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Process Design Engineering_September 2024 Batch banner

Process Design Engineering_September 2024 Batch

Cohort starts 7 Sep 2 enrolled

Process Design Engineering_September 2024 Batch banner
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Process Design Engineering_September 2024 Batch

4(316)
2 enrolled
3527 views
COMPLETED
45 hrs
Sep 7, 2024
Process Engineering World
Process Engineering World
  • 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 or Pharmaceutical & Healthcare
  • You're a Chemical & Process 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 Process Engineering

2. General Points in Process Engineering

3. Heat Exchangers

4. Vessels - Agitated

5. Compressors

6. Fans & Blowers

7. Pumps

8. Utility Equipments and design

9. Line sizing - Liquid, Vapor & Gas

10. Dryers

11. Pressure Safety Valve, Rupture disc working & its sizing

12. Breather valve and it's sizing

13. Vacuum generating equipments

14. Flame Arrestors

15. Instrumentation selection and sizing

16. Filtration

17. Valves - Manual & Control

18. Crystallization

19. Different types of Industrial projects handled by process engineer

20. Process engineering deliverables

21. P&IDs, PFD, ULD, GAD, Layout reading

22. Different types of safety studies in project

23. Automation & Control philosophy

24. MOC selection

Weekly 3 lectures

Opportunities that await you!

Career opportunities

Training details

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

Live session

Starts

Sat, Sep 7, 2024

2:30 PM UTC· your timezone

Duration

1 hour per day

45 days total

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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

Avatar icon
U B
Feb 26, 2026

This course turned out to be more technical than I anticipated. The sections on centrifugal versus piston pump behavior went deeper into pump curves, NPSH, and system resistance than most entry-level material. Coming from a chemical/pharmaceutical background, that was useful since pump selection issues show up fast in batch transfer and CIP systems. The examples also lined up well with what’s seen in energy utilities, especially around circulation pumps and steady-state operation. One challenge was working through the hydraulic calculations without oversimplifying. Translating textbook equations into something that matches real plant data—especially when suction conditions aren’t ideal—took a bit of effort. The discussion around cavitation and how it actually shows up on a curve helped clear that up. A practical takeaway was learning how to quickly identify the operating point and sanity-check vendor curves before accepting a pump for service. That’s already been applied on a small debottlenecking task where flow targets weren’t matching field performance. The course filled a gap between theory from school and day-to-day pump troubleshooting on projects tied to oil & gas and chemical processing. It definitely strengthened my technical clarity.

Mohammed Imtiyas
Mohammed Imtiyas
Feb 26, 2026

This course turned out to be more technical than I anticipated. The sections on centrifugal pump curves, NPSH available vs required, and where piston pumps actually make sense filled a gap that shows up on real jobs. On a recent refinery revamp in oil & gas, we were fighting cavitation on a charge pump, and the walkthrough on suction head losses and vapor pressure made it easier to explain the issue to operations. The examples tied closely to chemical/pharmaceutical services too, especially around viscosity corrections and why a pump that works for water struggles on syrups or solvent blends. One challenge was keeping track of units and assumptions during the hydraulic calculations. It took a couple of passes to reconcile the course examples with the data sheets used in our energy utilities group for cooling water pumps. Still, that struggle was useful. A practical takeaway was a simple, repeatable method for checking pump selection against system curves before issuing a datasheet. That’s already being used on a small utilities upgrade. The content felt aligned with practical engineering demands.

Avatar icon
Amir Hamza
Feb 26, 2026

This course turned out to be more technical than I anticipated. The sections on centrifugal versus piston pump behavior went deeper into pump curves, NPSH, and system resistance than most entry-level material. Coming from a chemical/pharmaceutical background, that was useful since pump selection issues show up fast in batch transfer and CIP systems. The examples also lined up well with what’s seen in energy utilities, especially around circulation pumps and steady-state operation. One challenge was working through the hydraulic calculations without oversimplifying. Translating textbook equations into something that matches real plant data—especially when suction conditions aren’t ideal—took a bit of effort. The discussion around cavitation and how it actually shows up on a curve helped clear that up. A practical takeaway was learning how to quickly identify the operating point and sanity-check vendor curves before accepting a pump for service. That’s already been applied on a small debottlenecking task where flow targets weren’t matching field performance. The course filled a gap between theory from school and day-to-day pump troubleshooting on projects tied to oil & gas and chemical processing. It definitely strengthened my technical clarity.

Avatar icon
Dickson Nahurira
Feb 26, 2026

This course turned out to be more technical than I anticipated. The sections on centrifugal versus piston pumps went beyond definitions and actually walked through how the hydraulics show up on real pump curves. Coming from a chemical/pharmaceutical background, the refresher on NPSH, cavitation margins, and efficiency islands helped close a gap I’ve had since moving into more utilities-focused work. One challenge was keeping track of the assumptions when calculating operating points, especially when switching between SI and US units. That’s something that also shows up on oil & gas projects, where vendor data doesn’t always line up cleanly with process conditions. Working through those examples made it clear where errors usually creep in. A practical takeaway was learning how to sanity-check a pump selection against the system curve before sending questions back to vendors. That’s immediately useful on energy utilities projects where pumps are often oversized “just to be safe,” causing long-term efficiency issues. The piston pump coverage was also relevant for batch transfer scenarios in pharma, which don’t behave like steady centrifugal systems. Overall, it felt grounded in real engineering practice.

COMPLETED

Sep 7, 2024

Questions and Answers

Q: You're reviewing a rev 4 P&ID under HSE audit and searching "how to interpret double isolation and bleed on upstream separator P&ID"; the drawing shows two gate valves with a 1/2" drain between them, but the instrument index lists only one block valve tag — what’s the defensible interpretation?

A: Option A would let operations credit isolation that isn't demonstrable during audit, creating a COMAH non-conformance. Option B assumes as-built status without evidence, which fails under inspection when tag reconciliation is requested. Option C misreads function and ignores bleed sizing and positive isolation criteria. Option D recognises intent versus evidence and forces verification before claiming DBB in a safety case.