Question: Consider a heat exchanger that operates with the objective of modifying an equimolar stream (steam) of methyl ethyl ketone(1)-toluene(2) from 50 C and 25 kPa

Consider a heat exchanger that operates with the objective of modifying an equimolar stream (steam) of methyl ethyl ketone(1)-toluene(2) from 50 C and 25 kPa to 100 C and 20 kPa. What is the heat load? Consider ideal gases
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