Novel Sorption-Enhanced Methanation with Simultaneous CO2 Removal for the Production of Synthetic Natural Gas

Soo Ik Im, Ki Bong Lee

Research output: Contribution to journalArticlepeer-review

8 Citations (Scopus)


With increasing consumption of natural gas as a clean energy source and demand for efficient use of cheap and abundant coal, the production of synthetic natural gas from coal has been receiving considerable interest. In this study, the methanation reaction of coal-derived syngas for the production of synthetic natural gas was investigated using numerical simulations. In particular, the concept of a sorption-enhanced reaction, in which CO2 removal by sorption is carried out simultaneously with the reaction, was newly applied to the methanation reaction. Effects of the operating parameters such as the fraction of catalyst and sorbent, temperature, pressure, and feed ratio (H2/CO, H2O/CO, and CO2/CO) on CO conversion and purity, selectivity, and productivity of CH4 were evaluated by computational studies. It was found that the performance of the sorption-enhanced methanation reaction is controlled by both thermodynamic equilibrium and reaction kinetics. Therefore, the reaction would require an optimal catalyst fraction, temperature, and pressure conditions for maximum efficiency. Optimal H2/CO and H2O/CO ratios exist considering reaction performance, and any CO2 content in the feed reduces CH4 productivity. Compared to the conventional methanation reaction, the sorption-enhanced methanation reaction produces CH4 in high purity (>95%), which can be directly used for synthetic natural gas without further separation processes.

Original languageEnglish
Pages (from-to)9244-9255
Number of pages12
JournalIndustrial and Engineering Chemistry Research
Issue number34
Publication statusPublished - 2016 Aug 31

Bibliographical note

Publisher Copyright:
© 2016 American Chemical Society.

ASJC Scopus subject areas

  • General Chemistry
  • General Chemical Engineering
  • Industrial and Manufacturing Engineering


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