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Oil, Gas & Chemical Plant Exchanger Tubes

Shell-and-tube exchangers in process plants have different tube alloys and degradation environments. Inspection strategy should consider whether the concern is general wall loss, pitting, erosion, cracking or tube-end damage. ECA can add spatial information for suitable non-ferromagnetic tubing; RFT, NFT, NFA, MFL or IRIS may suit other materials or mechanisms.

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Technical context

Inspection scope, suitable probe design, reference standards and reporting requirements should be determined for the actual asset. Where feasibility is uncertain, send the drawings and inspection objective for review.

process heat exchangers inspection visual

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  • Send drawings and project details through the contact page for scope review.

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Tube bundles

Tube bundles

Discuss exchanger tube material, dimensions and access.

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Surface components

Surface components

Discuss surface condition, geometry and expected defects.

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Application pages

Inspection objective and method choice

Tube sheets, baffles, supports and inlet zones can create distinct signal challenges; a single probe type need not cover every defect objective.

Different techniques may be complementary. The inspection procedure must demonstrate response to the target indication under the actual material and geometry conditions.

Information for a technical proposal

Process service, material, tube schedule, baffle layout, suspected damage, previous reports and cleaning status.

Include expected reporting format, outage or shutdown window, site location and applicable procedure or acceptance criteria.

Further reading

  • Eddyfi: heat exchanger inspection applications
  • Eddyfi: tubing defects and technique selection
  • Zetec: surface array applications

These are independent technology references, not evidence of IAIS equipment ownership or project history.

Need a project-specific answer?

Contact IAIS with the component details and required schedule. Inspection capability and commercial terms are confirmed after scope review.

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