Butenes present in butadiene and isobutene free C-4 fraction (a stream from
the production of methyl-tert-butyl ether - so-called raffinate II) were i
somerised over the hydrogen-chlorided and sulphated catalysts at 350-515 de
grees C. A natural clay (bentonite) and commercial gamma-alumina were used
as catalyst precursors. Hydrogen-chlorided catalysts were deactivated in ab
out 6 h by 10-15% with respect to butene conversion, and a regeneration wit
h air doped hydrogen chloride did not allow to renew the catalytic activity
to full extent. This behaviour should be ascribed to high volatility of ch
lorides which, moreover, pollute the product as itself and in the form of c
hlorinated organic compounds. On the other hand, catalysts prepared by trea
tment of calcinated and evacuated gamma-alumina with diluted sulphuric acid
, proved to be sufficiently active in 2500 h lasting experiments, whereas r
egeneration with air was necessary every 4-6 h. This stability is probably
caused by high melting point of aluminium sulphate which is formed in the c
ourse of the catalytic preparation and treatment. The selectivity, 50% of t
he isobutene formation, was achieved at approximately 50% conversion of but
enes, 450 degrees C, GHSV=0.6 g cm(-3) h(-1). Experiments at higher pressur
e allowed to increase the conversion, but larger amount of components with
higher molar weight was formed. Methanol and methyl-tert-butyl ether did no
t effect the process of skeletal isomerisation significantly, but a presenc
e of butadiene strongly enhanced deactivation of the catalyst. (C) 2000 Els
evier Science B.V. All rights reserved.