S. Awdry et St. Kolaczkowski, The condensation/polymerisation of dimethyl siloxane fluids in a three-phase trickle flow monolith reactor, CATAL TODAY, 69(1-4), 2001, pp. 275-281
For the production of siloxane fluids, the viability of using a multi-chann
el monolith as a catalyst support system in a three-phase reactor has been
studied. The catalyst was tripotassium phosphate (K3PO4). Experiments were
perfonned in a single-channel flow reactor (15 mm i.d. and 500 mm catalyst
coated length). The rate of reaction was followed by monitoring the disappe
arance of the hydroxyl group (-OH). Reaction experiments were performed at
a hydroxyl group concentration T = 373-413 K and P = 7.9 kPa with a nitroge
n purge. The maximum temperature of ran-e from 150 to 170 mol m(-3) operati
on was restricted to 413 K to avoid the formation of undesirable by-product
s. In the regime controlled by chemical kinetics, reaction was of an appare
nt first order with respect to -OH concentration, and in the apparent rate
constant, the pre-exponential factor was 4.19 x 10(-4) m s(-1), and the app
arent activation energy was 16.1 U mol(-1). These are only valid for the op
erating pressure and purge gas flowrate used, as both of these are shown to
affect water removal from the liquid phase and, hence, reaction rates. Mas
s transfer coefficients from the liquid to the catalyst surface were estima
ted and these increased rapidly with flowrate and were higher than expected
for a falling liquid film. (C) 2001 Elsevier Science BN. All rights reserv
ed.