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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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13.3 Effects <strong>of</strong> organic solvents on phase-transfer catalysis 827<br />

The catalyst may form a third layer during the PTC reaction, when using high salt concentrations<br />

and nonpolar organic solvents. Wang and Weng 123-126,154 found that a third layer<br />

phase was built when using a low polarity organic solvent in the PTC reaction system. This<br />

has been observed for PEGs, quaternary onium salts and crown ether. In such cases, catalyst<br />

recovery involves a simple phase separation. In industrial kettles (with limited visibility in<br />

the reactor) or when a “rag” layer distorts an otherwise sharp phase boundary, a phase separation<br />

operation may not be simple. Nevertheless, choosing conditions in which the catalyst<br />

separates as a third layer is usually advantageous. A dehydrohalgenation was performed<br />

four times consecutively, with no loss in catalytic activity by simply replacing the organic<br />

phase and replenishing the aqueous base phase after each use, leaving the third phase containing<br />

PEG in the reactor.<br />

Table 13.3.23 Effect <strong>of</strong> organic solvent<br />

on current efficiency<br />

Organic solvent Current efficiency, %<br />

CH2Cl2 80<br />

CH2ClCH2Cl 75<br />

CHCl3 86<br />

CH3COOC2H5 64<br />

Data obtained from the work <strong>of</strong> Do and Chou; 23 0.5<br />

M<strong>of</strong>C 6H 5CH 2OH in the organic phase; 25 o C, 600<br />

rpm, 20 mAcm -2 <strong>of</strong> current density, 70 mL <strong>of</strong> organic<br />

phase, 70 mL <strong>of</strong> aqueous phase, 0.005 M <strong>of</strong><br />

Bu 4NHSO 4, 1.0 M <strong>of</strong> NaCl, pH=6.9, electricity<br />

passed 2 Fmol -1 <strong>of</strong> benzyl alcohol<br />

(B) Electrochemical and PTC reaction<br />

The combination <strong>of</strong> phase transfer catalysis<br />

(PTC) with other processes, such as supercritical<br />

fluid extraction 22 and electrochemical<br />

process 5-7,23,120 have been investigated in detail.<br />

Do and Chou 23 carried out the anodic oxidation<br />

<strong>of</strong> benzyl alcohol in the two-phase system containing<br />

both the redox mediator, ClO - /Cl - , and a<br />

phase-transfer catalyst (PTC). The reaction<br />

mechanism and the factors which affect the efficiency<br />

<strong>of</strong> benzaldehyde production were explored.<br />

The current efficiency is mainly<br />

governed by the pH value and the nature <strong>of</strong> the<br />

organic solvent as well as the types and the<br />

concentration <strong>of</strong> phase transfer catalyst (PTC).<br />

When ethyl acetate and chlorinated hydrocarbons<br />

were used as solvents, the current efficiencies<br />

were between 64 and 86%,<br />

respectively as shown in Table 13.3.23. 23 With ethyl acetate as solvent, the current efficiency<br />

was less than for chlorinated hydrocarbons. The results indicate that the chlorinated<br />

hydrocarbons have a higher extraction capacity for Bu 4N + ClO - from the aqueous phase than<br />

has ethyl acetate. Similar results were obtained by Dehmlow and Dehmlow. 16 The current<br />

efficiencies change slightly when different chlorinated hydrocarbons were used as organic<br />

solvents.<br />

Tsai and Chou 120 carried out the indirect electrooxidation <strong>of</strong> cyclohexanol by using a<br />

double mediator consisting <strong>of</strong> ruthenium and chlorine redoxes in the multiphase system.<br />

Table 13.3.24 shows that the current efficiency had the highest value at 83% using carbon<br />

tetrachloride as organic solvent. 120 The current density decreased in order, carbon tetrachloride<br />

> chlor<strong>of</strong>orm > toluene > cyclohexane. The selectivity was 100% except when toluene<br />

was used as organic solvent. For this case, the concentration <strong>of</strong> cyclohexanol in carbon tetrachloride<br />

is higher than that <strong>of</strong> the other solvents.

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