The influence of the product on the kinetics of the MTBE synthesis reaction
has been investigated. Experimental reaction rates for the MTBE synthesis
reaction in the liquid phase by addition of methanol (MeOH) to isobutene (I
B) were determined on the sulfonic macroporous resin Bayer K2631 at 45-90 d
egreesC for a wide range of IB, MeOH, and MTBE concentrations and operating
in the differential regime in a tubular reactor system. The affinity betwe
en the bulk phase and the resin depends on the composition of the reaction
medium, and it plays an important role in the catalyst activity. This effec
t has been implemented into the kinetic equation as a function of the resin
and the medium solubility parameters. Experimental data are well described
through a LHHW mechanism, the surface reaction being the limiting step. Th
e obtained kinetic equation correctly predicted the additional experimental
data obtained in a batch reactor. The apparent activation energy was estim
ated to be 84.31 +/- 1.09 kJ/mol, and the resin solubility parameter was es
timated as 23.79 +/- 0.83 MPa1/2 at 25 degreesC.