Steam Consumption in Pipes and Air Heaters: Warm-up, Heat Loss and Condensate Loads

 

Steam entering a cold pipeline immediately condenses on the inside wall. During start-up, the metal mass of the main must be heated to operating temperature. Once the pipe is hot, a smaller continuous condensate load remains because heat is lost to the surroundings.

The distinction between warm-up load and running load is fundamental for steam-consumption estimates, condensate drainage and insulation assessment.

Steam-main warm-up load

ṁs = 60 · W · (Ts − Ta) · cp / (hfg · t)

Why slow warm-up is preferred

A longer warm-up time reduces peak condensate production and thermal and mechanical stress.

Typical specific heat values

Material cp kJ/(kg·°C)
Copper 0.385
Carbon steel 0.490
Chromium steel 0.443
AISI 302 0.480
AISI 304 0.477
AISI 316 0.468
AISI 347 0.480

Worked warm-up example

  • 100 m DN100 carbon-steel main
  • 9 PN40 flange pairs
  • 1 isolation valve
  • 20°C initial temperature
  • 14 bar(g), 198°C steam
  • hfg = 1,947 kJ/kg
  • 30-minute warm-up

Total metal mass: 1,798 kg

Mean warm-up condensate load: 161 kg/h

Steam traps during warm-up

Start-up is commonly the most demanding condition for steam traps and condensate drainage equipment. Within this sizing method, the warm-up load is multiplied by two before being distributed between the installed traps.

Running load

After warm-up, steam condensation is caused by continuing heat loss to the environment.

Effect of air movement

Air velocity Emission factor
0–0.5 m/s 1.0
1.0 m/s 1.3
2.0 m/s 1.7
3.0 m/s 2.0
4.0 m/s 2.3
6.0 m/s 2.9
8.0 m/s 3.5
10.0 m/s 4.0

Effect of insulation

For DN100 at approximately 15 bar(g), representative insulation factors are:

  • 50 mm: f ≈ 0.08
  • 75 mm: f ≈ 0.07
  • 100 mm: f ≈ 0.06

Running condensate calculation

ṁs = 3.6 · Q · L · f / hfg

For the worked line, effective length is 103 m and running condensate load is:

approximately 18.3 kg/h

Condition Condensate load
Warm-up 161 kg/h
Running 18.3 kg/h

Without effective insulation, the running load in this example would be approximately fourteen times higher.

Steam air heating

In unit heaters and air-heater batteries, steam condenses inside tubes and transfers useful heat to an air stream.

A nominal volumetric heat capacity of 1.3 kJ/(m³·°C) can be used for practical air-heating calculations.

Finned tubes

Fins increase external heat-transfer area and allow a more compact heater. Actual manufacturer data should be used for finned elements.

Unit heaters

Unit heaters combine a steam heating battery and a fan in one casing. Output depends on steam pressure, fan speed, mounting and leaving-air temperature.

Air heater batteries

Air heater batteries are normally installed in ducted systems and may include multiple heating banks, filters, fans and adjustable fresh/recirculated-air louvres.

Steam consumption from rated output

ṁs = Q̇ · 3,600 / hfg

For 44 kW at 3.5 bar(g), hfg = 2,120 kJ/kg:

steam consumption ≈ 75 kg/h

Steam consumption from airflow

ṁs = 3,600 · V̇ · ΔT · cv / hfg

Air-heater battery example

  • air flow: 2.3 m³/s
  • 18°C → 82°C
  • ΔT = 64°C
  • steam at 3 bar(g)
  • hfg = 2,133 kJ/kg

steam consumption ≈ 323 kg/h

Effect of tube arrangement

In natural convection, additional horizontal rows become progressively less effective. With ten pipes, the representative emission factor falls to approximately 0.63.

Forced airflow increases heat transfer and therefore steam condensation.

Control and drainage

Actual heating duty should be considered together with control-valve selection, condensate drainage, steam pressure and heater configuration.

Conclusion

Warm-up and normal running are different design conditions. In well-insulated mains, warm-up usually produces the highest condensate load, while insulation controls permanent energy loss.

For air heaters, steam consumption can be calculated from rated thermal output or from actual airflow and temperature rise.

Frequently Asked Questions

Why is warm-up load higher?

Because the entire metal mass of the main must be heated.

How can it be reduced?

By allowing a longer warm-up period.

How does insulation affect steam use?

It greatly reduces continuous running heat loss.

Which load is used for trap sizing?

The more demanding of warm-up and running duty should be checked.

How is heater steam use calculated from kW?

Using ṁs = Q̇·3,600/hfg.

Why are fins used?

To increase external heat-transfer area.

 
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