The feed (equimolar A and B) to a reactor is heated from (100^{circ} mathrm{F}) to (500^{circ} mathrm{F})

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The feed (equimolar A and B) to a reactor is heated from \(100^{\circ} \mathrm{F}\) to \(500^{\circ} \mathrm{F}\) in a \(1-2\) parallel-counterflow heat exchanger with a mean overall heat-transfer coefficient of \(75 \mathrm{Btu} / \mathrm{hr}-\mathrm{ft}^{2{ }^{\circ} \mathrm{F}}\). It is converted to \(\mathrm{C}\) by the exothermic reaction \(\mathrm{A}+\mathrm{B} \rightarrow \mathrm{C}\) in an adiabatic plug-flow tubular reactor (Figure 7.35). For a process simulator, prepare a simulation flowsheet and show the calculation sequence to determine:

(a) Flow rates and unknown temperatures for each stream.

(b) Heat duty and area of the countercurrent shell-and-tube heat exchanger.

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Product And Process Design Principles Synthesis Analysis And Evaluation

ISBN: 9781119355243

4th Edition

Authors: Warren D. Seider, Daniel R. Lewin, J. D. Seader, Soemantri Widagdo, Rafiqul Gani, Ka Ming Ng

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