Industrial & Engineering Chemistry Research · 2011 · 46 citations · 41 references
Natural SciencesChemical EngineeringChemistryCatalysisProcess DynamicsReaction EngineeringCatalyst DeactivationCatalyst DesignCatalyst StabilityCatalytic MaterialsCatalytic Reaction EngineeringCatalytic Reaction KineticsCatalyst Deactivation CharacterizationCatalyst Deactivation ControlCatalyst Deactivation In Packed BedsCatalyst RecyclingCokingDeactivation KineticsDeactivation MechanismsTransient Kinetic Analysis
Deoxygenation of dilute and concentrated stearic acid over 2% Pd/C beads was performed in a continuous reactor at 300 °C and 20 bar pressure of Ar or 5% H 2 /Ar. Stable operation was obtained in 5% H 2 atmosphere, with 95% conversion of 10 mol % dilute stearic acid in dodecane and 12% conversion of pure stearic acid. Deactivation took place in H 2 -deficient gas atmosphere, probably as a result of the formation of unsaturated products and coking in the pore system. Transient experiments with step changes were performed: 1 h was required for the step change to be visible in liquid sampling, whereas steady states were achieved after a total of 2.5–3 h. Postreaction analysis of the spent catalyst revealed that a deactivation profile was formed downward over the catalyst bed.
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George W. Huber, Paul O’Connor, Avelino Corma · Applied Catalysis A General · 2007 · 626 citations
Life Sciences, Chemical Engineering, Downstream Processing +10
Hydrocarbons for diesel fuel via decarboxylation of vegetable oils
Iva Kubičková, Mathias Snåre, Kari Eränen et al. · Catalysis Today · 2005 · 397 citations
Catalytic Deoxygenation of Fatty Acids and Their Derivatives
Päivi Mäki‐Arvela, Iva Kubičková, Mathias Snåre et al. · Energy & Fuels · 2006 · 355 citations