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Density oxidation reactions

Because the reaction takes place in the Hquid, the amount of Hquid held in the contacting vessel is important, as are the Hquid physical properties such as viscosity, density, and surface tension. These properties affect gas bubble size and therefore phase boundary area and diffusion properties for rate considerations. Chemically, the oxidation rate is also dependent on the concentration of the anthrahydroquinone, the actual oxygen concentration in the Hquid, and the system temperature (64). The oxidation reaction is also exothermic, releasing the remaining 45% of the heat of formation from the elements. Temperature can be controUed by the various options described under hydrogenation. Added heat release can result from decomposition of hydrogen peroxide or direct reaction of H2O2 and hydroquinone (HQ) at a catalytic site (eq. 19). [Pg.476]

The oxidation products are almost insoluble and lead to the formation of protective films. They promote aeration cells if these products do not cover the metal surface uniformly. Ions of soluble salts play an important role in these cells. In the schematic diagram in Fig. 4-1 it is assumed that from the start the two corrosion partial reactions are taking place at two entirely separate locations. This process must quickly come to a complete standstill if soluble salts are absent, because otherwise the ions produced according to Eqs. (2-21) and (2-17) would form a local space charge. Corrosion in salt-free water is only possible if the two partial reactions are not spatially separated, but occur at the same place with equivalent current densities. The reaction products then react according to Eq. (4-2) and in the subsequent reactions (4-3a) and (4-3b) to form protective films. Similar behavior occurs in salt-free sandy soils. [Pg.140]

By definition a current of positive charge (an oxidation reaction) is taken as a positive current, a current of negative charge (a reduction reaction) is taken as a negative current. When the electrode is at equilibrium, the net current density j equals zero. This implies, that... [Pg.264]

We have previously considered the mechanism of electrospray ionization in terms of the charging of droplets containing analyte and the formation of ions as the charge density on the surface of the droplet increases as desolvation progresses. The electrospray system can also be considered as an electrochemical cell in which, in positive-ion mode, an oxidation reaction occurs at the capillary tip and a reduction reaction at the counter electrode (the opposite occurs during the production of negative ions). This allows us to obtain electrospray spectra from some analytes which are not ionized in solution and would otherwise not be amenable to study. In general terms, the compounds that may be studied are therefore as follows ... [Pg.163]

Such bimetallic alloys display higher tolerance to the presence of methanol, as shown in Fig. 11.12, where Pt-Cr/C is compared with Pt/C. However, an increase in alcohol concentration leads to a decrease in the tolerance of the catalyst [Koffi et al., 2005 Coutanceau et ah, 2006]. Low power densities are currently obtained in DMFCs working at low temperature [Hogarth and Ralph, 2002] because it is difficult to activate the oxidation reaction of the alcohol and the reduction reaction of molecular oxygen at room temperature. To counterbalance the loss of performance of the cell due to low reaction rates, the membrane thickness can be reduced in order to increase its conductance [Shen et al., 2004]. As a result, methanol crossover is strongly increased. This could be detrimental to the fuel cell s electrical performance, as methanol acts as a poison for conventional Pt-based catalysts present in fuel cell cathodes, especially in the case of mini or micro fuel cell applications, where high methanol concentrations are required (5-10 M). [Pg.361]

The density function calculations for the ammonia oxidation reaction do, however, depend on models where the reactants are in stable adsorption states... [Pg.98]

Fig. 2. Current-potential curves in Evans diagram [29] format for reduction of Cu2+ ions and oxidation of H2CO. and are the equilibrium, or open circuit, potentials for the Cu2+ reduction and H2CO oxidation reactions, respectively. Assuming negligible interfering reactions, the vertical dashed lines indicate the exchange current densities for the two half reactions, and the deposition current for the complete electroless solution. Adapted from ref. 23. Fig. 2. Current-potential curves in Evans diagram [29] format for reduction of Cu2+ ions and oxidation of H2CO. and are the equilibrium, or open circuit, potentials for the Cu2+ reduction and H2CO oxidation reactions, respectively. Assuming negligible interfering reactions, the vertical dashed lines indicate the exchange current densities for the two half reactions, and the deposition current for the complete electroless solution. Adapted from ref. 23.
Figure 10.19 A histogram of Au cluster density after the indicated treatment normalized to the cluster density after nucleation at room temperature. The Au coverage in each of the experiments was 0.4 ML Au. The first three columns compare the cluster density on Ti-free Si02, TiOJt(8%)-Si02, and Ti0x(17%)-Si02thin films, respectively, after a 850 K anneal. The fourth column shows the normalized Au cluster density of a Ti0x(17%)-Si02thin film after a CO oxidation reaction (CO/02 = 2 1,60 torr, 370 K, and 120 min). (Reprinted from Min, B.K. et al., J. Phys. Chem. B, 108, 14609-14615, 2004. Copyright 2004. With permission from American Chemical Society.)... Figure 10.19 A histogram of Au cluster density after the indicated treatment normalized to the cluster density after nucleation at room temperature. The Au coverage in each of the experiments was 0.4 ML Au. The first three columns compare the cluster density on Ti-free Si02, TiOJt(8%)-Si02, and Ti0x(17%)-Si02thin films, respectively, after a 850 K anneal. The fourth column shows the normalized Au cluster density of a Ti0x(17%)-Si02thin film after a CO oxidation reaction (CO/02 = 2 1,60 torr, 370 K, and 120 min). (Reprinted from Min, B.K. et al., J. Phys. Chem. B, 108, 14609-14615, 2004. Copyright 2004. With permission from American Chemical Society.)...
Ultimately, the catalyst performance of a real fuel cell is of the greatest importance. The DEFC polarization curves for the two PtSn anode catalysts are tested and shown in Fig. 15.9. The characteristic data are summarized in Table 15.4. The PtSn-1 catalyst shows a strongly enhanced electron-oxidation reaction (EOR) activity and much better performance in both the activation-controlled region (low-current density region) and... [Pg.320]

Both anodic oxidation reactions proceeded well. As illustrated in Scheme 44, an anodic methoxylation of menthyl pyroglutamate followed by the trapping of an incipient A-acyliminium ion with allyl-silane in the presence of Lewis acid led to (138) [86]. While the stereoselectivity of this reaction was not high, the major product from the reaction could be fractionally crystallized from hexane and the route used to conveniently prepare (138) on a scale of 10 g. In this case, a platinum wire anode was used in order to keep the current density high. This was required because of the high oxidation potential of the secondary amide relative to the methanol solvent used in the reaction. [Pg.304]

The density of the corrosive current of jamesonite in NaOH solution is basically the same as that in Ca(OH)2 solution, but it is minimal in Na2C03 solution, about a fraction of the fourth of the former. There are obvious appearances of passivation and its breaking-down in strong polarization area in NaCOa solution Because COj ion is easier to form insoluble alkaline carbonate than OH ion, the carbonate salts are passive on the mineral surface to inhibit oxidation reaction. [Pg.121]

The previous discussion has focused on the properties of perovskite materials rather than on their performance as anodes. The number of actual fuel-cell studies is more limited, but this literature has been reviewed recently by Irvine. Various perovskites have been investigated as potential SOFC anode materials however, these early efforts were hampered by low electrochemical activity toward methane oxidation,poor anode structure,or insufficient electrode conductivity. Most recently, Tao and Irvine demonstrated that an anode based on (Lao.75Sro.25)o.9Cro.5Mno.503 can provide reasonable power densities at 1173 K in 3% humidified CH4. Barnett and co-workers also reported stable power generation with methane and propane fuels on an anode based on LaCr03 however, they reported that the addition of Ni, in levels too small to affect the conductivity, was crucial in providing activity for the electrochemical oxidation reactions. [Pg.616]

The mechanism for replacement of a methoxyl group by cyanide in these reactions follows Scheme 6.7. The radical-cation reacts with cyanide ion at the point of highest positive charge density. Oxidation of the radical so formed to the carbon-ium ion is followed by elimination of proton and formaldehyde [79]. The elimination step is analogous to the conversion of cyanhydrins to the carbonyl compound and cyanide ion in basic solution. [Pg.200]

Electrocatalytic Oxidation of Hydrogen The rate constant of the hydrogen oxidation reaction (HOR), as measured by the exchange current density jo (i.e. the current... [Pg.11]


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See also in sourсe #XX -- [ Pg.494 ]




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Density oxidizers

Density reactions

Hydrogen oxidation reaction densities

Hydrogen oxidation reaction exchange current density

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