Master Onshore Pipeline Engineering: Comprehensive Course from Basics to Advanced Concepts | EveryEng

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Master Onshore Pipeline Engineering: Comprehensive Course from Basics to Advanced Concepts

4(31)

10 enrolled

3667 views

₹ 89999

2974 min

Anytime

English

3667 views

Mohamed FadlAllah

Energy & Utilities

Oil & Gas Upstream

7-day money-back guarantee
Lifetime access
Certificate of completion

Volume pricing for groups of 5+

Why enroll

- Industry-Experienced Instructors with years in major oil & gas companies

- Real-World Case Studies to Learn from actual pipeline projects and lessons learned

- Hands-On Practical Exercises to Apply knowledge through calculations and problem-solving

- Current Industry Standards Latest codes, standards, and best practices

- Opportunities to Connect with professionals worldwide

Your instructor

Mohamed FadlAllah

Pipeline Engineer

Egypt

Is this course for you?

You should take this if

You work in Energy & Utilities or Oil & Gas Upstream
You're a Onshore Pipeline Engineering professional
You have 3+ years of hands-on experience in this field
You prefer self-paced learning you can revisit

You should skip if

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

Course details

Onshore pipeline engineering is a multidisciplinary field focused on the planning, design, construction, operation, and maintenance of pipelines that transport oil, gas, water, and other fluids across land. It begins with route selection and feasibility studies, where engineers evaluate topography, soil conditions, environmental constraints, land access, and regulatory requirements to determine the safest and most cost-effective alignment. The design phase involves hydraulic analysis to ensure adequate flow capacity and pressure control, selection of suitable pipe materials and wall thickness, stress and flexibility analysis, and the application of international codes and standards such as ASME, API, and ISO. Construction engineering addresses trenching, welding, non-destructive testing, coating, lowering-in, backfilling, and commissioning, with a strong emphasis on quality control, health, safety, and environmental protection. Once operational, onshore pipeline engineering focuses on integrity management through corrosion control, inspection, monitoring, leak detection, and maintenance programs to ensure long-term reliability and safety. Overall, onshore pipeline engineering plays a critical role in energy and infrastructure development by enabling the efficient, safe, and environmentally responsible transportation of fluids over long distances.

Course suitable for

Key topics covered

Our in-depth pipeline engineering course curriculum covers 12 essential modules designed to take you from fundamentals to advanced pipeline engineering practices, including design, construction, procurement, inspection, and emerging industry trends.

The course contains the following 12 Modules:

1. Introduction to Pipeline Engineering

2. Pipeline Project Lifecycle

3. Codes, Standards & Specifications

4. Components of a Pipeline System

5. Pipeline Routing

6. Pipeline Engineering Deliverables

7. Introduction to Mechanical Design

8. Procurement Cycle & Documentation

9. Construction & Field Engineering

10. Inspection, Pigging & Integrity Management

11. Future Trends

12. Actual Project Quick Example

See the attached PDF course outlines for more details:

Enroll now to advance your career in Onshore Pipeline Engineering!

Course content

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

55 lectures49 hr 34 min

Opportunities that await you!

Career opportunities

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

₹89999

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Questions and Answers

Q: You're watching line pack increase during hot commissioning and searching "pipeline line pack increase downstream pressure response during commissioning". Upstream pump speed is held constant, downstream block valve is cracked open to flare, and gas temperature rises 15°C along a long onshore export line. What happens at the downstream custody meter, and what’s the least risky immediate response?

A: A: Warmer gas lowers density, so at fixed speed the mass indication creeps up while pressure margin tightens. Trimming speed protects MAOP. B: First instinct from liquid thinking; gas compressibility doesn’t drive volumetric flow that way here and opening the valve worsens pressure loss control. C: DP doesn’t spike from uniform temperature rise along the line; isolation creates a trapped volume risk. D: Chasing Reynolds during commissioning ignores pressure limits and adds risk.

Q: A lead asks you after a trip to explain a release seen on CCTV, so you search "onshore pipeline ESD valve fails closed physical consequence". The ESD valve at a pig receiver fails to close on demand. What physical consequence follows, and what does the ESD not protect against in this case?

A: A: A failed-close ESD leaves the barrel connected, so inventory keeps draining; ESDs don’t solve blocked-in thermal growth. B: Overpressure from pump trip is a different safeguard gap; here the valve never shut. C: The release source is the receiver, not a localized body leak. D: Assuming perfect checks ignores real leakage and avoids the actual cause–effect path.

Q: You're reviewing a design note and googling "ASME B31.8 temperature derating purpose for onshore gas pipeline". A high-temperature segment crosses a compressor discharge area. Why does the code require temperature derating of MAOP there?

A: A: The code intent is material strength versus temperature, tied to hoop stress and rupture risk. B: Erosion-corrosion is managed by velocity and materials, not MAOP derating. C: Axial stress is real but not the driver for MAOP limits in B31.8. D: Measurement error isn’t a pressure design basis.

Q: Operations reports erratic flow with rising DP and you search "onshore pipeline wax deposition symptoms increasing pressure drop". Liquid line, stable inlet conditions, no change in pump amps. What root cause fits all observations?

A: A: Gradual DP rise with steady amps points to internal roughness growth. B: Cavitation would show amp swings and vibration. C: Hunting shows oscillatory signals, not a steady DP trend. D: A dent causes a step change, not progressive behavior.