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Continuous oxidation

Oxidation. Oxidation of the -amyl alcohols produces aldehydes, which after continued oxidation can yield acids. This route to aldehydes has httle merit. However, oxidative esterifications with alkah metal hypohaUtes (eg, calcium chlorite, Ca(OCl)2) (49), bromates (eg, sodium bromate, NaBrO )... [Pg.373]

Continuous oxidizers are usually operated at a constant temperature (260 °C) and a constant Hquid level with the production rate and product characteristics controlled by air rate and charging rate. [Pg.364]

The Ni-base alloy surface is exposed to an oxidizing gas, oxide nuclei form, and a continuous oxide film forms (Ni) (Cr203, etc.)- This oxide film is a protective layer. The metal ions diffuse to the surface of the oxide layer and combine with the molten Na2S04 to destroy the protective layer. Ni2S and Cr2S3 results sulfidation) ... [Pg.421]

The burners used are modulating burners, that is, if the organic is preheated to an adequate temperature, the burners will modulate down to zero so that there is no energy required for the continued oxidation. [Pg.483]

Metals are most active when they first deposit on the catalyst. With time, they lose their initial effectiveness through continuous oxidation-reduction cycles. On average, about one third of the nickel on the equilibrium catalyst will have the activity to promote dehydrogenation reactions. [Pg.64]

The presence in an oxide of an excess of one component provides a mechanism for the transport of material. This transport mechanism, which is vital in understanding the formation of a continuous oxide him on a metal, is also discussed in this section. An important feature here is that an excess of one component may provide a transport mechanism, not for itself, but for the other component. [Pg.245]

The models derived for continuous oxide layers remain valuable when porous oxides are formed they provide a frame of reference against which deviations may be examined and give a basis for understanding the factors governing the location of new oxide. In many cases, however, the experimentally derived rate laws no longer have a unique interpretation. For example, the linear rate law relating the thickness of oxide, x, to the time, t... [Pg.268]

The second type of behaviour (Fig. 1.89) is much closer to that which one might predict from the regular cracking of successive oxide layers, i.e. the rate decreases to a constant value. Often the oxide-metal volume ratio (Table 1.27) is much greater than unity, and oxidation occurs by oxygen transport in the continuous oxide in some examples the data can be fitted by the paralinear rate law, which is considered later. Destructive oxidation of this type is shown by many metals such as molybdenum, tungsten and tantalum which would otherwise have excellent properties for use at high temperatures. [Pg.279]

Probably the only feature common to the mechanism of oxidation of the two groups is that, because of crack or pore formation in the continuous oxide, the rate of transport of oxygen in a molecular form has increased to the point where a phase-boundary reaction has assumed rate control. In... [Pg.280]

The high-chromium irons undoubtedly owe their corrosion-resistant properties to the development on the surface of the alloys of an impervious and highly tenacious film, probably consisting of a complex mixture of chromium and iron oxides. Since the chromium oxide will be derived from the chromium present in the matrix and not from that combined with the carbide, it follows that a stainless iron will be produced only when an adequate excess (probably not less than 12% of chromium over the amount required to form carbides is present. It is commonly held, and with some theoretical backing, that carbon combines with ten times its own weight of chromium to produce carbides. It has been said that an increase in the silicon content increases the corrosion resistance of the iron this result is probably achieved because the silicon refines the carbides and so aids the development of a more continuous oxide film over the metal surface. It seems likely that the addition of molybdenum has a similar effect, although it is possible that the molybdenum displaces some chromium from combination with the carbon and therefore increases the chromium content of the ferrite. [Pg.614]

Solids are generally considered chemically inert at room temperatures and the most common-place evidence is often overlooked. That is, solids do not appear to be reactive until they are heated. However, the atoms or ions comprising solids are under constant vibratory motion with the lattice and can "diffuse" from site to site. If vacancies are present, they are continually being "fQled" and "emptied" even at room temperature. Those solids based upon Iron (Fe) undergo continuous oxidation to form a layer of "rust". Thus, solids are not completely stable and are under continuous change over time. [Pg.129]

Weaver and co-workers have carried out extensive smdies of CO electro-oxidation on Au single crystals [Chang et al., 1991 Edens et al., 1996]. Continuous oxidation of CO on Au starts at potentials where the formation of surface oxides or surface-bonded hydroxyl (OH) is not apparent from voltammetry. Weaver suggested the following mechanism ... [Pg.175]

In order to distinguish more clearly between effects induced by the varying potential and kinetic contributions, the continuous oxidation of the three Cj molecules was followed at a constant potential after the potential step. The corresponding faradaic and mass spectrometric (m/z = 44) current transients recorded after 3 minutes adsorption at 0.16 V and a subsequent potential step to 0.6 V (see Section 13.2) are reproduced in Figs. 13.5-13.7. In all cases, the faradaic current exhibits a small initial spike, which is associated with double-layer charging when stepping the electrode potential to 0.6 V. [Pg.434]

Oxidation of Adsorbed CO The electro-oxidation of CO has been extensively studied given its importance as a model electrochemical reaction and its relevance to the development of CO-tolerant anodes for PEMFCs and efficient anodes for DMFCs. In this section, we focus on the oxidation of a COads monolayer and do not cover continuous oxidation of CO dissolved in electrolyte. An invaluable advantage of COads electro-oxidation as a model reaction is that it does not involve diffusion in the electrolyte bulk, and thus is not subject to the problems associated with mass transport corrections and desorption/readsorption processes. [Pg.539]

Tetra(o-aminophenyl)porphyrin, H-Co-Nl TPP, can for the purpose of electrochemical polymerization be simplistically viewed as four aniline molecules with a common porphyrin substituent, and one expects that their oxidation should form a "poly(aniline)" matrix with embedded porphyrin sites. The pattern of cyclic voltammetric oxidative ECP (1) of this functionalized metal complex is shown in Fig. 2A. The growing current-potential envelope represents accumulation of a polymer film that is electroactive and conducts electrons at the potentials needed to continuously oxidize fresh monomer that diffuses in from the bulk solution. If the film were not fully electroactive at this potential, since the film is a dense membrane barrier that prevents monomer from reaching the electrode, film growth would soon cease and the electrode would become passified. This was the case for the phenolically substituted porphyrin in Fig. 1. [Pg.410]

Under these conditions, many types of continuous oxide fiber were developed. The physical properties of these oxide fibers are shown in Table 2 [11]. Methods for preparation of these oxide fibers include spinning of a sol, a solution, or slurry, usually containing fugitive organics as part of a precursor. [Pg.121]


See other pages where Continuous oxidation is mentioned: [Pg.229]    [Pg.259]    [Pg.480]    [Pg.1080]    [Pg.1]    [Pg.249]    [Pg.254]    [Pg.255]    [Pg.256]    [Pg.257]    [Pg.258]    [Pg.259]    [Pg.260]    [Pg.261]    [Pg.262]    [Pg.263]    [Pg.265]    [Pg.266]    [Pg.267]    [Pg.286]    [Pg.887]    [Pg.974]    [Pg.607]    [Pg.312]    [Pg.102]    [Pg.203]    [Pg.216]    [Pg.308]   
See also in sourсe #XX -- [ Pg.463 ]




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Acetylene oxidation—continued

Acid continued) conjugated oxidation

Acid continued) oxidation rate

Acid continued) oxidative degradation

Addition reactions (continued oxidative

Alcohols continuous-flow aerobic oxidation

Alkenes continued) oxidation

Aluminium alloys continued oxide film

Aluminium continued oxide film

Aluminium continued oxides

Azines—continued N-oxidation, effect on reactivity

Bromine (continued oxidations states

Carbon continued oxidation

Cast iron continued oxidation

Catalyst [continued) oxide

Catalyst [continued) titanium oxide

Catalyst [continued) zirconium oxide

Chemicals continued propylene oxide

Continuous fiber reinforced glass composites with oxide fibers

Continuous fine oxide fibers

Continuous metal-free aerobic oxidations

Continuous-flow microreactors oxidations

Covalent hydration—continued of quinazoline 3-oxides

Electrodes continued oxide

Enzymes continued oxidizing

Ethanol—continued oxidation

Hydrogen separation continued) oxidation

Hydrogen separation continued) with oxidative

Infrared (continued oxidized

Iron continued oxidation

Iron oxide process continuous

Lactate, continued oxidation

Lysine (continued oxidation

Metal complexes—continued oxidation

Metal complexes—continued oxidation-reduction potentials

Metal complexes—continued oxidation-reduction reactions

Methane continued) oxidation

Methane continued) oxide

Methanol—continued oxidation

Nickel continued oxides

Nitric oxide, continued

Nitric oxide, continued signaling

Nitropyridines—continued 1-oxides

Nucleophilic substitution—continued N-oxidation, effect

Nucleophilic substitution—continued of pyridine N-oxides, kinetics for

Nucleophilic substitution—continued of quinoline N-oxides

Octanes—continued oxidation

Oxidation continued reactions

Oxidation continued sulphur

Oxidation continued tantalum

Oxidation continued uranium

Oxidation continued volume change

Oxidation continued zirconium

Oxidation continued) selenium

Oxidation continuous selective

Oxidation—continued

Oxidation—continued

Oxidation—continued peroxide

Oxidation—continued with hydrogen peroxide

Oxidation—continued with lead tetraacetate

Oxidation—continued with mercuric acetate

Oxidation—continued with oxygen

Oxidation—continued with ozone

Oxidation—continued with potassium ferricyanide

Oxidation—continued with selenium dioxide

Oxidation—continued with sodium dichromate

Oxidation—continued with sodium persulfate

Oxide films continued

Oxide films continued cation vacancies

Oxide films continued experimental techniques

Oxide films continued formation

Oxide films continued linear rate

Oxide films continued passive

Oxide films continued porous

Oxide films continued protective

Oxide films continued voids

Oxide films continuous

Photosensitized Singlet Oxygen Oxidations in Continuous Flow

Processes continuous aldehyde oxidation

Proteins - continued oxidation

Pyridine 1 -oxide—continued reactions

Pyridine 1 -oxide—continued reactions with

Pyridine 1 -oxide—continued substitution reactions

Pyridine 1-oxides—continued

Pyridine 1-oxides—continued reactivity

Pyridine 1-oxides—continued reduction

Pyridines, 1-oxides—continued sodium

Pyrolysis continued) partial oxidation

Steam continued oxidation effects

Steels continued oxidation

Steels continued oxidation resistance

Sulfur continued oxidation catalyst

Tannins (continued oxidation

Thallium (continued oxidation

Transition Metal-Catalyzed Aerobic Oxidations in Continuous Flow

Tryptophan—continued oxidation

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