Improvements in the Design of the Cyclohexane Production Process implementing Mass Exchange with a Counter Current Gas Permeation Membrane

FISCHER, CARLOS D.; IRIBARREN, OSCAR A.

INDUSTRIAL & ENGINEERING CHEMICAL RESEARCH

AMER CHEMICAL SOC

Lugar: Washington; Año: 2013 vol. 52 p. 1698 - 1704

0888-5885

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, 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.