Roles and Responsibilities of Process Engineer & Basic Design Requirement
Roles and Responsibilities of Process Engineer & Basic Design Requirement
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What enrolled engineers say
Relevant if you're touching real designs instead of classroom theory; it maps process roles to how work actually lands in prod. The Basic Design Requirement module where they walk through the design basis memo and the PFD vs P&ID handoff at battery limits stuck, especially the note on revising assumptions before freezing specs. I've used similar gates in arch/infra PRs, so the framing clicked, though I wasn't sold on how lightly HAZOP was treated. Mostly a handy reference when thinking about throughput vs constraints—process capacity feels a lot like RPS under load.
Much of it mirrored issues popping up in our current sprint: role boundaries, handoffs, and what actually belongs in basic design versus later. the battery limits example in the Basic Design Requirements chapter (sizing a transfer pump and flagging missing vendor data) stuck with me. It maps to how we sanity-check arch and infra before prod; I've already reused the role checklist during a PR review. I wasn't sold on the brief control-narratives section and wished there was more on ops handover in chemicalpharmaceutical plants, but it's still a handy add to the toolkit.
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 self-paced learning you can revisit
You should skip if
- You need a different specialisation outside Chemical & Process
- You need live interaction with an instructor
Course details
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Key topics covered
Course content
The course is readily available, allowing learners to start and complete it at their own pace.
- Roles of Process Engineer60 min
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What learners say about this course
Coming from software, this course reframed an old control problem the way refactoring a legacy service does: same constraints, clearer mental model. The walk through the ISA sizing equation, especially the Cv vs Kv example with water at 60°F, stuck because it mirrored how I sanity-check RPS assumptions in prod before a PR lands. I liked the section on flashing vs cavitation; the pressure drop chart felt like reading infra limits instead of hand-wavy arch talk, and it clicked fast. As a beginner track it mostly lands, though I wasn't sold on how briefly valve trim selection was handled; a few more edge cases would help folks crossing over from chemicalpharmaceutical or energyutilities. The pacing works for between-meeting study, and the exercises felt closer to CI checks than homework. I've already reused the sizing worksheet like a repo snippet, which is saying something.
Module 4 dragged a bit, and the homework assumes you’re already fluent in Excel Solver. That aside, the selection logic is what pulled me in: the decision trees for choosing shell-and-tube vs plate in Chapter 2, especially the LMTD vs ε‑NTU fork with the fouling factor example at minute ~18. As someone who thinks in arch diagrams and failure modes, mapping thermal constraints the way we map infra tradeoffs clicked. The counterflow vs parallel-flow section tied pressure drop back to maintenance in a way I’ve actually seen in chemicalpharmaceutical plants. it wasn’t fluffy, and it didn’t pretend everyone’s starting from zero. I’ve already bookmarked the pinch-temperature walkthrough for quick reference between meetings.
Needed material that wouldn’t fall apart under a PR-level sanity check, and this mostly held. The LMTD vs ε-NTU section, especially the shell-and-tube example where fouling factors changed sizing, stuck with me and maps well to how I think about legacy arch versus modern constraints. It connects old plant math to how I reason about infra tradeoffs in prod, even if the plate exchanger coverage felt light. still, it trimmed a lot of mental tech debt I’d been carrying from chemicalpharmaceutical work.
This course nudged my mental model of heat exchangers; the way LMTD and ε-NTU were contrasted exposed gaps I didn't know I had. The counterflow vs parallel temp profile plot in the 'Shell-and-Tube Basics' section, plus the fouling factor table, stuck. It mapped cleanly to how we reason about infra—assumptions, bounds, and where obs should flag drift in prod. I wasn't sold on the brief pass over transient start-up; wished there was more for chemicalpharmaceutical cases, but I've already queued a PR to refactor our sizing logic in the repo.
Aug 29, 2026 
