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Catalytic hydrogen combustion

Catalytic hydrogen combustion, hydrogen combustion, hydrogen utilisation in PEM fuel cells, hydrogen production from fossil fuels (TUBITAK-MRC). [Pg.178]

Catalytic Hydrogen Combustion 1 [CHC 1] Single-channel Micro Reactor for Catalytic Hydrogen Combustion... [Pg.321]

Catalytic Hydrogen Combustion 3 [CHC 3] Combined Mixer/Cross-flow Com-bustor/Heat Exchanger for Determination of the Kinetics of Hydrogen Oxidation... [Pg.322]

Catalytic Hydrogen Combustion 4 [CHC 4] Cross-flow Combustor/Heat Exchanger lor Hydrogen Oxidation... [Pg.324]

CHC CHCC CNC coc CP AC CPR CPU CVD CW Catalytic hydrogen combustion Catalytic hydrocarbon combustion Computerized Numeric Control Cyclo olefin copolymer Center for Process Analytical Chemistry Catalytic plate reactor Central processing unit Chemical vapor deposition Continous wave... [Pg.683]

V. M. Shinde, G. Madras, Nanostructured Pd modified Ni/Ce(>2 catalyst for water gas shift and catalytic hydrogen combustion reaction, Appl. Catal. B Environ. 132-133 (2013) 28 38. [Pg.94]

Large quantities of sulphur are recovered from petroleum and natural gas. Naturally occurring hydrogen sulphide, HjS, and that produced in the cracking and catalytic hydrogenation of petroleum is first removed by absorption and the regenerated gas is converted to sulphur by partial combustion with air, the overall reaction being,... [Pg.261]

Catalytic hydrogenations are generally highly selective with almost quantitative yield (Rylander, 1979 Augustine, 1976). As the metals are recovered from spent catalysts, essentially no non-combustible waste is generated. [Pg.30]

Dobereiner reports the first catalytic hydrogenation the Pt-catalyzed combustion of hydrogen in air [2,3]... [Pg.88]

Fig. 1.9. Coupling of dehydrogenation of ethylbenzene to styrene and hydrogen combustion in a catalytic fixed-bed reverse flow reactor [9]. (a, b) Fixed-bed temperature profiles during production and regeneration cycle. Fig. 1.9. Coupling of dehydrogenation of ethylbenzene to styrene and hydrogen combustion in a catalytic fixed-bed reverse flow reactor [9]. (a, b) Fixed-bed temperature profiles during production and regeneration cycle.
The CHC-concept shows the lowest HC-emissions in comparison to the other cold-start concepts. This is due to the fast and direct heating of the catalytic surface where the hydrogen combustion only takes place at active parts of the catalyst. [Pg.134]

Jessop and co-workers have pointed out that homogeneous catalysis in supercritical fluids can offer high rates, improved selectivity, and elimination of mass-transfer problems.169 They have used a ruthenium phosphine catalyst to reduce supercritical carbon dioxide to formic acid using hydrogen.170 The reaction might be used to recycle waste carbon dioxide from combustion. It also avoids the use of poisonous carbon monoxide to make formic acid and its derivatives. There is no need for the usual solvent for such a reaction, because the excess carbon dioxide is the solvent. If the reaction is run in the presence of dimethy-lamine, dimethylformamide is obtained with 100% selectivity at 92-94% conversion.171 In this example, the ruthenium phosphine catalyst was supported on silica. Asymmetric catalytic hydrogenation of dehydroaminoacid derivatives (8.16) can be performed in carbon dioxide using ruthenium chiral phosphine catalysts.172... [Pg.212]


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See also in sourсe #XX -- [ Pg.320 ]




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