4.7 Article

Simulation and energetic assessment of the ammonia synthesis loop with ionic liquid-Based ammonia recovery from recycle gas

Journal

SEPARATION AND PURIFICATION TECHNOLOGY
Volume 301, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.seppur.2022.121951

Keywords

Ionic liquids; Ammonia separation; Absorption; Process simulation; Process assessment

Funding

  1. National Natural Science Foundation of China
  2. Major Scientific and Technological Project of Shanxi Province of China
  3. Youth Innovation Promotion Association of the Chinese Academy of Sciences
  4. Henan Major Science and Technology Project
  5. [21890760]
  6. [21838010]
  7. [22122814]
  8. [20201102005]
  9. [2018064]
  10. [201300310900]

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This study proposes an IL-based ammonia synthesis loop that separates and recovers NH3 from recycle gas using ionic liquids as solvents, aiming to reduce energy consumption and increase NH3 production capacity. A systematic methodology considering thermodynamic models, process simulation, and assessment is established to evaluate the feasibility of the IL-HB. The simulation results demonstrate significant techno-economic potentials of the IL-HB, with reduced energy consumption and CO2 emissions compared to the conventional Haber-Bosch process.
Ammonia (NH3) synthesis by Haber-Bosch process is recognized as the most important pathway for NH3 pro-duction. However, NH3 recovery from recycle gas using conventional condensation separation is still an energy-intensive process. Ionic liquids (ILs) have been proved to be effective solvents for NH3 separation and recovery due to their unique properties. In this work, a novel IL-based ammonia synthesis loop (IL-HB) was proposed, taking the protic IL [Bim][NTf2] as the absorbent to separate and recover NH3 from recycle gas, aiming to reduce the energy consumption and increase the NH3 production capacity of the synthesis tower. Then, a systematic methodology that considers reliable thermodynamic models as well as process simulation and assessment was established to evaluate the feasibility of the IL-HB. Furthermore, two entire processes (ILa-HB and ILb-HB) that integrate the optimal sections of IL-based NH3 recovery from recycle gas with the ammonia synthesis loop as a whole were simulated, taking the conventional Haber-Bosch ammonia synthesis loop (HB) as the benchmark. The simulation results prove great techno-economic potentials of the proposed ILa-HB and ILb-HB. Compared with the HB, the energy consumption and CO2 emissions of ILb-HB can be reduced by 16.01% and 29.44%, respec-tively, presenting enormous energy-saving and environment-friendly superiority.

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