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Hydrogen Energy: Production

Hydrogen Energy: Production banner
Self-paced Advanced

Hydrogen Energy: Production

4(12)
4 enrolled
581 views
FREE
896 min
Anytime
English
581 views
Team ChemEE
Team ChemEEConsultant
  • Lifetime access
  • Certificate of completion
  • Anytime Learning
  • Learn from Industry Expert
Volume pricing for groups of 5+

Why enroll

Essential course for Energy science and Engineering professionals to understand basic concept, advanced research and technology in the area of Hydrogen production, storage and safety.

Is this course for you?

You should take this if

  • You work in Energy & Utilities or Oil & Gas Upstream
  • You're a Chemical & Process / Petroleum Technology 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 details

Course suitable for

Key topics covered

Hydrogen Energy: Production

  • Properties of Hydrogen

  • Status of Hydrogen

  • Methods of Hydrogen Production

  • Steam methane reforming part -1 and 2

  • Steam reforming of higher hydrocarbons

  • Advanced methods of steam reforming

  • Partial oxidation method for Hydrogen production

  • Autothermal Reforming

  • Combined dry, bi and tri reforming

  • Reforming using alternate energy sources

  • Hydrogen production by methane decomposition

  • Hydrogen production from Biomass part-1, 2, 3

  • Hydrogen production from coal

  • Hydrogen separation and purification Part-1, 2

  • Thermochemical cycles for hydrogen production

  • Electrolysis of water for hydrogen production

  • Fundamentals of electrolysis of water

  • Electrolytic cell components and electrolyzer stack

  • Different types of electrolyzer technologies

  • Photoelectrochemical hydrogen production

  • Technical Comparison of Various Hydrogen Production Routes

  • Economics and Status of Various Hydrogen Production Routes

  • Tutorials 1,2, 3, 4

Course content

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

2 modules30 lectures14 hr 56 min
  1. Properties of Hydrogen
    23 min
  2. Status of Hydrogen
    9 min
  3. Methods of Hydrogen Production
    25 min
  4. Steam methane reforming part -1
    28 min
  5. Steam methane reforming Part-2
    42 min
  6. Steam reforming of higher hydrocarbons
    0 min
  7. Tutorial 1
    27 min
  8. Advanced methods of steam reforming
    39 min
  9. Partial oxidation method for Hydrogen production
    32 min
  10. Autothermal Reforming
    32 min
  11. Combined dry, bi and tri reforming
    30 min
  12. Reforming using alternate energy sources
    33 min
  13. Tutorial 2
    33 min
  14. Hydrogen production by methane decomposition
    36 min
  15. Hydrogen production from Biomass part-1
    28 min
  16. Hydrogen production from Biomass Part-2
    34 min
  17. Hydrogen production from biomass- Part 3
    25 min
  18. Hydrogen production from coal
    28 min
  19. Tutorial 3
    41 min
  20. Hydrogen separation and purification Part-1
    37 min
  21. Hydrogen separation and purification part-2
    30 min
  22. Thermochemical cycles for hydrogen production
    36 min
  23. Electrolysis of water for hydrogen production
    38 min
  24. Fundamentals of electrolysis of water
    25 min
  25. Electrolytic cell components and electrolyzer stack
    31 min
  26. Different types of electrolyzer technologies
    32 min
  27. Photoelectrochemical hydrogen production
    16 min
  28. Tutorial 4
    43 min
  29. Technical Comparison of Various Hydrogen Production Routes
    21 min
  30. Economics and Status of Various Hydrogen Production Routes
    42 min

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Questions and Answers

A: The hard boundary is contract award. API standards aren’t retroactive unless the contract drags them forward with a ‘latest edition’ clause. Without that language, you’re tied to what was enforceable when the EPC took risk, even if the newer API 560 tightened flame geometry or minimum clearances.

A: The number that matters is the doubling of ΔP alongside higher CO. Sulfur kills activity but doesn’t choke flow. Attrition raises ΔP but usually improves apparent conversion early. Carbon fouling does both at once by blocking pores and shifting equilibrium away from H₂.

A: The threshold is membrane ΔP, not vessel MAWP. Relief valves protect steel. They don’t limit the transient pressure differential across a PEM stack, where even a few bar can tear the membrane before any PSV reacts.

A: 2.5 mol/mol is the red line. Below that, carbon risk dominates. More heat accelerates coke. The only move that arrests damage while you fix the valve is to back off feed and get steam back into ratio.