Built For Refineries.
Proven At Scale.

Hydrogen-induced cracking doesn't follow generic corrosion models. You need wet H2S partial pressure calculations, scheduled pH monitoring integration, and stress-oriented HIC projection.

Our HIC model uses your actual crude sulfur content, operating temps, and historical UT data to project susceptibility. We've calibrated against 4,200 sour service failures.

The HIC model helps identify susceptible assets earlier, enabling proactive inspection scheduling before damage propagates.

Generic RBI treats a 450°C reformer the same as a 200°C separator. But creep failure isn't linear. You need Larson-Miller parameter tracking and actual operating hour stress analysis.

We pull real operating temps from your PI historian, calculate cumulative creep damage using API 579, and flag when units exceed safe operational envelopes.

Continuous creep tracking enables metallurgical assessments to be scheduled based on actual cumulative damage, not arbitrary calendar intervals.

Traditional approach: inspect everything on a 4-year cycle. Result: 60% of inspections find nothing, while critical items get deferred due to budget/time constraints.

Risk-based turnaround scoping. We model which units MUST be inspected (high PoF × high CoF) vs. which can safely defer to next cycle. Includes budget optimization tool.

Risk-based scoping typically shifts 30-50% of inspection effort from low-risk to high-risk items, improving coverage where it matters most.

API 510, OSHA PSM, PER requirements—all require documented risk assessments. Manually maintaining compliance records across thousands of pressure boundaries is impossible.

Structured compliance tracking. Every asset has a full audit trail: RBI calculations, inspection history, deviations, and documented risk justifications. One-click export for audits.

Full traceability from risk calculation to inspection record enables efficient audit preparation and regulatory response.