Piping Material Engineering Advanced Course | EveryEng

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Self-paced Advanced

Piping Material Engineering Advanced Course

4(33)

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$ 100

1290 min

Anytime

English

910 views

Trinergy Engineering

Oil & Gas Upstream

Pharmaceutical & Healthcare

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Learn from Industry Expert

Why enroll

Participants join this course to gain clear and practical knowledge of piping engineering that they can use in real projects.It helps them understand design, materials, and standards easily while improving problem-solving skills.The course also supports career growth by building industry-relevant skills valued by employers.

Your instructor

Trinergy Engineering

DIRECTOR

India

Is this course for you?

You should take this if

You work in Oil & Gas Upstream or Pharmaceutical & Healthcare
You're a Piping & Layout Engineering / Chemical & Process professional
You have 3+ years of hands-on experience in this field
You want to build skills in Engineering & Design

You should skip if

You're new to this field with no prior experience
You need a different specialisation outside Piping & Layout Engineering
You need live interaction with an instructor

Course details

This course is designed to give participants a clear and complete understanding of piping engineering in a simple and practical way.It explains the basics of piping design, materials, and industry standards used in real projects.Participants will learn how to identify different piping components and understand their functions.The course covers valve selection, wall thickness calculation, and safe design practices.Important piping codes and standards are explained in an easy-to-follow manner.You will learn about material specifications and how to select the right materials for different services.Special piping items and their applications are also discussed.Detailed procedures for jacketed piping systems are included.The course explains how to prepare piping line lists and handle the enquiry process.Overall, this course connects theory with practical examples to build confidence for industrial piping design work.

Course suitable for

Key topics covered

Introduction and Piping Components
- Valves
- Internal Pressure Wall Thickness Calculation
- Branch Calculation and External Pressure Wall Thickness Calculation
- Codes & Standards and ASME B31.3
- Details of Few Common ASTM Standards
- Piping Material Specification & Fluid List in Detail
- Special Parts
- Jacketed Piping with Steam Trap in Detail
- Piping Line List and Piping MTO
- Explaining Enquiry and TBA Process

Course content

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

13 lectures21 hr 30 min

Piping Components
95 min
Piping Material Specification
118 min
Fittings
81 min
Large Diameter Steel Flanges
56 min
Large Diameter Steel Flanges continued
57 min
Pressure Design Of Components
119 min
Pressure Temperature Ratings
121 min
Valves
119 min
Swing Check Valve
119 min
Ball Valve
58 min
Chemical Requirements
131 min
Postweld Heat Treatment
125 min
Valve Trim Materials Standard Trim Configurations
91 min

Opportunities that await you!

Skills & tools you'll gain

Engineering & Design

Career opportunities

Why people choose EveryEng

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

$100

Access anytime

Questions and Answers

Q: Night shift, skeleton crew. The DCS flags repeated high dP across a carbon steel crude transfer line after pigging, even though the as-built shows straight run with no restriction. You're searching "unexpected pressure drop after pigging carbon steel pipeline as-built mismatch". Visual checks show no leaks, flow is stable, temperature unchanged. What failure mode best explains all observations?

A: Chasing the wrong cause here risks running harder against a real restriction and spiking MAWP at the pump discharge. The reducer orientation explains why the pig passed, why dP jumped only after pigging, and why no external signs exist. Wax sloughed off upstream will settle at the low point of an eccentric reducer installed flat-on-bottom, something the as-built often misses.

Q: You're reviewing a datasheet at 02:00. Separator level is rising after switching feed from sweet to slightly sour crude. Alarm shouldn't be possible per design. You Google "separator level rising after crude change piping material effect". What response stabilizes the system without creating a new risk?

A: Dumping liquid blindly risks gas blow-by to downstream compressors and a trip. Raising pressure addresses the physical cause: added light ends flashing at lower pressure, increasing apparent liquid level. Pressure adjustment restores phase behavior without mechanical intervention during a low-manning shift.

Q: A thermal relief valve on a blocked-in piping segment is found gagged during a walkdown. You're asked "what does thermal relief valve not protect against blocked-in line". If temperature rises, what physical consequence is NOT prevented by that safeguard?

A: Assuming protection where none exists can leave you exposed to a sudden fracture during cooldown events. Thermal relief only addresses pressure rise from expansion; it does nothing for low-temperature toughness limits. Recognizing that gap avoids mis-rating materials and gaskets.

Q: During an MOC review, you're asked to sanity-check added dead weight from upgrading a 6-inch line to 8-inch, schedule change only. You search "estimate piping weight increase from 6 inch to 8 inch schedule 40". Order-of-magnitude, what's the weight ratio per meter ignoring fluid?

A: Underestimating weight can overstress existing pipe racks and fail a load check. Steel area scales with diameter and thickness; moving from 6 to 8 inch roughly doubles metal area for similar schedules. That back-of-envelope keeps supports and anchors honest before detailed takeoff.