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11. Interfacial Mechanism and Kinetics of Phase-Transfer Catalysis

11. Interfacial Mechanism and Kinetics of Phase-Transfer Catalysis

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FIG. 4 Yields <strong>of</strong> products <strong>and</strong> conversion <strong>of</strong> reactant as a function <strong>of</strong> reactant C 6 H 5 OH=ðNPCl 2 Þ 3consumption ratio at different NaOH concentrations: (abcd) 0.5 kmol=m 3 , (efgh) 0.9 kmol=m 3 , (ijkl)1.8 kmol=m 3 ;(*) (NPCl 2 Þ 3 ,(*)N 3 P 3 Cl 5 ðOC 6 H 5 Þ 1 ,(!)N 3 P 3 Cl 4 ðOC 6 H 5 Þ 2 ,(&)N 3 P 3 Cl 3 ðOC 6 H 5 Þ 3 ,(^) N 3 P 3 Cl 2 ðOC 6 H 5 Þ 4 ; ðÞ N 3 P 3 CLðOC 6 H 5 Þ 5 .reactant in the particle. In Fig. 4, the maximum yield <strong>of</strong> monophenolated product shifts tothe right by more than 0.2 unit, <strong>and</strong> the maximum yield <strong>of</strong> diphenolated product shifts tothe right by more than 0.1 unit. This reveals that the effect <strong>of</strong> intraparticle diffusion on theorganic reaction influences the reaction rate. This trend <strong>of</strong> shifting to the right <strong>of</strong> themaximum yield was increased with increasing concentration <strong>of</strong> NaOH.The reactivity <strong>of</strong> a triphase reaction is influenced by the structure <strong>of</strong> the active sites,particle size, degree <strong>of</strong> cross-linkage, degree <strong>of</strong> ring substitution, swollen volume, <strong>and</strong>spacer chain <strong>of</strong> a catalyst pellet. All these make the triphase reaction a complicatedone. Past efforts have carried out this investigation macroscopically. However, themechanism <strong>and</strong> effects <strong>of</strong> the internal molecular structure <strong>of</strong> the polymer support haveseldom been discussed.According to the steric effect <strong>of</strong> phenolate ion reacting with hexachlorocyclotriphosphazene<strong>and</strong> the reports <strong>of</strong> Wu <strong>and</strong> Meng two-phase catalysis [69]; triphase catalysis[165]), the maximum yield <strong>of</strong> partially substituted phenolated product was increasedwith increasing degree <strong>of</strong> substitution reaction. Figure 4 shows that the maximum yield<strong>of</strong> monophenolated product was larger than that <strong>of</strong> the diphenolated product, <strong>and</strong> themaximum yield <strong>of</strong> partially phenolated product decreased when the NaOH concentrationincreased (i.e., reactivity <strong>of</strong> the active site increased). This result reveals that the reactionrate <strong>of</strong> phenolate reacting with monophenolated (or diphenolated) product was greaterthan the diffusion rate <strong>of</strong> monophenolated (or diphenolated) product from active site tobulk solution <strong>and</strong> hexachlorocyclotriphosphazene from bulk solution to active site. Mostmonophenolated (or diphenolated) product reacted in situ with Resin þ OC 6 H 5 in theCopyright © 2003 by Taylor & Francis Group, LLC

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