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Direct Hydrogen Production

As mentioned earlier, photo-electrochemical (PEC) reactions may be employed not only to generate electricity, but also to decompose water to hydrogen a [Pg.127]


Doong, S., Ong, E., Atroshenko, M., Lau, F., Roberts, M. (2004). A raove/ membrane reactor for direct hydrogen production from coal. DOE Report (DE-FC26—03NT41851). [Pg.179]

Boggs BK, King RL, Botte GG (2009) Urea electrolysis direct hydrogen production from urine. Chem Commun 32 4859 861... [Pg.658]

Photovoltaic solar cells for direct hydrogen production by electrolysis. [Pg.450]

Reduction. Because of a lack of discrimination between the double bond and carbonyl moieties, direct hydrogenation of acrolein leads to the production of mixtures containing propyl alcohol, C HgO [71-28-8] propionaldehyde, C H O [123-38-6J, and aHyl alcohol, C H O [107-18-16]. Both the... [Pg.124]

Direct, One-Step Thermal Water Splitting. The water decomposition reaction has a very positive free energy change, and therefore the equihbrium for the reaction is highly unfavorable for hydrogen production. [Pg.424]

Direct Hydrogenation. Direct hydrogenation of lignitic and other coals has been studied by many investigators. Lignite can be slurried with an anthracene-oil solvent, heated to a temperature of 460—500°C with 1 1 CO H2 synthesis gas at pressures to 28 MPa (280 atm) in a 2 kg/h reactor. The product hquids are separated, and in a commercial process, a suitable hydrogen-donor solvent would be recycled (54). [Pg.160]

Survey of the patent Hterature reveals companies with processes for 1,4-butanediol from maleic anhydride include BASF (94), British Petroleum (95,96), Davy McKee (93,97), Hoechst (98), Huels (99), and Tonen (100,101). Processes for the production of y-butyrolactone have been described for operation in both the gas (102—104) and Hquid (105—108) phases. In the gas phase, direct hydrogenation of maleic anhydride in hydrogen at 245°C and 1.03 MPa gives an 88% yield of y-butyrolactone (104). Du Pont has developed a process for the production of tetrahydrofuran back-integrated to a butane feedstock (109). Slurry reactor catalysts containing palladium and rhenium are used to hydrogenate aqueous maleic acid to tetrahydrofuran (110,111). [Pg.453]

Note that the yield of extract product presented here is lower than that reported earlier in Table 4 because the hydrogenated products were not extracted with NMP but were centrifuged directly. The data show that centrifugation by itself, and without any accompanying filtration, appears to provide pitches of acceptable purity, albeit with an associated lower yield. [Pg.223]

The mechanisms of corrosion by steam are similar to those for water up to 450°C, but at higher temperatures are more closely related to the behaviour in carbon dioxide. Studies at 100°C have demonstrated that uranium hydride is produced during direct reaction of the water vapour with the metal and not by a secondary reaction with the hydrogen product. Also at 100°C it has been shown that the hydride is more resistant than the metal. Inhibition with oxygen reduces the evolution of hydrogen and does not involve reaction of the oxygen with the uranium . Above 450°C the hydride is not... [Pg.909]

Cobalt(II) complexes of three water-soluble porphyrins are catalysts for the controlled potential electrolytic reduction of H O to Hi in aqueous acid solution. The porphyrin complexes were either directly adsorbed on glassy carbon, or were deposited as films using a variety of methods. Reduction to [Co(Por) was followed by a nucleophilic reaction with water to give the hydride intermediate. Hydrogen production then occurs either by attack of H on Co(Por)H, or by a disproportionation reaction requiring two Co(Por)H units. Although the overall I easibility of this process was demonstrated, practical problems including the rate of electron transfer still need to be overcome. " " ... [Pg.287]

Direct dynamics trajectory calculations at the MP2/6-31-FG level of theory were then used to explore the reaction dynamics of this system [63]. Sixty-four trajectories were started from the central barrier shown at A in Fig. 11, with initial conditions sampled from a 300 K Boltzmann distribution. Of the 31 trajectories that moved in the direction of products, four trajectories followed the MEP and became trapped in the hydrogen-bonded [CH3OH ... [Pg.247]


See other pages where Direct Hydrogen Production is mentioned: [Pg.115]    [Pg.213]    [Pg.178]    [Pg.326]    [Pg.142]    [Pg.249]    [Pg.53]    [Pg.53]    [Pg.582]    [Pg.802]    [Pg.584]    [Pg.127]    [Pg.193]    [Pg.235]    [Pg.28]    [Pg.147]    [Pg.155]    [Pg.566]    [Pg.115]    [Pg.213]    [Pg.178]    [Pg.326]    [Pg.142]    [Pg.249]    [Pg.53]    [Pg.53]    [Pg.582]    [Pg.802]    [Pg.584]    [Pg.127]    [Pg.193]    [Pg.235]    [Pg.28]    [Pg.147]    [Pg.155]    [Pg.566]    [Pg.74]    [Pg.426]    [Pg.427]    [Pg.159]    [Pg.361]    [Pg.287]    [Pg.2378]    [Pg.435]    [Pg.687]    [Pg.112]    [Pg.654]    [Pg.1301]    [Pg.132]    [Pg.468]    [Pg.247]    [Pg.372]    [Pg.197]    [Pg.817]    [Pg.26]    [Pg.499]    [Pg.140]   


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Direct product

Direct production

Directive hydrogenation

Hydrogenation directed

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