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type fluorinated phosphines (currently commercially available from
Strem),[32] PMQl,[43] PMoNH2,[44] PMoNMe2,[45] BMImAcO,[46,47]
BMImBF4,[48] and BMIm(13C(2)-enriched)AcO[49] were prepared ac-
cording to reported procedures.
Table 6. Scale-up of the reaction and stability of the catalyst.[a]
Entry
AcOH
IL
Selectivity
[%]
TON
[mmol]
[mmol]
1
3+4
5+6 (6/5)
1
2
3
4
80
200
200
80
0.30
0.30
0.75
–
9.5
5.0
3.6
9.7
1.9
9.3
44.2
5.8
88.6 (88/12)
85.7 (90/10)
52.2 (92/8)
84.5 (87/13)
14600
7270
10640
9200
Synthesis of 3-(2-methoxyethyl)-1-methylimidazolium
acetate (MeOImAcO)
1-Methylimidazole (40.1 g, 482 mmol) and 2-methoxyethylmethane
sulfonate (75.1 g, 487 mmol) were mixed in a flask and kept at
508C under stirring for 48 h (Scheme 2). The obtained methylimi-
dazolium mesylate was washed five times with ethyl acetate to
remove 2-methoxyethylmethane sulfonate. The remaining solvent
was removed under reduced pressure to afford the pure product
in 83% yield. This salt (6.75 g) was diluted in deionized water, and
the solution was passed through an anionic exchange column Am-
berlite IRA-400 (1.4 equiv. OHÀ/L). The resulting solution was neu-
tralized with AcOH to produce MeOImAcO quantitatively after
[a] Reaction Conditions: Pd(OAc)2 =2.7 mg (0.012 mmol); Dan2phos/Pd=
3; C4H6 =25.0 mL (300 mmol); 24 h, 1008C, 700 rpm. n-Dodecane was
added as an internal standard; 1=dimer; 3+4=butenyl acetates; 5+6=
telomers; 6/5 is the ratio of linear and branched telomers.
1008C the effective TOF at 5 h (550 hÀ1) is very similar to that
at 24 h (610 hÀ1), which indicates that after 24 h there is not
a significant degradation of the catalyst (cf. entry 3, Table 5
and entry 1, Table 6). Under these optimized conditions, the
AcOH is consumed completely to produce an increased
amount of dimer 1. Therefore, an increase in the amount of
AcOH used from 80 to 200 mmol was assayed, which led to an
approximate 50% decrease of the TON and an increase of the
amount of butenyl acetates (entry 2, Table 6). The use of
a larger amount of the IL further increased the production of
butenyl acetates (entry 3, Table 6).
1
water evaporation (7.2 g, 94% yield). H NMR (400 MHz, D2O): d=
1.74 (s, 3H, CH3COO), 3.24 (s, 3H, NCH3), 3.70 (t, JHÀH =4.9 Hz, 2H,
NCH2), 3.78 (s, 3H, OCH3), 4.27 (t, JHÀH =4.9 Hz, 2H, OCH2), 7.35 (d,
J
HÀH =22.6 Hz, 1H, arom. H), 7.41 (d, JHÀH =22.6 Hz, 1H, arom. H),
8.66 ppm (s, 1H, NCHN); 13C NMR (100 MHz, D2O): d=23.34
(CH3COO), 35.64 (d, J 13C =2.8 Hz, NCH3), 48.75 (d, J 13C =2.4 Hz,
13CÀ
13CÀ
NCH2), 58.07 (OCH3), 69.67 (OCH2), 122.40 (d, J 13C =105.4 Hz,
13CÀ
arom. C), 123.46 (d, J 13C =105.4 Hz, arom. C), 136.25 (NCN),
13CÀ
180.53 ppm (CH3COO); IR (pure IL): n˜max =621.52 (gNÀCH , ring-puck-
2
ering), 697.78, 833.89 (gC2ÀH), 921.50 (ns CÀOÀC), 1011.45 (nNÀCH ),
3
Under the optimized conditions, the TON decreased by
more than 5000 turnovers in the reaction performed without
MeOImAcO (cf. entries 1 and 4, Table 6).
1043.10 (dring), 1117.27 (nNÀCH ), 1171.73 (nas COC), 1391.33 (nas C N C ),
2
2 3 4
1560.83 cmÀ1 (CH3COOÀ); MS (ESI+, MeOH): m/z: 141.1025 [M]+; el-
emental analysis calcd (%) for C9H16N2O3 (200.11 gmolÀ1): C 53.98,
H 8.05, N 13.99; found: C 53.13, H 8.35, N 13.17.
Unfortunately, the catalyst system could not be recycled
under these conditions because of the formation of polybuta-
diene, which hindered the recovery and reuse of the catalytic
system.
Telomerization reactions
The telomerization reactions in a batch system were performed in
a 50 mL stainless-steel reactor that was stirred magnetically. The re-
action temperature was controlled by using a thermocouple
dipped inside the reaction and a heating unit. The desired quanti-
ties of phosphine, n-dodecane (internal standard), and IL were dis-
solved in AcOH (2.0 mL) that contained the appropriate amount of
Pd(OAc)2. This solution was transferred, along with the remaining
AcOH, to the reactor under a flow of N2 by syringe, and the reactor
was frozen in liquid N2. Butadiene was liquefied in a flask cooled in
a bath at À788C, and the desired amount of the diene was trans-
ferred to the reactor by syringe. The reactor was heated to RT by
using a heating gun, then it was connected to the heating unit,
and the stirring was turned on once the working temperature was
reached. The pressure of the reactor was checked carefully
throughout the reaction to ensure that enough liquid butadiene
remained in the reactor. After the reaction time, heating and stir-
ring were turned off, the reactor was immersed in an ice bath, and
the remaining butadiene was vented in a hood. The reaction mix-
ture was treated with a saturated solution of NaHCO3 to neutralize
unreacted AcOH and extracted three times with CH2Cl2. The prod-
ucts were analyzed by GC with flame ionization detection (FID) by
using a Hewlett Packard 5890 Series II system and by GC–MS by
using a Hewlett Packard G1800A GCD system both equipped with
HP5 columns. 4-Vinylcyclohexene, 1-acetoxy-2,7-octadiene, and
trans-2-butenyl acetate (Sigma Aldrich) were used to calculate the
response factors to dimers, telomers, and butenyl acetates, respec-
tively. n-Dodecane (Sigma Aldrich) was used as an internal stan-
dard. The catalyst efficiency was determined by calculating the
Conclusions
The telomerization of 1,3-butadiene with AcOH to octadienyl
acetates is achieved readily by using Pd(OAc)2 plus a remark-
able p-acid sulfonated phosphine Dan2phos in 3-(2-meth-
oxyethyl)-1-methylimidazolium acetate. Under the optimized
conditions, a turnover number of 14600 can be reached with
89.0% of selectivity to telomers. Although the reaction occurs
in the absence of the ionic liquid, lower turnover numbers and
selectivities were obtained compared to the reactions per-
formed if the catalysts were supported in this medium. It is
also clear that the ionic liquid acts as solvent, stabilizer, and co-
catalyst for the activation of the AcOH. It can be anticipated
that this approach can be extended for other transformations
in which the basicity/nucleophilicity has to be modulated.
Experimental Section
Materials
1,3-Butadiene (Linde 2.5), AcOH (Sigma Aldrich), Pd(OAc)2 (Aldrich),
PPh3 (Acros Organics), PTpF, PTpOMe, PTpMe, DPPE, DPPP, DPPB
(Aldrich), 1-methylimidazole (Sigma Aldrich), and 2-methoxyethyl-
methanesulphonate (Acros Organics) were used without further
purification. NaTPPMS,[41] Na2TPPDS,[42] Dan2phos, and Danphos-
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