G Model
CCLET-3555; No. of Pages 3
2
X.-L. Zheng et al. / Chinese Chemical Letters xxx (2016) xxx–xxx
Fig. 1. Structures of ligands L1–L6.
3. Results and discussion
afford 3-phenylbutanal as the dominant product. 1H NMR
(400 MHz, CDCl3): 9.73 (s, 1H), 7.42–7.20 (m, 5H), 3.38 (s, 1H),
2.79 (d, 2H, J = 14.9 Hz), 1.34 (s, 3H). 13C NMR (100 MHz, CDCl3):
d
From the outset, six different ligands (Fig. 1) were studied in the
d
Rh-catalyzed hydroformylation of
a-methylstyrene under 5 MPa
201.90, 145.50, 128.72, 126.81, 51.76, 34.30, 22.22 (see Supporting
information).
of syngas at 100 8C. As demonstrated in Table 1, all the ligands
exhibited excellent selectivity for aldehydes and regioselectivity
for linear aldehyde (3-phenylbutanal, >97.0%). L1 and L3, which
contained a di(N-pyrrolyl)phosphino group, resulted in much
higher activity. In contrast, L2, bearing the N-carbazolyl group with
a larger steric hindrance, resulted in relatively lower activity. L4–
L6, which contained triphenylphosphine and its derivatives, also
gave lower activity, and the one with an electron-withdrawing
substituent –CF3 (L5) demonstrated higher activity compared to
the one with the electron-donating substituent –OCH3 (L6)
(Table 1, entries 4 and 5). Of the tested ligands, L1, which
contained an electron-withdrawing N-pyrrolyl group and caused
less steric hindrance, is the best ligand in terms of activity and
regioselectivity. This is because the electron-withdrawing group
substituted on the phosphorus weakens the Rh-carbonyl bond and
thus favors the insertion of CO and the formation of Rh-acyl active
species. In addition, a smaller ligand might somehow facilitate the
The hydroformylation is highly dependent on the reaction
conditions; therefore, the optimization of L1/Rh molar ratio, initial
pressure, and reaction temperature was performed in the presence
of Rh(acac)(CO)2/L1 as catalyst, and the results were shown in
Table 2. When L1/Rh molar ratio of 5:10 was used, high activity
(Table 2, entries 1 and 2) could be achieved at 100 8C. Further
increasing the L1/Rh molar ratio decreases the activity (Table 2,
entry 3). Considering the stability of the catalyst, a L1/Rh molar
ratio of 10 is selected for the sequent experiments. A clear impact of
the reaction temperature on the activity was observed (Table 2,
entries 4–8). For instance, the reaction rate was unsatisfactory at
90 8C, while at 110 8C a high activity was achieved. From entries 4 to
8, it is not difficult to find that the chemoselectivity of the aldehyde
decreased slightly when the temperature increased, because high
temperatures were likely to benefit the hydrogenation of
a
-methylstyrene, which was confirmed by the observation of
coordination of
a-methylstyrene to the Rh center [7], and thus
2-phenylpropane via GC. The total pressure of syngas (CO/H2: 1/1)
Table 1
Effect of ligand on Rh-catalyzed hydroformylation of
a
-methylstyrene.a
e
Entry
Ligand
Con. (%)b
Sel. of Aldehydes (%)c
Regiosel. of linear aldehyde (%)d
TOF (hÀ1
)
1
2
3
4
5
6
L1
L2
L3
L4
L5
L6
97.2
67.5
72.9
42.6
48.6
46.7
98.2
94.3
98.3
98.6
98.4
99.1
99.2
97.7
99.0
97.0
98.8
97.1
194
135
146
85
97
93
a
[Rh(acac)(CO)2] =1.5 mmol/L,
a
-methylstyrene (1.0 mL), S/C = 1000, L/Rh = 10, 100 8C, 5 MPa (CO/H2 = 1, pressure ratio), 5 h, toluene 4.0 mL.
b
c
Conversion of
a-methylstyrene was determined on the basis of GC.
Selectivity for aldehydes, determined on the basis of GC.
d
e
Regioselectivity for linear aldehyde, determined on the basis of GC.
Turnover frequency: moles of aldehydes per mole of Rh per hour.
Table 2
Effect of reaction conditions on Rh-catalyzed hydroformylation of
a
-methylstyrene.a
e
Entry
L1/Rh
T (8C)
P (MPa)
t (h)
Con. (%)b
Sel. of aldehydes (%)c
Regiosel. of linear aldehyde(%)d
TOF (hÀ1
)
1
2
3
4
5
6
7
8
9
10
5
10
20
10
10
10
10
10
10
10
100
100
100
90
5
5
5
5
5
5
5
5
4
6
2
2
2
1
1
1
1
1
1
1
85.3
86.2
57.6
38.2
65.3
73.1
60.8
47.3
64.0
80.8
96.9
97.6
97.1
98.5
96.9
95.4
92.1
91.2
94.1
95.8
99.2
99.2
99.0
99.0
99.1
99.1
99.1
99.1
99.1
99.2
426
431
288
382
653
731
608
473
640
808
100
110
120
130
110
110
b–e
See Table 1.
a
[Rh(acac)(CO)2] =1.5 mmol/L,
a-methylstyrene (1.0 mL), S/C = 1000, CO/H2 =1 (pressure ratio), toluene 4.0 mL.
Please cite this article in press as: X.-L. Zheng, et al., Highly active rhodium/phosphorus catalytic system for the hydroformylation of
a-