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V-1335 — Lean MDEA Amine Drum V-1335

Fluid Catalytic Cracker · Lean MDEA Amine service · Installed Aug 25, 2015 (11 yrs in service)

Low-Medium
Current Min. Thickness
0.636 in
t-min 0.520 in
Measured Corrosion Rate
2.12 mpy
ML-predicted: 5.48 mpy
Remaining Life
54.9 yrs
Next Inspection Due
Aug 19, 2036
Interval: 10.0 yrs (API 510)

UT Thickness Trend

Minimum CML reading per inspection vs. ASME Sec. VIII t-min

Vessel Specification

MaterialSA-516-70 Carbon Steel
Design CodeASME BPVC Section VIII, Div. 1
Joint Efficiency0.85
Design Pressure299 psig
Design Temperature509 °F
Operating Pressure245 psig
Operating Temperature396 °F
Diameter58 in
Nominal Thickness0.667 in
Corrosion Allowance0.1250 in
H2S / Chloride638 / 22 ppm
Flow Velocity20.0 ft/s
Process pH4.91
InsulatedNo

Corrosion & Remaining-Life What-If

Adjust operating conditions to see the live model-predicted corrosion rate and implied remaining life

Live Prediction — What-If Model
9.52 mpy
Predicted corrosion rate under these conditions (+7.40 mpy vs. current measured rate)
Implied Remaining Life
12.2 yrs
Implied Reinspection Interval
6.1 yrs

What-if model: standardized Ridge regression, R² 0.56 on held-out fleet data (3.25 mpy MAE). Runs entirely client-side for instant feedback — see Model Insights for the full fleet-scale ensemble model used for official predictions.

Governing Damage Mechanism — Amine Corrosion

API 571 §4.2.4

Localized corrosion in amine treating services, accelerated by high velocity, heat-stable salts, and CO2/H2S loading.

Recommended inspection approach: UT thickness at high-turbulence points (elbows, tees, reboiler returns); monitor amine quality (HSAS, degradation products).

Inspection History

UT thickness readings, most recent first

DateMethodCML CountAvg ThicknessMin CML Thickness
Aug 22, 2026UT Grid + RT60.6428 in0.6360 in
Jul 16, 2026UT Grid + RT60.6447 in0.6415 in
Jan 15, 2024UT Grid (API 572)60.6484 in0.6409 in
Jan 17, 2021UT Spot60.6564 in0.6386 in
Dec 3, 2018UT Spot60.6591 in0.6408 in