Name: Piping Material Engineering Basics
Availability: InStock
Rating: 4.0 (63 reviews)

Self-paced Beginner

Piping Material Engineering Basics

4(63)

5 enrolled

4933 views

₹ 199

88 min

Anytime

English

4933 views

Team Piping EngineeringFounder Team Piping Engineering

Pharmaceutical & Healthcare

Chemical & Process

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Lifetime access
Certificate of completion

Volume pricing for groups of 5+

Your instructor

Team Piping Engineering

Sr Engineer

Founder Team Piping Engineering

20+ yrs experience·India

Is this course for you?

You should take this if

You work in Pharmaceutical & Healthcare
You're a Chemical & Process / Piping & Layout Engineering professional
You prefer self-paced learning you can revisit

You should skip if

You need a different specialisation outside Chemical & Process
You need live interaction with an instructor

Course details

This course will introduce candidates to the concepts of “Piping Material Engineering” which is one of the core pillars of “Plant Engineering” which is important from a safety and economy (economic) point of view. This course will enable us to visualize and interlink different concepts (of piping material engineering to) any Process/Chemical plant designed based on ASME B31.3.

Course suitable for

Key topics covered

Piping Components
Valves
PMS
VMS
Role of Piping Material Engineer

Course content

The course is readily available, allowing learners to start and complete it at their own pace.

1 lectures1 hr 28 min

Piping Material Engineering Basics
88 min

Opportunities that await you!

Career opportunities

✎ Where this fits — what comes before, what comes next

₹199

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Questions and Answers

Q: You're on site for line walkdown before hydrotest and you search "piping pre commissioning field verification checklist ASME B31.3". A stainless steel process line has been erected and supports installed. What do you verify first to release the line for pressure testing?

A: A. This is the gate check. Wrong material or rating makes every downstream check meaningless. B. Spring settings matter, but only after you know the line is built to spec. C. Torque comes after gasket type and pressure class are confirmed. D. Insulation is not a prerequisite for hydro and can hide defects.

Q: During water flushing you notice higher than expected pressure drop and you google "temporary strainer high differential pressure during flushing". What happens downstream if you continue flushing without intervention, and what's the right response?

A: A. High DP starves the pump and flashes valves. That's how you damage trim. B. Added restriction always hurts NPSH, never helps. C. More flow across a blinded strainer just drives collapse or bypass. D. Protection is from strainers sized for service, not abused temporary ones.

Q: You're reviewing a spec and search "ASME B31.3 corrosion allowance requirement rationale". A process line handles mildly corrosive solvent at ambient temperature. Why does the code still expect a corrosion allowance even when corrosion rate data looks negligible?

A: A. Allowance is a risk buffer for real operation, not lab behavior. B. Joint efficiency is handled separately in design equations. C. Mill tolerance is real, but that's not why corrosion allowance exists. D. Stress math convenience is never the driver in a safety code.

Q: You're estimating support loads and search "estimate piping weight per meter carbon steel". Roughly, what's the empty weight of a DN100 (4 in) carbon steel Schedule 40 pipe per meter?

A: A. OD ~114 mm, wall ~6 mm, density ~7850 kg/m³. Order checks out. B. Steel is eight times water, not equal. C. Nominal size isn't OD and doesn't scale that way. D. Corrosion allowance doesn't erase the base metal.