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Titlebook: Electrochemical Process Engineering; A Guide to the Desig F. Goodridge,K. Scott Book 1995 Springer Science+Business Media New York 1995 Ion

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发表于 2025-3-21 19:44:56 | 显示全部楼层 |阅读模式
书目名称Electrochemical Process Engineering
副标题A Guide to the Desig
编辑F. Goodridge,K. Scott
视频video
图书封面Titlebook: Electrochemical Process Engineering; A Guide to the Desig F. Goodridge,K. Scott Book 1995 Springer Science+Business Media New York 1995 Ion
描述As the subtitle indicates, the overriding intention of the authors has been to provide a practical guide to the design of electrolytic plant. We wanted to show that the procedures for the design and optimization of such a plant are essentially simple and can be performed by readers comparatively new to the electrochemical field. It was important to realize that electrochemical engineering should not be confused with applied electrochemistry but had to be based on the principles of chemical engineering. For this reason, reference is often made to standard chemical engineering texts. Since this is a practical guide rather than a textbook, we have included a large number of worked examples on the principle that a good worked example is worth many paragraphs of text. In some examples we have quoted costs, e.g., of chemicals, plant or services. These costs are merely illustrative; current values will have to be obtained from manufacturers or journals. If this is not possible, approximate methods are available for updating costs to present-day values (see Refs. 1 and 3, Chapter 6).
出版日期Book 1995
关键词Ion; chemical engineering; chemical process engineering; electrochemical engineering; heat transfer; opti
版次1
doihttps://doi.org/10.1007/978-1-4899-0224-5
isbn_softcover978-1-4899-0226-9
isbn_ebook978-1-4899-0224-5
copyrightSpringer Science+Business Media New York 1995
The information of publication is updating

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sessed, usually in terms of .,the discounted cash flow rate of return (DCFRR), which is related to payback time. The company decides whether . is acceptable or if another process must be looked at. Unfortunately, an optimized plant design does not guarantee profitability.
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. We wanted to show that the procedures for the design and optimization of such a plant are essentially simple and can be performed by readers comparatively new to the electrochemical field. It was important to realize that electrochemical engineering should not be confused with applied electrochemi
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Rate Processes and Reaction Models,t variables. This requires, ideally, knowledge of the individual reaction steps, the rate at which they occur, and the mass transport rates for the species in the reaction. But often, detailed quantitative kinetic data are not available and not easy to determine Semiempirical relations may have to be used.
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Reactor Models,er of phases involved and the energy requirements. The size depends on the rate of reaction: we shall see that a reactor model can provide important answers about this rate. The reaction rate of an electrolytic reactor is defined by the possible current density, expressed in terms of reaction models in Chapter 3.
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Versioning Resource Files in .NET,c electrosynthesis. As indicated in Section 1.2, we do not intend to describe electrochemical processes in detail, since there are many books on electrochemical technology.’ We will discuss the design of individual reactors, with emphasis on modularized, general purpose flow electrolyzers. We will classify reactors by their mode of operation.
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Electrolytic Reactor Design, Selection, and Scale-up,c electrosynthesis. As indicated in Section 1.2, we do not intend to describe electrochemical processes in detail, since there are many books on electrochemical technology.’ We will discuss the design of individual reactors, with emphasis on modularized, general purpose flow electrolyzers. We will classify reactors by their mode of operation.
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