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A novel recovery loop for reducing greenhouse gas emission: Simultaneous production of syngas and pure hydrogen in a membrane reformer

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  • Parvasi, P.
  • Jokar, S.M.
  • Shamseddini, A.
  • Babapoor, A.
  • Mirzaie, F.
  • Abbasfard, H.
  • Basile, A.

Abstract

In this work, a novel loop is designed for simultaneous production of pure hydrogen and synthesis gas (syngas) from a domestic refinery purge gas. The purge gases are the combination of flare gas (consist mainly of methane) and high-temperature flue gas (containing CO2 and steam). The proposed loop including three main parts: 1) flare gas desulfurization unit; 2) CO2 and steam recovery unit and, 3) a membrane reformer for combined dry-steam reforming of methane, heating with high-temperature flue gas. The hazardous hot gases convert to valuable products instead of discharging to the atmosphere.

Suggested Citation

  • Parvasi, P. & Jokar, S.M. & Shamseddini, A. & Babapoor, A. & Mirzaie, F. & Abbasfard, H. & Basile, A., 2020. "A novel recovery loop for reducing greenhouse gas emission: Simultaneous production of syngas and pure hydrogen in a membrane reformer," Renewable Energy, Elsevier, vol. 153(C), pages 130-142.
    • Handle: RePEc:eee:renene:v:153:y:2020:i:c:p:130-142
    DOI: 10.1016/j.renene.2020.01.147
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    References listed on IDEAS

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    1. Comodi, Gabriele & Renzi, Massimiliano & Rossi, Mosè, 2016. "Energy efficiency improvement in oil refineries through flare gas recovery technique to meet the emission trading targets," Energy, Elsevier, vol. 109(C), pages 1-12.
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    3. Cao, Xia, 2003. "Climate change and energy development: implications for developing countries," Resources Policy, Elsevier, vol. 29(1-2), pages 61-67.
    4. Huang, Weijia & Zheng, Danxing & Xie, Hui & Li, Yun & Wu, Weize, 2019. "Hybrid physical-chemical absorption process for carbon capture with strategy of high-pressure absorption/medium-pressure desorption," Applied Energy, Elsevier, vol. 239(C), pages 928-937.
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