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Module 1: Fuels characterization and energy balance

Lecture 8: Gasification: Material and Heat Balance

Sensible heat of dry producer gas at 900K

Heat Balance
Heat Input:

Input	Kcal
CV of coal	7566.32
Sensible heat in coal, air	0
Enthalpy of water vapour in air	9.93
Enthalpy of steam	166
Total	7742.25

Heat Output:

Output	Kcal
CV of dry PG	5640
Sensible heat of dry PG	932.8
Enthalpy of water vapour in hot gas	81.6
Heat losses	1087.85
Total	7742.25