358 A Text Book of Thermal Engineering Feed water temperaturç 12° C; Pressure of steam = 11 bar; Dryness fraction of steam - 0.95: Mass of coal burnt 300 kg/h , Calorific value of coal 32 000 kJ/kg of coal : Mass of water suppiied to boiler in 7 hrs 14 min 14 625 kg. %3D The mass ofw ster in the boiler at the end of the test was less than that at the commence ment by 900 kg. Calculate:L. Actual evaporation per kg of coal: 2. Equivalent evaporation from and at 100 C per kg [Ans. 7.15 kg; 8.33 kg: 58.75 %) of coal ; and 3. Thermal efficiency of the boiler.

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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6 In a boiler test, the following observations wcre made:
358
A Text Book of Thermal Engineering
Feed water temperaturç
e=
12" C; Pressure of steam = 11 bar; Dryness fraction of steam 095
Mass of coal burnt 300 kg/h, Calorific value of coal 32 000 kJkg of coal; Mass of water supplied to boiler
in 7 hrs 14 min= 14 625 kg.
The mass of w ster in the boiler at the end of the test was less than that at the commencement by
900kg. Calculate I. Actual evaporation per kg of coal: 2 Equivalent evaporation from and at 100 C per kg
[Ans. 7 15 kg, 8 33 kg: 58.75 %
of coal ; and 3. Thermal efficiency of the boiler
Transcribed Image Text:6 In a boiler test, the following observations wcre made: 358 A Text Book of Thermal Engineering Feed water temperaturç e= 12" C; Pressure of steam = 11 bar; Dryness fraction of steam 095 Mass of coal burnt 300 kg/h, Calorific value of coal 32 000 kJkg of coal; Mass of water supplied to boiler in 7 hrs 14 min= 14 625 kg. The mass of w ster in the boiler at the end of the test was less than that at the commencement by 900kg. Calculate I. Actual evaporation per kg of coal: 2 Equivalent evaporation from and at 100 C per kg [Ans. 7 15 kg, 8 33 kg: 58.75 % of coal ; and 3. Thermal efficiency of the boiler
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