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E-raamat: Numerical Simulation of Multiphase Reactors with Continuous Liquid Phase

(Institute of Process Engineering, Chinese Academy of Sciences), (Institute of Process Engineering, Chinese Academy of Sciences)
  • Formaat: PDF+DRM
  • Ilmumisaeg: 04-Sep-2014
  • Kirjastus: Academic Press Inc.(London) Ltd
  • Keel: eng
  • ISBN-13: 9780124115798
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Numerical Simulation of Multiphase Reactors with Continuous Liquid PhaseSuurem pilt
  • Formaat: PDF+DRM
  • Ilmumisaeg: 04-Sep-2014
  • Kirjastus: Academic Press Inc.(London) Ltd
  • Keel: eng
  • ISBN-13: 9780124115798
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Numerical simulation of multiphase reactors with continuous liquid phase provides current research and findings in multiphase problems, which will assist researchers and engineers to advance this field. This is an ideal reference book for readers who are interested in design and scale-up of multiphase reactors and crystallizers, and using mathematical model and numerical simulation as tools. Yang and Maos book focuses on modeling and numerical applications directly in the chemical, petrochemical, and hydrometallurgical industries, rather than theories of multiphase flow. The content will help you to solve reacting flow problems and/or system design/optimization problems. The fundamentals and principles of flow and mass transfer in multiphase reactors with continuous liquid phase are covered, which will aid the readers understanding of multiphase reaction engineering.

Muu info

The definitive reference book on multiphase reactors!
Preface x
Chapter 1 Introduction
1(4)
Chapter 2 Fluid flow and mass transfer on particle scale
5(70)
2.1 Introduction
5(1)
2.2 Theoretical basis
6(4)
2.2.1 Fluid mechanics
6(1)
2.2.2 Mass transfer
7(1)
2.2.3 Interfacial force balance
8(1)
2.2.4 Interfacial mass transport
9(1)
2.3 Numerical methods
10(14)
2.3.1 Orthogonal boundary-fitted coordinate system
10(5)
2.3.2 Level set method
15(6)
2.3.3 Mirror fluid method
21(3)
2.4 Buoyancy-driven motion and mass transfer of a single particle
24(13)
2.4.1 Drop, bubble and solid particle motion
25(9)
2.4.2 Mass transfer to/from a drop
34(3)
2.5 Mass transfer-induced Marangoni effect
37(13)
2.5.1 Solute-induced Marangoni effect
37(3)
2.5.2 Effect of surfactant on drop motion and mass transfer
40(8)
2.5.3 Surfactant-induced Marangoni effect
48(2)
2.6 Behavior of particle swarms
50(9)
2.6.1 Introduction
50(2)
2.6.2 Forces on single particles
52(4)
2.6.3 Cell model
56(3)
2.7 Single particles in shear flow and extensional flow
59(4)
2.7.1 Mass/heat transfer from a spherical particle in extensional flow
60(1)
2.7.2 Flow and transport from a sphere in simple shear flow
61(2)
2.8 Summary and perspective
63(12)
2.8.1 Summary
63(2)
2.8.2 Perspective
65(2)
Nomenclature
67(1)
References
68(7)
Chapter 3 Multiphase stirred reactors
75(78)
3.1 Introduction
75(1)
3.2 Mathematical models and numerical methods
76(20)
3.2.1 Governing equations
78(1)
3.2.2 Interphase momentum exchange
78(2)
3.2.3 RANS method
80(6)
3.2.4 LES model
86(2)
3.2.5 Impeller treatment
88(4)
3.2.6 Numerical details
92(4)
3.3 Two-phase flow in stirred tanks
96(33)
3.3.1 Solid-liquid systems
96(10)
3.3.2 Gas-liquid systems
106(15)
3.3.3 Liquid-liquid systems
121(8)
3.4 Three-phase flow in stirred tanks
129(9)
3.4.1 Liquid-liquid-solid systems
129(4)
3.4.2 Gas-liquid-liquid systems
133(1)
3.4.3 Liquid-liquid-liquid systems
134(1)
3.4.4 Gas-liquid-solid systems
135(3)
3.5 Summary and perspective
138(15)
3.5.1 Summary
138(3)
3.5.2 Perspective
141(1)
Nomenclature
142(3)
References
145(8)
Chapter 4 Airlift loop reactors
153(78)
4.1 Introduction
153(1)
4.2 Flow regime identification
154(3)
4.3 Mathematical models and numerical methods
157(37)
4.3.1 Eulerian-Eulerian two-fluid model
158(1)
4.3.2 Closure of interfacial forces
159(22)
4.3.3 Closure of turbulence models
181(2)
4.3.4 Numerical methods
183(11)
4.4 Hydrodynamics and transport in airlift loop reactors
194(8)
4.4.1 Hydrodynamic behavior
194(2)
4.4.2 Interphase transport phenomena
196(6)
4.5 Macromixing and micromixing
202(12)
4.5.1 Macromixing in airlift loop reactors
203(8)
4.5.2 Micromixing in airlift loop reactors
211(3)
4.6 Guidelines for design and scale-up of airlift loop reactors
214(3)
4.7 Summary and perspective
217(14)
Nomenclature
218(2)
References
220(11)
Chapter 5 Preliminary investigation of two-phase microreactors
231(32)
5.1 Introduction
231(1)
5.2 Mathematical models and numerical methods
232(4)
5.3 Simulation using lattice Boltzmann method
236(10)
5.3.1 Numerical simulation of two-phase flow in microchannels
236(4)
5.3.2 Numerical study of heat transfer in microchannels
240(1)
5.3.3 Numerical simulation of mass transfer in microchannels
241(5)
5.4 Experimental
246(5)
5.4.1 Flow pattern
246(3)
5.4.2 Pressure drop
249(1)
5.4.3 Mass transfer performance
250(1)
5.4.4 Micromixing
251(1)
5.5 Summary and perspective
251(12)
Nomenclature
253(1)
References
254(9)
Chapter 6 Crystallizers: CFD-PBE modeling
263(32)
6.1 Introduction
263(1)
6.2 Mathematical models and numerical methods
264(8)
6.2.1 General population balance equation
264(2)
6.2.2 Standard method of moments
266(2)
6.2.3 Quadrature method of moments
268(1)
6.2.4 Multi-class method or discretized method
269(3)
6.3 Crystallizer modeling procedures
272(9)
6.3.1 Species transport equations
273(1)
6.3.2 Nucleation and growth kinetics
273(1)
6.3.3 Aggregation and breakage kernels
274(2)
6.3.4 Computational details
276(1)
6.3.5 Simulated results of precipitation processes
277(4)
6.4 Macromixing and micromixing
281(5)
6.5 Summary and perspective
286(9)
Nomenclature
288(1)
References
289(6)
Index 295
Institute of Process Engineering, Chinese Academy of Sciences Institute of Process Engineering, Chinese Academy of Sciences
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