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Chloride-formate exchanger

The second pathway is represented by Eqs. (8)—(11). These reactions involve reduction of the Nin halide to a Ni° complex in a manner similar to the generation of Wilke s bare nickel (37, 38) which can form a C8 bis-77-alkyl nickel (17) in the presence of butadiene [Eq. (9)]. It is reasonable to assume that in the presence of excess alkyaluminum chloride, an exchange reaction [Eq. (10)] can take place between the Cl" on the aluminum and one of the chelating 7r-allyls to form a mono-77-allylic species 18. Complex 18 is functionally the same as 16 under the catalytic reaction condition and should be able to undergo additional reaction with a coordinated ethylene to begin a catalytic cycle similar to Scheme 4 of the Rh system. The result is the formation of a 1,4-diene derivative similar to 13 and the generation of a nickel hydride which then interacts with a butadiene to form the ever-important 7r-crotyl complex [Eq. (11)]. [Pg.292]

With both the Fu and the Denmark catalysts it can be assumed that catalysis is effected by formation of a highly electrophilic silicon cation D from tetrachlorosi-lane and the nucleophilic catalyst C, i.e. by attack of the pyridine N-oxide or of the phosphoramide O-atom on silicon, followed by ionization (Scheme 13.38). The latter cation can then activate the epoxide toward nucleophilic attack by the chloride ion. Exchange of the product silane for another molecule of tetrachlorosilane completes the catalytic cycle [75],... [Pg.382]

Figure 9 Simplified model for the formation of active centres of Ziegler-Natta catalysts by adsorption ofTiCl4 on solid MgCl2, reduction ofTi(IV) to Ti(III) chloride-alkyl exchange with aluminium alkyls and polyethylene (PE) formation by coordination and insertion of ethylene molecules. Figure 9 Simplified model for the formation of active centres of Ziegler-Natta catalysts by adsorption ofTiCl4 on solid MgCl2, reduction ofTi(IV) to Ti(III) chloride-alkyl exchange with aluminium alkyls and polyethylene (PE) formation by coordination and insertion of ethylene molecules.
The resin in the chloride form exchanges chloride against tungstate and thiomolybdate. In the case of tungstate the equation is idealized, because in reality isopolytungstates are present Sodium ions as well as the anions silicate, phosphate, and arsenate are not retained and pass the column. The pH is too high for heteropolytungstate formation with these anions. [Pg.200]

Functional studies in transfected HEK-293 cells revealed that pendrin can function as an exchanger of chloride with bicarbonate, hydroxide, and formate (Soleimani et ai, 2001). Ghloride/formate exchange has also been documented in pendrin-expressing oocytes (Scott and Karniski, 2000). Renal tubules isolated from alkali-loaded... [Pg.238]

Anions have also been determined using conventional IMS with an FSI ion source and included arsenate, phosphate, sulfate, nitrate, nitrite, chloride, formate, and acetate. Distinct peak patterns and reduced mobility constants were observed for respective anions. Application to authentic water samples for the determination of nitrate and nitrite demonstrated the feasibility of using FSI-IMS as a rapid analytical method for monitoring nitrate and nitrite in water systems. The method was used for on-site measurement by exchanging air for nitrogen as the drift gas without complications. The linear dynamic range was 1,000, and detection limits were 10 ppb for nitrate and 40 ppb for nitrite. [Pg.358]

Formation of carbonic acid from HjO and CO2 is a relatively slow process, but within the corpuscles it is speeded up by the presence of the enzyme carbonic anhydrase. As a result the concentration of bicarbonate ions rises more rapidly in the corpuscles than in the plasma and some of them leave the corpuscles in exchange for chloride ions. This chloride-bicarbonate exchange ensures that a large fraction of the acidic CO2 produced in the tissues is carried as plasma bicarbonate. Consequently there is very little increase in the acidity of venous blood. [Pg.376]

If to take the AM iu the form of chloride, an exchange reaction between ChT acetate and AM chloride reduees the formation of dissociated soluble salts. Accordingly, the reaction product in this case will consist of the H-complex ChT-AM. [Pg.150]

Allylic ethers of aldehyde cyanohydrins have also been prepared under phase transfer conditions [23]. The organic phase, consisting of aldehyde cyanohydrin, an allylic halide (preferably the bromide) and dichloromethane is brought into contact with aqueous sodium hydroxide and tricaprylmethylammonium chloride. Anion exchange in the aqueous phase leads to the tricaprylmethylammonium/hydroxide ion pair, which reacts with the cyanohydrin to form the corresponding alkoxide. Reaction of the alkoxide with the allylic halide leads to the allylic ether of the cyanohydrin (Eq. 7.9). The formation of small amounts of allylic nitriles is apparently due to the side... [Pg.103]

The solubility of hydrogen chloride in solutions of aromatic hydrocarbons in toluene and in w-heptane at —78-51 °C has been measured, and equilibrium constants for Tr-complex formation evaluated. Substituent effects follow the pattern outlined above (table 6.2). In contrast to (T-complexes, these 7r-complexes are colourless and non-conducting, and do not take part in hydrogen exchange. [Pg.117]

Stabilization Mechanism. Zinc and cadmium salts react with defect sites on PVC to displace the labHe chloride atoms (32). This reaction ultimately leads to the formation of the respective chloride salts which can be very damaging to the polymer. The role of the calcium and/or barium carboxylate is to react with the newly formed zinc—chlorine or cadmium—chlorine bonds by exchanging ligands (33). In effect, this regenerates the active zinc or cadmium stabilizer and delays the formation of significant concentrations of strong Lewis acids. [Pg.549]

The per pass ethylene conversion in the primary reactors is maintained at 20—30% in order to ensure catalyst selectivities of 70—80%. Vapor-phase oxidation inhibitors such as ethylene dichloride or vinyl chloride or other halogenated compounds are added to the inlet of the reactors in ppm concentrations to retard carbon dioxide formation (107,120,121). The process stream exiting the reactor may contain 1—3 mol % ethylene oxide. This hot effluent gas is then cooled ia a shell-and-tube heat exchanger to around 35—40°C by usiag the cold recycle reactor feed stream gas from the primary absorber. The cooled cmde product gas is then compressed ia a centrifugal blower before entering the primary absorber. [Pg.457]


See other pages where Chloride-formate exchanger is mentioned: [Pg.235]    [Pg.235]    [Pg.238]    [Pg.56]    [Pg.18]    [Pg.10]    [Pg.649]    [Pg.253]    [Pg.208]    [Pg.20]    [Pg.418]    [Pg.456]    [Pg.188]    [Pg.3282]    [Pg.301]    [Pg.935]    [Pg.270]    [Pg.376]    [Pg.83]    [Pg.419]    [Pg.494]    [Pg.378]    [Pg.311]    [Pg.2059]    [Pg.124]    [Pg.259]    [Pg.81]    [Pg.551]    [Pg.376]    [Pg.647]    [Pg.1114]    [Pg.359]    [Pg.156]    [Pg.186]    [Pg.51]    [Pg.133]    [Pg.95]    [Pg.96]    [Pg.219]   


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