n-Hexane isomerization was carried over CsxH3-xPW12O40 catalysts promoted w
ith Pt by mechanical mixing with a Pt on alumina catalyst. Different parame
ters as caesium and platinum content in the catalyst, temperature and atmos
phere of heteropolyacids pre-treatment were optimized. The catalytic perfor
mances of the best catalyst were compared with those of industrial Pt promo
ted mordenite. 0.3 wt.% Pt-promoted Cs2H1PW12O40 pre-treated under hydrogen
flow at 473 K showed the highest conversion and selectivity. Its performan
ces are very close to those of the industrial zeolitic catalyst in the same
reaction conditions. The gain in dibranched isomers selectivity is really
promising for the future. With this catalyst, the reaction proceeds by a no
n-ideal bifunctional mechanism resulting from the superposition of a monofu
nctional acid and a bifunctional metal-acid mechanism. (C) 2001 Elsevier Sc
ience B.V. All rights reserved.