Answer part E only please.

Determine the full exergy accounting for the overall plant, in MW $.$ Let $\backslash ($ T$\_\{0\}=300\backslash$mathrm$\{$~K$\},$ p$\_\{0\}=1\backslash$mathrm$\{$bar$\}\backslash ).$

Exergy input $($Combustion$)$

Exergy output $($Power$)$

Magnitude of Exergy Losses:

Exhaust

Condenser

Exergy Destructions:

Compressor

Gas Turbine

Steam Turbine

Pump

Heat Exchanger

Total $($Exergy output plus all Exergy losses and destructions$)$

MW

MW

MW

MW

MW

MW

MW

MW

MW

MW

A combined gas turbine$-$steam power plant operates as shown in the figure below. Pressure and temperature data are given at

principal states, and the net power developed by the combined power is $115$ MW $.$ Using air$-$standard analysis for the gas turbine,

determine:

$($a$)$ the isentropic efficiencies of both turbines and the gas cycle compressor.

$($b$)$ the mass flow rates of air and steam, in kg$/$sec

$($c$)$ the net power developed by both gas and vapor cycle, in MW$.$

$($d$)$ the overall thermal efficiency of the plant.

$($e$)$ the full exergy accounting for the overall plant, in MW$.$ Let T$\_(0)=300$K$,$p$\_(0)=1$bar.

$($f$)$ the exergetic efficiency.