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Methodology Step 1
  • 09 Aug 2024
  • 2 Minutes to read
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Methodology Step 1

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Article summary

 Step 1 Define the Asset (and set up the Hierarchy):

Below the Step 1 Methodology is described. See also Software Step 1.

Set up the IMS Hierarchy: Create Corrosion Loop, FLOC, Equipment, Circuits, Components

To set up the IMS hierarchy, the Plant, Site and Unit must first be setup. This is normally done by the CSA. When this is in place, the Corrosion Loop, FLOC, Equipment, Circuits and Components can be set up in IMS. This setup is typically also done by the CSA or INSP ADMIN. 

Collect Asset Information, Verify and Store in IMS

Collect all relevant asset information:

  • Equipment data, e.g.,
    • Asset type,
    • Tag names,
    • Installed date,
    • As-built materials,
    • Main Components,
    • Location on the site,
    • Process design conditions;
    • Process as-operated, including excursions and special operating modes, etc.
  • Documents (latest revision), e.g.,
    • Process Engineering Flow Schemes (PEFS) with their latest revision;
    • Documentation of historical plant changes and evidence of MOC;
    • Mechanical design of Equipment (general arrangement, Isometrics, etc.);
    • Material selection (reports);
    • Inspection history and records, including Wall Thickness measurements.

This asset data should be stored in IMS, mainly as specifications and attachments and verified for correctness prior to identification of potential Degradation Mechanisms.

Specific Guidance Summary

For additional information with regards to defining the Special Emphasis Equipment / Components in IMS, refer to Guidance per Special Emphasis and Guidance per DM (see the table below).

Specific guidance summary - Defining the Asset:

DM / Special Emphasis Component
Description

Corrosive Deadleg

Modelled as a separate Component. Corrosive Deadlegs with CMLs should be tracked in a Circuit separate from the mainline piping.

Corrosive Injection and Mixing Points

Potentially Corrosive vs Non-Corrosive explained. Potentially Corrosive IP/MPs are identified in IMS as unique corrosion Circuits.

Dissimilar Welds

Modelled as a separate Component of either a Piping System or an Equipment.

Heat Exchanger Bundles (Shell and Tube)

Typically, Heat Exchanger Channel and Shell Components are monitored by different Circuits.

Pressure Relief Devices 

Add Component of Type BODY to PRV Equipment. A CL must always be assigned to this Component. This can be the CL of the Equip. that the PRV protects or all PRVs for unit can be placed in one dedicated CL.

Small Bore Connections

Small Bore piping is ≤ 2". Mostly these are Deadlegs. In some cases, they could be the main pipe. In these cases, the bleeders/vents would be the Deadlegs.

Tanks

Load Cases calculations apply to tanks. For these additional specs and other data are data are needed.

Thermal Injection Points and Mixing Points

For piping, Thermal IPs and Thermal MPs can be modelled as separate Components.

Underground Piping

Use Component type Piping UG.

Corrosion Under Insolation (CUI)

The CCAM priority is assessed on the Equipment. It is advised to manage CUI using CCAM for CCAM priority 1 and S-RBI for priority 2. For all Priority 2 Components (i.e., S-RBI), the “Component CUI material” must be applied, since this will determine the StF questionnaire (see Step 7). For Duplex, select the SS CUI material.


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