10.1002/cctc.201701058
ChemCatChem
FULL PAPER
ionic liquid and n-dodecane (internal standard) were added to the glass
vessel and the reactor was closed and purged with nitrogen. 4 mL of
acetonitrile was transferred to the reactor under a flow of nitrogen gas
with the aid of a syringe. The reactor was frozen in liquid nitrogen and
then butadiene was liquefied in a flask cooled in a bath at 78°C and the
desired amount of the diene was transferred to the reactor via syringe.
The reactor was heated to room temperature with the aid of a heating
gun, then it was connected to the heating unit. Finally, the reactor was
connected to the gas line for carbon dioxide loading up to a pressure of
30 bar, held constant by a backpressure valve. Once the working
temperature was reached, the stirring was turned on. The pressure
reactor was carefully checked along the reaction to warrant that enough
liquid butadiene remains in the reactor. After the reaction time, heating
and stirring were turn off, the reactor was immersed in an ice bath and
the remaining butadiene/CO2 was vented in a hood. The obtained
mixture was diluted in CH2Cl2 and analyzed using (GC-FID) Hewlett
Packard 5890 Series II and GC-MS Hewlett Packard G1800A GCD
System, both equipped with HP5 columns. 4-vinylcyclohexene and δ-
lactone (3-ethylidene-6-vinyltetrahydro-2H-pyran-2-one) were used to
calculate the response factors to dimers and lactones, respectively. n-
dodecane (Sigma Aldrich) was used as an internal standard. The TON
was calculated from the mols of butadiene converted, excluding the
amount of vinylcyclohexene formed, and the mols of Pd catalyst used.
these carbene species in the case of ionic liquids non-
substituted at the C2 position.[31,32]
Table 2. Telomerization of butadiene with carbon dioxide in the presence of
different imidazolium ionic liquids.[a]
Selectivity (%)
1+2+3 (1/2+3)
Ionic
Liquid
Entry
TON
8
3.3
20.1
0.0
0.0
0.0
3.1
96.7 (99/1)
79.9 (100/0)
100.0 (100/0)
0.0
4500
80
13
14
15
16
17
18
-
BMImBF4
BMImPF6
BMImCl
30
0
100.0 (100/0)
96.9 (99/1)
25
MeOImAcO
BMMImBF4
1630
[a]Reaction Conditions: Pd(OAc)2 = 2.7 mg (1.2 10-2 mmol); PTpOMe/Pd = 3;
p-hydroquinone = 33 mg (0.30 mmol); DIPEA = 77.4 mg (0.60 mmol); 4 mL of
acetonitrile; C4H6 = 10.0 mL (120 mmol); 30 bar of CO2; 70 °C; 5 h; 700 rpm.
n-dodecane was added as an internal standard; 8 = octatriene; 1+2+3 =
lactones; 1/2+3 is the ratio between δ-lactone and γ-lactone; TON = turnover
number after 5 h reaction.
Acknowledgements
We would like to thank the CNPq for the scholarship to Mr.
Balbino.
Conclusions
Keywords: butadiene, telomerization, carbon dioxide, δ-lactone,
3-ethylidene-6-vinyltetrahydro-2H-pyran-2-one, ionic liquid.
The telomerization of 1,3-butadiene with carbon dioxide to δ-
lactone is readily achieved by using Pd(OAc)2 plus tris-(p-
methoxyphenyl)-phosphine in the presence of p-hydroquinone,
N,N-diisopropylethylamine and acetonitrile. A remarkably high
TON of 4500 with 96% selectivity to the valuable δ-lactone was
obtained after 5 h reaction at 70°C. This is the highest catalytic
activity reported so far for this reaction. The telomerization was
deactivated by the presence of different 1,3-dialkylimidazolium
ionic liquids, likely by the formation of inactive Pd-carbene
species.
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Telomerization reactions
The telomerization reactions in a batch system were carried out in a 50
mL magnetically stirred stainless steel reactor provided with a glass
vessel. The temperature reaction was controlled with a thermocouple
dipped inside the reaction and a heating unit. 1 mL of 12 mM solution of
Pd(AcO)2 in dichloromethane was added to the reactor glass and the
solvent was evaporated under reduced pressure. Then the desired
quantities of phosphine, p-hydroquinone, N,N-diisopropylethylamine,
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