Inflection Point Engineering Pressure Vessel Engineering Curriculum

In-Service

Module from the Pressure Vessel Engineering Curriculum curriculum.

Module 10 - In-Service Inspection and Fitness for Service · Learning Objectives · 1. Apply API 510 inspection intervals by vessel classification · 2. Compute remaining corrosion allowance and corrosion rate · 3. Conduct Level 1 or 2 FFS per API 579 for LTAs (local thin areas) · 4. Perform re-rating per UG-98 and NBIC when conditions change · 5. Document inspection per ASME B31.3 owner user responsibilities · API 510 Inspection Intervals

Class Examples External Interval Internal / On-Stream Notes Ref
1 (High) LPG, toxics, high-P H2 5 yr Half RL or 10 yr Most critical API 510 Table 6.1
2 (Moderate) Most HC vessels 5 yr Half RL or 10 yr Standard API 510
3 (Low) Utilities, low-P 10 yr Half RL or 15 yr Least API 510
RBI-managed Per risk matrix Per RBI Per RBI Extended allowed API 580
FFS Decision Matrix (API 579 Level 1)
LTA Finding Measurement Level 1 Action Level 2 Trigger Notes Ref
General corrosion uniform t_avg > tmin + CA Continue service If near limit Common 579 Pt 4
LTA (local thin area) s < 1.123*sqrt(D*tmin) and Rt > 0.8 Accept LTA with Rt 0.2-0.8 Blended profile 579 Pt 4
Pitting PI depth < 0.5*tmin Accept (reduced CA) If deeper Corrosion per API 571 579 Pt 6
Crack-like flaw Any Level 2 or 3 required - Needs fracture mech 579 Pt 9
Creep damage T > 0.4*Tm Level 2 or 3 - Remaining life 579 Pt 10

Source: Pressure_Vessel_Engineering_Curriculum_v1.xlsx · Sheet: In-Service