Experimental Investigation of the Application of Ionic Liquids to Methanol Synthesis in Membrane Reactors

In this study, a high-pressure membrane reactor (MR) was employed to carry out the methanol synthesis (MeS) reaction. Syngas was fed into the MR shell side where a commercial MeS catalyst was used, while the tube side was swept with a high boiling point liquid with good solubility toward methanol. A...

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Published inIndustrial & engineering chemistry research Vol. 58; no. 27; pp. 11811 - 11820
Main Authors Zebarjad, Fatemeh Sadat, Hu, Sheng, Li, Zhongtang, Tsotsis, Theodore T
Format Journal Article
LanguageEnglish
Published American Chemical Society 10.07.2019
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ISSN0888-5885
1520-5045
1520-5045
DOI10.1021/acs.iecr.9b01178

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Abstract In this study, a high-pressure membrane reactor (MR) was employed to carry out the methanol synthesis (MeS) reaction. Syngas was fed into the MR shell side where a commercial MeS catalyst was used, while the tube side was swept with a high boiling point liquid with good solubility toward methanol. A mesoporous alumina ceramic membrane was utilized after its surface had been modified to be rendered more hydrophobic. The efficiency of the MR was investigated under a variety of experimental conditions (different pressures, temperatures, sweep liquid flow rates, and types of sweep liquids). The results reveal improved per single-pass carbon conversions when compared to the conventional packed-bed reactor. An ionic liquid (IL), 1-ethyl-3-methylimidazolium tetrafluoroborate, was utilized in the MR as the sweep liquid. The experimental results are compared to those previously reported by our group (Li, Z.; Tsotsis, T. T. J. Membrane Sci. 2019, 570, 103 ) while using a conventional petroleum-derived solvent as sweep liquid, tetraethylene glycol dimethyl ether (TGDE). Enhanced carbon conversion (over the petroleum-derived solvent) was obtained using the IL.
AbstractList In this study, a high-pressure membrane reactor (MR) was employed to carry out the methanol synthesis (MeS) reaction. Syngas was fed into the MR shell side where a commercial MeS catalyst was used, while the tube side was swept with a high boiling point liquid with good solubility toward methanol. A mesoporous alumina ceramic membrane was utilized after its surface had been modified to be rendered more hydrophobic. The efficiency of the MR was investigated under a variety of experimental conditions (different pressures, temperatures, sweep liquid flow rates, and types of sweep liquids). The results reveal improved per single-pass carbon conversions when compared to the conventional packed-bed reactor. An ionic liquid (IL), 1-ethyl-3-methylimidazolium tetrafluoroborate, was utilized in the MR as the sweep liquid. The experimental results are compared to those previously reported by our group (Li, Z.; Tsotsis, T. T. J. Membrane Sci.2019, 570, 103) while using a conventional petroleum-derived solvent as sweep liquid, tetraethylene glycol dimethyl ether (TGDE). Enhanced carbon conversion (over the petroleum-derived solvent) was obtained using the IL.
Author Hu, Sheng
Li, Zhongtang
Tsotsis, Theodore T
Zebarjad, Fatemeh Sadat
AuthorAffiliation Mork Family Department of Chemical Engineering and Materials Science
AuthorAffiliation_xml – name: Mork Family Department of Chemical Engineering and Materials Science
Author_xml – sequence: 1
  givenname: Fatemeh Sadat
  orcidid: 0000-0002-2330-1987
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  fullname: Zebarjad, Fatemeh Sadat
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  givenname: Sheng
  surname: Hu
  fullname: Hu, Sheng
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  givenname: Zhongtang
  surname: Li
  fullname: Li, Zhongtang
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  givenname: Theodore T
  surname: Tsotsis
  fullname: Tsotsis, Theodore T
  email: tsotsis@usc.edu
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SubjectTerms aluminum oxide
boiling point
carbon
catalysts
ceramics
hydrophobicity
ionic liquids
liquids
methanol
porous media
process design
solubility
synthesis gas
temperature
Title Experimental Investigation of the Application of Ionic Liquids to Methanol Synthesis in Membrane Reactors
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