1.In a single-heater regenerative cycle the steam enters the turbine at 30 bar, 400°C and the exhaust pressure is 0.10 bar. The feed water heater is a direct contact type which operates at 5 bar. Find (i) The efficiency and the steam rate of the cycle. (ii) Compare the efficiency and steam rate to the Rankine cycle (without regeneration)

Elements Of Electromagnetics
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1.In a single-heater regenerative cycle the steam enters the turbine at 30
bar, 400°C and the exhaust pressure is 0.10 bar. The feed water heater is
a direct contact type which operates at 5 bar. Find (i) The efficiency
and the steam rate of the cycle. (ii) Compare the efficiency and steam
rate to the Rankine cycle (without regeneration)
2. A steam power plant of 110 MW capacity is equipped with
regenerative as well as reheat arrangement. The steam is supplied at 80
bar and 55°C of superheat. The steam is extracted at 7 bar for feed
heating and remaining steam is reheated to 350°C, and then expanded to
0.4 bar in the L.P. stage. Assume indirect type of feed heaters.
Determine : (i) The ratio of steam bled to steam generated, (ii) The
boiler generating capacity in tonnes of steam/hour, and (iii) Thermal
efficiency of the cycle. Assume no losses and ideal processes of
expansion.
Transcribed Image Text:1.In a single-heater regenerative cycle the steam enters the turbine at 30 bar, 400°C and the exhaust pressure is 0.10 bar. The feed water heater is a direct contact type which operates at 5 bar. Find (i) The efficiency and the steam rate of the cycle. (ii) Compare the efficiency and steam rate to the Rankine cycle (without regeneration) 2. A steam power plant of 110 MW capacity is equipped with regenerative as well as reheat arrangement. The steam is supplied at 80 bar and 55°C of superheat. The steam is extracted at 7 bar for feed heating and remaining steam is reheated to 350°C, and then expanded to 0.4 bar in the L.P. stage. Assume indirect type of feed heaters. Determine : (i) The ratio of steam bled to steam generated, (ii) The boiler generating capacity in tonnes of steam/hour, and (iii) Thermal efficiency of the cycle. Assume no losses and ideal processes of expansion.
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