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Solvent exchange reactions concepts

This concept of the prior reorganization of the solvent is best illustrated by a charge shift e.t, something like the self-exchange reaction of a neutral molecule M with its ion M+ see scheme 3 [57]. [Pg.113]

A step further in the utilization of these solvent-extracted compounds is their use as reagents. Irving and co-workers (8, 16) have reported what they call a colored liquid anion exchanger based on this concept. They use a xylene-hexone solution of tetrahexylammonium erdmannate. Erdmannate ion is the yellow [Co(NH3)2(N02)4] anion, which absorbs strongly at 353 m/x in aqueous solution. The exchange reaction is... [Pg.22]

The difference in energy consumption between put-and-take distillation and the membrane setup is difficult to estimate. Both technologies result in waste streams that require further treatment. Moreover, the required pressure for the membrane setup is hard to define on the base of pilot-scale experiments. It is, however, clear that the membrane setup shows a much lower mass intensity than the distillation. Mass intensity is a commonly used concept in the context of green energy and is defined as the ratio of the total mass of the reactants and the mass of the reaction products (Curzons et al., 2001). Solvent exchange by distillation typically shows a mass intensity of 5-10 kg/kg, whereas the use of membrane technology results in a value of 2-3 kg/kg. Both values are vahd for a 95% exchange, which is often the required value in industrial apphcations. [Pg.287]

The application of the solvent system concept to liquid sulfur dioxide chemistry stimulated the elucidation of reactions such as those of aluminum sulfite. However, there is no direct evidence at all for the formation of S02+ in solutions of thionyl halides. In fact, there is evidence to the contrary. When solutions of thionyl bromide or thionyl chloride are prepared in 3JS-labeled (S ) sulfur dioxide, almost no exchange takes place. The half-life for the exchange is about two years or more. If ionization took place ... [Pg.174]

In Chapter 8 we introduced the concept of pKa in which we saw acids and bases exchanging protons. Among the strongest organic acids are those containing O-H bonds. Yet you have seen no radical reactions in which an O-H bond is broken—in fact the reaction on p. 1030 used ethanol as a solvent Carbon adds tend to be much weaker—yet you ve seen plenty of examples of C-H bonds being broken by radical attack. [Pg.1047]

Although more studies need to be performed to study the scope and generality of this system, the use of amine hydrochloride salts as initiators for controlled NCA polymerizations shows tremendous promise. The concept of fast, reversible deactivation of a reactive species to obtain controlled polymerization is a proven concept in polymer chemistry, and this system can be compared to the persistent radical effect employed in all controlled radical polymerization strategies [34]. Like those systems, the success of this method requires a carefully controlled matching of the polymer chain propagation rate constant, the amine/amine hydrochloride equilibriiun constant, and the forward and reverse exchange rate constants between amine and amine hydrochloride salt. This means it is likely that reaction conditions (e.g. temperature, halide counterion, solvent) will need to be optimized to obtain controlled polymerization for each different NCA monomer, as is the case for most vinyl monomers in controlled radical polymerizations. Within these constraints, it is possible that controlled NCA polymerizations utilizing simple amine hydrochloride initiators can be obtained. [Pg.10]

Solvent isotope effects. Much mechanistic information can be obtained about reactions involving proton transfer from solvent kinetic isotope effects, particularly in solvents of mixed isotopic composition. For practical reasons work is essentially confined to H/D effects, especially those in water. Unlike ordinary primary hydrogen isotope effects, solvent isotope effects have to take into account a host of exchangeable sites, subject to equilibrium as well as kinetic isotope effects. A key concept is that of the fractionation factor, (p, which is the deuterium occupancy of a site in a 1 1 H2O/D2O mixture more formally it is defined by equation l.l ... [Pg.25]


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