Pt-black, 6% Pt/SiO2 and a 0.6% industrial Pt/Al2O3 catalysts were compared
in reactions of n-nonane. The main products were olefins and fragments. Of
the three samples, Pt/Al2O3 showed the lowest degradative activity. Produc
ts of direct C-6- and C-5-cyclization were present, together with minor amo
unt of trimethylbenzene. Isomers contained mostly monobranched ones which c
ould have been formed by the C-5-cyclic or the bond shift route. The fragme
nt composition pointed to metal catalysed hydrogenolysis. The C-6 and C-7 f
ragments also contained aromatic and cyclopentanic products. Long-term runs
led to consumption of primary olefins into fragments (Pt-black and Pt/SiO2
) and also into aromatics on Pt/Al2O3. n-Nonane was, as a rule, less reacti
ve than n-hexane which latter produced more nondegradative products (isomer
s, C-5-cyclics and benzene). The composition of hydrocarbons removed by hyd
rogen treatment after run (with ca. 10% conversion)was determined first of
all by the nature of the catalyst. It contained much methane in the case of
Pt-black whereas much benzene was removed from supported catalysts, both a
fter n-hexane and n-nonane reaction. In the latter case n-nonane was the on
ly C-9 hydrocarbon in the removed fraction. Higher hydrogen excess during c
atalysis led, as a rule, to higher conversions but hardly affected the amou
nt and composition of the removed hydrocarbons with one spectacular excepti
on: methylcyclopentane left EUROPT-1 after a run of with much H-2. We propo
se that the composition of removed hydrocarbons may reflect the structure o
f hydrocarbonaceous adspecies during reaction with supported catalysts whil
e it may transform into carbonaceous deposits on Pt-black. H-2 can split th
em up to C-1 units, appearing as methane in the gas phase. Surface electron
spectroscopy is in agreement with this latter assumption. (C) 2000 Elsevie
r Science B.V. All rights reserved.