Basic Engineering Package & Detail Engineering Package | EveryEng

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Self-paced Beginner

Basic Engineering Package & Detail Engineering Package

4(400)

1 enrolled

6129 views

₹ 99

148 min

Anytime

English

6129 views

Process Engineering World

Oil & Gas Upstream

Pharmaceutical & Healthcare

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

Why enroll

Mastering "Basic Engineering Package & Detail Engineering Package" accelerates career growth for engineers and project managers in the oil and gas, chemical, and process industries. Professionals can transition into senior roles like Project Manager, Engineering Lead, or Technical Director, or specialize in FEED, detailed design, and project execution. Understanding engineering packages enhances job prospects, earning potential, and leadership opportunities, enabling successful project delivery and career advancement.

Your instructor

Process Engineering World

Is this course for you?

You should take this if

You work in Oil & Gas Upstream or Pharmaceutical & Healthcare
You're a Health, Safety & Environmental / Onshore Pipeline Engineering professional
You prefer self-paced learning you can revisit

You should skip if

You need a different specialisation outside Health, Safety & Environmental
You need live interaction with an instructor

Course details

To provide participants with a comprehensive understanding of the development and components of basic and detail engineering packages, ensuring effective project execution and design.

Explore the principles and processes involved in creating basic and detail engineering packages, covering essential elements such as design criteria, specifications, drawings, and documentation. Gain insights into best practices and industry standards for engineering project deliverables.

Course suitable for

Key topics covered

Introduction to Engineering Packages
- Definition and importance of engineering packages
- Overview of basic and detail engineering packages
- Role in project lifecycle
Components of Basic Engineering Package (BEP)
- Project scope and objectives
- Design criteria and basis
- Process flow diagrams (PFDs)
- Preliminary equipment lists and specifications
Development of Basic Engineering Package
- Steps in creating a BEP
- Collaboration with multidisciplinary teams
- Initial cost estimation and feasibility studies
- Preliminary safety and environmental assessments
Components of Detail Engineering Package (DEP)
- Detailed design specifications
- Piping and instrumentation diagrams (P&IDs)
- Equipment and instrumentation data sheets
- Detailed layout and arrangement drawings
Development of Detail Engineering Package
- Steps in creating a DEP
- Integration of vendor data and specifications
- Detailed cost estimation and budgeting
- Comprehensive safety and regulatory compliance
Design and Documentation Standards
- Industry standards and best practices (e.g., ISO, ANSI)
- Document control and management systems
- Ensuring consistency and accuracy in documentation

Course content

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

3 lectures2 hr 28 min

Basic Detail Engineering Package & Detail Engineering Package-1
41 min
Basic Detail Engineering Package & Detail Engineering Package-2
66 min
Basic Detail Engineering Package & Detail Engineering Package-3
41 min

Opportunities that await you!

Career opportunities

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

Manish Kumar

Jan 8, 2026

Great

Balaji Paskanti mechanical engineer

May 3, 2026

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.

Kinjal Chauhan

May 3, 2026

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.

Raju Bhai Student

May 3, 2026

The course helped me visualize how pump data moves from curves to decisions, bridging old plant habits with newer infra thinking. The Chapter 6 NPSH vs cavitation walkthrough stuck, especially the moment the impeller eye pressure plot flips and you see why prod margins vanish; it's similar to watching obs metrics lie under load. I've used that framing in a PR already. wasn't sold on the light coverage of VFDs and parallel pumps, but I'm flagging this as preread ahead of our next platform decision in chemicalpharmaceutical.

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Questions and Answers

Q: You're closing the BEP for a three-phase horizontal separator and searching "BEP vs DEP separator residence time mismatch EPC". The liquid residence time passes the BEP criterion on paper, but FAT trending over three runs shows rising carryover at constant inlet flow. What's the most likely root cause tied to the engineering package boundary?

A: 100–150 micron is the hidden threshold. Many BEPs size residence time assuming a droplet size that never gets written into the DEP datasheet. When the DEP swaps in a vane pack rated closer to 300 microns, it still meets the written residence time but loses separation margin as soon as fouling nudges velocity up. That trend fits all three runs without changing flow.

Q: During detail engineering you're checking hydraulics and Googling "detail engineering control valve Cv higher than BEP basis". The selected control valve Cv is 25% higher than BEP, everything else unchanged. What happens at low flow and what's the right response?

A: Below ~20% travel is where most globe valves get ugly. A 25% Cv increase pushes normal operation into that region, and no amount of PID tuning fixes stiction-driven oscillation. The BEP assumption on controllability quietly breaks in the DEP unless trim strategy is revisited.

Q: You're sanity-checking a pump spec and type "BEP DEP pump NPSH margin quick check". BEP states NPSHa = 5.5 m at design. DEP vendor data shows NPSHr = 4.8 m at rated flow. With hot hydrocarbon service, is this acceptable at order-of-magnitude level?

A: The 0.7 m gap is the number that hurts. API 610 experience shows hot services eat margin fast through vapor pressure rise and line roughness, and sub‑1 m headroom disappears before commissioning ends. That gap explains why the paper check passes but field risk stays high.

Q: You're comparing documents and searching "BEP P&ID mismatch with DEP GA drawing". The BEP P&ID shows a PSV on the separator vapor outlet. The DEP GA omits the nozzle entirely but lists the PSV in the line list. What do you do first?

A: One missing nozzle is the trigger. Pressure relief hardware can’t be reconciled informally because overpressure scenarios and MAWP checks hinge on physical location, not just tags. Two weeks to MC is exactly when these silent deletions slip through.