Chemical Reactor Analysis and DesignWiley Global Education, 2011 M08 24 - 912 páginas This is the Third Edition of the standard text on chemical reaction engineering, beginning with basic definitions and fundamental principles and continuing all the way to practical applications, emphasizing real-world aspects of industrial practice. The text includes updated coverage of computer modeling methods and many new worked examples. Most of the examples use real kinetic data from processes of industrial importance. |
Contenido
| 1 | |
Kinetics of Heterogeneous Catalytic Reactions | 60 |
Transport Processes with Reactions Catalyzed by Solids | 152 |
Noncatalytic GasSolid Reactions | 240 |
Catalyst Deactivation | 269 |
GasLiquid Reactions | 322 |
The Modeling of Chemical Reactors | 366 |
The Batch and Semibatch Reactors | 383 |
The Perfectly Mixed Flow Reactor | 453 |
Fixed Bed Catalytic Reactors | 491 |
Complex Flow Patterns | 638 |
Fluidized Bed and Transport Reactors | 718 |
Multiphase Flow Reactors | 778 |
Author Index | 848 |
Subject Index | 854 |
The Plug Flow Reactor | 427 |
Otras ediciones - Ver todas
Chemical Reactor Analysis and Design Gilbert F. Froment,Kenneth B. Bischoff,Juray De Wilde Sin vista previa disponible - 2010 |
Términos y frases comunes
adiabatic adsorption AIChE axial bed reactors Bischoff boundary conditions bubble calculated catalyst catalyst particle catalytic cracking catalytic reforming Chapter Chem chemical reaction coefficient coke coke content complete mixing component concentration considered constant continuity equation conversion correlation curve deactivation function defined dehydrogenation derived determined diameter diffusion limitations effective diffusivity effectiveness factor energy equilibrium example experimental feed Figure film first first-order flow rate flow reactor fluid elements flux fraction Froment gas phase given gradients heat exchanger heat transfer hydrocracking hydrogen inlet integration interfacial isothermal kinetic liquid phase mass transfer micro-mixing molecular obtained operation optimal packed bed parameters partial pressure plug flow pore profile profiles rate coefficient rate equations rate-determining step reactant reacting reaction rate Section shown in Fig simulation solid species specific steam reforming sufficient surface temperature transfer coefficient transport tube turbulent velocity volume