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Grant: Collaborative Research and Development Grants

University of Western Ontario

$45,500.00

Biomass gasification: product quantification and reaction kinetics

FY 2010-11

Summary
The goal of the present study is to develop new product quantification approaches for syngas and tars obtained from biomass catalytic gasification. The laboratory scale and analytical equipments to be used will allow quantitative assessments of syngas components and tar species using GC-MS with FID and TCD detectors, packed and capillary columns. A number of capillary columns with different polarities will be characterized and studied to separate tar components, such as oxygenates and aromatics, determining adsorption parameters, retention times and statistical moments of different order. This will provide to the partner company of this CRD research, Mandel Scientific, a competitive and scientific advantage, establishing a niche market for their GC-MS-capillary column instruments for biomass gasification product analysis. Furthermore, in order to perform these experiments in realistic scenarios that simulate industrial conditions, catalysts as well as kinetic models for catalytic gasification of biomass will be studied under relevant process conditions. The ultimate goal of these new catalysts will be to optimize H2/CO ratios for alcohol production (e.g. ethanol), with minimum coke and tar formation and for long term catalyst stability. To accomplish this, we propose to consider nickel based catalysts modified with dopants and kinetic models accounting for adsorption, diffusion and reaction phenomena. Kinetics will be established using data from the advanced analytical equipment developed in collaboration with Mandel.
Program
Collaborative Research and Development Grants
Location
Ontario, Canada
Recipient Type
Academia
Type
Grant
Source
NSERC's Awards Data

As published

Application id
385786-2009
Name nom
DeLasa, Hugo
Department département
Chemical and Biochemical Engineering
Organization id
36
Institution établissement
University of Western Ontario
Province en
Ontario
Province fr
Ontario
Country en
CANADA
Country fr
CANADA
Fiscal year exercice financier
2010
Competition year année de concours
2009
Award amount
45500
Program id
CRDPJ
Program name en
Collaborative Research and Development Grants
Program name fr
Subventions de recherche et développement coopérative
Group en
Research partnerships programs
Group fr
Programmes de partenariat
Committee code
96
Committee name en
RPP Internal Decision Cttee
Committee name fr
Cté de décision interne - PPR
Area of application code
303
Area of application group en
Energy resources
Area of application group fr
Ressources d'énergie
Area of application en
Alternative energy resources
Area of application fr
Autres ressources d'énergie
Research subject code
1801
Research subject group en
Chemical engineering
Research subject group fr
Génie chimique
Research subject en
Reaction fundamentals and reactor design
Research subject fr
Principes des réactions et conception de réacteurs
Partie
2
Nb partie
3
Application title
Biomass gasification: product quantification and reaction kinetics
Keyword
NSERC
Application summary
The goal of the present study is to develop new product quantification approaches for syngas and tars obtained from biomass catalytic gasification. The laboratory scale and analytical equipments to be used will allow quantitative assessments of syngas components and tar species using GC-MS with FID and TCD detectors, packed and capillary columns. A number of capillary columns with different polarities will be characterized and studied to separate tar components, such as oxygenates and aromatics, determining adsorption parameters, retention times and statistical moments of different order. This will provide to the partner company of this CRD research, Mandel Scientific, a competitive and scientific advantage, establishing a niche market for their GC-MS-capillary column instruments for biomass gasification product analysis. Furthermore, in order to perform these experiments in realistic scenarios that simulate industrial conditions, catalysts as well as kinetic models for catalytic gasification of biomass will be studied under relevant process conditions. The ultimate goal of these new catalysts will be to optimize H2/CO ratios for alcohol production (e.g. ethanol), with minimum coke and tar formation and for long term catalyst stability. To accomplish this, we propose to consider nickel based catalysts modified with dopants and kinetic models accounting for adsorption, diffusion and reaction phenomena. Kinetics will be established using data from the advanced analytical equipment developed in collaboration with Mandel.