Critiquing What You Read |
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220 | (1) |
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220 | (2) |
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222 | (1) |
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5 COLLECTION AND ANALYSIS OF RATE DATA |
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223 | (59) |
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224 | (15) |
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5.1.1 Differential Method of Rate Analysis |
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224 | (11) |
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235 | (4) |
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5.2 Method of Initial Rates |
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239 | (3) |
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242 | (1) |
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5.4 Differential Reactors |
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243 | (7) |
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5.5 Least-Square Analysis |
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250 | (12) |
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5.5.1 Linearization of the Rate Law |
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250 | (2) |
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5.5.2 Nonlinear Least-Squares Analysis |
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252 | (9) |
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5.5.3 Weighted Least-Squares Analysis |
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261 | (1) |
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5.6 Experimental Planning (CD-ROM) |
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262 | (1) |
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5.7 Evaluation of Laboratory Reactors (CD-ROM) |
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263 | (5) |
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5.7.1 Integral (Fixed-Bed) Reactor |
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264 | (1) |
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5.7.2 Stirred Batch Reactor |
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264 | (1) |
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5.7.3 Stirred Contained Reactor (SCSR) |
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265 | (1) |
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5.7.4 Continuous-Stirred Tank Reactor (CSTR) |
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265 | (1) |
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5.7.5 Straight-Through Transport Reactor |
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266 | (1) |
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5.7.6 Recirculating Transport Reactor |
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266 | (1) |
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5.7.7 Summary of Reactor Ratings |
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267 | (1) |
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268 | (1) |
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269 | (10) |
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Journal Critique Problems |
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279 | (1) |
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280 | (1) |
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280 | (2) |
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282 | (57) |
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6.1 Maximizing the Desired Product in Parallel Reactions |
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284 | (7) |
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6.1.1 Maximizing the Rate Selectivity Parameter S for One Reactant |
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285 | (3) |
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6.1.2 Maximizing the Rate Selectivity Parameter S for Two Reactants |
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288 | (3) |
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6.2 Maximizing the Desired Product in Series Reactions |
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291 | (4) |
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6.3 Algorithm for Solution to Complex Reactions |
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295 | (19) |
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295 | (1) |
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6.3.2 Net Rates of Reaction |
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296 | (1) |
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297 | (1) |
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6.3.4 Stoichiometry: Relative Rates of Reaction |
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297 | (3) |
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6.3.5 Stoichiometry: Concentrations |
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300 | (1) |
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301 | (6) |
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6.3.7 Multiple Reactions in a CSTR |
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307 | (7) |
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314 | (1) |
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315 | (1) |
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6.6 The Attainable Region CD-ROM |
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316 | (2) |
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318 | (2) |
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320 | (15) |
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Journal Critique Problems |
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335 | (1) |
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335 | (1) |
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336 | (3) |
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7 NONELEMENTARY REACTION KINETICS |
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339 | (87) |
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340 | (4) |
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7.1.1 Active Intermediates |
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340 | (2) |
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7.1.2 Pseudo-Steady-State Hypothesis (PSSH) |
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342 | (2) |
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7.2 Searching for a Mechanism |
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344 | (10) |
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7.2.1 General Considerations |
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344 | (8) |
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352 | (2) |
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354 | (29) |
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7.3.1 Step Polymerization |
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356 | (4) |
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7.3.2 Chain Polymerizations Reactions |
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360 | (8) |
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7.3.3 Modeling a Batch Polymerization Reactor |
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368 | (2) |
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7.3.4 Molecular Weight Distribution |
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370 | (5) |
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7.3.5 Anionic Polymerization |
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375 | (8) |
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7.4 Enzymatic Reaction Fundamentals |
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383 | (10) |
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7.4.1 Definitions and Mechanisms |
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383 | (3) |
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7.4.2 Michaelis-Menten Equation |
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386 | (3) |
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7.4.3 Batch Reactor Calculations |
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389 | (2) |
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7.4.4 Inhibition of Enzyme Reactions |
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391 | (1) |
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7.4.5 Multiple Enzyme and Substrate Systems |
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392 | (1) |
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393 | (15) |
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394 | (2) |
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396 | (2) |
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398 | (2) |
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400 | (4) |
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404 | (1) |
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404 | (2) |
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406 | (1) |
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7.5.8 Oxygen-Limited Germentation |
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407 | (1) |
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407 | (1) |
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408 | (2) |
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410 | (13) |
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423 | (1) |
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Journal Critique Problems |
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424 | (1) |
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424 | (2) |
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8 STEADY-STATE NONISOTHERMAL REACTOR DESIGN |
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426 | (108) |
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426 | (1) |
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427 | (13) |
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8.2.1 First Law Thermodynamics |
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427 | (2) |
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8.2.2 Evaluating the Work Term |
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429 | (1) |
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8.2.3 Dissecting the Steady-State Molar Flow Rates to Obtain the Heat of Reaction |
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430 | (2) |
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8.2.4 Dissecting the Enthalpies |
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432 | (2) |
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8.2.5 Relating DeltaH(Rx)(T), DeltaH(0)(Rx), and DeltaC(p) |
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434 | (1) |
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8.2.6 Constant of Mean Heat Capacities |
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435 | (1) |
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8.2.7 Variable Heat Capacities |
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436 | (2) |
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8.2.8 Heat Added to the Reactor, Q |
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438 | (2) |
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8.3 Nonisothermal Continuous-Flow Reactors |
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440 | (28) |
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8.3.1 Application to the CSTR |
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441 | (10) |
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8.3.2 Adiabatic Tubular Reactor |
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451 | (7) |
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8.3.3 Steady-State Tubular Reactor with Heat Exchange |
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458 | (10) |
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8.4 Equilibrium Conversion |
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468 | (10) |
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8.4.1 Adiabatic Temperature and Equilibrium Conversion |
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468 | (8) |
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8.4.2 Optimum Feed Temperature |
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476 | (2) |
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8.5 Nonadiabatic Reactor Operation: Oxidation of Sulfur Dioxide Example |
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478 | (12) |
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8.5.1 Manufacture of Sulfuric Acid |
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478 | (3) |
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8.5.2 Catalyst Quantities |
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481 | (1) |
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8.5.3 Reactor Configuration |
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482 | (1) |
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8.5.3 Operating Conditions |
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482 | (8) |
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8.6 Multiple Steady States |
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490 | (10) |
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8.6.1 Heat-Removed Term, R(T) |
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491 | (1) |
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8.6.2 Heat of Generation, G(T) |
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492 | (1) |
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8.6.3 Ignition-Extinction Curve |
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493 | (4) |
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497 | (1) |
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8.6.5 Steady-State Bifurcation Analysis |
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498 | (2) |
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8.7 Nonisothermal Multiple Chemical Reactions |
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500 | (7) |
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500 | (4) |
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504 | (3) |
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507 | (4) |
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511 | (19) |
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Journal Critique Problems |
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530 | (1) |
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530 | (2) |
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532 | (2) |
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9 UNSTEADY-STATE NONISOTHERMAL REACTOR DESIGN |
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534 | (47) |
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534 | (1) |
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9.2 Unsteady Operation of CSTRs and Semibatch Reactors |
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535 | (18) |
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537 | (1) |
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9.2.2 Adiabatic Operation of a Batch Reactor |
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537 | (11) |
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9.2.3 Transient CSTR, Batch, and Semibatch Reactors with Heat Exchanger--Ambient Temperature Not Spatially Uniform |
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548 | (5) |
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9.3 Approach to the Steady State |
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553 | (5) |
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9.4 Control of Chemical Reactors |
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558 | (8) |
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9.4.1 Falling Off the Steady State |
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558 | (3) |
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9.4.2 Adding a Controller to a CSTR |
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561 | (5) |
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9.5 Nonisothermal Multiple Reactions |
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566 | (4) |
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9.6 Unsteady Operation of Plug-Flow Reactors |
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570 | (1) |
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571 | (1) |
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572 | (7) |
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579 | (1) |
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579 | (2) |
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10 CATALYSIS AND CATALYTIC REACTORS |
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581 | (105) |
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581 | (10) |
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582 | (1) |
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10.1.2 Catalyst Properties |
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583 | (1) |
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10.2 Steps in a Catalytic Reaction |
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591 | (12) |
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10.2.1 Adsorption Isotherms |
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594 | (5) |
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599 | (2) |
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601 | (1) |
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10.2.4 The Rate-Limiting Step |
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601 | (2) |
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10.3 Synthesizing a Rate Law, Mechanism, and Rate-Limiting Step |
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603 | (16) |
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10.3.1 Is the Adsorption of Cumene Rate-Limiting? |
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606 | (3) |
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10.3.2 Is the Surface Reaction Rate-Limiting? |
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609 | (1) |
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10.3.3 Is the Desorption of Benzene Rate-Limiting? |
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610 | (2) |
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10.3.4 Summary of the Cumene Decomposition |
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612 | (4) |
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10.3.5 Rate Laws Derived from the Pseudo-Steady-State Hypothesis |
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616 | (3) |
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10.4 Design of Reactors for Gas-Solid Reactions |
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619 | (1) |
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619 | (1) |
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10.4.2 The Design Equations |
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619 | (1) |
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10.5 Heterogeneous Data Analysis for Reactor Design |
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620 | (11) |
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10.5.1 Deducing a Rate Law from the Experimental Data |
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622 | (1) |
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10.5.2 Finding a Mechanism Consistent with Experimental Observations |
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623 | (1) |
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10.5.3 Evaluation of the Rate Law Parameters |
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624 | (3) |
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627 | (4) |
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10.6 Chemical Vapor Deposition |
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631 | (3) |
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10.7 Catalyst Deactivation |
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634 | (28) |
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10.7.1 Types of Catalyst Deactivation |
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636 | (11) |
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10.7.2 Temperature-Time Trajectories |
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647 | (2) |
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10.7.3 Moving-Bed Reactors |
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649 | (6) |
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10.7.4 Straight-Through Transport Reactors |
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655 | (5) |
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10.7.5 Determining the Order of Deactivation |
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660 | (2) |
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10.8 Reaction Engineering in Microelectronic Device Fabrication |
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662 | (3) |
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664 | (1) |
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665 | (3) |
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668 | (14) |
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Journal Critique Problems |
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682 | (1) |
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683 | (1) |
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684 | (2) |
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11 EXTERNAL DIFFUSION EFFECTS ON HETEROGENEOUS REACTIONS |
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686 | (52) |
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11.1 Mass Transfer Fundamentals |
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687 | (2) |
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687 | (1) |
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687 | (1) |
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688 | (1) |
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689 | (10) |
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11.2.1 Evaluating the Molar Flux |
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689 | (3) |
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11.2.2 Boundary Conditions |
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692 | (1) |
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11.2.3 Modeling Diffusion Without Reaction |
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692 | (5) |
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11.2.4 Temperature and Pressure Dependence of D(AB) |
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697 | (1) |
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11.2.5 Modeling Diffusion with Chemical Reaction |
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698 | (1) |
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11.3 External Resistance to Mass Transfer |
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699 | (16) |
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11.3.1 Mass Transfer Coefficient |
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699 | (3) |
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11.3.2 Mass Transfer to a Single Particle |
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702 | (4) |
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11.3.3 Mass Transfer-Limited Reactions in Packed Beds |
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706 | (8) |
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11.3.4 Mass Transfer-Limited Reaction on Metallic Surfaces |
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714 | (1) |
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11.4 What If...? (Parameter Sensitivity) |
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715 | (4) |
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11.5 The Shrinking Core Model |
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719 | (9) |
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11.5.1 Catalyst Regeneration |
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720 | (4) |
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11.5.2 Dissolution of Monodispersed Solid Particles |
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724 | (2) |
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11.5.3 Flow and Dissolution in Porous Media |
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726 | (2) |
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728 | (1) |
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729 | (6) |
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735 | (1) |
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Journal Critique Problems |
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735 | (1) |
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735 | (1) |
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736 | (2) |
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12 DIFFUSION AND REACTION IN POROUS CATALYSTS |
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738 | (71) |
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12.1 Diffusion and Reaction in Spherical Catalyst Pellets |
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739 | (8) |
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12.1.1 Effective Diffusivity |
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739 | (2) |
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12.1.2 Derivation of the Differential Equation Describing Diffusion and Reaction |
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741 | (2) |
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12.1.3 Writing the Equation in Dimensionless Form |
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743 | (3) |
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12.1.4 Solution to the Differential Equation for a First-Order Reaction |
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746 | (1) |
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12.2 Internal Effectiveness Factor |
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747 | (6) |
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753 | (2) |
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12.4 Overall Effectiveness Factor |
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755 | (3) |
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12.5 Estimation of Diffusion- and Reaction-Limited Regimes |
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758 | (3) |
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12.5.1 Weisz-Prater Criterion for Internal Diffusion |
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758 | (3) |
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12.6 Mass Transfer and Reaction in a Packed Bed |
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761 | (6) |
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12.7 Determination of Limiting Situations from Reaction Data |
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767 | (1) |
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768 | (18) |
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769 | (14) |
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12.8.2 Trickle Bed Reactors |
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783 | (3) |
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12.9 Fluidized-Bed Reactors(CD-ROM) |
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786 | (1) |
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787 | (2) |
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12.11 Chemical Vapor Deposition Reactors |
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789 | (4) |
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793 | (2) |
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795 | (9) |
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804 | (1) |
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Journal Critique Problems |
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805 | (1) |
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805 | (1) |
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806 | (3) |
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13 DISTRIBUTIONS OF RESIDENCE TIMES FOR CHEMICAL REACTORS |
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809 | (62) |
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13.1 General Characteristics |
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809 | (3) |
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13.1.1 Residence-Time Distribution Function |
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811 | (1) |
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13.2 Measurement of the RTD |
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812 | (7) |
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813 | (5) |
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13.2.2 Step Tracer Experiment |
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818 | (1) |
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13.3 Characteristics of the RTD |
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819 | (10) |
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13.3.1 Integral Relationships |
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819 | (2) |
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13.3.2 Mean Residence Time |
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821 | (2) |
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13.3.3 Other Moments of the RTD |
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823 | (2) |
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13.3.4 Normalized RTD Function, E(Tan) |
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825 | (1) |
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13.3.5 Internal-Age Distribution 1Alpha |
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826 | (3) |
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13.4 RTD in Ideal Reactors |
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829 | (7) |
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13.4.1 RTDs in Batch and Plug-Flow Reactors |
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829 | (1) |
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829 | (2) |
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13.4.3 Laminar Flow Reactor |
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831 | (2) |
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13.4.4 PFR/CSTR Series RTD |
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833 | (3) |
|
13.5 Reactor Modeling with the RTD |
|
|
836 | (2) |
|
13.6 Zero-Parameter Models |
|
|
838 | (13) |
|
|
|
838 | (6) |
|
|
|
844 | (7) |
|
|
|
851 | (1) |
|
13.7 Using Software Packages |
|
|
851 | (3) |
|
13.8 RTD and Multiple Reactions |
|
|
854 | (6) |
|
|
|
854 | (1) |
|
|
|
855 | (5) |
|
|
|
860 | (1) |
|
|
|
861 | (7) |
|
|
|
868 | (1) |
|
|
|
869 | (2) |
|
14 MODELS FOR NONIDEAL REACTORS |
|
|
871 | (50) |
|
|
|
871 | (1) |
|
14.2 One-Parameter Models |
|
|
872 | (21) |
|
14.2.1 Tanks-in-Series Model |
|
|
873 | (4) |
|
|
|
877 | (16) |
|
14.3 Two-Parameter Models--Modeling Real Reactors with Combinations of Ideal Reactors |
|
|
893 | (8) |
|
14.3.1 Real CSTR Modeled Using Bypassing and Dead Space |
|
|
893 | (1) |
|
14.3.1A Solving the Model System for C(A) and X |
|
|
894 | (1) |
|
14.3.1B Using a Tracer to Determine the Model Parameters in CSTR-with-Dead-Space-and-Bypass Model |
|
|
895 | (4) |
|
14.3.2 Real CSTR Modeled with an Exchange Volume |
|
|
899 | (1) |
|
14.3.2A Solving the Model System for C(A) and X |
|
|
900 | (1) |
|
14.3.2B Using a Tracer to Determine the Model Parameters in a CSTR with an Exchange Volume |
|
|
900 | (1) |
|
14.4 Use of Software Packages to Determine the Model Parameters |
|
|
901 | (3) |
|
14.5 Other Models of Nonideal Reactors Using CSTRs and PFRs |
|
|
904 | (1) |
|
14.6 Using the RTD Versus Needing a Model |
|
|
904 | (3) |
|
|
|
907 | (2) |
|
|
|
909 | (7) |
|
|
|
916 | (1) |
|
|
|
917 | (4) |
|
Appendix A NUMERICAL TECHNIQUES |
|
|
921 | (6) |
|
A.1 Useful Integrals in Reactor Design |
|
|
921 | (1) |
|
A.2 Equal-Area Graphical Differentiation |
|
|
922 | (2) |
|
A.3 Solutions to Differential Equations |
|
|
924 | (1) |
|
A.4 Numerical Evaluation of Integrals |
|
|
924 | (2) |
|
|
|
926 | (1) |
|
Appendix B IDEAL GAS CONSTANT AND CONVERSION FACTORS |
|
|
927 | (2) |
|
Appendix C THERMODYNAMIC RELATIONSHIPS INVOLVING THE EQUILIBRIUM CONSTANT |
|
|
929 | (6) |
|
Appendix D MEASUREMENT OF SLOPES ON SEMILOG PAPER |
|
|
935 | (1) |
|
Appendix E SOFTWARE PACKAGES |
|
|
936 | (2) |
|
|
|
938 | (3) |
|
Appendix G MOLECULAR DYNAMICS OF CHEMICAL REACTIONS |
|
|
941 | (12) |
|
|
|
941 | (3) |
|
G.2 Transition State Theory |
|
|
944 | (4) |
|
|
|
948 | (5) |
|
Appendix H OPEN-ENDED PROBLEMS |
|
|
953 | (3) |
|
H.1 Design of Reaction Engineering Experiment |
|
|
953 | (1) |
|
H.2 Effective Lubricant Design |
|
|
953 | (1) |
|
H.3 Peach Bottom Nuclear Reactor |
|
|
953 | (1) |
|
H.4 Underground Wet Oxidation |
|
|
954 | (1) |
|
H.5 Hydrosulfurization Reactor Design |
|
|
954 | (1) |
|
H.6 Continuous Bioprocessing |
|
|
954 | (1) |
|
|
|
954 | (1) |
|
|
|
954 | (2) |
|
Appendix I HOW TO USE THE CD-ROM |
|
|
956 | (2) |
|
Appendix J USE OF COMPUTATIONAL CHEMISTRY SOFTWARE PACKAGES |
|
|
958 | (3) |
| INDEX |
|
961 | (15) |
| ABOUT THE CD |
|
976 | |