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Oxidation of carbon

There have been many studies of the reduction of oxides and of oxy-acid salts with elemental carbon, some of which are of great technological importance. Although both reactants may be solids [Pg.277]

The reaction of Si02 with SiC [1229] approximately obeyed the zero-order rate equation with E = 548—405 kJ mole 1 between 1543 and 1703 K. The proposed mechanism involved volatilized SiO and CO and the rate-limiting step was identified as product desorption from the SiC surface. The interaction of U02 + SiC above 1650 K [1230] obeyed the contracting area rate equation [eqn. (7), n = 2] with E = 525 and 350 kJ mole 1 for the evolution of CO and SiO, respectively. Kinetic control is identified as gas phase diffusion from the reaction site but E values were largely determined by equilibrium thermodynamics rather than by diffusion coefficients. [Pg.277]

Hoffmann and Patai [1160] have investigated the influence of various pretreatments and ageing on the solid—solid interactions between KC104 and KI03 and carbon. The process [Pg.278]


Many solids have foreign atoms or molecular groupings on their surfaces that are so tightly held that they do not really enter into adsorption-desorption equilibrium and so can be regarded as part of the surface structure. The partial surface oxidation of carbon blacks has been mentioned as having an important influence on their adsorptive behavior (Section X-3A) depending on conditions, the oxidized surface may be acidic or basic (see Ref. 61), and the surface pattern of the carbon rings may be affected [62]. As one other example, the chemical nature of the acidic sites of silica-alumina catalysts has been a subject of much discussion. The main question has been whether the sites represented Brpnsted (proton donor) or Lewis (electron-acceptor) acids. Hall... [Pg.581]

There has been a general updating of the material in all the chapters the treatment of films at the liquid-air and liquid-solid interfaces has been expanded, particularly in the area of contemporary techniques and that of macromolecular films. The scanning microscopies (tunneling and atomic force) now contribute more prominently. The topic of heterogeneous catalysis has been expanded to include the well-studied case of oxidation of carbon monoxide on metals, and there is now more emphasis on the flexible surface, that is, the restructuring of surfaces when adsorption occurs. New calculational methods are discussed. [Pg.802]

Engei T and Erti G 1978 Eiementary steps in the cataiytic oxidation of carbon monoxide on piatinum metaisTIdv. Catal. 28 1... [Pg.956]

In this group the outer quantum level has a full s level and two electrons in the corresponding p level. As the size of the atom increases the ionisation energy changes (see Table 8.1) and these changes are reflected in the gradual change from a typical non-metallic element, carbon, to the weakly metallic element, lead. Hence the oxides of carbon and silicon are acidic whilst those of tin and lead are amphoteric. [Pg.160]

The most general methods for the syntheses of 1,2-difunctional molecules are based on the oxidation of carbon-carbon multiple bonds (p. 117) and the opening of oxiranes by hetero atoms (p. 123fl.). There exist, however, also a few useful reactions in which an a - and a d -synthon or two r -synthons are combined. The classical polar reaction is the addition of cyanide anion to carbonyl groups, which leads to a-hydroxynitriles (cyanohydrins). It is used, for example, in Strecker s synthesis of amino acids and in the homologization of monosaccharides. The ff-hydroxy group of a nitrile can be easily substituted by various nucleophiles, the nitrile can be solvolyzed or reduced. Therefore a large variety of terminal difunctional molecules with one additional carbon atom can be made. Equally versatile are a-methylsulfinyl ketones (H.G. Hauthal, 1971 T. Durst, 1979 O. DeLucchi, 1991), which are available from acid chlorides or esters and the dimsyl anion. Carbanions of these compounds can also be used for the synthesis of 1,4-dicarbonyl compounds (p. 65f.). [Pg.50]

Oxidation of Carbon Atoms in Carbon-Carbon Multiple Bonds... [Pg.123]

Oxidation of carbon side-chains has resulted in the synthesis of dithiazolyl ketone (82) and thiazolyl phenyl ketone (83). The hydrocarbon chain can also be dehydrogenated in acetic acid in the presence of... [Pg.341]

Oxidation of carbon corresponds to an increase in the number of bonds between carbon and oxygen or to a decrease in the number of carbon-hydrogen bonds Conversely reduction corresponds to an increase in the number of carbon-hydrogen bonds or to a decrease in the number of carbon-oxygen bonds From Table 2 4 it can be seen that each successive increase m oxidation state increases the number of bonds between carbon and oxygen and decreases the number of carbon-hydrogen bonds Methane has four C—H bonds and no C—O bonds car bon dioxide has four C—O bonds and no C—H bonds... [Pg.87]

Most of the time we are concerned only with whether a particular reaction is an oxidation or reduction rather than with determining the precise change m oxidation num ber In general Oxidation of carbon occurs when a bond between carbon and an atom that IS less electronegative than carbon is replaced by a bond to an atom that is more electronegative than carbon The reverse process is reduction... [Pg.88]

Hydrogenation of the oxides of carbon to methane according to the above reactions is sometimes referred to as the Sabatier reactions. Because of the high exothermicity of the methanization reactions, adequate and precise cooling is necessary in order to avoid catalyst deactivation, sintering, and carbon deposition by thermal cracking. [Pg.70]

Loss on ignition. GeneraUy, the oxides of carbon and sulfur (plus some chlorine, depending on the fining agent) volatilize during melting. [Pg.304]

Thermochemistry. From an overall heat and mass balance point of view, the main chemical reactions of the blast furnace include oxidation of carbon in the zone in front of the tuyeres (raceway) to give CO plus heat. [Pg.415]

The mechanism of carbon elimination is similar to those of the earlier open-hearth processes, ie, oxidation of carbon to carbon monoxide and carbon dioxide. The chemical reactions and results are the same in both cases. The progress of the reaction is plotted in Figure 5. [Pg.377]

Other important uses of stannic oxide are as a putty powder for polishing marble, granite, glass, and plastic lenses and as a catalyst. The most widely used heterogeneous tin catalysts are those based on binary oxide systems with stannic oxide for use in organic oxidation reactions. The tin—antimony oxide system is particularly selective in the oxidation and ammoxidation of propylene to acrolein, acryHc acid, and acrylonitrile. Research has been conducted for many years on the catalytic properties of stannic oxide and its effectiveness in catalyzing the oxidation of carbon monoxide at below 150°C has been described (25). [Pg.65]

A variety of instmments are available to analyze carbon monoxide in gas streams from 1 ppm to 90%. One group of analyzers determines the concentration of carbon monoxide by measuring the intensity of its infrared stretching frequency at 2143 cm . Another group measures the oxidation of carbon monoxide to carbon dioxide electrochemically. Such instmments are generally lightweight and weU suited to appHcations requiring portable analyzers. Many analyzers are equipped with alarms and serve as work area monitors. [Pg.53]

Carbon dioxide can cause product contamination through ammonium carbonate formation. Ammonium carbonate may also form by oxidation of carbon monoxide by cupric ion (eq. 27) ... [Pg.55]

CO Oxidation Catalyzed by Palladium. One of the best understood catalytic reactions occurring on a metal surface is the oxidation of carbon monoxide on palladium ... [Pg.176]

Oxides of carbon. Carbon monoxide, carbon dioxide... [Pg.2172]

The iron-carbon solid alloy which results from the solidification of non blastfurnace metal is saturated with carbon at the metal-slag temperature of about 2000 K, which is subsequendy refined by the oxidation of carbon to produce steel containing less than 1 wt% carbon, die level depending on the application. The first solid phases to separate from liquid steel at the eutectic temperature, 1408 K, are the (f.c.c) y-phase Austenite together with cementite, Fe3C, which has an orthorhombic sttiicture, and not die dieniiodynamically stable carbon phase which is to be expected from die equilibrium diagram. Cementite is thermodynamically unstable with respect to decomposition to h on and carbon from room temperature up to 1130 K... [Pg.184]

Oxides of sulphur and other sulphur compounds Oxides of nitrogen and other nitrogen compounds Oxides of carbon... [Pg.307]

Fig. 11. The loss of carbon rapidly increases with the increase of temperature. Heating of the catalysts in open air for 30 minutes at 973 K leads to the total elimination of carbon from the surface. The gasification of amorphous carbon proceeds more rapidly than that of filaments. The tubules obtained after oxidation of carbon-deposited catalysts during 30 minutes at 873 K are almost free from amorphous carbon. The process of gasification of nanotubules on the surface of the catalyst is easier in comparison with the oxidation of nanotubes containing soot obtained by the arc-discharge method[28, 29]. This can be easily explained, in agreement with Ref [30], by the surface activation of oxygen of the gaseous phase on Co-Si02 catalyst. Fig. 11. The loss of carbon rapidly increases with the increase of temperature. Heating of the catalysts in open air for 30 minutes at 973 K leads to the total elimination of carbon from the surface. The gasification of amorphous carbon proceeds more rapidly than that of filaments. The tubules obtained after oxidation of carbon-deposited catalysts during 30 minutes at 873 K are almost free from amorphous carbon. The process of gasification of nanotubules on the surface of the catalyst is easier in comparison with the oxidation of nanotubes containing soot obtained by the arc-discharge method[28, 29]. This can be easily explained, in agreement with Ref [30], by the surface activation of oxygen of the gaseous phase on Co-Si02 catalyst.
Very recently, considerable effort has been devoted to the simulation of the oscillatory behavior which has been observed experimentally in various surface reactions. So far, the most studied reaction is the catalytic oxidation of carbon monoxide, where it is well known that oscillations are coupled to reversible reconstructions of the surface via structure-sensitive sticking coefficients of the reactants. A careful evaluation of the simulation results is necessary in order to ensure that oscillations remain in the thermodynamic limit. The roles of surface diffusion of the reactants versus direct adsorption from the gas phase, at the onset of selforganization and synchronized behavior, is a topic which merits further investigation. [Pg.430]

H. P. Kaukonen, R. M. Nieminen. Computer simulations studies of the catalytic oxidation of carbon monoxide on platinum metals. J Chem Phys 97 4380- 386, 1989. [Pg.433]

E. V. Albano. Monte Carlo simulation of the oxidation of carbon monoxide on fractal surfaces. Surf Sci 255 351-359, 1990. [Pg.433]

Regardless of the hydrogen generation technique used, tlie unpurified syii gas contains the oxides of carbon, which deactivate tlie aimnonia syntliesis catalyst and must be removed. In tlie sliift converters, embon monoxide is calaljlically converted to carbon dioxide, wliich is removed more easily Ilian... [Pg.260]

The NAD- and NADP-dependent dehydrogenases catalyze at least six different types of reactions simple hydride transfer, deamination of an amino acid to form an a-keto acid, oxidation of /3-hydroxy acids followed by decarboxylation of the /3-keto acid intermediate, oxidation of aldehydes, reduction of isolated double bonds, and the oxidation of carbon-nitrogen bonds (as with dihydrofolate reductase). [Pg.590]

The operation of a large synthetic ammonia plant based on natural gas involves a delicately balanced sequence of reactions. The gas is first desulfurized to remove compounds which will poison the metal catalysts, then compressed to 30 atm and reacted with steam over a nickel catalyst at 750°C in the primary steam reformer to produce H2 and oxides of carbon ... [Pg.421]

On a laboratory scale reduction of KCIO3 with moist oxalic acid generates the gas suitably diluted with oxides of carbon ... [Pg.847]

The reactions of olefins with peracids to form epoxides allows for the selective oxidation of carbon-carbon double bonds in the presence of other functional groups which may be subject to oxidation (for example, hydroxyl groups). The epoxides that result are easily cleaved by strong acids to diols or half-esters of diols and are therefore useful intermediates in the synthesis of polyfunctional compounds. [Pg.8]


See other pages where Oxidation of carbon is mentioned: [Pg.21]    [Pg.142]    [Pg.177]    [Pg.185]    [Pg.486]    [Pg.63]    [Pg.172]    [Pg.147]    [Pg.536]    [Pg.288]    [Pg.211]    [Pg.381]    [Pg.273]    [Pg.97]    [Pg.1128]    [Pg.399]    [Pg.251]    [Pg.955]   


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Anodic Catalysts for Oxidation of Carbon-Containing Fuels

Butanoic acid via oxidation of carbon-tin bonds

Carbon, molar balances in derivation of SO2 oxidation

Catalytic oxidation of carbon monoxide

Characterization of carbon nanotube-metal oxide materials

Direct electrochemical oxidation of carbon

Electro-oxidation of carbon monoxide

Electrochemical Oxidation of Carbon Monoxide

Electrochemical oxidation of carbon

Explosion limits and oxidation characteristics of carbon monoxide

Formation of carbon oxides

Further oxidation reactions of carbon monoxide in homogeneous systems

Gas Hydrate Carbonate Formation and Anaerobic Oxidation of Methane

Gas-phase oxidation of carbon

Homocoupling and Oxidation of the Carbon Nucleophile

Hydrogenation of carbon oxides

Kinetics of carbon monoxide oxidation

Mechanisms of Carbon Monoxide Oxidation

Methanation of carbon oxides

Nezukone via oxidation of carbon-tin bonds

OXIDATION OF CARBON COMPOUNDS

Oxidation levels, of carbon

Oxidation of Carbon-Centered Radicals

Oxidation of Non-functional Carbon Atoms

Oxidation of activated carbon

Oxidation of carbon monoxide

Oxidation of carbon monoxide in flames and other high temperature flow systems

Oxidation of carbon-hydrogen bond

Oxidation of hydrocarbons containing four carbon atoms

Oxidation reactions of carbon monoxide

Oxidation states of carbon

Oxidative Aftertreatment of Carbon Black

Oxidative Carbonylation of Alcohols to Carbonates, Oxalates, and Carbamates

Oxidative Cleavage of Vicinal Diols in the Carbon Framework

Oxidative Cleavage of the Carbon Framework

Oxidative addition of the carbon-halogen bond

Oxide of carbon

Oxide of carbon

Oxides and oxoacids of carbon

Oxids and sulfids of carbon

Preferential oxidation of carbon

Preferential oxidation of carbon monoxide

REACTIONS OF HALOGEN COMPOUNDS WITH NITRIC OXIDE AND CARBON MONOXIDE

Reaction of lithium carbonate with ferric oxide

Reactions of barium carbonate with various oxides

Reduction of metal oxides with carbon

Reduction of nitric oxide by carbon

Reduction of nitric oxide by carbon monoxide

Reduction of nitrogen oxides with carbon monoxide

Reductions of carbon oxides

Selective oxidation of carbon monoxide

Selective oxidation of carbon monoxide in hydrogen

Sensing mechanism of carbon nanotube-metal oxide gas sensors

Surface Oxidation of Carbon Nanofibers Prior to Functionalization

The Adsorption and Oxidation of Carbon Monoxide

The Oxidation of Carbon Monoxide

The Selective Oxidation of Carbon Monoxide in Hydrogen

The oxidation of carbon monoxide on platinum

The oxides and sulphides of carbon

The reduction of stable oxides in carbon arc furnaces

The slow oxidation of carbon monoxide

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