Process Engineering Fundamentals for Oil & Gas
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- Session recordings included
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Why enroll
What enrolled engineers say
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.
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.
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.
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
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Training details
This is a live course that has a scheduled start date.
Live session
Starts
Sun, Nov 30, 2025
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
nice
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.
Chapter 3's retention-time calc with oilgas slugging example was usable for prod sizing; wasn't sold on the brief internals section.
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.