2.6). A gas-turbine plant operates on the regenerative Brayton cycle with two stages of reheating and two stages of intercooling between the pressure limits of 100 and 1200 kPa. The working fluid is air. The air enters the first and the Regenerator second stages of the compressor at 300 K and 350 K, respectively, and the first and Reheater the second stages of the turbine at Comb. cham. 1400 K and 1300 K, respectively. 6 Wnet Assuming both the compressor and the Comp. I Comp. II Turb. I Turb. II turbine have an isentropic efficiency of 3 80% and the regenerator has an effectiveness of 75%, determine (a) the Fig. p2.6. Intercooler back-work ratio and the network output, For two-stage compression and expansion, the work input is minimized and the work output is and (b) the thermal efficiency. maximized when both stages of the compressor

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2.6).
A gas-turbine plant operates on the regenerative Brayton cycle with two stages of reheating
and two stages of intercooling between the pressure limits of 100 and 1200 kPa. The working
fluid is air. The air enters the first and the
Regenerator
second stages of the compressor at 300 K
and 350 K, respectively, and the first and
Reheater
the second stages of the turbine at
Comb.
cham.
1400 K
and
1300 K, respectively.
6
Wnet
Assuming both the compressor and the
Comp. I
Comp. II
Turb. I
Turb. II
turbine have an isentropic efficiency of
80% and
the regenerator has
an
effectiveness of 75%, determine (a) the
Fig. p2.6.
Intercooler
back-work ratio and the network output,
For two-stage compression and expansion, the
work input is minimized and the work output is
maximized when both stages of the compressor
and the turbine have the same pressure ratio.
and (b) the thermal efficiency.
2.7).
A simple gas turbine, has the following data:
Compressor pressure ratio,
p = 20
Turbine inlet temperature,
T3
= 1400 K
Compressor isentropic efficiency,
Nc = 0.87
Turbine isentropic efficiency,
Ne = 0.9
Combustor pressure loss,
AP = 5%
Combustion efficiency,
Пь 3 0.99
Ambient conditions, Pa, Ta,
1.013 bar, 288 K
Ignore inlet and exhaust losses, draw cycle on T - s diagram and calculate:
a)
Turbine pressure ratio.
b)
The net specific output work.
c)
The gas turbine thermal efficiency.
2.8).
For the simple gas turbine, in problem (2.7), which produces 100 MW, calculate:
а)
Air mass flow rate.
b)
Fuel mass flow rate if the calorific value of kerosene fuel burned is 43.2 MJ/kg.
c)
Theoretical air to fuel ratio.
Transcribed Image Text:2.6). A gas-turbine plant operates on the regenerative Brayton cycle with two stages of reheating and two stages of intercooling between the pressure limits of 100 and 1200 kPa. The working fluid is air. The air enters the first and the Regenerator second stages of the compressor at 300 K and 350 K, respectively, and the first and Reheater the second stages of the turbine at Comb. cham. 1400 K and 1300 K, respectively. 6 Wnet Assuming both the compressor and the Comp. I Comp. II Turb. I Turb. II turbine have an isentropic efficiency of 80% and the regenerator has an effectiveness of 75%, determine (a) the Fig. p2.6. Intercooler back-work ratio and the network output, For two-stage compression and expansion, the work input is minimized and the work output is maximized when both stages of the compressor and the turbine have the same pressure ratio. and (b) the thermal efficiency. 2.7). A simple gas turbine, has the following data: Compressor pressure ratio, p = 20 Turbine inlet temperature, T3 = 1400 K Compressor isentropic efficiency, Nc = 0.87 Turbine isentropic efficiency, Ne = 0.9 Combustor pressure loss, AP = 5% Combustion efficiency, Пь 3 0.99 Ambient conditions, Pa, Ta, 1.013 bar, 288 K Ignore inlet and exhaust losses, draw cycle on T - s diagram and calculate: a) Turbine pressure ratio. b) The net specific output work. c) The gas turbine thermal efficiency. 2.8). For the simple gas turbine, in problem (2.7), which produces 100 MW, calculate: а) Air mass flow rate. b) Fuel mass flow rate if the calorific value of kerosene fuel burned is 43.2 MJ/kg. c) Theoretical air to fuel ratio.
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