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Download e-book for iPad: Chemical reactor design, optimization, and scaleup by E. Bruce Nauman

By E. Bruce Nauman

ISBN-10: 0071377530

ISBN-13: 9780071377539

This is often the trendy advisor to chemical reactors. within the most sensible expert sourcebook on chemical reactors ever written, world-class specialist Bruce Nauman offers instruments, info, and hands-on services to make very important engineering projects and judgements more uncomplicated. essentially and extensive, "Chemical Reactor layout, Optimization, and Scaleup" presents: up to date details to assist chemical and technique engineers keep time, funds, and fabrics; decision-aiding assurance of each point of choice, layout components and parameters, optimization, and scaleup; a handy resource of defined formulation, ideas, and knowledge; a variety of particular examples; labored mathematical suggestions; the newest details on reactor layout for biochemicals and polymers, in addition to different more recent and traditional elements. This publication is helping to layout and specify chemical reactors optimistically, with cutting-edge talents.

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4 Conversion versus dimensionless time, a0kt, for an autocatalytic batch reaction. com) Copyright © 2004 The McGraw-Hill Companies. All rights reserved. Any use is subject to the Terms of Use as given at the website. MULTIPLE REACTIONS IN BATCH REACTORS 56 CHEMICAL REACTOR DESIGN, OPTIMIZATION, AND SCALEUP same, high concentrations everywhere within the working volume of the reactor. In contrast, B may be quite low in concentration at early times in a batch reactor and only achieves its highest concentrations at the end of the reaction.

28) is growing. Eventually, however, this term must decrease as component A is depleted, even though the concentration of B continues to increase. The inflection point is caused by depletion of component A. 4 Conversion versus dimensionless time, a0kt, for an autocatalytic batch reaction. com) Copyright © 2004 The McGraw-Hill Companies. All rights reserved. Any use is subject to the Terms of Use as given at the website. MULTIPLE REACTIONS IN BATCH REACTORS 56 CHEMICAL REACTOR DESIGN, OPTIMIZATION, AND SCALEUP same, high concentrations everywhere within the working volume of the reactor.

C) Suggest means for increasing the productivity; that is, reducing the batch reaction time or the volume of the CSTR. 13. Ethyl acetate can be formed from dilute solutions of ethanol and acetic acid according to the reversible reaction C2 H5 OH þ CH3 COOH ! C2 H5 OOCCH3 þ H2 O Ethyl acetate is somewhat easier to separate from water than either ethanol or acetic acid. For example, the relatively large acetate molecule has much lower permeability through a membrane ultrafilter. Thus, esterification is sometimes proposed as an economical approach for recovering dilute fermentation products.

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Chemical reactor design, optimization, and scaleup by E. Bruce Nauman


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