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The Hydrogen Mine

The process of the calculation involves a reformer which gets its exergy not from combustion, but as electrical power generated by supplying CO and Fi2 to separate fuel cells which are able to create an excess above the need of the reformer. The invaluable JANAF thermochemical tables (Chase etah, 1985) provided the thermodynamic data. The excess is the chemical exergy of methane. [Pg.32]

Air Products, in its web site question and answer session, goes over the current status of hydrogen production by reforming natural gas, but [Pg.32]


Incompleteness in Chapters 4-6 is of two kinds, lack of circulators and lack of a hydrogen mine , or cheap source of hydrogen. Both of these represent major development problems, as do semi-permeable or permselective membranes, which must accompany circulators and feature in the flow sheet of the hydrogen mine. Figure A.4. [Pg.31]

The DMFC is showing promise as a portable power source, but the bulky fuel is a problem (see several papers in Williams, 2002). Vehicle application of the DMFC is some way away. The advent of better ways of processing natural gas, for example the hydrogen mine, will cheapen methanol substantially, and move the DMFC towards a competitive position with the PEFC, which it does not yet occupy. There are no DMFC buses being demonstrated, and no DMFC stationary power plants for sale. [Pg.122]

The book is doubly ambitious in attempting to point the way to the hydrogen mine or source of low-cost hydrogen. Moreover it highlights the difference between compressible gaseous fuels and relatively incompressible liquid fuels for fuel cells. [Pg.203]

Molybdenum is also recovered as a by-product of copper and tungsten mining operations. The metal is prepared from the powder made by the hydrogen reduction of purified molybdic trioxide or ammonium molybdate. [Pg.78]

Stannous oxalate is used as an esterification and transesterification catalyst for the preparation of alkyds, esters, and polyesters (172,173). In esterification reactions, it limits the undeskable side reactions responsible for the degradation of esters at preparation temperatures. The U.S. Bureau of Mines conducted research on the use of stannous oxalate as a catalyst in the hydrogenation of coal (174) (see Coal). [Pg.75]

Noyori et al. recently used ESI-MS to characterize species present in catalytically active solutions during the hydrogenation of aryl-alkyl ketones using their base-free catalyst precursors trans-[Ru((R)-tol-BINAP)((R, RJ-dpenJfHXf/ -BH ] (tol-BI-NAP = 2,2 -bis(ditolylphosphino) -1, T-binaphthyl dpen = 1,2-diphenylethylenedia-mine) in 2-propanol [9b]. Based upon ESI-MS observations, deuterium-labeling studies, kinetics, NMR observations, and other results, the authors proposed that the cationic dihydrogen complex trans-[Ru((R)-tol-BINAP)((R, R)-dpen)(H)( 2-H2)]+ is an intermediate in hydrogenations carried out in the absence of base. [Pg.367]

Most catalysts originally developed for C=C bonds show a rather poor performance for the hydrogenation of many ketones. However, this situation changed dramatically when it was found that selected Ru-binap and later Ru-binap-dia-mine complexes achieve excellent enantioselectivities, as well as very high TONs and TOFs, for a variety of ketones [92]. Since then, it has been demonstrated that many a- and yS-functionalized, as well as aromatic ketones, are suitable substrates for hydrogenation with industrially viable catalytic results. For the reduction of various ketones biocatalytic methods are an industrially viable alternative to chemocatalysts [15]. [Pg.1302]

The reduction of aliphatic nitrocompounds in acid solution proceeds in two steps. First the nitrosocompound is formed. A low steady state concen ation of 2-methyl-2-nitrosopropane has been detected during the reduction of 2-methyl-2-nitropropane [13]. At the cathode potential necessary to attach the first electron to a nitro group, the nitroso intermediate undergoes further reduction to the hydroxyla-mine. When the nitrocompound has one a-hydrogen substituent, tautomerism of the nitroso intermediate to an oxime is in competition with further reduction. Both temperature and proton availability affect the rate of this isomerisation. Reduction of aliphatic nitrocompounds to the hydroxylamine is usually carried out in acid solution at 0-5° C to minimise oxime formation [14, 15], The hydroxylamine is stable towards further reduction in acid solution. Oximes in acid solution are reduced... [Pg.373]

The transfer hydrogenation of a-keto- S -unsaturated esters, catalyzed by Ru(p-cymene)(TsDPEN) (TsDPEN monotosylated l,2-diphenylethylene-l,2-dia-mine) with 2-propanol as the hydrogen source, has been developed as an efficient method for the preparation of a-hydroxy-)S, y-unsaturated esters or acids. [Pg.136]

The reaction appears to be applicable to a wide range of aromatic starting materials, exceptions being aromatic aldehydes and aromatic primary amines [96]. In effect, the aromatic compound to be converted is stirred with an aqueous solution of hydroxylamine hydrochloride in the presence of metallic ions such as copper ions [95-97] or complex ions such as the pentacyanoam-mine ferrate(II) ion [98]. The mixture is then treated with 30% hydrogen peroxide and a highly colored complex of the nitrosophenol forms. Presumably, the free nitrosophenol may be isolated by treatment of the complex with an acid (Eq. 50). [Pg.464]

L. Pauling (Pasadena) I would, I think, have given the paper with use of exactly the same words as Professor Sokolov, if I had done the work—I might have used the expression the resonance structures 1, 2 and 3 . I should like to know if Professor Sokolov thinks that there is any difference between his view and mine about the structure of the hydrogen bond. [Pg.389]

The elemental analyses of the products from the extraction of Bruceton coal are shown in Table III. The mineral matter was separated from the extract quite efficiently as shown by the ash content of the extracts and the insoluble residue. The elemental composition of all fractions was quite similar to that of the original coal. Only the hydrogen content varied to some extent, increasing with increased solubility. The elemental analysis of the products from the extraction of Ireland Mine coal was incomplete. [Pg.448]


See other pages where The Hydrogen Mine is mentioned: [Pg.24]    [Pg.32]    [Pg.32]    [Pg.67]    [Pg.118]    [Pg.124]    [Pg.125]    [Pg.24]    [Pg.32]    [Pg.32]    [Pg.67]    [Pg.118]    [Pg.124]    [Pg.125]    [Pg.502]    [Pg.159]    [Pg.344]    [Pg.117]    [Pg.117]    [Pg.101]    [Pg.146]    [Pg.378]    [Pg.135]    [Pg.603]    [Pg.199]    [Pg.49]    [Pg.441]    [Pg.80]    [Pg.24]    [Pg.42]    [Pg.291]    [Pg.26]    [Pg.142]    [Pg.250]    [Pg.117]    [Pg.117]    [Pg.142]    [Pg.226]    [Pg.281]    [Pg.899]    [Pg.62]    [Pg.448]    [Pg.449]    [Pg.450]    [Pg.453]   


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