A steam boiler heats liquid water at 100°C to superheated steam at 1 MPa and 250°C. Fuel [CH4 (g)] is burned at atmospheric pressure with 50 percent excess air. The fuel and air enter the boiler at 25°C and the products of combustion leave at 300°C. Firstly: Sketch the T-s diagram for the boiler, and secondly: Calculate by parametric analysis (a) the amount of steam generated per unit of fuel mass burned, (b) the change in the exergy of the combustion streams, in kJ/kg fuel, (c) the change in the exergy of the steam stream, in kJ/kg steam, and (d) the lost work potential, in kJ/kg fuel. Take TO=25°C, PO=100kPa and assume air, fuel and products have constant Cp at average temperature.

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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A steam boiler heats liquid water at 100°C to superheated steam at 1 MPa and
250°C. Fuel [CH4 (g)] is burned at atmospheric pressure with 50 percent excess
air. The fuel and air enter the boiler at 25°C and the products of combustion
leave at 300°C. Firstly: Sketch the T-s diagram for the boiler, and secondly:
Calculate by parametric analysis (a) the amount of steam generated per unit of
fuel mass burned, (b) the change in the exergy of the combustion streams, in
kJ/kg fuel, (c) the change in the exergy of the steam stream, in kJ/kg steam, and
(d) the lost work potential, in kJ/kg fuel. Take TO=25°C, PO3100KPA and assume
air, fuel and products have constant Cp at average temperature.
Transcribed Image Text:A steam boiler heats liquid water at 100°C to superheated steam at 1 MPa and 250°C. Fuel [CH4 (g)] is burned at atmospheric pressure with 50 percent excess air. The fuel and air enter the boiler at 25°C and the products of combustion leave at 300°C. Firstly: Sketch the T-s diagram for the boiler, and secondly: Calculate by parametric analysis (a) the amount of steam generated per unit of fuel mass burned, (b) the change in the exergy of the combustion streams, in kJ/kg fuel, (c) the change in the exergy of the steam stream, in kJ/kg steam, and (d) the lost work potential, in kJ/kg fuel. Take TO=25°C, PO3100KPA and assume air, fuel and products have constant Cp at average temperature.
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