Steam is mmpressed from $10$ ber and $673K$ to an exit temperature of $373k.$ If the isentrupic

efficiertey is $75\%,$ salculate the power requirements to compress $25,000k\frac{g}{h}.$ Estimate the exit

glas. presqure.

A $3000kW$ compressor ts tuset ta compress steam to the exit temperature anct pressure of $973K$

and $10$ bar respectively, Calculate the initial temperature and pressure of the steam, If its

Flowrate is$.15$ th $0k\frac{g}{h}$ and the iseftraple $$ffictency of the compressor is $80\%$