Table 1 Results of tests for propene photometathesis on silica materials
Yield (%)
Conv. (%)
to
metathesis
Pretreatment
temperature/K
C2/C4
ratio
a
Sample
C2
trans-C4
cis-C4
1-C4
Adsorbed
873
AMS
1.4
8.2
0.0
1.0
5.7
0.0
0.7
2.8
0.0
0.0
4.4
4.7
0.0
0.0
0.0
0.3
0.0
0.0
0.0
0.4
0.0
0.0
1.0
5.8
2.3
100.0
2.0
5.6
3.1
16.9
0.0
0.82
0.94
—
FSM-16
Silicalite-1
DM
0.0
0.0
0.0
—
1073
AMS
16.8
16.2
0.0
11.8
12.0
0.0
33.0b
33.3b
0.0
1.04
0.95
—
FSM-16
Silicalite-1
DM
1.3
98.7
0.0
0.0
0.0
—
a C2 = ethene, C4 = butene. b Conversions on amorphous silica and FSM-16 reached equilibrium under the reaction conditions.5
the colour of DM after reaction, propene appears to have been
adsorbed and polymerized on acid sites of DM.
Upon evacuation at higher temperature (1073 K), the
activities of AMS and FSM-16 greatly increased, while DM
produced no gaseous products, as shown in Table 1. Activation
of amorphous silica upon evacuation at high temperature is in
agreement with a previous report.5
Upon evacuation at 1073 K the zeolite structure of silicalite-1
was destroyed and became XRD amorphous (BET surface area
7.5 m2 g21). This amorphous sample gave no metathesis
products even after 30 h reaction.
higher photocatalytic activity for propene metathesis than
amorphous silica. The key point is that FSM-16 has many
hydroxy groups on the amorphous walls which constitute the
hexagonal mesopore structure. The active sites are proposed to
be produced by desorption by hydroxy groups from the
amorphous surface of silica.
We thank Mr T. Abe, K. Nishi, T. Ishikura (Nagoya Univ.),
S. Inagaki and Dr Y. Fukushima (Toyota Central R & D Labs.,
Inc.) for their help in the preparation of samples.
It is suggested from the results on the catalyst samples
evacuated at 873 K that an amorphous phase of silica might be
necessary for photometathesis on silica since reaction did not
proceed on microporous crystalline silica, but only on amor-
phous silica (AMS) and on FSM-16 whose walls are amor-
phous.2,12 The results on the catalysts evacuated at 1073 K,
however, indicated that catalytic activity is governed by the
other factors, since amorphous samples produced by evacuation
of silicalite-1 showed no activity.
Another distinguishable factor between these samples is the
concentration of surface hydroxy groups: microporous crystals
have few hydroxy groups, while amorphous silica surfaces such
as AMS and FSM-16 would possess a large amount of hydroxy
groups, The increase of activity of AMS and FSM-16 evacuated
at higher temperature indicates that this process produces active
sites on the samples. Therefore it is suggested that sites
produced by desorption of hydroxy groups would regulate the
activity. For silicalite-1, there are only a small number of
hydroxy groups prior to evacuation. Therefore, silicalite-1
evacuated at high temperature possesses few active sites,
despite its amorphous surface.
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In conclusion, the catalytic activity of unmodified mesopo-
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Received, 30th October 1996; Com. 6/07406E
130
Chem. Commun., 1997