If the compression is done reversibly compute the heat and

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Ammonia is to be isothermally compressed in a specially designed flow turbine from 1 atm and 672 R to 50 atm. If the compression is done reversibly, compute the heat and work flows needed per lb-mole of ammonia by the following methods;

A. Assuming ideal gas behavior

B. From the generalized compressibility factor and residual property charts.

Reference no: EM13632548

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