Water tools
Packed tower air stripper: blower and pump power and specific energy
The blower pushes the air through the packing and the internals; the pump lifts the water to the top. Together they are most of what a stripper costs to run.
How it works
The blower sees the packing drop plus the demister, support plate and duct losses, and compresses adiabatically:
- blower discharge pressure, Pa absolute
- ambient pressure, Pa
- packing pressure drop, N/m² per m
- packing height, m
- loss coefficient of the internals, N·s²/m⁴
- air flow, m³/s
- tower cross-section, m²
- blower power, kW
- air mass flow, kg/s
- gas constant, 8.314 J/mol·K
- air temperature, K
- molar mass of air, 28.97 g/mol
- polytropic exponent, 0.283
- blower and pump efficiency
- pump power, W
- water density, kg/m³
- water flow, m³/s
- gravity, 9.81 m/s²
The pump term counts only the static lift to the distributor; piping losses are extra. Smaller packing and a higher pressure drop trade tower volume against blower energy; the packing type itself changes volume and power little. A typical VOC stripper at a stripping factor of 3.5 and 50 N/m² per m sits near 0.05 kWh/m³.
Related reading
These calculators use standard published formulas and are provided for preliminary engineering guidance. Confirm against measured data and vendor projections before design. Model your full water matrix in Nepti or post your project to compare provider proposals.