$2.(25$ points$)\backslash (0\mathrm{.}5\backslash$mathrm$\{$~kg$\}/\backslash$mathrm$\{$s$\}\backslash )$ of $\backslash (\backslash$mathrm$\{$R$\}-134\backslash$mathrm$\{$a$\}\backslash )$ starts as a superheated vapor at $600$ kPa and $\backslash (40^\{\backslash$circ$\}\backslash$mathrm$\{$C$\}\backslash )$ and is then condensed to a saturated liquid at constant pressure.

$($a$)(5$ points$)$ Determine the final $($saturation$)$ temperature for the liquid.

$($b$)(5$ points$)$ Determine the heat removed from the R$-134$a during this process, in kW $.$

$($c$)(5$ points$)$ Determine the change in the specific entropy $($in $\backslash (\backslash$mathrm$\{$kJ$\}/\backslash$mathrm$\{$kg$\}^\{*\}\backslash$mathrm$\{$~K$\}\backslash ))$ of the $\backslash (\backslash$mathrm$\{$R$\}-134\backslash$mathrm$\{$a$\}\backslash )$ in this process.

$($d$)(5$ points$)$ Assuming that heat is rejected to a temperature equivalent to the one that you found in part $($a$),$ calculate the total entropy generation rate $($in $\backslash (\backslash$mathrm$\{$kW$\}/\backslash$mathrm$\{$K$\}\backslash ))$ during this process.

$($e$)(\backslash (\backslash$mathbf$\{5\}\backslash )$ points$)$ Sketch the process on a T$-$s diagram with respect to saturation lines.