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Process Equipment Design: Fundamentals and Applications

Process Equipment Design: Fundamentals and Applications banner
Self-paced Advanced

Process Equipment Design: Fundamentals and Applications

3(115)
17 enrolled
1140 views
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1939 min
Anytime
English
1140 views
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Why enroll

Upon completion, students will be able to design and analyze process equipment, considering safety, regulatory, and practical requirements.

What enrolled engineers say

12 verified reviews
  • May 3, 2026

    Material maps cleanly to day-to-day design work when you’re building or reviewing equipment. The shell-and-tube heat exchanger chapter, the baffle spacing example with fouling margins and ΔP math, stuck because it shows tradeoffs instead of hand-waving. I treated the calcs like a PR checklist for prod issues; it’s similar to how we sanity-check arch and infra before k8s changes, and I’ve reused it. Pace is uneven—some parts assume advanced background while others reset to beginner, and I wasn’t sold on the light coverage of chemicalpharmaceutical cases, but I don’t get stuck as long debugging specs.

    VISHWANATH H. Verified
  • May 3, 2026

    Chapter 4’s shell-and-tube fouling calc stuck—it's the first time heat-transfer theory clicked for chemicalpharmaceutical work, though I've wanted more on spec tolerances.

    Sairaj G. Verified
  • May 3, 2026

    Jumped in halfway through and the context snapped in fast; slides didn't assume too much and the arch built logically. The ASME VIII pressure vessel thickness calc in the “Design for Internal Pressure” section, especially the corrosion allowance callout, stuck. I wasn't sold on the pump NPSH segment; wished there was more on cavitation checks under variable RPS, and fewer screenshots. I've already dropped the exchanger-sizing checklist and nozzle spacing rules into our repo style guide; it'll show up in PRs.

    Yogesh R. Verified

Is this course for you?

You should take this if

  • You work in Pharmaceutical & Healthcare
  • You're a Chemical & Process / Mechanical Engineering professional
  • You have 3+ years of hands-on experience in this field
  • You prefer self-paced learning you can revisit

You should skip if

  • You're new to this field with no prior experience
  • You need a different specialisation outside Chemical & Process
  • You need live interaction with an instructor

Course content

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

61 lectures32 hr 19 min
  1. Introduction
    5 min
  2. Introduction of Process Equipment Design
    43 min
  3. Classification of exchangers-1
    34 min
  4. Classification of exchangers-2
    42 min
  5. Basic design parameters-1
    37 min
  6. Basic design parameters-2
    40 min
  7. Double pipe exchanger-1
    34 min
  8. Double pipe exchanger-2
    41 min
  9. Double pipe exchanger-3
    25 min
  10. Types of Shell and Tube exchangers
    37 min
  11. Exchanger Tubes
    38 min
  12. Exchanger Shell
    33 min
  13. STE design- Kern’s method-1
    30 min
  14. STE design- Kern’s method-2
    31 min
  15. STE design- Kern’s method-3
    25 min
  16. STE design- Kern’s method-Example-4
    40 min
  17. STE design- Kern’s method-Example-5
    25 min
  18. STE design- Bell’s method-1
    36 min
  19. STE design- Bell’s method-2
    31 min
  20. STE design- Bell’s method-3
    33 min
  21. STE design – Bell’s method: Example-4
    32 min
  22. STE design – Bell’s method: Example-5
    29 min
  23. Design of Condenser-1
    33 min
  24. Design of Condenser-2
    38 min
  25. Design of Condenser-3
    31 min
  26. Design of Condenser-4
    31 min
  27. Design of Condenser-5
    22 min
  28. Design of Reboiler-1
    38 min
  29. Design of Reboiler-2
    36 min
  30. Design of Reboiler-3
    25 min
  31. Design of Reboiler-4
    29 min
  32. Design of Reboiler-5
    36 min
  33. Design of Reboiler-6
    34 min
  34. Design of Reboiler-7
    26 min
  35. Design of Evaporator-1
    35 min
  36. Design of Evaporator-2
    29 min
  37. Design of Evaporator-3
    28 min
  38. Design of Evaporator-4
    29 min
  39. Design of Evaporator-5
    33 min
  40. Design of Crystallizer-1
    31 min
  41. Design of Crystallizer-2
    29 min
  42. Design of Crystallizer – Examples
    32 min
  43. Design of Crystallizer – Types
    26 min
  44. Design of Packed Column-1
    29 min
  45. Design of Packed Column-2
    29 min
  46. Design of Packed Column-3
    36 min
  47. Design of Packed Column-4
    26 min
  48. Design of Packed Column-5
    31 min
  49. Distillation Column – 1
    34 min
  50. Distillation Column – 2
    30 min
  51. Distillation Column – 3
    35 min
  52. Distillation Column – 4
    30 min
  53. Distillation Column – 5
    34 min
  54. Distillation Column – 6
    24 min
  55. Distillation Column – 7
    35 min
  56. Distillation Column – 8
    34 min
  57. Distillation Column – Mechanical Design-1
    34 min
  58. Distillation Column – Mechanical Design-2
    28 min
  59. Distillation Column – Mechanical Design-3
    31 min
  60. Distillation Column – Mechanical Design-4
    32 min
  61. Distillation Column – Mechanical Design-5
    35 min

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Questions and Answers

A: 0.000035 m²·K/W is the boundary most vendors default to for treated tower water when velocities stay above about 1 m/s. Below that, fouling accelerates; above it, erosion becomes the limit. The other values either drop fouling without evidence, double-count conservatism, or misapply it by side.

A: 5–10 kPa across a startup strainer is the tripwire here. Anything higher risks cavitation on first rotation. Rotation checks and logic proofs matter, but a blocked suction will damage the pump before those errors show up.

A: A doubling of ΔP with falling U points to flow area loss. Internal bypass from gasket creep usually drops ΔP while losing duty. Deformation and maldistribution show up earlier and often during startup, not gradually.

A: 0.85 is the threshold engineers miss. Effective ΔT is F×LMTD, not the inverse. Using 42 K oversizes duty; dividing by F understates area and fails performance.