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Titlebook: Chemical Reactor Development; from Laboratory Synt Dirk Thoenes Book 1994 Springer Science+Business Media B.V. 1994 catalysis.chemical engi

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41#
發(fā)表于 2025-3-28 17:49:41 | 只看該作者
PLM-Voraussetzungen im Unternehmen,een these reactor types is mostly based on the relative requirements for mass transfer, degree of conversion and heat transfer. Heterogeneous catalysis is a well developed science, with its own specific literature. In this chapter some technical acpects will be presented, particularly those related to scale-up.
42#
發(fā)表于 2025-3-28 21:35:57 | 只看該作者
43#
發(fā)表于 2025-3-29 01:56:49 | 只看該作者
Integral Isothermal Reactor Modelsr axial mixing are used..Mass balances including volume element models and macro-flow effects have to be integrated to arrive at integral reactor models..For reactors with two process streams, mass balances have to be made for each stream, and these have to be integrated. The results are different f
44#
發(fā)表于 2025-3-29 06:19:52 | 只看該作者
45#
發(fā)表于 2025-3-29 08:09:03 | 只看該作者
46#
發(fā)表于 2025-3-29 13:40:29 | 只看該作者
er between two phases, andthe formation of another phase, such as in precipitations. Thesescale-dependent effects are not only important in view of theconversion of chemical reactions, but also with regard to theselectivity, and in the case of solid products, to their morphology.In Part III, some applications978-90-481-4446-4978-94-015-8382-4
47#
發(fā)表于 2025-3-29 18:12:41 | 只看該作者
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48#
發(fā)表于 2025-3-29 21:57:38 | 只看該作者
49#
發(fā)表于 2025-3-30 01:15:25 | 只看該作者
50#
發(fā)表于 2025-3-30 06:25:56 | 只看該作者
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