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Piping Layout Engineering_September 2024 Batch banner

Piping Layout Engineering_September 2024 Batch

Piping Layout Engineering_September 2024 Batch banner
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Piping Layout Engineering_September 2024 Batch

4(63)
4 enrolled
2096 views
COMPLETED

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25 hrs
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2096 views
Team Piping Engineering
Team Piping EngineeringFounder Team Piping Engineering
Oil & Gas UpstreamEnergy & Utilities
  • 7-day money-back guarantee
  • Session recordings included
  • Certificate of completion
Volume pricing for groups of 5+

What enrolled engineers say

6 verified reviews
  • 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.

    432Abdullah Verified
  • 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.

    Saurabh Kumar G. · Content Manager Verified
  • May 3, 2026

    The pipe rack spacing calc in Module 3, where we walked a pump suction line past a heat exchanger, connected stress theory to shop drawings. I wasn't sold on the brief section on supports; wished there was more on clash checks in prod with Navis, but it's mostly practical for oilgas layouts.

    Mohammed A. Verified

Your instructor

Team Piping Engineering

Team Piping Engineering

Sr Engineer

Founder Team Piping Engineering

20+ yrs experience·India

22Courses
617Learners
4Avg rating
32Followers

Is this course for you?

You should take this if

  • You work in Oil & Gas Upstream or Energy & Utilities
  • You're a Piping & Layout Engineering / Mechanical Engineering professional
  • You prefer live, instructor-led training with Q&A

You should skip if

  • You need a different specialisation outside Piping & Layout Engineering
  • You need fully self-paced, on-demand content

Course details

Course suitable for

Key topics covered

  1. Introduction to Piping Layout Engineering:

    • Overview of Piping and Instrumentation Diagrams (P&ID)

    • Importance of accurate piping layouts in industrial projects

  2. Converting P&ID into Piping Layouts:

    • Step-by-step methodology for converting P&ID into detailed piping layouts

    • Common challenges and solutions in the conversion process

  3. Understanding Process Equipment:

    • Types of process equipment and their functions

    • Installation requirements and piping connections for process equipment

    • Case studies and real-world examples

  4. Understanding Utility Equipment:

    • Types of utility equipment (e.g., boilers, compressors, pumps)

    • Installation requirements and piping connections for utility equipment

    • Best practices for integrating utility equipment into overall piping layouts

  5. Plot Plan Development:

    • Principles of plot plan development

    • Standards and statutory requirements for plot plans

    • Layout of various units within an industrial plant

    • Case studies of successful plot plans

  6. Pipe Rack Design:

    • Importance and function of pipe racks in industrial plants

    • Designing pipe racks: considerations for placing lines, width, and height calculations

    • Development of pipe rack layouts

    • Preparation of isometric drawings for pipe racks

    • Hands-on exercises and practical examples

  7. Storage Terminal / Tank Farm Design:

    • Overview of storage terminals and tank farms

    • Designing storage terminals: equipment layout, piping layout, and support design

    • Nozzle orientation and its impact on piping design

    • Construction isometrics for storage terminals

    • Differences between greenfield and brownfield projects

    • Real-world examples and design exercises

  8. Standards and Codes in Piping Layout Engineering:

    • Overview of relevant standards and codes (e.g., ASME, ASTM)

    • Ensuring compliance with industry standards

    • Case studies of projects adhering to standards

Opportunities that await you!

Career opportunities

Training details

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

Live session

Starts

Fri, Sep 6, 2024

3:30 PM UTC· your timezone

Duration

1 hour per day

25 days total

✎ Where this fits — what comes before, what comes next
Piping Layout Engineeri… Master Dynamic Analysis… Fundamentals and advanc… Piping Material Enginee…

COMPLETED

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Questions and Answers

A: Pick wrong and you’ll hear it first as water hammer, then see it as cracked welds and a failed pressure test that stops commissioning. Thermal cycling and high reverse velocities punish swing and dual-plate designs in this service. A forged piston check with damping manages closure speed and tolerates cycling without relying on operator behaviour or elastomers that age under temperature.

A: Get this wrong and you risk a PSV rendered inoperative, which is a straight regulatory non‑conformance. On a P&ID, a spectacle blind symbol is not temporary unless explicitly tagged as such. Treating it as permanent forces you to verify the normal position and locking, keeping overpressure protection intact during operation.

A: Ignore this and you’ll commission a line that pits through at the crown while wall thickness elsewhere looks fine, leading to an unexpected leak under normal operation. The real driver here is condensation at low spots and temperature gradients, concentrating CO2 corrosion at the top. Recognising that steers you toward coatings, inhibition, or material upgrades where they actually work.

A: Choose poorly and you’ll be fighting leaks during reinstatement, followed by a failed pressure test that halts pigging plans. High pressure and repeated break-ins demand joint integrity. A welded spool with one RTJ flanged break minimises leak paths while still allowing removal when needed.