Module 08 · Condensate Recovery4 min read

Condensate Return Lines and Condensate Pumps

Between the trap and the feed tank, condensate travels as a mixture of water and flash steam. Lines sized as if they carried only water back up, hammer and pressurize the traps feeding them. Where condensate cannot drain by gravity, a pump lifts it.

ByShikhar Singh·Steam Consultant & IT Consultant·Published

You'll learn

  • Distinguish drain lines before the trap from return lines after it
  • Size return lines for two-phase flow
  • Understand lift and back pressure
  • Compare electric and pressure-powered condensate pumps

Before this: Flash steam, Trap sizing and testing

BeginnerThe idea in plain words, and where you meet it. No maths.

Before the trap and after it

Upstream of the trap, the drain line carries water at steam pressure and is sized on water velocity — GyanTosh’s code uses 1.5 m/s for short runs and 1 m/s for long ones. Downstream, the pressure has dropped and part of the condensate has flashed. The return line now carries a little water and a great deal of steam by volume.

Ideally condensate falls by gravity to a receiver, from which it is pumped back to the feed tank. Where equipment sits low, or the return must rise to an overhead main, it has to be lifted.

IntermediateThe formula, its units, and a worked example on real plant numbers.

Sizing for the flash, not the water

Worked example
1,000 kg/h of 7 kg/cm²(g) condensate into a vented return
Given
  • Discharged from the trap to a line at atmospheric pressure.
  1. Flash: 13.3% = 133 kg/h of steam, occupying 222 m³/h.
  2. Water: 867 kg/h, about 0.91 m³/h.
Answer: By volume the flash is about 240 times the water. A line sized for 0.91 m³/h of water is drastically undersized; it must be sized as a steam line for the flash volume at a modest velocity.

Undersized return lines raise back pressure on every trap discharging into them, which cuts trap capacity, floods equipment upstream and drives the steam-water mixture fast enough to hammer. Common returns from traps at different pressures make it worse.

ExpertThe fine print: where the simple model breaks, and what it costs.

Lifting condensate and pumping it

A trap can lift condensate only with its own differential pressure, roughly 1 kg/cm² for every 10 m of lift plus line losses. That works on a steadily loaded main drain, but not on a temperature-controlled heater, where the steam pressure in the coil can fall below what the lift needs and condensate stops draining altogether — stall, covered in Module 09.

  • Electric condensate pumps: a receiver with a vent and a level-controlled centrifugal pump. Simple; the pump must suit near-boiling water, so it needs enough suction head to avoid cavitation.
  • Pressure-powered pumps: a vessel that fills by gravity and is emptied by steam or compressed air pressure, with no motor or seals. They handle hot condensate without cavitation and can be combined with a trap to drain stalled equipment.

Key takeaways

  • Drain lines before the trap carry water; return lines after it carry water and a large volume of flash.
  • Flash from 7 kg/cm²(g) condensate is hundreds of times the water’s volume: size returns for the flash.
  • Lift costs about 1 kg/cm² per 10 m; temperature-controlled equipment may not have it.
  • Electric pumps need suction head; pressure-powered pumps handle hot condensate and stall.

Check your understanding

Questions run from beginner to expert. Try each before opening the answer.

  1. Beginner

    Q1. What does a condensate return line after a trap carry?

    1. A.Only water
    2. B.Water and flash steam
    3. C.Only steam
    4. D.Air
    Show answer

    B. Part of the condensate flashes at the lower pressure.

  2. Intermediate

    Q2. What should a return line be sized for?

    1. A.The water flow only
    2. B.The flash steam volume
    3. C.The boiler output
    4. D.The trap size
    Show answer

    B. Flash dominates the volume.

  3. Intermediate

    Q3. Roughly what pressure does a 20 m lift need?

    1. A.0.2 kg/cm²
    2. B.2 kg/cm²
    3. C.20 kg/cm²
    4. D.None
    Show answer

    B. About 1 kg/cm² per 10 m.

  4. Expert

    Q4. Why are pressure-powered pumps used on hot condensate?

    1. A.They are faster
    2. B.No impeller to cavitate and no seals to leak
    3. C.They are electric
    4. D.They cool the water
    Show answer

    B. They push condensate with steam or air pressure.

Frequently asked

How do you size a condensate return line?
For the flash steam it carries, not just the water. Calculate the flash at the line pressure and size the line as a low-pressure steam line for that volume.
Can a steam trap lift condensate?
Yes, using its own differential pressure — roughly 1 kg/cm² per 10 m of lift plus losses. Where steam pressure can fall, as in temperature-controlled equipment, a pump is needed.

Training a boiler team?

These lessons follow the order we train operators in. We also run on-site operator and maintenance training, built around your own plant.

Boiler operator training →

Sources

  • GyanTosh Condensate Recovery Calculator — Flash quantities and drain-line velocity limits from the same code.

About the author

Shikhar SinghSteam Consultant & IT Consultant

Shikhar Singh is a Steam Consultant and IT Consultant at GyanTosh Fabricators Pvt. Ltd., where he works on steam system sizing, condensate recovery and the engineering content published on this site.

Full profile and background →