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

By E. Bruce Nauman

ISBN-10: 0071377530

ISBN-13: 9780071377539

This is often the fashionable advisor to chemical reactors. within the most sensible expert sourcebook on chemical reactors ever written, world-class professional Bruce Nauman offers instruments, info, and hands-on services to make very important engineering projects and judgements more uncomplicated. sincerely and intensive, "Chemical Reactor layout, Optimization, and Scaleup" presents: updated info to assist chemical and technique engineers store time, funds, and fabrics; decision-aiding insurance of each element of choice, layout elements and parameters, optimization, and scaleup; a handy resource of defined formulation, ideas, and knowledge; various particular examples; labored mathematical recommendations; the most recent details on reactor layout for biochemicals and polymers, in addition to different more recent and conventional components. This publication is helping to layout and specify chemical reactors optimistically, with state of the art abilities.

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This is sometimes observed. Solid rocket propellants or fuses used to detonate explosives can burn at an essentially constant rate (a zero-order reaction) until all reactants are consumed. These are multiphase reactions limited by heat transfer and are discussed in Chapter 11. For single phase systems, a zero-order reaction can be expected to slow and become first or second order in the limit of low concentration. com) Copyright © 2004 The McGraw-Hill Companies. All rights reserved. Any use is subject to the Terms of Use as given at the website.

6 Relative performance of piston flow and continuous-flow stirred tank reactors for first-order reactions. 7 Relative performance of piston flow and continuous-flow stirred tank reactors for second-order reactions. com) Copyright © 2004 The McGraw-Hill Companies. All rights reserved. Any use is subject to the Terms of Use as given at the website. 8 Comparison of reactor volume required for a given conversion for a first-order reaction in a PFR and a CSTR. 1. 2. (a) Write the overall and component mass balances for an unsteady, perfectly mixed, continuous flow reactor.

D) Repeat (c) for the case where the key component is consumed by a first-order reaction with rate constant k. The homogeneous gas-phase reaction NO þ NO2 Cl ! 3. 4. is believed to be elementary with rate R ¼ k½NOŠ½NO2 ClŠ: Use the kinetic theory of gases to estimate fR at 300 K. 5  10À10 m. The experimentally observed rate constant at 300 K is k ¼ 8 m3/(molEs). 2 are in moles of the given component per mole of mixed feed. These are obviously calculated values. Check their consistency by using them to calculate the feed composition given that the feed contained only para-xylene and chlorine.

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


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