The present work is focused on the aqueous-phase reforming of ethylene glycol at 500 K. The influence of the system pressure (27 to 36 bar) and the catalyst weight/ethylene glycol flow rate ratio has been studied using a Pt/Al2O3 research catalyst. A comparison of the latter with a Ni/Al coprecipitated catalyst showed a significant influence on hydrogen and alkane selectivities.
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- Bioenergy II: Tin Catalysed Esterification of Free Fatty Acids
- Bioenergy II: Modeling and Multi-Objective Optimization of Different Biodiesel Production Processes
- Bioenergy II: Characterization of the Pesticide Properties of Tobacco Bio-Oil
- Bioenergy II: Hydrogen Production by Aqueous-Phase Reforming
- Bioenergy II: Suitability of Wood Chips and Various Biomass Types for Use in Plant of BtL Production by Gasification
- Bioenergy II: Bio-Ethanol from Municipal Solid Waste (MSW): The Role of Biomass Properties and Structures During the Ethanol Conversion Process
- Bioenergy II: The Development of a Reactive Distillation Process for the Production of 1,1 Diethoxy Butane from Bioalcohol: Kinetic Study and Simulation Model
- Bioenergy II: Comparison of Laboratory and Industrial Saccharomyces cerevisiae Strains for their Stress Tolerance
- Experimental Study of a Novel Fast Gas-Solid Separator for Pyrolysis Reactors
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- Biomass Sourcing and Logistics: From Theory to Practice
- Ionic Liquid-Aided Carboxymethylation of Kraft Pulp
- Synthesis and Characterization of Pt-Sn Incorporated MCM-41 and Pt Incorporated Sn-SiO Type Mesoporous Catalysts for Direct Ethanol Fuel Cell
- Toluene Combustion over Metal Oxide Washcoated Monolithic Catalyst
- Low Temperature Water-Gas Shift Reaction on Au-CeO/AlO Catalysts
- Electrochemical Performance of Low Pt and Ru Loaded Fe-Ni Bimetallics as an Anode Electrode in Direct Ethanol Fuel Cells
- FTIR Studies of Urea Decomposition over Pt-Alumina and Cu-Alumina Catalysts
- HZSM-5 and H-Ferrierite Acidity Modification by Silylation and Their Activities in n-Butene Isomerisation
- Production of Syngas by Combination of CO Reforming and Partial Oxidation of CH over Ni/AlO Catalysts in Fixed-bed Reactor
- Modelling Catalyst Deactivation by External Coke Deposition during Fluid Catalytic Cracking
- Cascade Control Scheme for Tubular Reactors with Multiple Temperature Measurements
- Effect of Gas Jet on Agglomeration of Inhalable Particles
- Microwave-Enhanced Alkali Catalyzed Transesterification of Kenaf Seed Oil
- Relation between Volumetric Mass Transfer Coefficient and Power Input per Unit Volume for Converging-Diverging Tube Airlift Fermenter
- Effects of AlCl-NaCl Content on the Formation of Mesocarbon Microbeads
- Removal of Zinc Ions from Water Using Emulsion Liquid Membrane
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Bioenergy II: Hydrogen Production by Aqueous-Phase Reforming
1University of Zaragoza, anaval@unizar.es
2University of Zaragoza, medcat@unizar.es
3University of Zaragoza, miroliva@unizar.es
4University of Zaragoza, jruizp@unizar.es
5University of Zaragoza, luciag@unizar.es
6University of Zaragoza, qtarauzo@unizar.es
Citation Information: International Journal of Chemical Reactor Engineering. Volume 8, Issue 1, Pages –, ISSN (Online) 1542-6580, DOI: 10.2202/1542-6580.1924, February 2010
Publication History:
- Published Online:
- 2010-02-03
Keywords: aqueous-phase reforming; ethylene glycol; hydrogen; Pt/Al<sub>2</sub>O<sub>3</sub>; Ni catalyst; coprecipitated catalyst
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