Guide

Condensate Corrosion

Condensate is naturally corrosive. Dissolved oxygen and carbon dioxide form acids that eat through steel piping. Learn the causes, prevention methods, and how to protect your condensate return system.

6 min readUpdated July 2026

Why Condensate is Corrosive

Pure condensate is actually aggressive. It wants to dissolve things. But the main corrosion culprits are dissolved gases: oxygen (O2) and carbon dioxide (CO2).

Oxygen causes pitting corrosion, deep localised holes that can penetrate pipe walls quickly. CO2 forms carbonic acid in condensate, causing generalised thinning of pipe walls, especially at the bottom of horizontal pipes where condensate collects.

Sources of Corrosive Gases

  • Dissolved oxygen in feedwater: If the deaerator is not functioning correctly, dissolved oxygen enters the boiler, passes through with the steam, and ends up in the condensate.
  • Carbonate breakdown: Bicarbonates in boiler water break down under heat to form CO2, which travels with steam into the condensate system.
  • Air ingress: Vacuum conditions in condensate return lines (caused by steam condensing) can draw in air through leaks at valves, traps, and flanges.

Symptoms of Condensate Corrosion

  • Red or brown water: Iron oxide (rust) dissolved in condensate indicates active corrosion of steel piping.
  • Pinhole leaks: Small leaks at the bottom of horizontal condensate pipes, especially at elbows and welds.
  • Thin pipe walls: Ultrasonic thickness measurement reveals thinning, particularly at the bottom of horizontal runs.
  • Frequent trap failures: Corrosion debris (iron oxide particles) fouls steam trap valves, causing premature failure.

Prevention Methods

  1. Ensure the deaerator is functioning correctly. Target dissolved oxygen below 0.007 mg/L in feedwater.
  2. Dose neutralising amines (e.g., cyclohexylamine, morpholine) into the steam to raise condensate pH to 8.5 to 9.5, neutralising carbonic acid.
  3. Dose filming amines to create a protective film on pipe walls, preventing both oxygen and CO2 attack.
  4. Maintain condensate return lines under slight positive pressure to prevent air ingress.
  5. Install vacuum breakers at equipment to prevent air being drawn in when steam condenses.
  6. Use stainless steel or copper alloy piping for condensate return in critical or high-corrosion areas.

Test condensate for iron content

Regular iron content testing (target below 1 mg/L) is the best indicator of condensate corrosion. Rising iron levels mean your corrosion control program needs attention. Check deaerator performance and amine dosing.

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