Heat Exchanger Design

by UAChE
Tags: design, exchanger, heat
UAChE is offline
Apr3-09, 10:23 AM
P: 1
I have 1,935,420 lbs/hr of process fluid entering all liquid at 168F. 38,000 lbs/hr boils, and the mixture exits at 190F. Total duty is 45,500,000 BTU/hr. Is there a way to calculate the liquid specific heat and the vapor specific heat with this information?
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russ_watters is offline
Apr5-09, 07:28 PM
P: 22,001
Sorry, no. You need more temperature measurements becuase there is no set ratio of specific heats.

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