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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

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25 hrs
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2077 views
Team Piping Engineering
Team Piping EngineeringFounder Team Piping Engineering
  • 7-day money-back guarantee
  • Session recordings included
  • Certificate of completion
Volume pricing for groups of 5+

Is this course for you?

You should take this if

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

  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

COMPLETED

-

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.