Catalytic steam reforming of biogas – Effects of feed composition and operating conditions

A study was conducted on the steam reforming of biogas mixtures over a 4 wt.% Rh/La–Al2O3 catalyst, where the effects of temperature (590–685 °C), steam (S/C molar ratio = 1.28–3.86), CO2/CH4 molar ratio (0.55–1.51), and the gas hourly space velocity (9810–27,000 hr−1) on the conversions and product...

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Published inInternational journal of hydrogen energy Vol. 40; no. 2; pp. 1005 - 1015
Main Authors Ahmed, Shabbir, Lee, Sheldon H.D., Ferrandon, Magali S.
Format Journal Article
LanguageEnglish
Published United Kingdom Elsevier Ltd 12.01.2015
Elsevier
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Abstract A study was conducted on the steam reforming of biogas mixtures over a 4 wt.% Rh/La–Al2O3 catalyst, where the effects of temperature (590–685 °C), steam (S/C molar ratio = 1.28–3.86), CO2/CH4 molar ratio (0.55–1.51), and the gas hourly space velocity (9810–27,000 hr−1) on the conversions and product yields were evaluated. Within these ranges, temperature and steam had the most pronounced effect on methane and carbon dioxide conversions. The highest methane conversion observed was 99%. Low temperatures and high S/C resulted in a net CO2 production. The water gas shift reaction appeared to have a stronger effect on the CO2 conversion than the CO2 reforming reaction. Experimental methane conversions were lower than the equilibrium predicted values. Lower temperature operations yielded a lower carbon balance suggesting the tendency to form carbonaceous species other than CO, CO2, and CH4. The presence of CO2 in the biogas contributed to the CO yield (beyond that from CH4 steam reforming) only above certain CO2/CH4 ratios. •A study of the steam reforming of biogas was conducted with a rhodium catalyst.•The effects of temperature, feed composition (S/C, CO2/CH4), and GHSV were studied.•99% of the methane was converted at 650 °C, 19,600 hr−1, and [H2O/(CO2+CH4)] = 3.87.•Net conversion of CO2 is favored at high CO2/CH4 ratios, high temperatures, and low H2O/C ratios.
AbstractList A study was conducted on the steam reforming of biogas mixtures over a 4 wt.% Rh/La-Al sub(2)O sub(3) catalyst, where the effects of temperature (590-685 degree C), steam (S/C molar ratio = 1.28-3.86), CO sub(2)/CH sub(4) molar ratio (0.55-1.51), and the gas hourly space velocity (9810-27,000 hr super(-1)) on the conversions and product yields were evaluated. Within these ranges, temperature and steam had the most pronounced effect on methane and carbon dioxide conversions. The highest methane conversion observed was 99%. Low temperatures and high S/C resulted in a net CO sub(2) production. The water gas shift reaction appeared to have a stronger effect on the CO sub(2) conversion than the CO sub(2) reforming reaction. Experimental methane conversions were lower than the equilibrium predicted values. Lower temperature operations yielded a lower carbon balance suggesting the tendency to form carbonaceous species other than CO, CO sub(2), and CH sub(4). The presence of CO sub(2) in the biogas contributed to the CO yield (beyond that from CH sub(4) steam reforming) only above certain CO sub(2)/CH sub(4) ratios.
A study was conducted on the steam reforming of biogas mixtures over a 4 wt.% Rh/La–Al2O3 catalyst, where the effects of temperature (590–685 °C), steam (S/C molar ratio = 1.28–3.86), CO2/CH4 molar ratio (0.55–1.51), and the gas hourly space velocity (9810–27,000 hr−1) on the conversions and product yields were evaluated. Within these ranges, temperature and steam had the most pronounced effect on methane and carbon dioxide conversions. The highest methane conversion observed was 99%. Low temperatures and high S/C resulted in a net CO2 production. The water gas shift reaction appeared to have a stronger effect on the CO2 conversion than the CO2 reforming reaction. Experimental methane conversions were lower than the equilibrium predicted values. Lower temperature operations yielded a lower carbon balance suggesting the tendency to form carbonaceous species other than CO, CO2, and CH4. The presence of CO2 in the biogas contributed to the CO yield (beyond that from CH4 steam reforming) only above certain CO2/CH4 ratios. •A study of the steam reforming of biogas was conducted with a rhodium catalyst.•The effects of temperature, feed composition (S/C, CO2/CH4), and GHSV were studied.•99% of the methane was converted at 650 °C, 19,600 hr−1, and [H2O/(CO2+CH4)] = 3.87.•Net conversion of CO2 is favored at high CO2/CH4 ratios, high temperatures, and low H2O/C ratios.
Author Ferrandon, Magali S.
Lee, Sheldon H.D.
Ahmed, Shabbir
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  givenname: Magali S.
  surname: Ferrandon
  fullname: Ferrandon, Magali S.
BackLink https://www.osti.gov/biblio/1254761$$D View this record in Osti.gov
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Keywords Biogas
Reforming
CO2/CH4 molar ratio
Rhodium catalyst
S/C molar ratio
Hydrogen
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Snippet A study was conducted on the steam reforming of biogas mixtures over a 4 wt.% Rh/La–Al2O3 catalyst, where the effects of temperature (590–685 °C), steam (S/C...
A study was conducted on the steam reforming of biogas mixtures over a 4 wt.% Rh/La-Al sub(2)O sub(3) catalyst, where the effects of temperature (590-685...
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SubjectTerms Biogas
Carbon
Carbon dioxide
Carbon monoxide
Catalysts
CO2/CH4 molar ratio
Conversion
Hydrogen
Hydrogen-based energy
Methane
Reforming
Rhodium catalyst
S/C molar ratio
Title Catalytic steam reforming of biogas – Effects of feed composition and operating conditions
URI https://dx.doi.org/10.1016/j.ijhydene.2014.11.009
https://search.proquest.com/docview/1669847009
https://www.osti.gov/biblio/1254761
Volume 40
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