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WHRB Payback Estimator

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:
Hot gas
Steam side
Use of the steam
Money

The project cost is a placeholder, not a price. Enter the cost you were quoted.

-Steam, t/h
-Net power, MW
-Saving, ₹ crore / year
-Simple payback, years
-IRR
-CO₂ avoided, t / year

How it works
  1. 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)].
  2. 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).
  3. 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.
  4. Steam properties come from IAPWS-IF97 (regions 1, 2 and 4), checked against the official verification values.
  5. Power: isentropic expansion to the condenser, times turbine and generator efficiency, minus auxiliaries. Fuel: steam heat ÷ old boiler efficiency ÷ GCV.
  6. 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.

Educational estimate built from public methods and made-up example data. Not a design, an offer or advice. Presets are illustrative. © 2026 Adari Praveen · personal project · views are my own.