#2 Separate streams of steam and air flow through the turbine and heat exchanger arrangement shown in the figure below, where the air stream mass rate m'5 ranges from 1500 kg/min to 3500 kg/min in increments of 500 kg/min and Wt1= 10,000 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. Steam in Turbine T₁ = 600°C P₁ = 20 bar T₂=400°C P210 bar mw tmt T6 = 1200 K P = 1 bar Py = 10 bar T₂=? Heat exchanger I Turbine W₂=? Air in T₁ = 240°C P= 1 bar T₁ = 1500 K -5 Ps= 1.35 bar 4 ms Analyze the two-compressor system for different air mass flow rates into the heat exchanger. Provide clearly detailed professional written sample of the calculations needed to analyze each component of the system and the overall system. Complete the following table and plot the mass of air MS against the Temperate T3, plot the mass rate M5 against the power output of turbine 2, plot the mass rate M5 against the mass rate M1 of steam, plot the mass rate of air M5 against the value of the energy output provided by both turbines for a 24 hours period at the energy cost of $0.15/kxxbut

Elements Of Electromagnetics
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Author:Sadiku, Matthew N. O.
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#2 Separate streams of steam and air flow through the turbine and heat exchanger arrangement shown
in the figure below, where the air stream mass rate m'5 ranges from 1500 kg/min to 3500 kg/min in
increments of 500 kg/min and Wt1= 10,000 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.
Steam
in
1500 kg/min
2000 kg/min
2500 kg/min
Mass Rate of
Air M5 in
kg/min
3000 kg/min
3500 kg/min
Turbine
T₁ = 600°C
P₁ = 20 bar
W₁
T3
T₂=400°C
P2 10 bar
Temperature
T6 = 1200 K
P6 = 1 bar
tmt
tm
Heat exchanger
TWO TURBINE PROBLEM
Py = 10 bar
T3 = ?
Analyze the two-compressor system for different air mass flow rates into the heat exchanger. Provide
clearly detailed professional written sample of the calculations needed to analyze each component of
the system and the overall system. Complete the following table and plot the mass of air M5 against
the Temperate T3, plot the mass rate M5 against the power output of turbine 2, plot the mass rate M5
against the mass rate M1 of steam, plot the mass rate of air M5 against the value of the energy output
provided by both turbines for a 24 hours period at the energy cost of $0.15/kwht
Power
Output
Turbine 2
Turbine
2
Mass
Rate of
Water
Min
kg/sec
ms
Ts= 1500 K
5 ps 1.35 bar
Air in
W₂=?
Value of total
energy
provided by
turbines
T₁ = 240°C
P₁ = 1 bar
running 24
hours at
$0.13/kw.br
Transcribed Image Text:#2 Separate streams of steam and air flow through the turbine and heat exchanger arrangement shown in the figure below, where the air stream mass rate m'5 ranges from 1500 kg/min to 3500 kg/min in increments of 500 kg/min and Wt1= 10,000 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. Steam in 1500 kg/min 2000 kg/min 2500 kg/min Mass Rate of Air M5 in kg/min 3000 kg/min 3500 kg/min Turbine T₁ = 600°C P₁ = 20 bar W₁ T3 T₂=400°C P2 10 bar Temperature T6 = 1200 K P6 = 1 bar tmt tm Heat exchanger TWO TURBINE PROBLEM Py = 10 bar T3 = ? Analyze the two-compressor system for different air mass flow rates into the heat exchanger. Provide clearly detailed professional written sample of the calculations needed to analyze each component of the system and the overall system. Complete the following table and plot the mass of air M5 against the Temperate T3, plot the mass rate M5 against the power output of turbine 2, plot the mass rate M5 against the mass rate M1 of steam, plot the mass rate of air M5 against the value of the energy output provided by both turbines for a 24 hours period at the energy cost of $0.15/kwht Power Output Turbine 2 Turbine 2 Mass Rate of Water Min kg/sec ms Ts= 1500 K 5 ps 1.35 bar Air in W₂=? Value of total energy provided by turbines T₁ = 240°C P₁ = 1 bar running 24 hours at $0.13/kw.br
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