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V-1041 — Hot Hydrocarbon Vapor Vessel V-1041

Fluid Catalytic Cracker · Hot Hydrocarbon Vapor service · Installed Aug 24, 2019 (7 yrs in service)

Low-Medium
Current Min. Thickness
1.297 in
t-min 1.149 in
Measured Corrosion Rate
0.61 mpy
ML-predicted: 0.34 mpy
Remaining Life
60+ 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. 2
Joint Efficiency1.00
Design Pressure432 psig
Design Temperature365 °F
Operating Pressure274 psig
Operating Temperature230 °F
Diameter105 in
Nominal Thickness1.313 in
Corrosion Allowance0.0938 in
H2S / Chloride6 / 172 ppm
Flow Velocity14.0 ft/s
Process pH8.61
InsulatedYes

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
0.10 mpy
Predicted corrosion rate under these conditions (-0.51 mpy vs. current measured rate)
Implied Remaining Life
60+ yrs
Implied Reinspection Interval
10.0 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 — Corrosion Under Insulation (CUI)

API 571 §4.3.5

Localized external corrosion beneath insulation where moisture is trapped, most severe in the 140–250°F operating band.

Recommended inspection approach: Insulation removal at high-risk locations (nozzles, low points), profile radiography, or guided-wave UT screening per API 570/RP 583.

Inspection History

UT thickness readings, most recent first

DateMethodCML CountAvg ThicknessMin CML Thickness
Aug 22, 2026UT Grid (API 572)41.3072 in1.2967 in
Oct 29, 2025UT Grid (API 572)41.3074 in1.2894 in
Jun 9, 2024UT Grid (API 572)41.3128 in1.2950 in
Jan 4, 2022UT Spot41.3079 in1.2991 in