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Storage tank design with special focus on Cryogenic fluids

Storage tank design with special focus on Cryogenic fluids banner
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Storage tank design with special focus on Cryogenic fluids

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Jyoti Swarup
Jyoti Swarup
  • 7-day money-back guarantee
  • Session recordings included
  • Certificate of completion
Volume pricing for groups of 5+

Why enroll

API 650 tanks design concepts.

Storage Tank Accessories

Typical sizes, design pressures, horizontal and vertical Vacuum insulated tanks with inner/outer shell in SS/CS

Evaporation rates etc.

API 620 design Annex Q and R and API 625 tanks

Use of European codes for such tanks

Standard vacuum insulated tanks in the market

Large flat bottom storage tanks details.

Is this course for you?

You should take this if

  • You work in Oil & Gas or Pharmaceutical & Healthcare
  • You're a Chemical & Process / Mechanical 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

Course suitable for

Key topics covered

Types of above ground storage Tanks

Applicable API codes

Difference: API 620 and API 650 tanks

Tank Shell, Bottom Plate design

API 625 Storage concepts

Cryogenic Storage tanks types

Shop or site built?

Vacuum insulated tanks

Pressure Stretching

Flat Bottom tanks

Materials for tanks

Compression Rings

Shell connections

Insulations

Reference Codes and Standards

Opportunities that await you!

Career opportunities

Training details

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

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Why people choose EveryEng

Industry-aligned courses, expert training, hands-on learning, recognized certifications, and job opportunities-all in a flexible and supportive environment.

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Questions and Answers

Q: You're on night shift and typing "estimate LNG tank boil off gas rate per day quick check" while staring at a 160,000 m³ full-containment LNG tank. The DCS shows average BOG at 0.18% vol/day. As-built insulation heat leak is 8 W/m², tank diameter 80 m, straight-side height 40 m. No recondenser upset flagged. What's the most defensible back-of-envelope position?

A: A: Surface area ~15,000 m² times 8 W/m² is ~120 kW. Divide by LNG latent heat and inventory, you land near 0.1%/day. That's the sanity check you do at 2 a.m. B: Vapor density doesn't rescue the energy balance; heat leak still rules. C: Roof losses matter, but not enough to double the rate at this scale. D: CFD refines it later; this call is about order-of-magnitude risk triage.