PROBLEM $4$

Steam enters an isentropic compressor $($no heat transfer, no entropy difference$)$ as saturated water$-$

steam mixture with a quality of $x4=0\mathrm{.}2848099958856609$kgvapo$\frac{r}{k}g$ total with pressure $P4=100$kPa

and exit with pressure of $P4=6000$kPa. If mass flow rate of steam $m=1k\frac{g}{s},$ calculate

a$)$ work transfer kW

b$)$ enthalpy difference between inlet and outlet of the condenser

c$)$ outlet quality of steam