@CQXS ¼ D e@t@C s QY@th i@ r 2 @CQXS =@r r 2 k@rs¼ D e @ r 2 @C s QY =@rr 2 þ k@rsIn the organic bulk solution:dC orgQX¼ kdt 2 C orgRX Corg QYdC orgRX¼dtC orgQY ¼ q 0k 2 C orgRX Corg QYhk q aC oegQXC s QXC s QXC s QXiC s QYKCQYs Kð155Þð156Þð157Þð158ÞC orgQXC s QX;a C s QY;a ð159ÞC s QX;a ¼ 3ð 10 2 C s QXdThe initial <strong>and</strong> boundary conditions are:IC: t ¼ 0; C orgRX ¼ C0 RX; C s QX ¼ 0; C s QY ¼ 0; C orgQX ¼ q 0; C orgQY ¼ 0ð160Þð161ÞBC: r ¼ 0; dCs QXdrr ¼ R; D qdC s QXdrr ¼ R; D qdC s QYdr¼ dCs QYdr¼ 0h¼ k q C orgQXh¼ k q C orgQYC s QX;RC s QY;Riið162Þð163Þð164ÞThe above equations can be rendered dimensionless in terms <strong>of</strong> Thiele’s modulus, Biotnumber for mass transfer, <strong>and</strong> nondimensional time <strong>and</strong> distance, which are defined as 2 ¼ k sR 2; BiD m ¼ k qR; ¼ D ete D q R 2 ; ¼ r Rð165ÞIn the analysis <strong>of</strong> heterogeneous solubilization, the role <strong>of</strong> the solid-phase reaction ininfluencing the overall reaction is different from that for the usual gas–solid catalyticreaction. The most important situation is that the film <strong>and</strong> internal diffusion effects withinthe solid <strong>and</strong> at the solid–liquid interface are significant.V. TRI-LIQUID PHASE TRANSFER CATALYSISNeumann <strong>and</strong> Sasson [221] investigated the isomerization <strong>of</strong> allylanisole using PEG as thecatalyst in a toluene <strong>and</strong> aqueous KOH solution. They observed that a third-liquid phasewas formed between the aqueous <strong>and</strong> the organic phases. This was the first report regardingtri-liquid PTC. In 1987, Wang <strong>and</strong> Weng [222] performed the reaction <strong>of</strong> benzylchloride <strong>and</strong> sodium bromide using tetra-n-butylammonium bromide as the PT catalystin liquid–liquid phases. They found that the overall reaction rate rapidly increased whenthe amount <strong>of</strong> catalyst used exceeded some critical value. In such reaction conditions, thePT catalyst was found to be concentrated within a viscous liquid phase that was insolubleCopyright © 2003 by Taylor & Francis Group, LLC
in both aqueous <strong>and</strong> organic phases [222]. This liquid phase enhanced the overall reactionrate as much as several fold that in two-liquid phase systems with PTC, <strong>and</strong> was called thethird-liquid phase. The third-liquid phase was found to contain little <strong>of</strong> the organic <strong>and</strong>aqueous reactants, but mainly the highly concentrated catalyst, which exhibited hydrophilic<strong>and</strong> lipophilic properties. In the bromide–chloride exchange reaction system <strong>of</strong>Wang <strong>and</strong> Weng [222], the third liquid phase was found to consist mainly <strong>of</strong> Bu 4 NBr,small amounts <strong>of</strong> toluene, water, <strong>and</strong> sodium bromide. Above about 70% <strong>of</strong> the tetrabutylammoniumbromide was forced to form a separate liquid phase. The organic <strong>and</strong>aqueous reactants readily reacted with the concentrated catalyst to yield a high reactionrate. The PTC reaction in this situation was termed as tri-liquid PTC (TLPTC).From the point <strong>of</strong> view <strong>of</strong> industrial practice, the formation <strong>of</strong> a third phaseprovides not only enhancement <strong>of</strong> the reaction rate, but also easier separation <strong>of</strong> thePT catalyst from the product stream than that in a two-liquid phase. However, in someparticular reaction systems, the catalyst could lose as much as approximately 25% <strong>of</strong>the initial amount used. <strong>Catalysis</strong> by TLPTC was briefly reviewed by Naik <strong>and</strong>Doraiswamy in 1998 [223]. The key results from the previous publications are discussedas follows.A. Formation <strong>of</strong> the Third Liquid <strong>Phase</strong>Tetrabutylammonium salts are found to be able to form a third liquid phase underappropriate conditions. In principle, the formation <strong>of</strong> a third catalyst phase can beobtained by using a PT catalyst having limiting solubility both in the aqueous phase<strong>and</strong> organic phase under the interaction <strong>of</strong> other concentrated ingredients. Ido et al.[224] effected the elimination reaction <strong>of</strong> 2-bromo-octane with aqueous sodium hydroxideusing PEG as the catalyst [224]. By adding small quantities <strong>of</strong> methanol the solubility<strong>of</strong> PEG in the organic phase was greatly reduced, leading to the formation <strong>of</strong> athird liquid phase. Mason et al. [225] investigated the elimination <strong>of</strong> phenethyl bromideto styrene using tetrabutylammonium bromide under PT-catalytic conditions. Theyfound that the rate <strong>of</strong> reaction was accelerated rapidly due to the addition <strong>of</strong> morethan the critical amount <strong>of</strong> PT catalyst, <strong>and</strong> the third phase was rich in catalyst. Whenthe PT catalyst used was replaced by the tetrapropyl- or tetrapentyl-ammonium salts,the third liquid phase was not formed, <strong>and</strong> the precipitation <strong>of</strong> excess catalyst wassimply induced.Wang <strong>and</strong> Weng [226] explored the effects <strong>of</strong> solvents <strong>and</strong> salts on the formation <strong>of</strong> athird liquid phase for the reaction between n-butyl bromide <strong>and</strong> sodium phenolate. Theyconcluded that the polarity <strong>of</strong> the solvent <strong>and</strong> the amount <strong>of</strong> NaOH are two importantfactors in influencing the formation <strong>of</strong> a third liquid phase, the distribution <strong>of</strong> catalyst, <strong>and</strong>the reaction rate. The aqueous reactant NaOPh also exhibitis significant behavior incertain conditions. With the catalytic intermediate QOPh produced by the reaction <strong>of</strong>NaOPh <strong>and</strong> the catalyst QBr, NaOH has the ability to extract QOPh from the organicphase or the third liquid phase into the aqueous phase. For example, when the amount <strong>of</strong>NaOH added was 2 g, the amount <strong>of</strong> catalyst in chlorobenzene decreased to less than 10%<strong>of</strong> the original content, while the concentration <strong>of</strong> the catalyst in the aqueous phaseincreased with increasing NaOH added. In addition, when hexane was used as the solvent,adding a small amount <strong>of</strong> NaOH caused the disappearance <strong>of</strong> the third liquid phase, whichhad been formed before the addition <strong>of</strong> NaOH. This phenomenon is due to the dissolution<strong>of</strong> QOPh in the aqueous phase.Copyright © 2003 by Taylor & Francis Group, LLC