Abstract
Calcined dolomites and commercial steam reforming catalysts are used downstream biomass gasifiers for hot catalytic raw gas cleaning. To further compare these solids under a rigorous basis, a reaction network and a kinetic model are presented. The apparent kinetic constant for the tar reduction is here proposed as a basis of comparison. Tar sampling and analysis, and the units used for the space-time in the catalytic reactor affect the kinetic constants observed. (author) (2 refs.)
Citation Formats
Corella, J, Narvaez, I, and Orio, A.
Criteria for selection of dolomites and catalysts for tar elimination from biomass gasification gas. Kinetic constants.
Finland: N. p.,
1996.
Web.
Corella, J, Narvaez, I, & Orio, A.
Criteria for selection of dolomites and catalysts for tar elimination from biomass gasification gas. Kinetic constants.
Finland.
Corella, J, Narvaez, I, and Orio, A.
1996.
"Criteria for selection of dolomites and catalysts for tar elimination from biomass gasification gas. Kinetic constants."
Finland.
@misc{etde_464538,
title = {Criteria for selection of dolomites and catalysts for tar elimination from biomass gasification gas. Kinetic constants}
author = {Corella, J, Narvaez, I, and Orio, A}
abstractNote = {Calcined dolomites and commercial steam reforming catalysts are used downstream biomass gasifiers for hot catalytic raw gas cleaning. To further compare these solids under a rigorous basis, a reaction network and a kinetic model are presented. The apparent kinetic constant for the tar reduction is here proposed as a basis of comparison. Tar sampling and analysis, and the units used for the space-time in the catalytic reactor affect the kinetic constants observed. (author) (2 refs.)}
place = {Finland}
year = {1996}
month = {Dec}
}
title = {Criteria for selection of dolomites and catalysts for tar elimination from biomass gasification gas. Kinetic constants}
author = {Corella, J, Narvaez, I, and Orio, A}
abstractNote = {Calcined dolomites and commercial steam reforming catalysts are used downstream biomass gasifiers for hot catalytic raw gas cleaning. To further compare these solids under a rigorous basis, a reaction network and a kinetic model are presented. The apparent kinetic constant for the tar reduction is here proposed as a basis of comparison. Tar sampling and analysis, and the units used for the space-time in the catalytic reactor affect the kinetic constants observed. (author) (2 refs.)}
place = {Finland}
year = {1996}
month = {Dec}
}