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V-1186 — Vacuum Gas Oil Vessel V-1186

Fluid Catalytic Cracker · Vacuum Gas Oil service · Installed Aug 24, 2017 (9 yrs in service)

High
Current Min. Thickness
0.104 in
t-min 0.238 in
Measured Corrosion Rate
22.64 mpy
ML-predicted: 20.89 mpy
Remaining Life
0.0 yrs
Next Inspection Due
Feb 20, 2027
Interval: 0.5 yrs (API 510)

UT Thickness Trend

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

Vessel Specification

MaterialSA-240 Duplex 2205
Design CodeASME BPVC Section VIII, Div. 2
Joint Efficiency0.85
Design Pressure71 psig
Design Temperature304 °F
Operating Pressure47 psig
Operating Temperature224 °F
Diameter142 in
Nominal Thickness0.320 in
Corrosion Allowance0.0625 in
H2S / Chloride6 / 40 ppm
Flow Velocity17.4 ft/s
Process pH4.84
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
16.71 mpy
Predicted corrosion rate under these conditions (-5.93 mpy vs. current measured rate)
Implied Remaining Life
0.0 yrs
Implied Reinspection Interval
0.5 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 — Naphthenic Acid Corrosion

API 571 §4.2.10

Aggressive, velocity-assisted corrosion in high-TAN crude fractions, most severe 450–750°F; low-alloy/carbon steel is far more susceptible than Mo-bearing or 316 SS.

Recommended inspection approach: UT thickness at high-velocity/turbulent locations; feed TAN monitoring; consider alloy upgrade per API 571 guidance.

Inspection History

UT thickness readings, most recent first

DateMethodCML CountAvg ThicknessMin CML Thickness
Aug 22, 2026UT Spot40.1189 in0.1045 in
Jan 26, 2025UT Spot40.1474 in0.1310 in
Jun 15, 2023UT Spot40.1857 in0.1670 in
Apr 26, 2020UT Spot40.2584 in0.2562 in