| API 579-1/ASME® FFS-1 Calculations With Detailed Reports |
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| Part 3 – Brittle Fracture, Levels 1 and 2, includes Minimum Safe Operating Temperature assessments and curves |
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| Part 4 – General Metal Loss, Levels 1 and 2 |
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| Part 5 – Local Metal Loss, Levels 1 and 2 (includes groove-like flaws and a Level 3, FEA based assessment) |
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| Part 6 – Pitting Corrosion, Levels 1 and 2 |
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| Supplemental loads for Part 5 and 6 |
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| Combined Local Metal Loss and Pitting |
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| Part 8 – Out-Of-Roundness, both simplified Dmin/Dmax and multiple point Dmin/Dmax assessments |
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| Part 9 – Crack-like Flaws (Level 1), Combined Crack-like Flaws and Local Metal Loss (Level 2, FEA based) |
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| Part 10 – Creep assessments, Levels 1 and 2 |
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| Part 11 – Assessment of Fire Damage, Levels 1 and 2 |
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| Part 12 – Dents, Gouges and Dent-Gouge Combinations, Levels 1 and 2 |
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| API 579-1 remaining life calculations |
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| 3D visual confirmation that equipment and flaws are input correctly |
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| Integrated 3D Inspection Data Management System (IDMS) |
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| Automatic and manual inspection point (CML) placement |
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| Attach images and related documentation to any CML |
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| User defined CML data fields, as many as required, provide information tracking flexibility |
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| Governing CML locations highlighted on 3D models |
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| API 510, API 570 and API 653 calculations and reports |
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| Minimum thickness calculations (tmin) |
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| Determines inspection schedules (time based) |
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| Quickly perform pressure vessel re-rating simulations |
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| 3D plant modeling for Fixed Equipment Engineers |
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| Vessel Wizard for fast vessel model creation |
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| Intuitive user interface for quick piping layout creation |
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| Ability to copy and paste piping components |
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| Supporting ASME calculations and reports |
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| ASME VIII-1 (Division 1) |
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| ASME VIII-2 (Division 2), includes Class 1 and Class 2 vessels |
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| ASME UHX heat exchanger calculations |
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| Multiple ASME VIII Code Editions in one program (1995 – present) |
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| Multiple ASME II-D Editions, including consideration of table notes (1995 – present) |
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| API 570 and API RP 579/ASME FFS-1 piping tmin’s calculated using ASME B31.3 and ASME B31.4 rules |
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| TEMA 7th, 8th & 9th Ed. heat exchanger calculations |
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| NBIC R-1, R-2 Repair Forms |
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| ASME A-1, A-2 Alteration Forms |
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| Includes all COMPRESS features and options |
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| Supports equipment design for new construction projects |
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| Process piping inspection checklists with user-defined commentary |
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| Associate API RP 970 Corrosion Control Documents with 3D process loops |
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| Brittle fracture checks as recommended by The National Certified Pipe Welding Bureau (NCPWB) |
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| FEA on support saddles, clips (on shells and heads) and pipe shoes |
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| Minimum pipe structural thickness check per API RP 574 |
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| Short term, long term and user-defined corrosion rate trend analysis |
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| Mechanical Integrity RAGAGEP comply with OSHA 1910.119(d)(3)(ii) and EPA Title 40 Part 68 |
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| Tmin calculations use local CML joint efficiencies to extend vessel remaining life and inspection intervals |
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| WRC-489 – Paragraph 4.2.8 Creep and Stress Rupture check |
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| Documents undocumented pressure vessels |
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| API 653 tank bottom patch plates (repair plates) |
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| Exports piping showing flaw locations and types to SOLIDWORKS for fast creation of 3D PDF documents |
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