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Titlebook: Conventional Three-Phase Fixed-Bed Technologies; Analysis and Critiqu Leonid B. Datsevich Book 2012 The Editor(s) (if applicable) and The A

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书目名称Conventional Three-Phase Fixed-Bed Technologies
副标题Analysis and Critiqu
编辑Leonid B. Datsevich
视频video
概述Reviews the Two-Zone Model.Alerts plant designers and others to the lack of potential for process enhancement in the framework of the traditional technological paradigms.Presents oscillation Theory.Fo
丛书名称SpringerBriefs in Applied Sciences and Technology
图书封面Titlebook: Conventional Three-Phase Fixed-Bed Technologies; Analysis and Critiqu Leonid B. Datsevich Book 2012 The Editor(s) (if applicable) and The A
描述This book analyzes conventional fixed-bed reactors such as trickle-bed, bubble (packed) column, and multitubular reactors with regard to process efficiency, design and safety. It is shown that these reactors do not possess any substantial potential for improving industrial processes. Modern concepts in mass transfer, kinetics and process design are applied to process development. In light of the given analysis, new approaches to the development of technologies based on innovative principles are elucidated. For the first time, first-hand knowledge about Two-Zone Model, Oscillation Theory, map of the energy dissipation is presented in full.
出版日期Book 2012
关键词Bubble (packed) Column Reactors; Exothermic Reactions; Fischer-Tropsch Synthesis; Hydrogenation; Hydrotr
版次1
doihttps://doi.org/10.1007/978-1-4614-4836-5
isbn_softcover978-1-4614-4835-8
isbn_ebook978-1-4614-4836-5Series ISSN 2191-530X Series E-ISSN 2191-5318
issn_series 2191-530X
copyrightThe Editor(s) (if applicable) and The Author(s), under exclusive license to Springer Science+Busines
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Variant Map System of Random Sequences into the particularities inherent in a specific process, let us point out three main problems that should be solved in all multiphase reactions mentioned in Table 1.1 regardless of their chemical nature.
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Elementary Equations of Variant Measurement generations of process developers. On the one hand, it is interesting to retrace why the original ideas have established such a rigid paradigm that is widely shared by the industrial and scientific communities and, by force of habit, remains without any critical view till date. On the other hand, i
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https://doi.org/10.1007/978-981-13-2282-2lation of a reacting gas is arranged. Since the typical gas velocity in the channels formed by the catalyst particles is relatively high, the flow of liquid should be directed concurrently with the gas phase either downwards or upwards. The reactors, where the first flow pattern is realized, are ref
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https://doi.org/10.1007/978-981-13-3717-8ys the prize should be awarded to the catalyst developers. Catalysts created by chemists, as a rule, can demonstrate a great ability to do their “chemical” work, if only the process arrangements do not pose impervious limitations toward the desired catalyst performance.
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