Increase the utility feed temperature by (50^{circ} mathrm{C}). Retain the IPA conversion at 0. 9 . a.

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Increase the utility feed temperature by \(50^{\circ} \mathrm{C}\). Retain the IPA conversion at 0. 9 .

a. Determine the process feed rate.

b. Determine the percent change in acetone production.

Problems 23. 21-23.26 investigate the performance of the acetone reactor system. The reaction kinetics are presented in Section 23. 5.3. The reactor and internal heat exchanger are fixed. For the base case, the active volume of the reactor is \(5.1 \mathrm{~m}^{3}\) at the operating conditions given in Figure 23. 10. Unless otherwise stated, the heat transfer coefficient and reactor pressure drop are to be assumed constant. The feed temperature, pressure, and component concentrations remain constant. For these calculations, assume the utility fluid to be n-heptadecane (at pressures more than \(30 \mathrm{bar}\) ). At the base case, the utility flow is \(58 \mathrm{kmol} / \mathrm{h}\).

Figure 23.10

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Data from section 23.5.3

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Analysis Synthesis And Design Of Chemical Processes

ISBN: 9780132618120

4th Edition

Authors: Richard Turton, Richard C. Bailie, Wallace B. Whiting, Joseph A. Shaeiwitz, Debangsu Bhattacharyya

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