反应工程 化工技术 李绍芬 新华正版
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江苏无锡
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作者李绍芬
出版社化学工业出版社
ISBN9787122306722
出版时间2019-01
版次1
装帧平装
开本16
页数664页
字数994千字
定价298元
货号xhwx_1201768406
上书时间2024-05-05
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目录：
list of contributors ii
preface xv
1. introduction 1
1.1 chemical reaction engineering 1
1.2 conversion and yield of chemical reactions 4
1.2.1 extent of reaction 4
1.2.2 conversion 5
1.2.3 yield and selectivity 7
1.3 classifications of chemical reactors 10
1.4 operation modes of chemical reactors 13
1.5 models in reactor design 16
1.6 scale-up of industrial reactors 19
further rea 22
problems 22
2. fundamentals of reaction kiics 25
2.1 reaction rate 26
2.2 reaction rate equations 30
2.3 effect of temperature on reaction rate 37
2.4 multiple reactions 44
2.4.1 consumption rate and formation rate 44
2.4.2 basic types of multiple reactions 45
2.4.3 reaction work 50
2.5 transformation and integration of reaction rate equations 52
2.5.1 single reaction 52
2.5.2 multiple reactions 57
2.6 heterogeneous catalysis and adsorption 60
2.6.1 heterogeneous catalysis 61
2.6.2 adsorption and desorption 62
2.7 kiics of heterogeneous catalytic reactions 67
2.7.1 steady-state appromation and rate-determining step 68
2.7.2 rate equations of heterogeneous catalytic reactions 70
2.8 determination of kiic parameters 77
2.8.1 integration method 77
2.8.2 differential method 79
2.9 procedure for developing reaction rate equation 86
further rea 87
problems 88
3. tank reactor 95
3.1 mass balance for tank reactor 96
3.2 design of isothermal batch tank reactor(single reaction) 97
3.2.1 calculation of reaction time and reaction volume 98
3.2.2 optimal reaction time 102
3.3 design of isothermal batch tank reactor (multiple reactions) 103
3.3.1 parallel reactions 103
3.3.2 consecutive reactions 107
3.4 reactor volume for continuous tank reactor (cstr) 111
3.5 cstr in series and parallel 115
3.5.1 overview 115
3.5.2 calculations for multiple reactors in series 117
3.5.3 optimal reaction volume ratio for cstr in series 122
3.6 yield and selectivity for multiple reactions in a tank reactor 123
3.6.1 overall yield and overall selectivity 124
3.6.2 parallel reactions 125
3.6.3 consecutive reactions 129
3.7 semibatch tank reactor 133
3.8 nonisothermal batch reactor 138
3.9 steady-state operation of cstr 145
3.9.1 heat balance for cstr 145
3.9.2 steady-states of cstr 147
summary 151
further rea 152
problems 153
4. tubular reactor 161
4.1 plug flow 161
4.2 design of isothermal tubular reactor 163
4.2.1 single reaction 164
4.2.2 multiple reactions 168
4.2.3 eudo homogeneous model 176
4.3 parison of reactor volumes of tubular and tank reactors 178
4.4 recycle reactor 184
4.5 nonisothermal tubular reactor 185
4.5.1 heat balance equation for tubular reactor 186
4.5.2 adiabatic tubular reactor 188
4.5.3 nonadiabatic nonisothermal tubular reactor 193
4.6 optimal temperature sequence for tubular reactors 197
4.6.1 single reaction 198
4.6.2 multiple reactions 200
further rea 203
problems 203
5. residence time distribution and flow models for reactors 213
5.1 residence time distribution 214
5.1.1 overview 214
5.1.2 quantitative delineation of rtd 215
5.2 experimental determination of rtd 218
5.2.1 pulse experiments 219
5.2.2 step experiments 221
5.3 statistical eigenvalues of rtd 224
5.4 rtd of ideal reactors 228
5.4.1 plug-flow model 228
5.4.2 perfectly-mixed flow model 230
5.5 nonideal flow phenomenon 234
5.6 nonideal flow models 238
5.6.1 segregation model 238
5.6.2 tanks-in-series model 242
5.6.3 aal dispersion model 247
5.7 design of nonideal reactors 251
5.8 ming of fluids in flow reactors 256
further rea 260
problems 261
6. chemical reaction and transport phenomena in heterogeneous system 265
6.1 ste in heterogeneous reactions 266
6.1.1 macroscopic structures and properties of solid catalyst particles 266
6.1.2 ste in a catalytic reaction 269
6.2 heat and mass transfer between bulk fluid and the catalyst external surface 270
6.2.1 transport coefficient 270
6.2.2 concentration and temperature difference between the external surface of catalyst and bulk fluid 272
6.2.3 effect of external diffusion on heterogeneous catalytic reactions 275
6.3 gas diffusion in porous media 279
6.3.1 diffusion in pores 279
6.3.2 diffusion in porous particles 280
6.4 diffusion and reaction in porous catalysts 281
6.4.1 reactant concentration profile in porous catalysts 282
6.4.2 internal effectiveness factor 285
6.4.3 internal effectiveness factor for non-first order reactions 290
6.4.4 effectiveness factor under the influences of both internal and external diffusions 292
6.5 effect of internal diffusion on selectivity of multiple reactions 294
6.6 determination of diffusion impact on heterogeneous reactions 297
6.6.1 determination of the effects of external diffusion 297
6.6.2 determining the effects of internal diffusion 299
6.7 effects of diffusion on experimental measurement of reaction rate 301
further rea 305
problems 306
7. analysis and design of heterogeneous catalytic reactors 311
7.1 transport phenomena inside fixed bed reactors 312
7.1.1 fluid flow inside a fixed bed 312
7.1.2 mass and heat dispersion along aal direction 316
7.1.3 mass and heat transfer in radial direction 317
7.2 mathematical model for fixed bed reactor 320
7.3 adiabatic fixed bed reactor 325
7.3.1 adiabatic reactors 325
7.3.2 catalyst volume for adiabatic fixed bed reactor 327
7.3.3 multistage adiabatic reactors 331
7.4 fixed bed reactor with internal heat exchanger 337
7.4.1 overview 337
7.4.2 analysis for single reaction 339
7.4.3 analysis of multiple reaction systems 342
7.5 autothermal fixed bed reactors 347
7.5.1 feed flow direction 348
7.5.2 mathematical model 349
7.6 parameter sensitivity 351
7.7 laboratory catalytic reactor 355
7.7.1 basic requirements 355
7.7.2 main types of experimental reactor 357
further rea 361
problems 361
8. fluidized bed reactor 369
8.1 introduction 369
8.2 fluidization 369
8.2.1 fluidization phenomenon 369
8.2.2 particle classifications 370
8.2.3 fluidization parameters 371
8.2.4 fluidization regimes 375
8.3 bubbling fluidized bed 376
8.3.1 bubble behaviors 377
8.3.2 mathematical model of bubbling fluidized bed 380
8.4 turbulent fluidized bed 388
8.4.1 regime transition 388
8.4.2 hydrodynamic characteristics 389
8.5 circulating fluidized bed 389
8.5.1 introduction 389
8.5.2 configuration of cfb 391
8.5.3 mathematical models of cfb 392
8.6 downer reactor 398
further rea 401
problems 402
9. multiple-phase reactors 405
9.1 gas-liquid reactions 405
9.1.1 eudo first order reaction 408
9.2 gas-liquid reactors 412
9.2.1 main types of reactors 412
9.2.2 design of bubble column reactor 414
9.2.3 design of stirred tank reactor 419
9.3 gas-liquid-solid reactions 421
9.3.1 introduction 421
9.3.2 mass transfer ste and rates in gas-solid-liquid catalytic reactions 422
9.4 trickle bed reactors 425
9.4.1 introduction 425
9.4.2 mathematical model 427
9.5 slurry reactor 431
9.5.1 types of reactors 431
9.5.2 mass transfer and reaction 432
9.5.3 design of mechanically stirred slurry tank reactor 437
further rea 441
problems 441
10. fluid-solid noncatalytic reaction kiics and reactors 445
10.1 fluid-solid noncatalytic reactions and their applications 446
10.2 reaction rate of particles in different shapes 448
10.3 theoretical models of solid reactions 451
10.4 kiic analysis of continuous model 452
10.5 kiic analysis at constant particle size using the shrinking core model 454
10.5.1 overall macroreaction rate 456
10.5.2 macroreaction rate under internal diffusion control 459
10.5.3 macroreaction rate under external diffusion control 460
10.5.4 intrinsic reaction rate under surface reaction control 461
10.5.5 parison and differentiation of rate-controlling ste at constant particle size 463
10.6 kiic analysis with changing particle diameter using the shrinking core model 466
10.6.1 internal diffusion control 469
10.6.2 external diffusion control 470
10.6.3 chemical reaction control 471
10.6.4 overall reaction time 473
10.7 microparticle model 473
10.8 chemical vapor deition 477
10.9 design of fluid-solid noncatalytic reactor 479
10.9.1 reactor types 480
10.9.2 flowing and ming of reaction ponents 480
10.9.3 reactor design when fluid is a plete ming flow and solid phase is a plug flow 483
10.9.4 reactor design when fluid and solid phases can be treated as plete ming flow 484
further rea 487
problems 487
11. fundamentals of biochemical reaction engineering 491
11.1 introduction 491
11.2 fundamentals of biochemical reaction kiics 494
11.2.1 enzyme-catalyzed reactions and its kiics 494
11.2.2 kiics of microbial reactions 507
11.3 immobilized biocatalysts 513
11.3.1 introduction 513
11.3.2 enzyme and cell immobilization 514
11.3.3 catalytic kiics of immobilized biocatalyst 517
11.4 bioreactors 521
11.4.1 types of bioreactors 522
11.4.2 bioreactor calculations 527
reference 536
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