Outputs
Direct Method Efficiency - %
Indirect Method Efficiency - %
Enthalpy rise of steam over feed - kCal/kg
Estimated Saturation Temp @ Pressure - °C
Dry Flue Gas Loss - %
Loss due to H₂ in Fuel (assumed) 2.00 %
Moisture in Fuel Loss (assumed) 1.00 %
Unburnt Carbon (Ash) Loss - %
Radiation & Other Loss 2.00 %