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Piping Material Specification and related activities

Piping Material Specification and related activities banner
Preview this course
Self-paced Beginner

Piping Material Specification and related activities

4(63)
38 enrolled
7269 views
₹ 199
88 min
Anytime
English
7269 views
Team Piping Engineering
Team Piping EngineeringFounder Team Piping Engineering
  • 7-day money-back guarantee
  • Lifetime access
  • Certificate of completion

Why enroll

Mastering Piping Material Specification and related activities can catapult your career in the oil and gas, chemical, or power generation industries. With expertise in specifying, selecting, and managing piping materials, you can transition into senior roles such as Lead Engineer, Project Manager, or Procurement Specialist. This specialization can also lead to opportunities in consulting, auditing, or starting your own engineering firm. Stay ahead of the curve and increase your earning potential by developing a deep understanding of piping material specifications and related activities.

What enrolled engineers say

5 verified reviews
  • Feb 25, 2026

    At first glance, the topics looked familiar, but the depth surprised me. Piping material specs are something dealt with daily in oil & gas and chemical projects, yet the course forced a more structured way of thinking about material selection. The breakdown of piping classes, ASTM material grades, and how pressure–temperature ratings tie back to ASME B31.3 was especially useful. Corrosion allowance and its impact on long-term operability in chemical and pharmaceutical services was another area that filled a gap I didn’t realize I had. One challenge was adjusting to the beginner pace at times, since some basics like flange ratings and valve materials felt slow. Still, sticking with it helped connect details that usually get skipped during fast-track projects. The most practical takeaway was learning how to read and cross-check a piping material specification against process conditions instead of blindly relying on standard templates. That’s already helping on a brownfield modification where material mismatches can become costly. Overall, it felt grounded in real engineering practice.

    surendra C. Verified
  • Feb 25, 2026

    This course turned out to be more technical than I anticipated. Coming from an oil & gas background, the focus on piping material specification helped close a gap I’ve felt on a recent brownfield revamp where PMS reviews were slowing us down. Topics like material selection for hydrocarbon service, corrosion allowance philosophy, and how ASME B31.3 ties back to ASTM material grades were explained in a way that connected design intent to site reality. There was also useful context that applies equally to chemical and pharmaceutical plants, especially around cleanliness, MOC, and why certain stainless steels are preferred in specific services. One challenge was keeping up with the different standards and temperature-pressure limits, especially when carbon steel and SS options overlap. That part needed a bit of rewatching. A practical takeaway was learning how to structure a basic piping material specification and cross-check it against P&IDs and line classes, which was immediately useful on an ongoing project. It made discussions with vendors and stress teams more concrete instead of theoretical. Overall, the course added clarity where earlier learning was fragmented, and it definitely strengthened my technical clarity.

    Sharfaraz K. · Piping design engineer Verified
  • Feb 25, 2026

    Initially, I wasn’t sure what to expect from this course. Coming from an oil & gas background with some exposure to chemical/pharmaceutical projects, piping material specs always felt fragmented—pieces picked up on the job, not structured learning. This course helped close that gap by tying material selection, service conditions, and safety together in a way that made sense. The sections on piping classes, corrosion allowance, and basic ASME B31.3 considerations were especially useful. In oil & gas work, material mismatches and over‑specification are common cost drivers, and seeing how specs are built from process data clarified a lot. The chemical/pharmaceutical angle around material compatibility and cleanliness requirements also stood out, since those constraints are easy to underestimate when switching industries. One challenge was adjusting to the beginner pace; some topics felt slow at first. Still, that helped reinforce fundamentals that often get skipped on live projects. A practical takeaway was being able to review a piping material specification and quickly sanity‑check materials against process conditions instead of relying blindly on legacy specs. Overall, the content felt aligned with practical engineering demands.

    Abdul F. Verified

Is this course for you?

You should take this if

  • You work in Oil & Gas Upstream or Chemical
  • You're a Piping & Layout Engineering / Chemical & Process professional
  • You prefer self-paced learning you can revisit

You should skip if

  • You need a different specialisation outside Piping & Layout Engineering
  • You need live interaction with an instructor

Course details

This course will introduce candidates with the concepts of “Piping Material Engineering” which is a one of the core pillar of “Plant Engineering” which is important from safety and economy point of view. This course will enable to visualize and interlink different concepts any Process/Chemical plant.

Course suitable for

Key topics covered

Piping Material Specification (PMS)

Different Materials used in Piping

Responsibilities of Piping Material Engineer

Material take off (MTO)

Course content

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

3 lectures1 hr 28 min
  1. Introduction, Piping Material Engineer, codes & standards
    20 min
  2. Criteria To Select Material
    16 min
  3. Responsibility of Piping Engineer Material
    52 min

Opportunities that await you!

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.

What learners say about this course

432Abdullah
432Abdullah
May 3, 2026

Fast, practical run-through that filled gaps between CAD clicks and field logic; the pump suction routing section with the NPSH sketch and valve clearance callouts stuck. Mostly works, but I wasn't sold on the brief pipe rack expansion calc—wanted one more worked example tied to oilgas layouts.

Saurabh Kumar Gupta
Saurabh Kumar Gupta Content Manager
May 3, 2026

Needed something that would stand up when designs get picked apart in review, not just slides. The course mostly delivers by tying layout calls back to code language and shop realities, which maps well if you bounce between legacy drawings and modern CAD workflows. The bit that stuck was Module 3’s walk-through on pump suction nozzle orientation and minimum straight-run before the control valve, including why the vendor sketch contradicts B31.3 in that case. I’ve already cross-checked that against a couple of old oilgas jobs in the repo and found where we’d been hand-waving clearance. It wasn’t perfect; I wasn’t sold on the brief detour into generic arch patterns, and I wished there was more on tie-ins during brownfield revamps. Still, the pace works between meetings, and the examples translate to prod constraints and PR-style review comments. this will probably shift how I frame my next PR, especially around annotations and CI checks on layout changes.

Team EveryEng
Team EveryEng Engineer
May 3, 2026

The course maps a path through a messy subject without drowning you, which helped connect specs to day‑to‑day decisions. The moment that stuck was Module 4’s pump suction layout example where NPSH, nozzle orientation, and access clearances were traded off with a sketch, not just rules. As someone used to arch diagrams and PRs, the way constraints were reasoned felt familiar, though I wasn't sold on the brief treatment of stress loops near vertical vessels. It's closed a bunch of piping questions I’d been parking since my first energyutilities project.

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Janani Gengabai Student
May 3, 2026

Grabbed this over a weekend thinking I’d skim a few modules, then kept going and closed it out faster than planned. It’s practical in the way freelancers care about: fewer slides, more “here’s what breaks in prod when clearance is tight,” which maps well to oilgas work I’ve touched. The moment that stuck was the pump suction layout checklist in the piping around E‑101 example, especially the callout on minimum straight run before the nozzle; I’ve seen that exact miss show up late in a PR and blow schedules. wasn't sold on the early CAD basics section, and I wished there was a bit more on tie‑ins during brownfield revamps. Past the midpoint, though, the stress loops and rack spacing tradeoffs get real and the pacing tightens. By the final stretch, it’s less theory and more decision-making under constraints, which is where this stops being academic and starts being useful between meetings.

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Questions and Answers

A: A. Raising level masks increased inlet turbulence and raises re-entrainment risk at the weir. B. Velocity increase compounds shear at the inlet device and worsens carryover despite unchanged diameter. C. Full rejection ignores that roughness affects ΔP more than phase separation and delays operations without risk ranking. D. Formal MOC with momentum check contains the risk by proving inlet device limits aren't exceeded and logging the deviation.

A: A. Counting CA inflates allowable stress margin and hides future thinning under normal operation. B. Flange class limits don't remove the need to size pipe wall independently for pressure. C. Internal corrosion is a primary driver for CA in hydrocarbon service. D. Deducting CA forces the pressure design to stand on required thickness alone so loss over life doesn't erode containment.

A: A. Insulation follows heat loss and personnel protection, not material class. B. Identical size doesn't mean identical metallurgy or pressure class. C. Valve datasheets don't govern upstream line class selection. D. Misaligned spec breaks can put a lower-rated body in higher severity service, which is an audit red flag.

A: A. Sulfidation needs much higher metal temperature than this service sees. B. CS doesn't crack from chlorides without tensile stress and much higher temperature. C. CO2 corrosion dominates only when H2S is absent or very low. D. Iron sulfide films form in wet sour service and dictate corrosion behavior at these conditions.