How the blowdown rate is calculated
When water evaporates in a boiler, the dissolved solids stay behind and concentrate. To keep them below the limit, part of the boiler water must be drained continuously. In steady operation the solids coming in with the feedwater equal the solids leaving with the blowdown:
Blowdown = Steam output · F ÷ (B − F)
Heat loss = Blowdown · (hf − hfeed)
- F
- total dissolved solids (TDS) in the feedwater, ppm
- B
- maximum TDS allowed in the boiler water, ppm
- hf
- enthalpy of saturated water at boiler pressure
- hfeed
- enthalpy of the feedwater, about 4.19 × temperature in °C
Worked example
A boiler produces 5,000 kg/h of steam at 10 bar g. The feedwater carries 150 ppm TDS and the boiler water may hold 3,000 ppm. The blowdown is 5,000 × 150 ÷ 2,850 = 263 kg/h, or 5 % of the feedwater. Each kilogram leaves as saturated water at 184 °C carrying 780 kJ, against 335 kJ in the 80 °C feedwater. The heat lost is 32.6 kW, around 10,900 per year at 0.05 per kWh of fuel and 90 % boiler efficiency.
Recovering blowdown heat
Blowdown water at boiler pressure partly flashes into steam when it drops to low pressure. A flash vessel recovers this steam for the deaerator or feed tank, typically 10 to 15 % of the blowdown mass. The remaining hot water can preheat make-up water in a heat exchanger. Together, flash and heat recovery can save 50 to 80 % of the blowdown heat.
Reducing blowdown
- Return as much condensate as possible; it is almost free of dissolved solids.
- Treat make-up water by softening, dealkalisation or reverse osmosis.
- Use automatic TDS control, which blows down only as much as needed.
- A deaerator removes oxygen and carbon dioxide and protects the boiler, but does not remove dissolved solids.