ZENG Yan et al. / Chinese Journal of Catalysis, 2012, 33: 402–406
In a typical hydroformylation reaction, ILPEG750 (0.25 g,
ꢀ3
containing 2.6 × 10 mmol of Rh), 1-octene (0.6 g, 5.2 mmol),
toluene (3.8 g), n-heptane (0.3 g), and n-decane as an internal
standard (0.1 g) were charged into a 75-ml stainless-steel
autoclave. The autoclave was sealed and flushed three times
Conversion of 1-octene
Yield of aldehyde
1
00
80
6
4
2
0
0
0
0
with CO at 1.0 MPa, pressurized with syngas (CO:H = 1:1) to
2
the required pressure, and held at the designated temperature,
with magnetic stirring, for a fixed length of time. The autoclave
was then cooled to room temperature and depressurized. The
upper organic phase was separated by phase separation and
immediately subjected to GC and GC-MS analyses.
1
2
3
4
5
6
7
8
GC analysis was performed on a Tianmei 7890 GC instru-
ment equipped with an OV-101 column (50 m × 0.25 mm) and
Recycle number
Fig. 2. Recycling efficiency of ILPEG750-stabilized Rh nanoparticle
catalyst for hydroformylation of 1-octene.
a flame-ionization detector; N was used as the carrier gas.
2
GC-MS measurements were performed on an HP 6890
GC/5973 MSD instrument with an HP-5MS column (30 m ×
.25 mm); He was used as the carrier gas. Transmission elec-
of aldehyde decreased a little (entry 7). It is also evident from
the data in Table 1 that prolonged reaction times led to in-
creases in the conversion of 1-octene and aldehyde yields
0
tron microscopy (TEM) images were taken with a Philips
2
Tecnai G 20 TEM (Philips, Eindhoven, The Netherlands) at an
(
entries 3, 8, and 9). The molar ratios of normal to branched
accelerating voltage of 200 kV. Inductively coupled plasma
atomic emission spectroscopy (ICP-AES) analyses of Rh were
carried out using an Optima 2000 DV (Perkin Elmer, USA).
Optimization of the reaction conditions was carried out us-
ing the hydroformylation of 1-octene as a model reaction. As
shown in Table 1, the conversion of 1-octene and the yield of
aldehyde increased with increasing reaction pressure (entries
aldehydes (n/b = 1.2–4.7) obtained with ILPEG750-stabilized Rh
nanoparticles were similar to the ratios previously reported for
reactions catalyzed by Rh nanoparticles [11,13]. It should be
noted that when n-heptane was used as the organic phase in-
stead of a toluene/n-heptane mixture, much lower conversion
was obtained (entry 10). This result implies that for reactions
carried out in a homogeneous system under heating, the choice
of an appropriate organic phase is crucial, because we observed
that ILPEG750 and n-heptane cannot mix to form a homogeneous
phase at the reaction temperature.
The recycling efficiency of the Rh nanoparticle catalyst was
investigated under the optimized reaction conditions (Table 1,
entry 3). After reaction, the lower ILPEG750 phase containing the
catalyst was separated from the upper organic phase by phase
separation and directly used in the next run. The catalyst was
used eight times without evident loss of activity, as shown in
Fig. 2.
TEM images were used to examine the morphologies of the
Rh nanoparticle catalyst before and after reaction, as shown in
Fig. 3. The mean diameter of the freshly prepared Rh
nanoparticles was 2.1 nm, with a standard deviation of 0.3 nm
(see Fig. 3(a)). Analysis of the Rh nanoparticles after eight
cycles of use showed an average diameter of 2.6 nm, with a
standard deviation of 0.7 nm (see Fig. 3(b)). TEM analysis
indicated that there was no apparent size increase.
We also studied the leaching of Rh in the upper organic
phase (see Table 2). ICP-AES analysis showed that the loss of
Rh decreases with increasing recycling number. The average
leaching of Rh was 1.1%.
1
ꢀ4). The effects of temperature on the reaction were studied.
In the range of 70ꢀ90 °C, the conversion of 1-octene and the
yield of aldehyde increased with increasing reaction tempera-
ture (entries 3, 5, and 6). Further increasing the temperature to
1
00 °C achieved a slightly improved conversion, but the yield
Table 1 Hydroformylation of 1-octene catalyzed by ILPEG750-stabilized
Rh nanoparticles
Pressure Temperature Time Conversion Aldehyde
a
Entry
n/b
o
(
MPa)
3.0
4.0
5.0
6.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
( C)
(h)
15
15
15
15
15
15
15
17
20
15
15
(%)
40
68
93
99
83
88
96
99
99
48
94
yield (%)
22
1
2
3
4
5
6
7
8
90
90
90
90
70
80
100
90
90
90
90
4.7
2.8
1.5
1.4
1.8
2.5
1.2
1.4
1.4
2.3
1.4
54
86
87
58
80
83
90
91
9
b
1
1
0
1
43
c
86
ꢀ
3
Other conditions: ILPEG750 0.25 g (containing 2.6 × 10 mmol of Rh),
toluene 3.8 g, n-heptane 0.3 g, CO:H = 1:1, substrate:Rh = 2000:1 (molar
2
ratio), internal standard n-decane 0.1 g, the miscibility temperature of the
system is 80 °C.
The molar ratio of normal to branched aldehydes.
Using n-heptane as the sole upper-phase organic solvent.
Extension of the hydroformylation reaction to other sub-
strates, including cyclohexene, 1-tetradecene, and styrene, also
afforded good conversions, as shown in Table 3.
a
b
c
Using toluene as the sole upper-phase organic solvent.
In conclusion, we have demonstrated that ILPEG750-stabilized