ASME PRESSURE VESSELS
The scope of this presentation is to present basic information and understanding of the ASME code for the design of pressure vessels for the chemical and process industry as applicable in the United States and most of North and South America. For more information about our products, heavy plate & custom fabrication services or fabrication capabilities contact us today!
API 579-1 Fitness-For-Service (FFS) – Pitting Assessment
Did a recent external inspection on an exchanger reveal pitting corrosion under the insulation? Did a unit upset result in internal pitting on the bottom head of the reactor? If you answered yes to these questions, or if pitting corrosion due to other factors is occurring in your plant, an API-579-1 FFS pitting assessment may provide an alternative to costly repairs.
In this article, we will take a look at evaluating widely scattered pitting by applying API 579-1 / ASME FFS-1 2007 Fitness-For-Service Level 1 assessment procedures.
What is Pitting?
Pitting is defined by API 579 as localized regions of metal loss characterized by a pit diameter on the order of the plate thickness or less. Widely scattered pitting is pitting that occurs over a significant region of the component.
Level 1 Pitting Assessment Limitations
Level 1 pitting assessments are permitted only if certain conditions are satisfied. The complete list of limitations in Parts 2 and 6 of API 579 should be reviewed before proceeding with a Level 1 pitting assessment. Some of the limitations are:
- The pitting damage must be:
- located on only one surface of the component, e.g., internal or external
- composed of many pits
- The component is:
- a type A component subjected to internal pressure. These are components that have a design equation that specifically relates pressure or liquid fill height, and other loads, to a required wall thickness, such as pressure vessel cylindrical and conical shell sections
- not in cyclic service
- not operating in the creep regime
- considered to have sufficient material toughness
Level 1 Methodology
In a Level 1 assessment, surface damage, quantified by the pitted area and pit depth, is compared to standard pit charts to determine acceptability. If the depth of all the pits is less than the specified corrosion allowance, then a pitting assessment is not required.
However, if the pit depth exceeds the corrosion allowance, then a pitting assessment should be considered. Note that for a Level 1 assessment, the future pitting damage (FCA) is assumed to be zero, e.g., pitting corrosion due to corrosion under insulation that has been mitigated by application of an epoxy coating and permanent removal of the insulation. Below is a summary of the assessment process. Details of the process, as well as the nomenclature, can be found in API 579-1 Part 6.
- Review the limitations for a Level 1 assessment
- Characterize the pitting damage, e.g., diameter, area, depth
- Evaluate the component as detailed in API 579 Paragraph 6.4.2
- Determine the uniform measured thickness trd away from the pitted area
- Calculate the MAWP using the thickness measured above
- Locate the area of the component that has the highest density of pitting damage
- Obtain photographs and rubbings of the damaged areas
- Determine the maximum pit depth wmax o Determine the ratio below. If Rwt < 0.2, the Level 1 assessment is not acceptable
- Compare the surface damage from the photographs and rubbings to the standard pit charts and select the chart that approximates the actual damage of the component. Examples of different grades of pitting are shown below, where black indicates pitting of the component.
- Determine the remaining strength factor (RSF) from the table related to the pit chart selected. A typical RSF table is shown below.
- If RSF > RSFa, then the pitting damage is acceptable for the MAWP calculated above. RSFa is the allowable remaining strength factor. It is typically set at 0.90 for ASME Section VIII Division 1 equipment.
- If the pitting is unacceptable:
- Repair, rerate or replace.
- Lower the FCA.
- Conduct a Level 2 assessment.
This is presented to you as a service from BOARDMAN, LLC located in Oklahoma City, Oklahoma.
Since 1910, Boardman has been a respected custom fabricator. We take pride in our ability to take the most stringent specifications and requirements to provide a high quality solution to our customers. With more than 75 years of ASME Section VIII, Division I engineering experience, we have the unique ability to provide custom solutions to our customers.
Fabricated Projects Include:
- Trayed Towers & Columns
- ASME Pressure Vessels
- Molecular Sieves
- Rotary Dryers & Kilns
- API Tanks
- Acid settlers
- Stacks, Scrubbers
- Thermal Oxidizers
- Accumulators, Condensers
The sizes of these projects are up to 200’ in length, 350 tons, 16’ diameter and 4” thick.
BOARDMAN, LLC is available for shop tours and Pressure Vessel and Static Equipment Fabrication Classes.