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Consider the liquid - phase reaction ( 2 A + 3 BP + s with rate law ( - P _ A = 0
Consider the liquidphase reaction ABPs with rate law PACACB V Find the reactor volume needed if the desired production rate of Pis molmin CAM VCBOM V and the desired conversion of reactant Ais a Batch reactor volume if shut down time is hour; b CSTR volume c plug flow reactor volume
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