Improvements in the Design of the Cyclohexane Production Process Implementing Mass Exchange with a Counter Current Gas Permeation Membrane
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https://figshare.com/articles/dataset/Improvements_in_the_Design_of_the_Cyclohexane_Production_Process_Implementing_Mass_Exchange_with_a_Counter_Current_Gas_Permeation_Membrane/2448571
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In this paper, we propose changes in the design of a cyclohexane production process, following a mass exchange design heuristic developed in a previous work (Ind. Eng. Chem. Res. 2011, 50 (11), 6849–6859). In the study case considered, an optimal design was obtained which exhibits a significant 40.08% reduction in the power of the compressor that recycles unreacted reagents, and a respectable 3.59% reduction of the hydrogen consumption, resulting in an increase of the plant Net Annual Income of a 1.31%. These results highlight the importance of considering a mass exchange between the input and output streams from the reactor, at the time of synthesizing a new process.
创建时间：
2016-02-20
