Separate streams of steam and air flow through the turbine and heat exchanger arrangement shown in the figure below, where mass flow rate m5 is 2000 kg/min and power output Wt1 is 12,000 KW. Steady-state operating data are provided on the figure. Heat transfer with the surroundings can be neglected, as can all kinetic and potential energy effects. m5 Steam in + Turbine T₁ = 600°C P₁ = 20 bar Determine: (a) T3, in K. T₂=400°C P2 = 10 bar -6 T6 = 1200 K P6= 1 bar K P3= 10 bar T3=? kW www www Heat exchanger Turbine 2 (b) the power output of the second turbine, in kW. Wn=? T₁=240°C P4 = 1 bar T5 = 1500 K -5 Ps= 1.35 bar Ams Air in

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Question 20
Separate streams of steam and air flow through the turbine and heat exchanger arrangement shown in the
figure below, where mass flow rate m5 is 2000 kg/min and power output Wt1 is 12,000 kW. Steady-state
operating data are provided on the figure. Heat transfer with the surroundings can be neglected, as can all
kinetic and potential energy effects. m5
Steam
in
Turbine
T₁ = 600°C
P₁ = 20 bar
Determine:
(a) T3, in K.
W₁l
T₂ = 400°C
P2= 10 bar
>
6
VT6 = 1200 K
P6 = 1 bar
kW
P3= 10 bar
T3=?
www
tw
Heat exchanger
Turbine
2
Air in
(b) the power output of the second turbine, in kW.
W₁2=?
T5 = 1500 K
-5 P5= 1.35 bar
m5
T₁ = 240°C
P4 = 1 bar
Transcribed Image Text:Question 20 Separate streams of steam and air flow through the turbine and heat exchanger arrangement shown in the figure below, where mass flow rate m5 is 2000 kg/min and power output Wt1 is 12,000 kW. Steady-state operating data are provided on the figure. Heat transfer with the surroundings can be neglected, as can all kinetic and potential energy effects. m5 Steam in Turbine T₁ = 600°C P₁ = 20 bar Determine: (a) T3, in K. W₁l T₂ = 400°C P2= 10 bar > 6 VT6 = 1200 K P6 = 1 bar kW P3= 10 bar T3=? www tw Heat exchanger Turbine 2 Air in (b) the power output of the second turbine, in kW. W₁2=? T5 = 1500 K -5 P5= 1.35 bar m5 T₁ = 240°C P4 = 1 bar
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