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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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802 Maw-Ling Wang<br />

Both cation and anion <strong>of</strong> phase-transfer catalyst can affect the distribution <strong>of</strong> the PTC<br />

between two phases, and hence the reaction rate. The partitioning equilibrium <strong>of</strong> the anion<br />

between organic and aqueous phases can be qualitatively estimated from the free energies<br />

<strong>of</strong> the anion transfer from water to organic phase. A large positive free energy <strong>of</strong> transfer<br />

from the aqueous phase to the organic phase clearly indicates that the anion prefers to reside<br />

in the aqueous phase. For example, the free energies <strong>of</strong> transfer <strong>of</strong> Cl - ,Br - , and I - from water<br />

to acetonitrile are +11.6, +8.1 and +4.8 Kcal/mol, respectively. 110 Thus, the transfer from<br />

aqueous to organic phase becomes less unfavorable as one proceeds from chloride to bromide<br />

to iodide. These trends may be understood in terms <strong>of</strong> the change in charge-to-volume<br />

ratios <strong>of</strong> the halide ions. Because chloride has the largest charge-to-volume ratio, it is the<br />

least polarizable and the most strongly hydrated. In contrast, iodide has a relatively diffuse<br />

charge and is less strongly hydrated.<br />

A successful phase-transfer catalytic reaction occurs when the process is able to transfer<br />

the anions from the aqueous phase to the organic phase or vice versa for the reaction to<br />

proceed, and the transferred anions are active and prepared for reaction. An active catalyst<br />

needs to be sufficiently distributed in the organic phase for the reaction to occur. The distribution<br />

<strong>of</strong> catalysts and the associated anion in the organic phase strongly depends on the<br />

structure <strong>of</strong> the quaternary cation and the hydration <strong>of</strong> anion being transferred into the aqueous<br />

phase. Therefore, the following results are used for the reference in selective NPTC catalyst.<br />

(1) Tetramethylammonium cation with a simple anion (CH 3) 4N + Y - (Y=Cl - ,Br - ,CN - ,<br />

etc.) is not easily distributed in most organic solutions. Therefore, (CH 3) 4N + Y - are usually<br />

not good PTCs. The only ways to increase the distribution <strong>of</strong> (CH 3) 4N + Y - is to couple the<br />

cation with a large organic anion 13,49,78,95,155,156 or to use an organic solvent <strong>of</strong> high purity.<br />

17,107,109,110,152<br />

(2) Tetraethylammonium ((C 2H 5) 4N + Y - ) and tetrapropylammonium ((C 3H 7) 4N + Y - )<br />

salts are also poor catalysts for transferring small anions into most organic solutions. 51,105<br />

(3) Tetrabutylammonium salts show high efficiencies as phase-transfer catalysts.<br />

They are readily available in high purity on a commercial scale.<br />

(4) Quaternary ammonium cations, R 4N + , R=C 5H 11 to C 10H 21 easily extract anions into<br />

organic phase and exhibit higher catalytic activities.<br />

(5) Higher tetraalkylammonium salts, R 4N + X, R: (C 12H 25) 4N + and higher groups, can<br />

easily extract anion into an organic phase. However, the interchange <strong>of</strong> anions between organic<br />

and aqueous phases is slow and the reaction rate decreases compared with quaternary<br />

salts where R=C 5H 11 to C 10H 21.<br />

Table 13.3.1 shows the effect <strong>of</strong> catalyst structure on the rate <strong>of</strong> PTC reaction <strong>of</strong><br />

thiophenoxide with 1-bromooctane.<br />

In addition to the preference <strong>of</strong> anion to reside in the aqueous or organic phase, a distribution<br />

ratio (or partition coefficient), α, <strong>of</strong> phase-transfer catalyst (QX) cation between<br />

aqueous and organic phase is defined as<br />

α =[QX] org/[QX] aq<br />

[13.3.4]<br />

Use <strong>of</strong> solvents having higher polarity facilitates distribution <strong>of</strong> quaternary salts into<br />

organic solvents. Hence, it also allows use <strong>of</strong> smaller quaternary salts as catalysts. With di-

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