Toluene was sulfonated by gaseous sulfur trioxide to prepare p-toluenesulfo
nic acid. The effects of reaction temperature and toluene conversion on the
isomer selectivities and the dynamic viscosity of the reaction mixture in
a well-stirred tubular glass reactor of 4cm diameter and 16 cm height were
investigated. Lower selectivity to the m-isomer was obtained at lower react
ion temperature and lower conversion of toluene, whereas the selectivity to
the p-isomer seemed to be less affected by these parameters. With the incr
ease in toluene conversion a sharp increase in viscosity of the reaction mi
xture was observed, which was attributed to the saturation of the toluenesu
lfonic acids dissolved in toluene. A pilot-scale stainless steel jet loop r
eactor (JLR) of 0.3 m diameter and 4m height with an external cooler was co
nstructed and used for the continuous sulfonation of toluene. It was found
that the JLR was very effective for the fast removal of the large amount of
reaction heat, and selectivities to the p-isomer around 85% and to the m-i
somer below 1.2% were obtained.
(C) 2001 Society of Chemical Industry.