Design, analyze, and optimize a triple pressure heat recovery steam generator (HRS arge advanced combined cycle power plant whose net steam power output is 150 M e gas turbine exhaust gases can be treated as ideal gases and the outlet temperatu ss flow rate are 550°C and 500 kg/s respectively. Water enters a low-pressure onomizer for this HRSG at P = 200 kPa and T = 40°C. Make reasonable assumption

Design, analyze, and optimize a triple pressure heat recovery steam generator (HRS arge advanced combined cycle power plant whose net steam power output is 150 M e gas turbine exhaust gases can be treated as ideal gases and the outlet temperatu ss flow rate are 550°C and 500 kg/s respectively. Water enters a low-pressure onomizer for this HRSG at P = 200 kPa and T = 40°C. Make reasonable assumption

Refrigeration and Air Conditioning Technology (MindTap Course List)

8th Edition

ISBN:9781305578296

Author:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson

Publisher:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson

Chapter45: Domestic Refrigerators And Freezers

Section: Chapter Questions

Problem 12RQ: Refrigerators currently being manufactured in the United States are using______as their refrigerant.

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Refrigerators currently being manufactured in the United States are using______as their refrigerant.
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An open-cycle gas turbine plant will exhaust into a waste heat boiler which receives 66 0C feedwater. The gas turbine plant produces 2611 kW. Air flow rate is 37 kg/kW-hr. Fuel rate, rf/a = 0.014 kg fuel/kg air. Actual exhaust gas temperature = 483 0C. Average exhaust gas Cp = 1.082 kJ/kg.K. Compute the saturated steam at 0.450 MPa that can be produced per hour, assuming that the final gas temperature is 38 0C above the saturation temperature.
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Design, analyze, and optimize a triple pressure heat recovery steam generator (HRSG) for a large advanced combined cycle power plant whose net steam power output is 150 MW. The gas turbine exhaust gases can be treated as ideal gases and the outlet temperature and mass flow rate are 550°C and 500 kg/s respectively. Water enters a low-pressure economizer for this HRSG at P = 200 kPa and T = 40°C. Make reasonable assumptions as required.
Task (4) Critically compare how the changes of the heat transfer efficiency will affect the lifetime of the turbine.
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