Hot gas that would go up the stack, turned into steam, then megawatts or fuel saved, rupees and tonnes of CO2.
A pinch-point heat balance with IAPWS-IF97 steam properties. Change any number and everything updates.
Start from:
-Steam, t/h
-Net power, MW
-Saving, ₹ crore / year
-Simple payback, years
-IRR
-CO₂ avoided, t / year
How it works
Pinch. Gas leaving the evaporator can be no colder than saturation + pinch: Tgas,pinch = Tsat + ΔTpinch.
Heat above that point makes the steam: ms = mg·cp·(Tin − Tgas,pinch)·(1 − loss) / [(hsteam − heco,out) + b·(hf − heco,out)].
Approach. The economiser leaves the water a little below saturation (Tsat − ΔTapproach) so it does not steam. Its duty sets the stack: Tstack = Tgas,pinch − Qeco / (mg·cp).
Cold end. If that stack would fall below the acid dew point limit, or within 15 °C of the feedwater, the cold end decides instead: steam is cut until the stack sits at the limit, and the real pinch grows.
Steam properties come from IAPWS-IF97 (regions 1, 2 and 4), checked against the official verification values.
Power: isentropic expansion to the condenser, times turbine and generator efficiency, minus auxiliaries. Fuel: steam heat ÷ old boiler efficiency ÷ GCV.
Money: saving − O&M = yearly net; payback = cost ÷ net; IRR assumes the same net every year. CO2: grid factor (power) or IPCC default fuel factors (fuel).
Not included: part load, gas composition (cp is held constant), fouling, pressure drop, fan power, taxes and financing. Good for a first conversation; a real offer needs a design.