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Aqueous phase reforming

Good reviews dealing with different aspects of this process can be found in the literature [80, 81]. [Pg.190]

Notably, once the oxygenated hydrocarbons have been converted into synthesis gas, it is then possible to carry out the subsequent conversion of synthesis gas into a variety of liquid products by well-established catalytic processes, such as the production of long-chain alkanes by Fischer-Tropsch synthesis and/or the production of methanol. [Pg.191]

The leaching of catalyst components into the aqueous phase during the reaction represents a possible disadvantage of the process. Therefore, the choice of catalyst support materials has to be limited to those that exhibit long-term hydrothermal stability (e.g. carbon, titania, zirconia). [Pg.191]

It is also interesting that if the goal is to produce H2-CO gas mixtures, for instance in the Fischer-Tropsch synthesis, one needs to suppress the WGSR operating in the vapor phase or to operate at higher concentrations of the oxygenated reactant in water or to use a catalyst on which the rate of the WGSR is slow. [Pg.192]


Shabaker, J. W. Davda, R. R. Huber, G. W. Cortright, R. D. Dumesic, J. A., Aqueous-phase reforming of methanol and ethylene glycol over alumina-supported platinum catalysts. Journal of Catalysis 2003, 215, 344. [Pg.225]

Dumesic has reviewed the aqueous-phase reforming of polyols to H2 and CO2 under milder conditions, i.e., 200-250 °C [43], He also showed the possibility to divert the reaction towards to production of alkanes by using an acidic support for the Pt or Pd reforming catalyst. [Pg.37]

The catalytic aqueous phase reforming might prove useful for the generation of hydrogen-rich gas from carbohydrates extracted from renewable biomass and biomass waste streams. The biomass-derived hydrocarbons are suitable to hydrogen generation from biomass, as well as for the reforming. [Pg.177]

Four hydrogen production techniques are reviewed hydrocarbon reforming ammonia cracking and two other, less common, production techniques, pyrolysis and aqueous phase reforming. [Pg.532]

An alternative approach for the utilization of biomass resources for energy applications is the production of dean-buming liquid fuels. In this respect, current technologies to produce liquid fuels from biomass are typically multi-step and energy-intensive processes. Aqueous phase reforming of sorbitol can be tailored to produce selectively a clean stream of heavier alkanes consisting primarily of butane, pentane and hexane. The conversion of sorbitol to alkanes plus CO2 and water is an exothermic process that retains approximately 95% of the heating value and only 30% of the mass of the biomass-derived reactant [278]. [Pg.213]

Aqueous phase reforming of EG takes place according to the following reaction H0CH2CH20H + 2H20 5H2 + 2C02 (6.35)... [Pg.215]

The addition of Sn to Raney Ni catalysts also improves the stability and corrosion resistance of the catalyst under aqueous phase reforming conditions. [Pg.218]

Aqueous phase reforming of glycerol in several studies by Dumesic and co-workers has been reported [270, 275, 277, 282, 289, 292, 294, 319]. The first catalysts that they reported were platinum-based materials which operate at relatively moderate temperatures (220-280 °C) and pressures that prevent steam formation. Catalyst performances are stable for a long period. The gas stream contains low levels of CO, while the major reaction intermediates detected in the liquid phase include ethanol, 1,2-pro-panediol, methanol, 1-propanol, propionic acid, acetone, propionaldehyde and lactic acid. Novel tin-promoted Raney nickel catalysts were subsequently developed. The catalytic performance of these non-precious metal catalysts is comparable to that of more costly platinum-based systems for the production of hydrogen from glycerol. [Pg.222]

Catalytic dihydrogen production form biomass is known as aqueous phase reforming (APR) [38]. It is interesting to note the absence of CO in the dihydrogen produced by the biosystem, which makes it immediately suitable for use in fuel-cells... [Pg.283]

A possibly more sophisticated method for utilizing biomass to produce synthesis gas is by aqueous phase reforming (APR), a processing method that was developed for carbohydrates and other more readily accessible biomass oxygenates by Dumesic et Valenzuela et al. however,... [Pg.18]

APR [Aqueous-Phase Reforming] A process for making hydrogen or lower alkanes from carbohydrates, biomass, or glycerol from biodiesel production. The catalyzed process operates at a relatively low temperature (180 to 260°C). Developed from 2001 at the University of Wisconsin and later by Virent Energy Systems, which operated a demonstration plant from 2006. [Pg.22]

Recently, extensive efforts have been made to synthesize liquid hydrocarbons from biomass feedstocks. In 2004, Dumesic and co-workers reported that a clean stream of alkanes could be produced by aqueous phase reforming of sorbitol over a bifunctional catalyst. The sugar is repeatedly dehydrated using a solid acid catalyst and then hydrogenated using a precious metal catalyst such... [Pg.113]


See other pages where Aqueous phase reforming is mentioned: [Pg.214]    [Pg.57]    [Pg.72]    [Pg.199]    [Pg.199]    [Pg.220]    [Pg.220]    [Pg.434]    [Pg.197]    [Pg.178]    [Pg.185]    [Pg.190]    [Pg.192]    [Pg.210]    [Pg.212]    [Pg.213]    [Pg.214]    [Pg.214]    [Pg.214]    [Pg.216]    [Pg.217]    [Pg.218]    [Pg.220]    [Pg.223]    [Pg.19]    [Pg.91]    [Pg.72]    [Pg.99]    [Pg.248]    [Pg.22]   
See also in sourсe #XX -- [ Pg.35 , Pg.219 ]

See also in sourсe #XX -- [ Pg.490 , Pg.492 ]




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Aqueous phase reforming process

Ethylene aqueous phase reforming

Glycerol aqueous phase reforming

Methanol aqueous-phase reforming

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