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Role of Process Engineers in the Oil and Gas Industry

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Process Engineering Fundamentals for Oil & Gas

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1 hrs
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English
1995 views
Sanjay Chakraborty
Sanjay Chakraborty
  • Session recordings included
  • Certificate of completion
  • Foundational Learning
  • Access to Study Materials

Why enroll

Participants should join this course

  1. To understand the core responsibilities and daily activities of process engineers in oil and gas projects.

  2. To gain practical knowledge of process design, simulation, and optimization used in real-world applications.

  3. To learn how process engineers contribute to safety, efficiency, and profitability across upstream, midstream, and downstream operations.

  4. To develop a strong foundation for career advancement or transition into process engineering roles within the energy sector.

  5. To become familiar with industry-standard tools, practices, and design methodologies used in major oil and gas companies.

  6. To improve their ability to collaborate effectively with multidisciplinary teams in engineering projects.

  7. To understand process safety principles and risk management techniques essential for plant reliability.

  8. To enhance technical decision-making and problem-solving skills through real-world examples and case studies.

  9. To strengthen their professional profile with a course that bridges theory and industrial practice.

  10. To gain mentor-led insights and practical tips from experienced professionals in the field.

This online course is ideal for:

  1. Fresh graduates in Chemical, Process, or Petroleum Engineering seeking to enter the oil and gas industry.

  2. Early-career engineers who want to understand the broader scope of process engineering roles and responsibilities.

  3. Mechanical, instrumentation, and piping engineers aiming to enhance their understanding of process interactions in plant design and operation.

  4. Operations and maintenance personnel interested in learning how process design influences plant performance and safety.

  5. Project engineers and coordinators who work with process teams and want to improve interdisciplinary collaboration.

  6. Engineering students preparing for a career in oil, gas, or energy sectors.

  7. Professionals from related industries (such as petrochemicals, energy, or refineries) who wish to expand their process engineering knowledge.

  8. Technical managers and supervisors seeking a better grasp of process-related decision-making in projects and operations.

What enrolled engineers say

265 verified reviews
  • Feb 25, 2026

    Initially, I wasn’t sure what to expect from this course. With a beginner-to-intermediate label, there was a risk it would stay too high level, but it actually touched on several realities of oil & gas work that new engineers usually only learn on the job. The sections on process flow diagrams and basic mass and energy balances were aligned with how upstream and midstream projects are framed in practice, especially when utilities like fuel gas and cooling water from the energy and utilities side start to constrain design choices. One challenge was the simplified treatment of edge cases. For example, transient operations during start-up and shutdown were mentioned, but not fully explored, even though those scenarios drive a lot of HAZOP actions in real oil and gas facilities. Compared with chemical or pharmaceutical plants, the course rightly emphasized variability in feed composition, but I would have liked a bit more on how that impacts control philosophy at the system level. A practical takeaway was the clear framing of the process engineer’s role across disciplines, particularly how early decisions affect downstream utilities and operability. I can see this being useful in long-term project work.

    Hosam Eldeen K. Verified
  • Feb 25, 2026

    Coming into this course, I had some prior exposure to the subject, mostly from brownfield oil and gas projects rather than classroom-style material. The modules on upstream separation trains and basic process flow diagrams were solid, especially when tied to real constraints like slugging and variable well composition. Coverage of utilities integration—fuel gas, instrument air, and cooling water—was useful, since that’s often glossed over in beginner content but ends up driving a lot of system-level decisions in operating facilities. One challenge was the simplified treatment of safety systems. Relief sizing and HAZOP discussions were introduced, but edge cases like blocked outlets during low-load operation or utilities failure scenarios could have been explored more deeply. In practice, those are the situations that tend to bite during startups and shutdowns. Compared with industry workflows, the course leaned more on idealized steady-state assumptions than what’s seen in live assets. A practical takeaway was a structured way to sanity-check mass and energy balances before reviewing a P&ID or utility load list. That’s something that carries over directly into day-to-day engineering reviews. It definitely strengthened my technical clarity.

    Ahammed S. Verified
  • Feb 25, 2026

    Initially, I wasn’t sure what to expect from this course. Coming from a working role on brownfield oil and gas projects, the basics are familiar, but the way the role of a process engineer was tied to real plant decisions helped fill a gap I didn’t realize I had. Topics like PFD and P&ID development, separator sizing, and crude dehydration were explained in a way that connects directly to day‑to‑day engineering work. There was also useful context around utilities in energy facilities, especially steam and cooling water systems, which often get overlooked early in design. One challenge was keeping up with the transition from high‑level concepts to practical constraints like operability and safety reviews. The sections touching on HAZOP inputs and how process engineers support them took a bit of effort to digest, but they reflected real project pressure. A practical takeaway was a clearer approach to doing material and energy balances before jumping into simulation tools like HYSYS, which is something that can save time on live projects. Overall, the course helped connect oil and gas process fundamentals with how decisions are actually made on site. It definitely strengthened my technical clarity.

    Shaikh S. Verified

Is this course for you?

You should take this if

  • You work in Oil & Gas Upstream
  • You're a Chemical & Process / Petroleum Technology professional
  • You want to build skills in Engineering & Design
  • 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

  • Introduction

  • Segments of the Oil and Gas Industry

  • Role of Process Engineers

  • Key Engineering Activities

  • Safety and Environmental Considerations

  • Challenges and Trends

  • Career Path and Skills

  • Case Study or Real-World Example

  • Q&A

  • How Everyeng can help you to become a Process Engineer

Opportunities that await you!

Skills & tools you'll gain

Engineering & Design

Career opportunities

Training details

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

Live session

Starts

Sun, Nov 30, 2025

3:00 PM UTC· your timezone

Duration

1 hour per day

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

MARK LESTER REAL
MARK LESTER REAL
Mar 22, 2026

nice

Avatar icon
Sneh Patel
May 3, 2026

Wasn't expecting the sizing math to get this granular for a beginner/intermediate course, and that caught my attention fast. The moment that stuck was Chapter 3’s walk-through of the Souders–Brown calc where they re-sized the vessel after tweaking inlet momentum; seeing the numbers move made the constraints real. As someone who thinks in arch and prod failure modes, it mapped cleanly to how we reason about RPS headroom and backpressure in infra, even if the domain’s oilgas. I wasn't sold on the quick pass over control valves, and wished there was a bit more on how bad inputs propagate, maybe a short sensitivity table. I’ve already applied the approach when reviewing a separator spec the same way I’d review a PR in a repo: assumptions first, then bounds. It’s changed how I think about scaling decisions before they become a CI fire drill.

Ali Taqi
Ali Taqi
May 3, 2026

Chapter 3's retention-time calc with oilgas slugging example was usable for prod sizing; wasn't sold on the brief internals section.

Naga raj
Naga raj
May 3, 2026

This feels like the material you grab when the arch cracks and the docs aren't cutting it. The worked example in the separator sizing section where they walk residence time vs droplet size and check liquid levels before gas capacity stuck, especially the callout on foaming risk. As a software person mapping this to prod infra, the obs mindset and sanity checks read like a PR review, not a hand-wavy wiki. Mostly good, though I wished there was more on transient slug handling; still, I've updated my internal model in ways the repo never did.

COMPLETED

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Questions and Answers

A: A would still happen if foam bridges the level taps and the shutdown comes late, pushing liquid into the gas line. B is addressed by pressure relief devices rather than a level shutdown, so relying on LSHH there misreads the safeguard layer. C can occur because LSHH stops inflow but doesn't drain the vessel, so inventory can still be swept out. D isn't affected because level protection doesn't change water chemistry or residence time driving corrosion.

A: Liquid carryover still occurs because PSVs don't control level and the gas outlet becomes a liquid path. Slugging downstream is credible since relief doesn't stop phase inversion or entrainment. Separation efficiency degrades as internals submerge even if pressure is relieved. The PSV limits pressure rise, so shell MAWP exceedance is what it's actually designed to prevent.

A: Thirty seconds underestimates volume by confusing superficial velocity with holdup. Ten minutes assumes the gas space doesn't exist and inflates usable volume. API guidance doesn't override geometry and flowrate math in a sanity check. Half-full volume is ~7.6 m³ and at ~2.2 m³/min flow gives a few minutes, which is defensible.

A: Assuming wireless changes response assumptions without evidence and can mask real delays. Letting the index override the P&ID skips configuration control and audit trail. Drafting conventions don't change signal physics or failure modes. The signal type affects common cause failure and proof testing, so it needs resolution under MOC.