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Valves for Amine (DEA / MEA / MDEA — Gas Sweetening) Service

Amine solutions — diethanolamine (DEA), monoethanolamine (MEA), and methyldiethanolamine (MDEA) — are used extensively in natural gas and refinery gas sweetening units to remove hydrogen sulphide (H₂S) and carbon dioxide (CO₂) from sour gas streams. The amine absorber and regenerator are among the most demanding corrosion environments in a gas plant.

Pressure Range

Absorber: 30–100 bar; Regenerator: 1–2 bar (vacuum flash)

Temperature

Absorber: 35–65°C; Regenerator reboiler: up to 135°C

Industries

Natural gas sweetening (H₂S and CO₂ removal), Refinery FCC off-gas treating, Hydrogen plant feed gas treating

INDICATIVE ONLY — Reference DisclaimerAmine systems handle hydrogen sulphide (H₂S), which is acutely toxic at low concentrations. All equipment specifications must comply with NACE MR0175 for sour service and applicable safety regulations. HAZOP review is mandatory for amine unit design. Vajra Industrial Solutions accepts no liability for material selection decisions based on this guide.

Key Properties — Amine (DEA / MEA / MDEA — Gas Sweetening)

  • Amine concentration: typically 30–50 wt% in water
  • Absorber conditions: low temperature (35–60°C), high pressure (up to 100 bar)
  • Regenerator: high temperature (110–130°C), low pressure (1–2 bar), highly corrosive
  • Rich amine (carrying H₂S + CO₂) is significantly more corrosive than lean amine
  • Heat stable salts (HSS) accumulate in amine — accelerate corrosion if not removed
  • SSCC (Sulphide Stress Corrosion Cracking) risk in sour service components

Material Compatibility — Amine (DEA / MEA / MDEA — Gas Sweetening)

Ratings are indicative. Actual compatibility depends on concentration, temperature, velocity, and presence of contaminants. Always consult corrosion tables or a materials engineer.

MaterialRatingNotes
Carbon Steel (WCB/A105)GoodAcceptable for lean amine at low temperature with velocity limits <3 m/s. Not for rich amine regenerator.
SS 316LExcellentStandard material for rich amine, regenerator, and reboiler service.
SS 304LGoodAcceptable for lean amine; 316L preferred in hot rich amine.
Duplex SS 2205ExcellentExcellent corrosion resistance in amine; sometimes used for critical valves.
PTFE seatsGoodAcceptable for lean amine at low temperature; check chemical compatibility at regenerator conditions.
Hastelloy C-276ExcellentUsed for hottest, most corrosive amine service points.

Recommended Valves

Ball Valve (SS 316L body, PTFE seats, NACE MR0175 trim)

Standard isolation for amine absorption and regeneration circuits in sour service.

Globe Valve (SS 316L, NACE-compliant)

Flow control on amine recirculation, lean/rich heat exchanger bypass.

Gate Valve (SS 316L, OS&Y, NACE)

Large-bore isolation on amine contactors and regenerator columns.

Control Valve (SS trim, NACE MR0175, anti-cavitation)

Rich amine level control on absorber — prone to cavitation due to pressure drop.

Valves to Avoid

Carbon steel valves in rich amine at high temperature (corrosion rates >1 mm/year)

Copper alloy valves (amine attacks copper)

Valves with hardened trim above NACE MR0175 limit (22 HRC maximum for wetted metal parts)

Elastomeric seals not rated for H₂S/amine co-service

Special Considerations

NACE MR0175 compliance for all metallic components in H₂S co-service — mandatory in sour gas plant design
Amine foaming: caused by valve-induced turbulence — flow velocities must be controlled
Corrosion allowance: specify minimum 3 mm additional wall for carbon steel in lean amine service
Shutdown and standby: amine systems must be kept full or nitrogen-blanketed to prevent oxidation during downtime

Applicable Standards

NACE MR0175 / ISO 15156 (sour service)ASME B16.34API 600 (large bore gate/globe)ASME B31.3

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