Anatural gas stream (essentially pure methane) is available at 310 k and 14 bar. the gas is to be com- pressed to 345 bar before transmission by underground pipeline. if the compression is carried out adiabati- cally and reversibly, determine the compressor outlet temperature and the work of compression per mole of methane. you may assume that methane obeys the peng-robinson equation of state. see appendix a. ii for heat capacity data.

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