A.P.R. Ehlert et al.
Catalysis Today xxx (xxxx) xxx–xxx
Table 1
It is important to note that: i) for all the reactions employing [Co-
NNNPhF] the dimers are exclusively linear (Sn−H= 100%) and ii) the
relative amount of 1-hexene is ≥ 50%. The catalytic activity for [Co-
NNNPhF] was found to be dependent on the Al/Co ratio with a higher
activity with a Al/Co ratio of 300 (T = 10 and 30 °C). Comparing runs 7
to 10; 8–11 and 9–12, a decrease in the catalytic activity is observed
upon increasing the reaction temperature, which is certainly due to the
deactivation of the catalytic species as observed with catalyst precursor
[Co-NNNPhH]. Such a deactivation, observed for both precursors, can
be related to a non-efficient heat dissipation of the equipment used in
this study. When the reactions were conducted at 50 °C, no activity was
observed confirming that the cobalt complexes herein employed are
thermally sensitive.
Taking in account the runs conducted with the highest (Al/Co) ratio
(equal to 600), i.e. runs 3 and 6 (conducted with [Co-NNNPhH]) and
runs 9 and 12 (conducted with [Co-NNNPhF]), it seems that a large
quantity of cocatalyst is detrimental to catalytic activity. Studies
performed with nickel [10,11] and cobalt [4,6] complexes as precursors
and alkylaluminium compounds as cocatalyts (Ziegler-Natta systems)
have already shown such behaviours.
The high activity and selectivity values achieved with catalytic
systems formed from [Co-NNNPhF] highlight the potential of such
complexes. For instance, run 8 (at 10 °C) corresponds to a TOF activity
of 47300 h−1 with 1-hexene selectivity of 60% and run 11 (at 30 °C) to
activity of 2570 h−1 with 1-hexene selectivity of 70%. Comparison of
the selectivity data observed for these two experiments confirms that
the cobalt complexes do not readily mediate olefin isomerization, since
the increase of catalytic activity does not come along with a decrease of
linear and terminal olefins production as usually observed for oligo-
merization Ziegler-Natta catalytic systems [12].
Comparison of runs 1- 6 (employing [Co-NNNPhH]) with runs 7–12
(employing [Co-NNNPhF]) shows that the presence of fluorinated
groups in the ligand of the diimine cobalt complex significantly
influences the catalytic performance, i.e., activity and 1-hexene selec-
tivity. Fig. 3 illustrates the 1-hexene selectivity data for runs conducted
with [Co-NNNPhH] and [Co-NNNPhF] with Al/Co ratios of 100 and
300, and temperatures of 10 and 30 °C.
Catalytic performance of precursors [Co-NNNPhH] and [Co-NNNPhF] associated to MAO.
Run
*Precursor
T
(°C)
Al/Co
TOF
SC6 (%)
Sn-H (%)
S1-H (%)
(h−1
)
1
2
3
4
5
6
10
10
10
30
30
30
100
300
600
100
300
600
135
35
0
50
45
0
100
100
0
100
100
0
100
91
0
100
100
0
20
25
0
30
15
0
[Co-NNNPhH]
7
8
9
10
11
12
10
10
10
30
30
30
100
300
600
100
300
600
1510
47300
705
1510
2570
380
84
90
88
83
93
88
100
100
100
100
100
100
70
60
65
65
70
50
[Co-NNNPhF]
*20 μmol of Cobalt complex associated to MAO;
t = 30 min.
Ppropylene = 6 bar; Vtoluene = 20 mL;
mol Ci
mol products
SCi (%) =
× 100 with Ci = 6 or 9
(2)
(3)
moli
molofdimers
Si−H (%) =
× 100withi = nor1
3. Results and discussion
1H and 13C NMR and IR data for bis(imino)pyridine ligands and the
corresponding cobalt complexes were compared to published data [4]
confirming the syntheses of the cobalt precursors [Co-NNNPhH] and
[Co-NNNPhF].
The results of catalytic tests employing [Co-NNNPhH] and [Co-
NNNPhF] as precursors and MAO as co-catalyst are summarized in
The results using [Co-NNNPhH] catalyst precursor (runs 1–2, 4–5)
led in most cases to 100% of dimerization (C6), with dimers being
mainly linear (> 90%). The highest selectivity in 1-hexene (S1-
H = 30%) is obtained with an Al/Co ratio of 300 and a reaction
conducted at 30 °C. In contrast, a higher ratio (Al/Co = 600, runs 3 and
6) led to no catalytic activity. Also, increasing the reaction temperature
yielded lower activities, which is probably due to catalyst deactivation.
When [Co-NNNPhF] is used (Run 7–12) dimers and trimers were
produced (C9 selectivity values being directly drived from SC6 data,
Fig. 3 evidences that, for each catalytic system, varying the Al/Co
ratio or the reaction temperature has no significant influence on 1-
hexene selectivity. In contrast, 1-hexene selectivity is strongly enhanced
with [Co-NNNPhF] precursor, showing the presence of fluorinated
phenyl groups in [Co-NNNPhF] positively impacts catalytic perfor-
mance. In this context, it is interesting to verify the influence of the
fluorinated groups in the structure of the two complexes.
X-ray diffraction analysis of a monocrystal of [Co-NNNPhF] allowed
the determination of its solid state molecular structure. The main
crystallographic data and structure refinement parameters are reported
S
C9 = 100 − SC6). Though trimers are produced as minor components,
the proportion of dimers is higher than 80% in all cases and all catalytic
activities are much higher (see run 7–12: TOF = 380–47300 h−1) than
those with precusor [Co-NNNPhH] (see run 1–6: TOF = 35–135 h−1).
Fig. 3. Selectivity in 1-hexene (1-H) with [Co-NNNPhH] and [Co-NNNPhF] precusors as a function of the MAO/Co ratio (100 and 300) and reaction temperature (10 and 30 °C).
3