Direct fluorination of toluene, pure or dissolved in either acetonitrile or
methanol, using elemental fluorine was investigated in gas/liquid microrea
ctors, namely a falling film microreactor and a micro bubble column. The ex
periments included measurements at high substrate concentrations and at hig
h fluorine contents diluted in a nitrogen carrier gas, e.g. up to 50 vol.%
fluorine. Results obtained were compared to the performance of a laboratory
bubble column which served as a technological benchmark.
Due to the formation of liquid layers of only a few tens of micrometers thi
ckness, the microreactors provide very large interfacial areas, e.g. up to
40,000 m(2)/m(3). These values exceed by far those of the laboratory bubble
column as well as all other devices applied in practice.
The potential for enhancing mass and heat transfer was verified by several
experiments resulting in an increase in conversion and selectivity for the
microreactors compared to the laboratory benchmark. For the falling film mi
croreactor, yields of up to 28% of monofluorinated ortho and para products
for a degree of toluene conversion of 76% were obtained. These values are o
f the same order as described for the industrially applied Schiemann proces
s. Space-time yields of the microreactors, when referred to the reaction ch
annel volume, were orders of magnitude higher than those of the laboratory
bubble column. Taking into account the construction material needed, the co
rresponding figures of merit, for an idealized geometry as well as the exis
ting total reactor geometry, still indicate technological and economic bene
fits.
A variation of operating conditions for the direct fluorination revealed th
at conversion can be increased in the microreactors by using higher fluorin
e-to-toluene ratios and reaction temperatures. The choice of solvent is als
o essential, with acetonitrile yielding much better results than methanol.
(C) 2000 Elsevier Science S.A. All rights reserved.