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Copper complex production rate

The kinetics suggest that oxygen reacts with a 2 1 diamine copper complex. The rate determining step is preceded by the formation of a dioxygen complex which decays, equation (124), with production of a free radical which undergoes further fast reactions to the final oxidation product. [Pg.52]

In addition to bonding with the metal surface, triazoles bond with copper ions in solution. Thus dissolved copper represents a "demand" for triazole, which must be satisfied before surface filming can occur. Although the surface demand for triazole filming is generally negligible, copper corrosion products can consume a considerable amount of treatment chemical. Excessive chlorination will deactivate the triazoles and significantly increase copper corrosion rates. Due to all of these factors, treatment with triazoles is a complex process. [Pg.270]

One example was reported by Tolman and coworkers (78) who found that the copper(I) complex C Tp112 (TpR2=tris(3-(R2)-5-methylpyrazol-l-yl)hydroborate) promotes NO disproportionation via a weakly bound CuITpR2(NO) intermediate (formally a MNO 11 species). The products are N20 and a copper(II) nitrito complex (Eq. (36)). The rate law established the reaction to be first-order in copper complex concentration and second-order in [NO], and this was interpreted in terms of establishment of a pre-equilibrium between NO and the Cu(I) precursor and the Cux(NO) adduct, followed by rate-limiting electrophilic attack of a second NO molecule (mechanism B of Scheme 5) (78b). [Pg.230]

These reaction rates show that these reactions are very rapid and limited only by the rate of diffusion of reactants. While it is uncertain as to whether or not these very reactive products of ionizing radiation would reach a copper complex before reacting with some other cellular component or dioxygen, if they did collide and react with a copper complex some protection would result. [Pg.520]

Synthesis of l,4-diacetoxy-2-butene by stoichiometric reaction of a halide complex was considered in an early period [8], and then some catalysts were developed. Although there are a series of Phillips patents, which include the InBrg-LiBr catalyst system, the l,4-diacetoxy-2-butene production rate was low and the 1,4-selectivity did not exceed 80%. The reaction of this system was summarized by Stapp [9] for example, the reaction using Cu(OAc)2-LiX-based catalysts proceeds by a copper-based redox cycle (Scheme 10.1). In addition, 20s-CuBr2-KBr, CuBr2-NaBr, and Ag(OAc)2-LiOAc were known for diacetoxylation, but either 1,4-selectivity or reaction rate was low. Furthermore, l,4-dichloro-2-butene is obtained in the production of chloroprene from 1,3-butadiene. [Pg.162]

The reaction is potentially important because the complex absorbs significantly above 300nm and CuCO is the major inorganic copper complex in seawater (12). Cu(I) production was extremely slow, negligible in sunlight and probably not significant in the environment. The low quantum yield may 1 due to back reaction of Cu with CO-, although addition of 10 mol L 2-propanol to react with the CO radical did not lead to an increase In rate. [Pg.119]

The oxidation of catecholamines like epinephrine has been widely used as source for superoxide dismutase assays. Upon oxidation the catecholamines are transformed to the coloured product adrenochrome. The rate of oxidation by superoxide is inhibited in the presence of superoxide dismutases Likewise the autoxidation of catecholamines at alkaline pH-values is diminished Intriguingly, low molecular mass copper complexes which display superoxide dismutase activity accelerate the autoxidation Therefore, the interaction between superoxide and catecholamines and its inhibition by SOD is thought not to be a simple chemical reactionRecently, this reaction was investigated in more detail Whilst adrenalin autoxidation is very specifically inhibited by SOD, the reaction with other catecholamines like noradrenalin or dihydroxyphenylalanine, having no free amino group, is much less specific. Only 20 % inhibition by CujZnjSuperoxide dismutase are observed. The autoxidation reaction itself is very complex (Scheme 2) and still not fully understood. [Pg.29]

In order to control the hi y exothermic polymerization reaction, the use of redox systems may be applied. The most commonly used system is posulfate, bisulfite and catalytic amounts of copper (or iron) ions, goKrating radicals by a chain reaction. This system has been studied in detail 1 Mfftk and Ugelstad [34]. The presence of trace impurities of metal ions in the reactants may be camouflaged by applying an excess of copper ions. The rate of radical production is in this case adjusted by addition of citrate (HCi ), which forms an inactive complex with Cu ions. Based on the observed kinetics, the following mechanism was postulated ... [Pg.308]

Smoke suppression in rigid PVC can also be accomplished by the utilisation of a copper and molybdenum complex. A binary mixture of cuprous oxide and molybdenum trioxide reduces total smoke production, the average extinction area and smoke production rate. Increased char is formed and a reduced level of flammability in the PVC. [Pg.47]

Secondary acetylenic alcohols are prepared by ethynylation of aldehydes higher than formaldehyde. Although copper acetyUde complexes will cataly2e this reaction, the rates are slow and the equiUbria unfavorable. The commercial products are prepared with alkaline catalysts, usually used in stoichiometric amounts. [Pg.112]

Today the sulphonation route is somewhat uneconomic and largely replaced by newer routes. Processes involving chlorination, such as the Raschig process, are used on a large scale commercially. A vapour phase reaction between benzene and hydrocholoric acid is carried out in the presence of catalysts such as an aluminium hydroxide-copper salt complex. Monochlorobenzene is formed and this is hydrolysed to phenol with water in the presence of catalysts at about 450°C, at the same time regenerating the hydrochloric acid. The phenol formed is extracted with benzene, separated from the latter by fractional distillation and purified by vacuum distillation. In recent years developments in this process have reduced the amount of by-product dichlorobenzene formed and also considerably increased the output rates. [Pg.636]

In addition to the boron trifluoride-diethyl ether complex, chlorotrimcthylsilanc also shows a rate accelerating effect on cuprate addition reactions this effect emerges only if tetrahydrofuran is used as the reaction solvent. No significant difference in rate and diastereoselectivity is observed in diethyl ether as reaction solvent when addition of the cuprate, prepared from butyllithium and copper(I) bromide-dimethylsulfide complex, is performed in the presence or absence of chlorotrimethylsilane17. If, however, the reaction is performed in tetrahydrofuran, the reaction rate is accelerated in the presence of chlorotrimethylsilane and the diastereofacial selectivity increases to a ratio of 88 12 17. In contrast to the reaction in diethyl ether, the O-silylated product is predominantly formed in tetrahydrofuran. The alcohol product is only formed to a low extent and showed a diastereomeric ratio of 55 45, which is similar to the result obtained in the absence of chlorotrimethylsilane. This discrepancy indicates that the selective pathway leading to the O-silylated product is totally different and several times faster than the unselective pathway" which leads to the unsilylated alcohol adduct. A slight further increase in the Cram selectivity was achieved when 18-crown-6 was used in order to increase the steric bulk of the reagent. [Pg.27]

Lewin and Cohen (1967) determined the products of dediazoniation of ben-zophenone-2-diazonium salt (10.42, Scheme 10-77) in five different aqueous systems (Table 10-7). About one-third of the yield is 2-hydroxybenzophenone (10.46) and two-thirds is fluorenone (10.45, run 1) copper has no effect (run 2). On the other hand, addition of cuprous oxide (run 3) has a striking effect on product ratio and rate. The reaction occurs practically instantaneously and yields predominantly fluorenone. As shown in Scheme 10-77, the authors propose that, after primary dediazoniation and electron transfer from Cu1 to 10.43 the sigma-complex radical 10.44 yields fluorenone by retro-electron-transfer to Cu11 and deprotonation. In the presence of the external hydrogen atom source dioxane (run 12) the reaction yields benzophenone cleanly (10.47) after hydrogen atom abstraction from dioxane by the radical 10.43. [Pg.264]


See other pages where Copper complex production rate is mentioned: [Pg.187]    [Pg.214]    [Pg.271]    [Pg.62]    [Pg.214]    [Pg.11]    [Pg.418]    [Pg.60]    [Pg.206]    [Pg.933]    [Pg.240]    [Pg.82]    [Pg.275]    [Pg.933]    [Pg.433]    [Pg.388]    [Pg.92]    [Pg.199]    [Pg.248]    [Pg.31]    [Pg.199]    [Pg.687]    [Pg.937]    [Pg.1299]    [Pg.3312]    [Pg.235]    [Pg.242]    [Pg.248]    [Pg.261]    [Pg.242]    [Pg.341]    [Pg.250]    [Pg.149]    [Pg.394]    [Pg.71]    [Pg.95]    [Pg.232]   
See also in sourсe #XX -- [ Pg.119 ]




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