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Full Course on Storage Tank Inspection banner

Full Course on Storage Tank Inspection

Full Course on Storage Tank Inspection banner
Live online Basic

Full Course on Storage Tank Inspection

4(6)
1919 views
₹ 2500
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Next month
1919 views
Jyoti Swarup
Jyoti Swarup
  • 7-day money-back guarantee
  • Session recordings included
  • Certificate of completion
Volume pricing for groups of 5+

Is this course for you?

You should take this if

  • You work in Oil & Gas Upstream or Pharmaceutical & Healthcare
  • You're a Chemical & Process / Mechanical Engineering professional
  • You prefer live, instructor-led training with Q&A

You should skip if

  • You need a different specialisation outside Chemical & Process
  • You need fully self-paced, on-demand content

Course details

To include types of tanks, tank degradation mechanisms, reasons for inspections difference between in-service and out of service Inspections calculations of shell thicknesses, minimum thickness required before failure, difference in bottom plate top side and bottom side corrosions, types of corrosions, methods of inspections and automations. Also In service and Out of service inspection techniques.


This course is combination of multiple modules, total 7 hours of course.

Course suitable for

Key topics covered

Types of Storage Tanks/ Selection Criteria

Design of Tank Terminal facilities

Tank Appurtenances/ Floating Roofs

Tank Degradation Mechanisms

Internal and External Corrosion

Reasons for Inspections

Routine Inservice Inspections

Out of Service Inspections

Tank Shell Plate thickness calculations

Bottom Plate Soil side and product side corrosions

Leak Detection Methods

Various Methods of tank Inspections

Differential Shell / Bottom settlement

Minimum Thickness Bottom Plate

API Std 653 Inspection Check Lists

Opportunities that await you!

Career opportunities

Training details

This is a live course that has a scheduled start date.

₹2500

Early bird

Coming in Next Month

Questions and Answers

A: The GA controls spatial envelope and interference checks, which is where projection length bites you during inspection and maintenance. The schedule often feeds procurement and can lag late changes. Option B feels safe because API 650 does give minimums, but minimum code compliance doesn't override drawing precedence when access and insulation clearance are at stake. Option C sounds procedurally clean, yet treating every mismatch as a hard NCR two weeks from MC ignores document hierarchy used on EPC jobs. Option D leans on field reality, but accepting as-built without reconciling drawings breaks traceability and future inspection planning.

A: As water displaces air, any vent restriction converts fill rate into pressure rise. Thin shell tanks don't tolerate much. Option B mirrors pump troubleshooting instincts, but higher rate accelerates pressure rise. Option C sounds reasonable because water is incompressible, yet it's the trapped air pocket that sets the failure path. Option D mixes up sequences; vacuum becomes an issue on draining or cooling, not during an active fill with a blocked vent.

A: Conservation vents address breathing losses, overpressure, and vacuum scenarios. Option A and D sit squarely in that envelope. Option C is a classic vacuum case when pump-out outruns air ingress. Option B feels tempting because fire is a pressure driver, but shell buckling under fire is governed by heat weakening and external loads; a stuck vent doesn't shield you there.

A: Lap orientation affects crevice exposure and how water and sludge migrate, which steers corrosion. Option B borrows from fatigue logic, but bottom lap orientation doesn’t reclassify weld strength under static storage. Option C stretches geotechnical impact beyond reality; orientation doesn’t shift load distribution. Option D overstates NDT sensitivity; MFL can still read, but interpretation without correct orientation skews risk ranking.