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V-1326 — Hot Hydrocarbon Vapor Drum V-1326

Fluid Catalytic Cracker · Hot Hydrocarbon Vapor service · Installed Aug 23, 2020 (6 yrs in service)

Low-Medium
Current Min. Thickness
0.589 in
t-min 0.474 in
Measured Corrosion Rate
6.46 mpy
ML-predicted: 5.98 mpy
Remaining Life
17.8 yrs
Next Inspection Due
Jul 9, 2035
Interval: 8.9 yrs (API 510)

UT Thickness Trend

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

Vessel Specification

MaterialSA-387-11 Cl.2 (1.25Cr-0.5Mo)
Design CodeASME BPVC Section VIII, Div. 2
Joint Efficiency1.00
Design Pressure449 psig
Design Temperature128 °F
Operating Pressure325 psig
Operating Temperature91 °F
Diameter37 in
Nominal Thickness0.636 in
Corrosion Allowance0.0938 in
H2S / Chloride45 / 206 ppm
Flow Velocity20.2 ft/s
Process pH4.30
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
5.93 mpy
Predicted corrosion rate under these conditions (-0.53 mpy vs. current measured rate)
Implied Remaining Life
19.4 yrs
Implied Reinspection Interval
9.7 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 + RT60.5967 in0.5886 in
Mar 18, 2026UT Spot60.6014 in0.5859 in
Jul 20, 2024UT Spot60.6108 in0.5974 in
Mar 2, 2022UT Spot60.6270 in0.6231 in