In-situ reforming of biomass primary tars via reactive flash volatilization

Research output: Contribution to journalArticleResearchpeer-review

Abstract

Tar formation during biomass gasification has remained a major challenge. Using acetol and guaiacol as model tar compounds from cellulose and lignin, respectively, in-situ tar conversion into synthesis gas (H2 and CO) was studied using a Rh–Ni/Al2O3 catalyst under reactive flash volatilization conditions. The influence of operating conditions, including temperature, steam-to-carbon molar ratio (S/C), carbon-to-oxygen molar ratio (C/O), gas hourly space velocity (GHSV), and catalyst weight, on the H2/CO molar ratio in the product gas were experimentally examined. The contribution of non-catalytic thermal oxidation on overall conversion was also measured by varying the distance between the catalyst bed and the feeding point position. In the case of acetol reforming at 650 °C, more than 60% of the carbon in the feed was converted via thermal oxidation into permanent gases before reaching the catalytic bed. Moreover, a minimum reaction temperature of 500 °C was necessary to avoid coke formation and the optimal operating conditions for reforming of acetol were 650 °C, C/O = 1.7, S/C = 1.2, and atmospheric pressure. Likewise, for guaiacol, the minimum operating temperature of 600 °C was required. By using two pure components, this study has provided insight into how reactive flash volatilization generates tar-free synthesis gas.

Original languageEnglish
Pages (from-to)1180-1187
Number of pages8
JournalRenewable Energy
Volume147
Issue numberPart 1
DOIs
Publication statusPublished - 1 Mar 2020

Keywords

  • Acetol
  • Guaiacol
  • Reaction kinetics
  • Reactive flash volatilization
  • Reforming

Cite this

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title = "In-situ reforming of biomass primary tars via reactive flash volatilization",
abstract = "Tar formation during biomass gasification has remained a major challenge. Using acetol and guaiacol as model tar compounds from cellulose and lignin, respectively, in-situ tar conversion into synthesis gas (H2 and CO) was studied using a Rh–Ni/Al2O3 catalyst under reactive flash volatilization conditions. The influence of operating conditions, including temperature, steam-to-carbon molar ratio (S/C), carbon-to-oxygen molar ratio (C/O), gas hourly space velocity (GHSV), and catalyst weight, on the H2/CO molar ratio in the product gas were experimentally examined. The contribution of non-catalytic thermal oxidation on overall conversion was also measured by varying the distance between the catalyst bed and the feeding point position. In the case of acetol reforming at 650 °C, more than 60{\%} of the carbon in the feed was converted via thermal oxidation into permanent gases before reaching the catalytic bed. Moreover, a minimum reaction temperature of 500 °C was necessary to avoid coke formation and the optimal operating conditions for reforming of acetol were 650 °C, C/O = 1.7, S/C = 1.2, and atmospheric pressure. Likewise, for guaiacol, the minimum operating temperature of 600 °C was required. By using two pure components, this study has provided insight into how reactive flash volatilization generates tar-free synthesis gas.",
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In-situ reforming of biomass primary tars via reactive flash volatilization. / Ahmed, Tigabwa Y.; Hoadley, Andrew F.A.; Tanksale, Akshat.

In: Renewable Energy, Vol. 147, No. Part 1, 01.03.2020, p. 1180-1187.

Research output: Contribution to journalArticleResearchpeer-review

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