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3 . 2 6 Consider the reaction A + B r = 0 . 1 5 ( mint ) CA in a CSTR . A
Consider the reaction A B r mint CA in a CSTR A costs $mole and B sells for $mole The cost of the operating the reactor is $ per liter hour. We need to produce moles of Bhour using CA molesliter Assume no value or cost of disposal of unreacted a What is the optimum conversion and reactor size? What is the cash flow from the process? c What is the cash flow ignoring operating cost? d At what operating cost do we break even?
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