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NACE MR103 SS Pressure Vessels For Amine Reflux Anti Corrosive U Stamp Approval

Categories Pressure Vessel
Brand Name: YUHONG
Model Number: Amine Reflux Vessel
Certification: ASME U STAMP
Place of Origin: China
MOQ: 1 set
Price: Negotiate
Payment Terms: L/C AT SIGHT, T/T
Supply Ability: 500 SETS PER YEAR
Delivery Time: 90 - 180 days
Packaging Details: EXPORT STANDARD
Design Code: ASME VIII + IBC 2018 + ASCE 7 + NACE MR103
DESIGN PRESSURE (INT / EXT): 3.5 / F.V. (bar g)
DESIGN TEMPERATURE: 100℃
OPERATING PRESSURE: 0.55 (bar g)
OPERATING TEMPERATURE: 65℃
M.D.M.T.: -6℃
DESIGN CODE FOR SEISMIC: IBC 2018
DESIGN CODE FOR WIND: ASCE/SEI 7-22
FLUID STATE (LIQUID/ GAS): LIQUID / GAS
Installation: pre assembly in workshop
Approval: U stamp
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NACE MR103 SS Pressure Vessels For Amine Reflux Anti Corrosive U Stamp Approval

Pressure Vessels for Amine Reflux Vessels: Design & Considerations


Amine reflux vessels are pressure vessels designed to handle condensed liquids (water + amine) and residual acid gases (H₂S, CO₂) from the overhead of an amine stripper column. Their design follows strict standards due to corrosive conditions and operational demands.


1. Design Codes & Standards


I.> ASME BPVC (Boiler & Pressure Vessel Code), Section VIII, Div. 1 or 2 – Mandatory for pressure containment.


II.> API 12GDU (Gas Dehydration Units) – Guidelines for amine system components.


III.> NACE MR0175/ISO 15156 – Material selection for H₂S service (sour environments).


IV.> GPSA Engineering Data Book – Industry best practices for gas processing.


2. Key Design Parameters


ParameterTypical RangeNotes
Design Pressure50–150 psig (3.5–10 barg)Must exceed stripper overhead pressure.
Design Temperature200–250°F (93–121°C)Matches stripper condenser outlet.
MaterialCarbon steel (SS for high corrosion)Lined or coated if severe HS/CO.
Corrosion Allowance1/8" to 1/4" (3–6 mm)Extra thickness for amine service.
Vent Size2–6 inches (DN50–DN150)For non-condensable gas release.

3. Material Selection


I.> Carbon Steel (SA-516 Gr. 70) – Most common, cost-effective, but requires amine-compatible coatings/inhibitors.


II.> Stainless Steel (SS 304/316) – Used for high H₂S/CO₂ or oxygen-contaminated systems.


III.> Clad Materials (CS + SS overlay) – For severe corrosion zones.


IV.> Internal Linings (Fiberglass, PTFE, Epoxy) – Additional protection against wet acid gas attack.


Note: Amine degradation products (e.g., heat-stable salts) can accelerate corrosion—material choice depends on amine type (MDEA, DEA, MEA).


4. Nozzle & Internals Requirements


NozzlePurposeTypical Size
InletFrom condenser6–12 inches (DN150–DN300)
Liquid OutletReflux to stripper3–6 inches (DN80–150)
VentNon-condensable purge2–4 inches (DN50–100)
DrainSludge removal2 inches (DN50)

5. Pressure Relief & Safety


  • PSV (Pressure Safety Valve) – Sized per API 520/521 for overpressure scenarios.


  • Rupture Disk (Optional) – For additional protection against sudden pressure spikes.


  • Flare/Scrubber Vent – Disposes H₂S/CO₂ safely.


6. Operational Challenges & Mitigation


IssueCauseSolution
CorrosionWet HS, heat-stable saltsUse corrosion-resistant materials, monitor amine quality.
FoamingContaminated amineInstall mist eliminator, add antifoam agents.
Level Control FailureFaulty instrumentationRedundant level switches (LT, LAL, LAH).
PluggingDegradation productsRegular flushing, filtration.

7. Inspection & Maintenance


  • NDT (UT, RT, PT) – Checks for wall thinning/cracks.


  • Thickness Monitoring – Ultrasonic testing (UT) for corrosion tracking.


  • Biannual Shutdown Checks – Demister integrity, nozzle condition.


Support and Services:


Our company offers comprehensive technical support and services for our Pressure Vessel product. Our team of experts is available to assist you with installation, maintenance, troubleshooting, and any other technical inquiries you may have. We are committed to ensuring that your Pressure Vessel operates efficiently and safely at all times


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