Fixed Equipment in High Temperature Service

Creep is a high temperature, time dependent failure mode that limits the life of stressed components. Creep failures commonly limit the useful life of heater tubes but can be the governing failure mode for any high temperature pressure vessel or pipe. The temperature at which creep becomes a concern depends on material and is generally around 700 degrees F. for carbon steels. ASME Code allowable (tensile) stresses consider creep by assuming a 100,000 hour service life and limiting the allowable stress such that creep deformation (strain) does not exceed 1%. Note also that the external pressure charts in the ASME Code do not consider creep buckling and are not used in these temperature ranges.

INSPECT makes performing Part 10 Level 1 and Level 2 Creep Assessments easy and fast. All API 579 calculations are reported in detail.
INSPECT Performs Part 10 Creep Assessments and Produces Detailed API 579 Reports

INSPECT and Part 10 Creep Damage Assessments

INSPECT makes performing Part 10 Level 1 and 2 creep assessments easy and fast.  It provides a consistent means of recording equipment operating histories and calculations. All calculations are reported in detail along with any associated charts.  In addition, you don’t need to spend your time moving information between programs manually to create reports. INSPECT’s all-in-one system creates professional looking, detailed reports with one button click.

Individual components or complete vessels can be modeled and assessed as required. A convenient creep summary report lists the components included along with applicable Pass/Fail conclusions. For Level 2 the MPC Project Omega, Larson-Miller Minimum, and Larson-Miller Average methods are available and can be run at the same time providing a very comprehensive report.

Request More Information

Performing API 579 Part 10 Creep Damage Assessments With INSPECT

Visit the following resources for more information on creep:

Creep and Creep Failures by The National Board of Boiler and Pressure Vessel Inspectors

Creep in Heater Tubes and Other Components by Inspectioneering

INSPECT Featured Capabilities

Part 3 API 579 Part 3 Ensure your operating procedures limit the risk of brittle fracture by automatically running Part 3 assessments. API 579-1 Part 3 MAT Curves Part 4 and 5 API 579 Part 4 & 5 Perform general and local metal loss assessments and quickly generate detailed reports. INSPECT performs API 579 FFS assessments and shows flaws on the 3D model Part 6 API 579 Part 6 INSPECT performs level 1, 2 and 3 pitting assessments and generates detailed API 579 reports with a click of a button. Combined Pitting and Local Metal Loss Flaws are Considered Part 7 API 579 Part 7 Perform Level 1 and 2 assessments from Hydrogen Induced Cracking (HIC) and Hydrogen Blister damage. API 579-1 Part 7 Hydrogen Cracking and Blister Damage Part 8 API 579 Part 8 Ensure that vessels subject to external pressure are within the allowed roundness tolerance with out-of-roundness assessments. API 579-1 Part 8 Out of Roundness Part 9 API 579 Part 9 Crack assessments quickly determines which crack-like flaws can be safely left in service and which require more investigation. API 579-1 Part 9 Crack-like flaw assessment Part 10 API 579 Part 10 Perform creep damage assessments by recording equipment operating histories and calculations. API 579-1 Part 10 Creep Damage Part 11 API 579 Part 11 Perform fire damage assessments and document conclusions in a consistent series of data entries and reports. API 579-1 Part 11 Fire Damage Assessments Part 12 API 579 Part 12 Perform Part 12 assessments and generate detailed API 579 reports. Level 1 and 2 dent, gouge and dent-gouge combinations are available. API 579-1 Part 12 dialog Part 13 API 579 Part 13 Model laminations and provide rapid results so you can make the necessary mediation decisions with confidence API 579-1 Part 13 Lamination Diagram API 510 API 510 Address in-service activities such as inspection, remaining life determination and repair. API 510 API 570 API 570 3D inspection data management and calculations simplify compliance with the requirements of the API-570 Code. API 570 API 653 API 653 Track tank thickness inspection measurements and provide calculation reports. API 653 Storage Tank Evaulations Gage Gage Integration Set up and retrieve inspection grids from thickness gages fast and easy. Thickness Gage Integration in INSPECT OSHA OSHA 1910 Meet the Mechanical Integrity requirements of OSHA1910.119 (j) and EPA Title 40 part 68.73. OSHA standards in COMPRESS Undocumented Undocumented Vessels Pressure Vessel Inspection Code requires owners to maintain permanent, progressive records as listed in API 510 Section 7.8 Undocumented Vessels in INSPECT IDMS The INSPECT IDMS Show condition monitoring locations (CML’s) and API 579-1 flaws directly on pressure equipment models. Inspection Data Monitoring System IDMS MSOT Auto-Refrigeration MSOT curves are employed to determine which process conditions put equipment at risk of failure by brittle fracture. Minimum Safe Operating Temperature (MSOT) curve in INSPECT Older Codes Old ASME® Codes Supported Increase vessel life automatically by using the higher allowable stresses per NBIC Section 3.4. Codes menu API 510 Pressure Relieving Devices Easily model pressure relieving devices (PRDs) on your fixed equipment. Easily model pressure relieving devices (PRDs) with INSPECT Excel Integration Excel Integration Export and import thickness inspection grids to and from Microsoft Excel. Excel Integration with INSPECT