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chemical engineering process equipment and plant design
1. High pressure fluid in a shell and tube heat exchanger should preferably be routed through the
(A): shell side for large overall heat transfer co-efficient.
(B): shell side for smaller total pressure drop.
(C): shell side, if the flow is counter-current and tube side if the flow is co-current.
(D): tubes to avoid the expansion of high pressure shell construction.
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