多相化学反应工程与工艺

PrefaceList of Common Symbols 1 Gas-Solid Cocurrent Down-Flow Fluidized Beds (Downers) 1.1 Hydrodynamics of downers 1.2 Mixing and dispersion in downers 1.3 Riser-downer coupled reactors 1.4 Catalytic cracking in downers 1.5 Modelling and simulation of downers 2 Gas-Solid Cocurrent Up-Flow Fluidized Beds (Risers) 2.1 Hydrodynamics and inlet and outlet structures in risers 2.2 High density circulating fluidized beds 2.3 Mixing in risers 2.4 Heat transfer in fast fluidized beds 2.5 Modeling and simulation of risers 3 Conventional Fluidization

PrefaceList of Common Symbols 1 Gas-Solid Cocurrent Down-Flow Fluidized Beds (Downers) 1.1 Hydrodynamics of downers 1.2 Mixing and dispersion in downers 1.3 Riser-downer coupled reactors 1.4 Catalytic cracking in downers 1.5 Modelling and simulation of downers 2 Gas-Solid Cocurrent Up-Flow Fluidized Beds (Risers) 2.1 Hydrodynamics and inlet and outlet structures in risers 2.2 High density circulating fluidized beds 2.3 Mixing in risers 2.4 Heat transfer in fast fluidized beds 2.5 Modeling and simulation of risers 3 Conventional Fluidization 3.1 Bubbling fluidized beds 3.2 Turbulent fluidized beds4 Liquid-Solid, Gas-Liquid and Gas-Liquid-Solid Multi-Phase Reactors 4.1 Fundamental studies 4.2 Liquid-solid circulating fluidized beds 4.3 Gas-liquid-solid circulating fluidized beds 4.4 Gas-liquid-solid packed columns with novel internals 4.5 Gas-liquid and gas-liquid-solid loop reactors 5 Moving Bed Reactors 5.1 Gas-solid moving beds 5.2 Liquid-solid moving beds 5.3 Standpipe technology 6 Particle and Powder Technology 6.1 Unique properties of 30 particles as the catalyst of fluidized-bed reactors 6.2 Resonance characteristics of a vibrated fluidized bed with a high bed hold-up 6.3 Studies on gas-solid-solid circulating fluidized-bed reactors 6.4 A novel granulation technology for producing spherical wax particles 6.5 Fluidization and agglomerate structure of SiO2 nanoparticles 6.6 Catalysts effect on morphology of carbon nanotubes prepared by catalytic chemical vapor deposition in a nano-agglomerate bed 6.7 Production of carbon nanotubes in a packed bed and a fluidized bed 6.8 Production of hydrogen and carbon nanotubes from methane decomposition in a two-stage fluidized bed reactor 6.9 Agglomerated CNTs synthesized in a fluidized bed reactor: agglomerate structure and formation mechanism 7 Green Chemical Reaction Engineering and Technology 7.1 Synthesis of linear alkylbenzene catalyzed by -zeolite 7.2 Synthesis of linear alkylbenzene in a liquid-solid circulating fluidized bed reactor 7.3 Catalytic decomposition process of cumene hydroperoxide using sulfonic resins as catalyst 7.4 Study on synergy effect in dimethyl ether synthesis from syngas 7.5 The synergy effect of process coupling for dimethyl ether synthesis in slurry reactors 7.6 Alkylation of benzene with dodecene over HY zeolite:deactivation,regeneration, and product distribution 8 The Recycle Economy and Ecological Industry Postscript

本书是清华大学化工系反应工程方面的集成之作。本书内容包括：流态化科学与工程方面的研究进展，与多相反应工程和工艺相关的粉体、造粒、绿色化工和生态工业等前沿领域的新内容和新进展，以及能源与环境等涉及可持续发展的战略问题，这对开发清洁能源技术，发展绿色化工和生态工业具有重要的意义。本书还涉及多相反应工程的先进的研究和数据处理方法。 本书可供化工、材料、能源等领域的科研工作者和高校相应专业的师生参考。作者简介： Yong JIN ，Professor，Department of Chemical Engineering，Tsinghua University；Member of CAE（Chinese Academy of Engineering）。 JIN was born in Beijing in 1935。He got his bachelor degree of chemical engineering in Ural Polytechnic College（Russia）in 1959 and stuied graduate courses of chemical engineering in Tianjin University from 1959 to 1960。He became an assistant professor of University of Science and Technology of China in 1960。Since 1973，he had been working in Tsinghua University。As a visiting scholar，he engaged in chemical reaction engineering in Pittsburgh University of USA in 1985。His speciality is fluidization reaction engineering，coupling technology in chemical process，environmental friendly chemical process，particle coating and surface modification，cycle economy and ecological process engineering。