Question: Example: CSTR design for EG production It is desired to produce 216 million pounds per year of EG. The reactor is to be operated isothermally.

Example: CSTR design for EG production It is desired to produce 216 million pounds per year of EG. The reactor is to be operated isothermally. A 1 lbmol/As solution of Eo in water is fed to the reactor together with equal volumetric solution of water. C2H40+ H20 (CH2OH)2 A + B C -PA = keca le = 0.311 min 1 case 1: Single CSTR targeting 80% conversion of EO What is volume of the reactor? =
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