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Grant: Research Tools and Instruments - Category 1 (<$150,000)

École Polytechnique de Montréal

$150,000.00

Particle characterization- size distribution, pore distribution- of precursor, micronized powder and cataslyst

FY 2006-07

Summary
This proposal concerns catalyst manufacture, which accounts for $5 billion worth of sales in North America.  On a global basis, products derived from catalysis represent $3 trillion.  Despite the enormous impact of catalysis in our daily lives, there remains significant challenges in developing economic and environmental processes  The difficulty in working in this field relates to the interaction between the three primary phases of matter - solids, liquids and gases.  For example, we often begin with solution chemistry to form crystals (G-L).  The next step in the manufacturing process may include drying followed by micronization where the crystals are pulverized to a sub-micron size in air or liquid (G-S, L-S).  The third step involves granulation or spray drying in order to produce micro-spheres that have mechanical stability - attrition resistance, abrasion resistance, and crush strength - as well as the correct particle morphology - size distribution, shape, surface area, and porosity (L-S, G-L-S).  Finally, powders are employed in physical systems at elevated temperatures (1250 K) and pressures in the gas or liquid phase (G-S, L-S).   Our group is also working on reactor systems where we are seeking solid-solid reactions at elevated temperature (G-S-S). My group works in the general field of catalyst but in particular partial oxidation and dehydration: butane to maleic anhydride over a VPO catalyst, methanol to olefins over proprietary catalysts fabricated by Haldor-Topsoe, as well as Chemical Looping Combustion that requires a solid oxidant.  In each of these programs, particle size, surface area and pore size distribution are critical factors - at the synthesis stage, spray drying, and finally as a tool to examine the attrition rates in the reactors (to be able to distinguish between fractured particles and elutriation of fines).  These standard processes will be accompanied by equipment development in which we will attempt to modify the Particle Size Analyzer in order to be capable of monitoring the growth of crystallites on-line and in real time.  Most research in this area is performed ex-situ with a large variability with respect to the "optimum" residence time for crystal growth.
Program
Research Tools and Instruments - Category 1 (<$150,000)
Location
Quebec, Canada
Recipient Type
Academia
Type
Grant
Source
NSERC's Awards Data

As published

Application id
346029-2007
Name nom
Patience, Gregory
Department département
Génie chimique
Organization id
64
Institution établissement
École Polytechnique de Montréal
Province en
Québec
Province fr
Québec
Country en
CANADA
Country fr
CANADA
Fiscal year exercice financier
2006
Competition year année de concours
2007
Award amount
150000
Program id
EQPEQ
Program name en
Research Tools and Instruments - Category 1 (<$150,000)
Program name fr
Outils et instruments de recherche - catégorie 1 (<150 000$)
Group en
Discovery grants programs
Group fr
Programmes de subventions à la découverte
Committee code
4
Committee name en
Chem. & Metallurgical Eng.
Committee name fr
Génies chimique et métal.
Area of application code
500
Area of application group en
Manufacturing processes and products
Area of application group fr
Procédés et produits industriels
Area of application en
Manufacturing processes and products
Area of application fr
Procédés et produits industriels
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
1
Nb partie
1
Application title
Particle characterization- size distribution, pore distribution- of precursor, micronized powder and cataslyst
Keyword
NA
Application summary
This proposal concerns catalyst manufacture, which accounts for $5 billion worth of sales in North America.  On a global basis, products derived from catalysis represent $3 trillion.  Despite the enormous impact of catalysis in our daily lives, there remains significant challenges in developing economic and environmental processes  The difficulty in working in this field relates to the interaction between the three primary phases of matter - solids, liquids and gases.  For example, we often begin with solution chemistry to form crystals (G-L).  The next step in the manufacturing process may include drying followed by micronization where the crystals are pulverized to a sub-micron size in air or liquid (G-S, L-S).  The third step involves granulation or spray drying in order to produce micro-spheres that have mechanical stability - attrition resistance, abrasion resistance, and crush strength - as well as the correct particle morphology - size distribution, shape, surface area, and porosity (L-S, G-L-S).  Finally, powders are employed in physical systems at elevated temperatures (1250 K) and pressures in the gas or liquid phase (G-S, L-S).   Our group is also working on reactor systems where we are seeking solid-solid reactions at elevated temperature (G-S-S). My group works in the general field of catalyst but in particular partial oxidation and dehydration: butane to maleic anhydride over a VPO catalyst, methanol to olefins over proprietary catalysts fabricated by Haldor-Topsoe, as well as Chemical Looping Combustion that requires a solid oxidant.  In each of these programs, particle size, surface area and pore size distribution are critical factors - at the synthesis stage, spray drying, and finally as a tool to examine the attrition rates in the reactors (to be able to distinguish between fractured particles and elutriation of fines).  These standard processes will be accompanied by equipment development in which we will attempt to modify the Particle Size Analyzer in order to be capable of monitoring the growth of crystallites on-line and in real time.  Most research in this area is performed ex-situ with a large variability with respect to the "optimum" residence time for crystal growth.