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Titlebook: Chemical Reactor Design and Technology; Overview of the New Hugo I. Lasa Book 1986 Martinus Nijhoff Publishers, Dordrecht 1986 dynamics.en

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樓主: ODE
41#
發(fā)表于 2025-3-28 17:00:01 | 只看該作者
42#
發(fā)表于 2025-3-28 21:08:45 | 只看該作者
Product lifecycle management systems,the liquid, a reactive solid or catalyst may be fluidized. BCR can be single staged or multi staged, batch or continuous with regard to the liquid (or slurry) phase. Continuous BCR can be operated cocurrently or countercurrently.
43#
發(fā)表于 2025-3-29 00:35:27 | 只看該作者
,e-Business — electronic business and PLM,from catalytic hydrogenation of edible oils, coal hydrogenation, Fischer- Tropsch reactions to biological reactors (e.g. single cell proteins) and polymerization reactors. Doraiswamy and Sharma [1] identified over 50 different processes in which slurry reactors have been used and more applications a
44#
發(fā)表于 2025-3-29 03:54:16 | 只看該作者
https://doi.org/10.1007/b138258thermodynamics,...) and by the contacting pattern. The importance of this contacting pattern is quite obvious in the case of multiphase reactors like trickle-bed reactors. Reactants are indeed present in both fluid phases and reactions occur at the contact of the catalytic solid phase. Unfortunately
45#
發(fā)表于 2025-3-29 07:51:49 | 只看該作者
,e-Business — electronic business and PLM,umn with a fixed bed of catalyst particles through which liquid flows in the form of films, droplets and rivulets. Gas moves cocurrently; sometimes counter-current flows are also used. Usually one reactant is introduced in the liquid phase and the other in the gas phase.
46#
發(fā)表于 2025-3-29 13:36:29 | 只看該作者
47#
發(fā)表于 2025-3-29 18:24:29 | 只看該作者
48#
發(fā)表于 2025-3-29 21:44:20 | 只看該作者
49#
發(fā)表于 2025-3-30 01:15:09 | 只看該作者
https://doi.org/10.1007/978-94-009-4400-8dynamics; energy consumption; engine; flow; fluidized bed; heat transfer; hydrodynamics; measurement; methan
50#
發(fā)表于 2025-3-30 07:53:00 | 只看該作者
978-94-010-8457-4Martinus Nijhoff Publishers, Dordrecht 1986
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