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Formation of COS and

A closer analysis of die equilibrium products of the 1 1 mixture of methane and steam shows the presence of hydrocarbons as minor constituents. Experimental results for die coupling reaction show that the yield of hydrocarbons is dependent on the redox properties of the oxide catalyst, and the oxygen potential of the gas phase, as well as die temperamre and total pressure. In any substantial oxygen mole fraction in the gas, the predominant reaction is the formation of CO and the coupling reaction is a minor one. [Pg.142]

The increase in volume as gaseous products are formed in a chemical reaction is even larger if several gas molecules are produced from each reactant molecule, such as the formation of CO and CO, from a solid fuel (Fig. 4.17). Lead azide, Pb(N3)2, which is used as a detonator for explosives, suddenly releases a large volume of nitrogen gas when it is struck ... [Pg.276]

The catalytic tests show that, over the Pt(l 0 0)/Al2O3 catalyst, the formation of CO and NH3 is largely prevented, whereas the yield of N2O increases compared with the Pt(polycrystalline)/Al203 catalyst. These main differences observed should be ascribed to the morphological differences between two catalysts, i.e., the dominant orientation of the crystallographic facets and the average size... [Pg.305]

As was suggested by Aylmer-Kelly et at. (1973) Gressin and co-workers (1979) also postulated that the formation of oxalate could occur via two possible routes the dimerisation of CO (route 2 in Figure 3.47) or the attack of the CO 2 on a second molecule of C02 followed by reduction (route 3). Both of these routes involve coupling via C-C bond formation. Coupling can also occur to give the C-O-C linkage (route 3 ), the route responsible for the formation of CO and CO - (steps 5,5 and 6). [Pg.300]

The large body of examples discussed in the previous section indicates that SCFs, and in particular scC02, offer a broad potential for applications in hydrogenation reactions. Very little is known, however, about possible interactions between the catalytically active species and the reaction medium in such systems. In particular, two possible transformations of C02 in the presence of hydrogen must be considered, which are also transition metal-catalyzed (Scheme 39.8). The water gas shift (WGS) reaction can lead to the formation of CO, and has... [Pg.1371]

Fig. 12. Conversions of CH4 and CO2 and selectivities for formation of CO and H2 as a function of time on stream for C02 reforming of CH4 catalyzed by 17 wt% Ni/La203. Before reaction, the catalyst was reduced in flowing H2 at 773 K for at least 5 h and then at 1023 K for 2 h. Reaction conditions pressure, 1 atm temperature, 1023 K feed gas molar ratio, CH4 /C02 = 1 /1 GHSV is unknown (228). Fig. 12. Conversions of CH4 and CO2 and selectivities for formation of CO and H2 as a function of time on stream for C02 reforming of CH4 catalyzed by 17 wt% Ni/La203. Before reaction, the catalyst was reduced in flowing H2 at 773 K for at least 5 h and then at 1023 K for 2 h. Reaction conditions pressure, 1 atm temperature, 1023 K feed gas molar ratio, CH4 /C02 = 1 /1 GHSV is unknown (228).
The introduction of the kinetics of the formation of CO and CO2 into the model modifies the temperature equation (31) and the oxygen equation (33). The slow and fast coke burning equations are unchanged except for a change in the effectiveness factor tjt of Eq. (29) to tjtc given by Eq. (73). A new equation for the conversion of CO is introduced. [Pg.49]

The difference in enthalpy for these reaction pathways is equal to the difference between the heat of formation of CO2 and the heats of formation of CO and FeO, which is less than 5 kcal/mol. These two steps would therefore be expected to compete, as observed. [Pg.24]

We reported previously that the addition of H3PO4 (probably present as PO2.5 on the surface after the calcination) to (VO)2P207> which was prepared by an organic solvent method (5), enhanced the selectivity to MA at high conversion levels, while the activity decreased (20). Considering the low selectivity of the side faces, it is possible that the H3PO4 added preferentially deactivated the side faces to suppress the formation of CO and CO2 and/or the secondary oxidation of the product MA there. [Pg.165]

CA 351636(1941 )(Nonsetting expls obtained by coating AN grains with tetram-minezinc nitrate) 29)O.Schmitz-Dumont, ZElektrochem 47, 221-2(1941) CA 35, 5052(I941)(Interaction of Co and Cr ammines with alkali metal amides results in formation of Co and Cr amides) 30)W.V,Smith, CanP 401,643(1941) CA 36, 1744(1942)(Prepn of... [Pg.284]

The high quantum yield of photolysis of C02 suggests the rapid destruction of C02 and the formation of CO and 02 by sunlight of wavelengths below about 2200 A (see Section VI- 5). According to an estimate by McElroy and McConnell (675), the column abundance of C02 in the atmosphere is 2 x 1023 molec cm"2. With a dissociation rate of 2.5 x 1012 cm-2 sec-, the entire C02 may be destroyed in less than 10,000 years. [Pg.115]

Bulldog Brand Powder, A safety mining expl KN03 83.5-86.3, sulfur 13-14 charcoal 1-2.5%, patented in England by Curtis et al in 1899. A fairly large propn of S and a small propn of C were proposed in order to lower the temp of combustion and to prevent formation of CO and... [Pg.324]

What is the mass change (in grams) accompanying the formation of CO and H2 in the water-gas reaction ... [Pg.982]

Table 9.1 summarizes catalyst compositions and corresponding performances. The oxidation of ethane to acetic acid is now commercial an industrial plant is installed, with the technology developed by Saudi Basic. Elements that have contributed to the successful development of the process are (1) the discovery of a catalytically active compound, the multifunctional properties of which can be modified and tuned to be adapted to reaction conditions through incorporation of various elements (2) the stability of the main products, ethylene and acetic acid, which do not undergo extensive consecutive degradation reactions (3) the possibility of recycling the unconverted reactant and the major by-product, ethylene (4) the use of reaction conditions that minimize the formation of CO and (5) an acceptable overall process yield. [Pg.294]

Raman and UV-visible spectroscopy, but no precise characterization was made. A report was made in 1981 where the IR spectrum of Cu atoms deposited with C02 at 80 K was interpreted in terms of the formation of a -coordinated complex between C02 and zerovalent copper [32]. Almond et al. [33] prepared a (C02) M(CO)5 molecule (M = Cr, W), that led to the formation of CO and oxometal carbonyl under UV irradiation. The first complete study of the reactivity of C02 with the first row of transition metals was made by Mascetti et al. [34, 35]. Here, it was shown that the late transition metal atoms (Fe, Co, Ni, and Cu) formed one-to-one M(C02) complexes, where C02 was bonded in a side-on (Ni), end-on (Cu), or C-coordinated (Fe, Co) manner, while the earlier metal atoms (Ti, V, and Cr) spontaneously inserted into a CO bond to yield oxocarbonyl species OM(CO) or 0M(C0)(C02). Normal coordinate analysis showed that the force constants of CO bonds were significantly decreased by 50%, compared to free C02, and that the OCO angle was bent between 120 and 150°. [Pg.61]

In another study, [Re(bpy)(CO)3(py)]+ was encapsulated into microp-orous NaY and mesoporous A1MCM-41 molecular sieves. Irradiation of the molecular sieve encapsulated rhenium complex in the presence of C02 and H20 (either gaseous or adsorbed onto the matrix) led to formation of CO and carbonate species. The proposed photoinduced process is outlined in Scheme 5 [95,96]. [Pg.86]


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See also in sourсe #XX -- [ Pg.428 ]




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