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Originally Posted by PIGSTi
Can I see some graphs to verify this claim John...........
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I've got hundreds of journal articles at home on heat exchanger processes, if you wanna read them feel free. I am looking purely at the efficiency of the exchanger. Bar and plate is good but never as efficient as a tube and fin. T&F also costs a shite load more to produce which is why you see a lot more B&P types.
P.S. If you read them, feel like writing me up a literature review?
