The liquid product stream (S-7) consisted of 58.91kg/hr IPA with a mass fraction of 96%. The pump work obtained was 500kJ/hr. The flash separator was modeled to have a zero heat duty and the cooler released 68430kJ/hr of energy. The acetone TCH simulation process resulted in a production of 58.91kg/hr of IPA with 97wt%, equivalent to 0.83kg/hr of H2 stored.