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Promoters oxygen

A.ctive driers promote oxygen uptake, peroxide formation, and peroxide decomposition. At an elevated temperature several other metals display this catalytic activity but are ineffective at ambient temperature. Active driers include cobalt, manganese, iron, cerium, vanadium, and lead. [Pg.221]

Slime is a network of secreted strands (extracellular polymers) intermixed with bacteria, water, gases, and extraneous matter. Slime layers occlude surfaces—the biological mat tends to form on and stick to surfaces. Surface shielding is further accelerated by the gathering of dirt, silt, sand, and other materials into the layer. Slime layers produce a stagnant zone next to surfaces that retards convective oxygen transport and increases diffusion distances. These properties naturally promote oxygen concentration cell formation. [Pg.124]

Each reaction was performed with a CYP biocatalyst concentration of 1 pM (1000 nmol L 1), in the presence of a corresponding CYP reaction mix containing reduced nicotinamide cofactor and a cofactor recycling system at 30 °C, with agitation to promote oxygen transfer to the reaction solution. [Pg.221]

Wehrli, B. and W. Stumm, 1989, Vanadyl in natural waters Adsorption and hydrolysis promote oxygenation. Geochimica et Cosmochimica Acta 53, 69-77. [Pg.533]

Keywords. Nar promoter, Oxygen-dependent, Inducible promoter. Fed-batch, Recombinant... [Pg.171]

Wessel and Crabtree reported that BU4NHSO5 is an effective primary oxidant with a high tendency to promote oxygen transfer rather than to react by a catalyzed radical pathway. A nonradical hydrocarbon oxidation with BU4NHSO5 and [Mn304bipy4(H202)] (0104)4 as catalyst was proved mechanistically, which contrasts the radical pathway followed for the same catalyst with t-BuOOH as the primary oxidant. [Pg.1031]

Fig. 26. Proposed structural model for two-site CO activation to promote oxygenate formation in olefin hydroformylation and CO hydrogenation reactions on RhFe, PdFe, and IrFe bimetal cluster-derived catalysts. Fig. 26. Proposed structural model for two-site CO activation to promote oxygenate formation in olefin hydroformylation and CO hydrogenation reactions on RhFe, PdFe, and IrFe bimetal cluster-derived catalysts.
Wehrii, B., and Stumm, W. (1989) Vanadyl in Natural Waters Adsorption and Hydrolysis Promote Oxygenation, Geochim. Cosmochim. Acta 53, 69-77. [Pg.972]

SCHEME 53. Co(salpr)-promoted oxygenation of 4- and 2-alkenyl substituted phenols... [Pg.1208]

Magnesium oxide bombarded with neutrons in vacuum acquired a reddish-blue color and (among others) two distinct ESB signals, one of which was associated with the color. These serve to mark two of the defects. At least three sites promoting oxygen adsorption are required, since the irradiated material showed enhancement of three types of adsorption ... [Pg.131]

Release of acid will lower the pH. A lower pH promotes oxygen dissociation in the tissues. However, the enhanced release of oxygen in the tissues will increase the concentration of deoxy-Hb, thereby increasing the likelihood that the cells will sickle. [Pg.1044]

The necessary reaction paths have now been established. The catalyst must promote oxygen insertion and mild dehydrogenation but inhibit strong oxidation and dehydrogenation. [Pg.89]

Figure 2 also shows this point At steady-state the rate, r< , of consumption of the promoting O species via reaction with C2H4, has to equal its rate of formation I/2F. Consequently, since A=Ar/(I/2F) and Ar=r, it follows A=r/r =TOF/TOF where TOF is the turnover frequency of the catalytic reaction in the NEMCA-promoted state and TOF is the turnover frequency of the reaction of the promoting oxygen species with ethylene. It thus follows for the experiment of Fig. 2 that TOFc=TOF/A=1.3xlO s. This implies that that average lifetime of the promoting species on the catalyst surface is TOF =770 s in excellent qualitative agreement with the catalytic rate relaxation time constant upon current interruption (Fig. 2). This observation provides strong support for the oxygen backspillover mechanism of electrochemical promotion. Figure 2 also shows this point At steady-state the rate, r< , of consumption of the promoting O species via reaction with C2H4, has to equal its rate of formation I/2F. Consequently, since A=Ar/(I/2F) and Ar=r, it follows A=r/r =TOF/TOF where TOF is the turnover frequency of the catalytic reaction in the NEMCA-promoted state and TOF is the turnover frequency of the reaction of the promoting oxygen species with ethylene. It thus follows for the experiment of Fig. 2 that TOFc=TOF/A=1.3xlO s. This implies that that average lifetime of the promoting species on the catalyst surface is TOF =770 s in excellent qualitative agreement with the catalytic rate relaxation time constant upon current interruption (Fig. 2). This observation provides strong support for the oxygen backspillover mechanism of electrochemical promotion.
The solvent of choice is methanol which gives higher rates than aprotic solvents [43]. This is attributed to the formation of a titanium(IV)-hydroperoxo comples (I) in which coordination of the alcohol promotes oxygen transfer to the olefin (Figure 6). Coordination of the alcohol becomes inoeasingly difficult with increasing steric bulk, consistent with the observed decrease in rate methanol > ethanol > tert-butanol. [Pg.163]

On the other hand, iron phosphate possesses both acidic and redox functions as like Mo and V oxides and phosphates. However, it possesses no double bonded oxygen species unlike the Mo and V compounds. Therefore, its function to promote oxygen insertion processes is very weak. As a result, in the reaction of glycolic acid, the formation of formaldehyde and formic acid is suppressed, to a certain extent, and a relatively good performance for glyoxylic acid is obtained. [Pg.534]


See other pages where Promoters oxygen is mentioned: [Pg.254]    [Pg.254]    [Pg.208]    [Pg.165]    [Pg.153]    [Pg.398]    [Pg.72]    [Pg.223]    [Pg.223]    [Pg.1031]    [Pg.851]    [Pg.261]    [Pg.470]    [Pg.244]    [Pg.192]    [Pg.97]    [Pg.214]    [Pg.302]    [Pg.443]    [Pg.453]    [Pg.851]    [Pg.54]    [Pg.1314]    [Pg.1206]    [Pg.104]    [Pg.104]    [Pg.163]    [Pg.324]    [Pg.32]    [Pg.416]    [Pg.150]    [Pg.161]   
See also in sourсe #XX -- [ Pg.174 , Pg.207 , Pg.208 , Pg.219 , Pg.220 ]




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Promoter effect oxygenation catalysts

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