A.A. Dabbawala et al. / Catalysis Communications 11 (2010) 616–619
617
Aldehydes
the optimum reaction temperature was 90 °C where maximum
TOF and selectivity was achieved.
O
O
CHO
O
The hydroformylation of vinyl acetate catalyzed by Rh/P(ONp)3
was studied at 90 °C under different syngas pressure (2.0–
6.0 MPa). Changes in the syngas pressure were found to affect
the reaction rate and selectivity (Table 1). The results indicate that
the hydroformylation of vinyl acetate proceeds slowly at low syn-
gas pressure. At low syngas pressure, CO insertion may be difficult
into the intermediate species as the ester carbonyl group form
thermodynamically stable five and/or six member rings, resulting
into considerably low TOF. TOF increased considerably with an in-
crease in the syngas pressure (2.0–4.0 MPa) and above that there
was a slight increase in the TOF. For example, when the syngas
pressure was increase from 2.0 to 4.0 MPa, TOF increased by a fac-
tor of ꢀ2.76, whereas with further increase in the syngas pressure
from 4.0 to 6.0 MPa, TOF was increased only by a factor ꢀ1.39 (see
Table 1). From the above discussion one can conclude that mini-
mum 4 MPa syngas pressure is require for achieving reasonable
TOF. In all instances, regioselectivity to branch aldehyde was great-
er then 98%.
The effect of ligand/Rh ratio on the catalytic activity/selectivity
of vinyl acetate hydroformylation was studied at 90 °C, 3.0 MPa
syngas pressure by varying ligand/Rh mmol ratio 3.0–18.0 (Ta-
ble 2). The results indicate that TOF was improved up to ligand/
Rh of 6.0. While TOF was found to decrease as ligand/Rh increased
from 6.0 to 18.0. However, chemo selectivity to aldehyde and reg-
ioselectivity to branched aldehyde were increased. This tendency is
also found in enamides hydroformylation catalyzed by Rh/biphe-
nyl based monodentate phosphite catalytic system [7].
Rh(CO)2acac/L
CHO
+
CO + H2
+
O
O
O
Vinyl acetate
2-acetoxypropanal
b (branched)
3-acetoxypropanal
l (linear)
L =
O
P
O
O
Scheme 1. Rh/tri-1-naphthyl phosphite catalyzed hydroformylation of vinyl
acetate.
phino)propane (dppp), 1,4-bis(diphenylphosphino)butane (dppb),
tris(4-methoxyphenyl)phosphine (p-MeO-C6H4)3P, tris(4-trifluoro-
methylphenyl)phosphine (p-CF3-C6H4)3P and vinyl acetate were
purchased from M/s Sigma-Aldrich Chemicals, USA and used as re-
ceived. The syngas (99.9%) used was from Hydro Gas India Pvt.,
Ltd., India.
The synthesis and characterization of phosphite ligand P(ONp)3
as well as corresponding rhodium complex has been described
elsewhere [17]. The hydroformylation reaction was performed in
a 100 mL stainless steel autoclave (Autoclave Engineers, EZE-Seal
Reactor, USA) and the reaction products were analyzed on a Shima-
dzu GC-17A gas chromatograph equipped with a flame ionization
detector.
When rhodium concentration was increased from 0.16 to
0.46 mM (ligand/Rh ratio 6) at 80 °C, 3.0 MPa syngas pressure, as
expected, the rate of vinyl acetate hydroformylation reaction was
found to increase with an increase in the rhodium concentration
indicating linear dependency with respect to the rhodium concen-
tration (Table 3). Similar result was also found for HRh(CO)(PPh3)3
catalyzed hydroformylation of vinyl acetate [18]. Aldehyde selec-
tivity was low (90%) at low 0.16 mM rhodium concentration and
improved up to 0.23 mM rhodium concentration, beyond that
aldehyde selectivity remained unaffected.
3. Results and discussion
The rhodium catalyst of P(ONp)3 was prepared in situ by mixing
P(ONp)3 with Rh(CO)2(acac). This system catalyzed the hydrofor-
mylation of vinyl acetate. The reaction products were 2-acetoxy-
propanal and 3-acetoxypropanal along with acetic acid and ethyl
acetate as side products. The branch aldehyde (2-acetoxypropanal)
was observed as the main product with high turnover frequency.
The selectivity of products in hydroformylation process is
mainly affected by variation in temperature. Temperature was var-
ied from 70 to 100 °C at constant syngas pressure (3.0 MPa). With
an increase of temperature from 70 to 100 °C, the reaction pro-
ceeds faster by a factor of ꢀ3.7 (Table 1) along with slight decrease
in the chemo selectivity toward aldehyde. However, an excellent
branch aldehyde regioselectivity (98%) was obtained in the entire
range of temperatures. At lower reaction temperature (70 °C), high
chemo selectivity toward aldehyde was observed (94.5%), the TOF
was rather low (1800 hÀ1). At 100 °C, the TOF increased up to
6720 hÀ1 with aldehyde selectivity decreased to 89.5%. Therefore,
For comparison, a variety of phosphine ligands were screened
for rhodium catalyzed hydroformylation of vinyl acetate under
Table 2
Effect of ligand/Rh ratio on Rh/tri-1-naphthyl phosphite catalyzed hydroformylation
of vinyl acetate.a
Entry
P/Rh
Conv. (%)
TOF (hÀ1
)
Saldehyde (%)
b/l
1
2
3
4
3.0
6.0
12.0
18.0
20.0
23.5
22.0
21.0
4800
5640
5280
5040
91.0
92.0
94.0
94.0
97/3
98/2
98/2
98/2
Table 1
a
Reaction
conditions:
sub/cat. = 4000,
[Rh(CO)2acac] = 0.23 mmol/L,
Effect of temperature and syngas pressure on Rh/tri-1-naphthyl phosphite catalyzed
temp. = 90 °C, syngas pressure (1:1) = 3.0 MPa, solvent (toluene) = 50 mL, and
reaction time = 10 min.
hydroformylation of vinyl acetate.a
Entry Temp.
Press.
(MPa)
Conv.
(%)
TOFb
(hÀ1
Saldehyde
(%)
b/l
(°C)
)
1c
2
3
4
5
6
7
8
70
80
90
100
90
90
3.0
3.0
3.0
3.0
2.0
4.0
5.0
6.0
15.0
17.0
23.5
28.0
12.5
34.5
42.0
48.0
1800
4080
5640
6720
3000
8280
10,000
11,520
94.5
93.0
92.0
89.5
86.0
93.0
93.0
93.5
98/2
98/2
98/2
98/2
98/2
99/1
99/1
99/1
Table 3
Effect of initial rhodium concentration on Rh/tri-1-naphthyl phosphite catalyzed
hydroformylation of vinyl acetate.a
Entry
[Rh(CO)2acac] (mmol/L)
Rate  103 (m sÀ1
0.17
0.26
0.32
0.40
)
Saldehyde (%)
b/l
90
90
1
2
3
4
0.16
0.23
0.35
0.46
90.0
93.0
93.0
93.0
97/3
98/2
98/2
98/2
a
Reaction conditions: sub/cat. = 4000, [Rh(CO)2acac] = 0.23 mmol/L, P/Rh = 6.0,
and solvent (toluene) = 50 mL.
b
a
Turnover frequency, determined based on GC, reaction time = 10 min.
Reaction time = 20 min.
Reaction conditions: sub/cat. = 4000, P/Rh = 6.0, temp. = 80 °C, syngas pressure
(1:1) = 3.0 MPa, solvent (toluene) = 50 mL, and reaction time = 10 min.
c