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

作者: thyroidectomy    時間: 2025-3-21 19:23
書目名稱Chemical Reactor Development影響因子(影響力)




書目名稱Chemical Reactor Development影響因子(影響力)學科排名




書目名稱Chemical Reactor Development網(wǎng)絡公開度




書目名稱Chemical Reactor Development網(wǎng)絡公開度學科排名




書目名稱Chemical Reactor Development被引頻次




書目名稱Chemical Reactor Development被引頻次學科排名




書目名稱Chemical Reactor Development年度引用




書目名稱Chemical Reactor Development年度引用學科排名




書目名稱Chemical Reactor Development讀者反饋




書目名稱Chemical Reactor Development讀者反饋學科排名





作者: 是限制    時間: 2025-3-22 00:08

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作者: 終止    時間: 2025-3-23 06:18
Reactors for Organic Chemical Synthesesaction rates and high selectivities are of primary importance. In this chapter a number of cases will be presented that are typical for various types of organic syntheses. In order to illustrate which factors are important and which are not, some numerical examples are given. Examples of single phas
作者: 核心    時間: 2025-3-23 11:38
Reactors for Conversion or Formation of Inorganic Solids In these processes solids are either converted or formed, or both. When converting solid reactants, the change of the solid structure is related to the reaction rate. In forming solid products, nucleation and agglomeration may play important parts. No attempt is made to cover any of these areas. Se
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作者: GENRE    時間: 2025-3-23 19:06
Polymerization Reactorslar reactant concentrations. Intrinsic reaction rates are generally high and there are usually transport limitations. The presence of the produced polymer generally influences the physical properties of the mixture considerably, and heat of reaction has to be removed under unfavourable conditions. I
作者: accomplishment    時間: 2025-3-23 23:01
Chemical Reactors, Product Quality and the Environmentss rates. These rates are not only important in relation to the dimensions of the equipment, but they also determine the selectivity of the chemical process. Aiming for higher selectivities is desirable for three reasons: to minimize raw materials’ consumption, to improve product quality and to redu
作者: Paraplegia    時間: 2025-3-24 05:39
Book 1994rom the laboratory bench scale, where thefirst successful experiments are performed, to the design desk, wherethe first commercial reactor is conceived. It is also written forthose chemists and chemical engineers who are concerned with thefurther development of a chemical process with the objective
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作者: 紋章    時間: 2025-3-24 14:04
The Path of Chemical Reactor Developmentvels. For describing the various combined effects we need mathematical models. A model that describes the entire process can be used for analysis of experimental results, as well as for the design of a larger reactor.
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作者: Bronchial-Tubes    時間: 2025-3-24 19:43
Reactors for Organic Chemical Synthesese reactions include relatively slow reactions in semi-batch reactors; continuous reactors for incomplete conversions; and very rapid reactions in stirred reactors (either continuous or semi-batchwise). Examples for two-phase reactions include slow and rapid gas/liquid reactions, liquid/liquid and solid/liquid reactions.
作者: mortgage    時間: 2025-3-25 02:56
Reactors for Conversion or Formation of Inorganic Solidsveral examples will be presented, with the purpose of showing the reader how these and similar problems may be dealt with. Though there are as yet no design procedures with a general validity for these types of processes, a semi-quantitative insight in the relevant phenomena may be a helpful guideline for experimental work.
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作者: 漫不經(jīng)心    時間: 2025-3-25 10:35
Polymerization Reactorsn addition, the requirements for product quality are usually very high. Though it is common practice to develop reactors for these processes in a purely empirical way, it is nevertheless possible to apply reactor engineering principles here with some success, even if only qualitative predictions can be made.
作者: Canary    時間: 2025-3-25 15:41
Business benefits of a PLM system,ulting reactor models can be used for approximating real reactors, in which transport phenomena are not rate determining. Therefore these reactor models are applicable irrespective of the scale of operation.
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作者: analogous    時間: 2025-3-26 08:45
The Physical Contacting of Reactants-phase system may also be used for separating reaction products in the reactor. Mass transfer in solid/gas, solid/liquid and liquid/gas dispersion processes are reviewed, and a brief survey is given of three phase-contacting. All these physical processes are considered without the occurrence of chemical reactions.
作者: 維持    時間: 2025-3-26 14:31
The Formation of Another Phase in the Reactorture of the formed solid particles. These phenomena are determined by the conditions in the reactor, including the hydrodynamical regime. Therefore, reactor conditions during precipitation processes generally determine the quality of solid products. This may have important consequences for reactor design.
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Enthalpy Management and Temperature Controlrature control of reactors are discussed: the well mixed isothermal reactor, the tubular reactor with a controlled temperature gradient, and the semi-batch reactor with a certain temperature profile in time.
作者: Expertise    時間: 2025-3-26 23:39
Product Lifecycle Management beherrschented for mixing combined with chemical reaction, and for mass transfer combined with chemical reaction..The influence of mass transport on the selectivity of a chemical process is also discussed. For some specific cases the local transport of heat will be considered.
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作者: cathartic    時間: 2025-3-27 05:57
The Interaction of Chemical Reactions and Physical Transport Phenomenated for mixing combined with chemical reaction, and for mass transfer combined with chemical reaction..The influence of mass transport on the selectivity of a chemical process is also discussed. For some specific cases the local transport of heat will be considered.
作者: DRILL    時間: 2025-3-27 13:32
Chemical Reactors, Product Quality and the Environmentach is also valuable. This is not always reconcilable with quantitative economic calculations. It is necessary to consider the quality of chemical operations in general, and of chemical reactors in particular. This is also a part of chemical reactor developement.
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Antti Saaksvuori,Anselmi Immonenhenomena is needed for the design of a chemical reactor. Also, the chemical reactor has to be considered as part of an industrial plant. This chapter gives a qualitative overview of the topics that are treated in the following chapters.
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作者: 消散    時間: 2025-3-28 05:12
Product Lifecycle Management beherrschenes presented in the preceeding sections. For the selection of a reactor type that is the most suitable for the given process, a sound combination of calculations and intuition is recommended. In particular situations, a novel reactor type might be conceived. However, an iterative procedure is often unavoidable.
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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.
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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
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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
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