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Technology
- Name
- Green Ammonia Process
- Owner
-
/ Undefined Technology Provider - Brand
- Generic Green Ammonia Process
- Process
- Industrial Gas Production
- Type
- Haber-Bosch Process
- Available
-
The majority of global Hydrogen Consumption is for Ammonia (NH3) Production, commonly using the Haber-Bosch process. Green Ammonia is produced through an integrated Process comprising the following Technology Components:
โก ๐๐น๐ฒ๐ฐ๐๐ฟ๐ผ๐น๐๐๐ถ๐ – Splits Water into Hydrogen (H2) and Oxygen (O2).
๐ง ๐๐ฒ๐ต๐๐ฑ๐ฟ๐ฎ๐๐ถ๐ผ๐ป – Removes Water that is a Poison to the Reactor Catalyst.
๐ฌ๏ธ ๐๐ถ๐ฟ ๐ฆ๐ฒ๐ฝ๐ฎ๐ฟ๐ฎ๐๐ถ๐ผ๐ป ๐จ๐ป๐ถ๐ (๐๐ฆ๐จ) – Separates Nitrogen (N2) from Air via Distillation or Adsorption.
โก๏ธ ๐๐ผ๐บ๐ฝ๐ฟ๐ฒ๐๐๐ผ๐ฟ๐ – Attain high pressures (~150 bar) to favor NH3 production as the Haber-Bosch Reaction has 4 mols of Gas as Reactants and 2 mols as Products.
โ๏ธ ๐๐บ๐บ๐ผ๐ป๐ถ๐ฎ ๐ฅ๐ฒ๐ฎ๐ฐ๐๐ผ๐ฟ – Uses an Iron Oxide Catalyst to produce NH3. A feed stoichiometric H2:N2 ratio of 3 is ideal.
โ๏ธ ๐ฅ๐ฒ๐ณ๐ฟ๐ถ๐ด๐ฒ๐ฟ๐ฎ๐๐ถ๐ผ๐ป – Condenses NH3 to separate it from unreacted Gases.
โป๏ธ ๐ฅ๐ฒ๐ฐ๐๐ฐ๐น๐ฒ – Unreacted Gases are sent back to the Reactor to improve overall conversion from ~15% per-pass to 95%+. A Purge Line might be needed to assist with imbalances in the N2 and H2 feed.
It is important to simulate the Ammonia Reactor to optimize its operating temperature and layout.
This is because if the temperature is:
๐ฅ ๐ง๐ผ๐ผ ๐๐ถ๐ด๐ต – The equilibrium would become unfavorable for NH3 Production as the Reaction is exothermic. This results in excessive Recycle flow rates required.
๐ง ๐ง๐ผ๐ผ ๐๐ผ๐ – The rate of Reaction will slow to a stop, as the Reaction has a high activation energy requirement.
Thus, optimizing the number and volume of Catalyst Beds and the methods of Interstage Cooling (via Heat Exchanger or Quench) is key to maximizing NH3 Production.Source: Joaquim Tsu, Bryan Research & Engineering, LLC, 28 Feb 2023, Green Ammonia Process Simulation, Linkedin

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3/4/2024 8:19 AM |
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3/1/2023 5:24 AM |