A.M. Trzeciak,J.Z Zidlkowski / Hydroformylationof L5-hexadienebyRh-complexes
109
main reaction product (81% at 60°C) (Table 2). Similar
effects of total (CO + H 2) pressure are observed for
the reaction catalyzed by the Rh(acacXCOXPPh3)/
PPh 3 system. Also in this system, lower total (CO + H z)
pressure stops the hydroformylation reaction at the
stage of monoaldehyde-6-heptenal (Table 2). With
pressure changing from 10 to 6 atm the yield of 6-
heptenal increases from 25 to 85%, but isomerization
of 6-heptenal ~ 4-heptenal does not occur.
TABLE 4. Composition of the monoaldehyde fraction of the product
of the hydroformylation reaction of 1,5-hexadiene catalyzed by
Rh(acac){P(OPh)3} 2 +L ([L]:[Rh]= 2) at 10 atm, 60°C, after 3 h
L=
4-Heptenal b 6-Heptenal a v(CO)* O
(cm-1) (deg)
PEtPh2
P(p-MeC6H4)3
PPh3
P(OEt)3
P(O-o,o-Me2C6H3)3 100
30
54
40
70
45
60
0
2066.7 140
2066.7 145
2068.9 145
2076.3 109
2083.2 190
100
0
In contrast to 6-heptenal, which is an intermediate
product and may undergo further hydroformylation,
the 4-heptenal may be treated as the side product
because in practical terms it is not reactive in hydro-
formylation. Applying the phosphine based catalytic
system (II), which is not active in 4-heptenal formation,
octanedials are obtained already at 100% yield at 60°C
whereas the phosphite based system (I) requires higher
temperature (80°C).
The selectivity factor, n/iso ratio, is practically inde-
pendent of changes of reaction parameters (tempera-
ture, CO/H 2 ratio and total pressure). For phosphite
based catalytic system (I) the n/iso factor is 2.5-3.2
whereas for the system (II) (phosphine based) it is
lower (1.8-2.1) for both mono- and di-aldehydes.
Decrease of isomerization reaction yield, caused by
reaction parameter changes, is not accompanied by
n/iso increase. Similarly, in hex-l-ene hydroformyla-
tion [2,6], with increase of n/iso parameter some in-
crease (not decrease) of hex-2-ene yield was observed.
Phosphite concentration increase causes decrease of
reaction rate only, and not changes of the final reac-
tion products. At seven-fold phosphite excess versus
the rhodium complex (at 50°C and 10 atm) 23% of
4-heptenal and 77% of octanedial were obtained (a
considerably higher percentage yield of dialdehydes
was obtained with increase of phosphite concentration).
Undoubtedly, the catalytic activity of each system
depends on the electronic and steric effects of the
ligands coordinated to the metal. To judge which domi-
nates in the phosphite system the content of the
mono-aldehydes fraction in the reaction catalyzed by
Rh(acac){P(OPh)3}2+ L (L -- PPh 3 or P(OR)3) was de-
termined. The data collected in Table 4 indicate the
prevailing electronic effect of the ligands applied and
only when the ligands have stronger donor properties
(according to Tolman scale [7]) does some 6-heptenal
appear in reaction products. This suggests that isomer-
ization was partially limited only by stronger donor
ligands. We failed to obtain the mixture of 4- and
6-heptenals in reaction catalyzed by Rh(acac)(CO)-
(PPh a) modified with P(OPh)3 or bulky P(O-2,4,6-
MeaC6H3)3. Even at [L]:[Rh] = 1, 4-heptenal was the
only monoaldehyde identified in both reaction mix-
tures. The results discussed above allow us to distin-
P(O-o-MeC6H4)3
P(OPh)3
100
100
0
0
2084.1
2085.3 130
141
* v(CO) (A1) of Ni(CO)3L in cn2c12.
a,b See Table 2.
guish some aspects of the behaviour of catalytic sys-
tems (I and II) revealed by studies using different
phosphorus ligands (e.g. PPh 3 and P(OPh)3) used for
their modification. Two catalytic systems of practically
identical content: Rh(acac){P(OPh)3}2/PPh 3 and
Rh(acac)(COXPPh3)/P(OPh)3 act differently as is
demonstrated by the reaction products. In the first
case, the presence of free phosphine causes retardation
of isomerization whereas in the second system only
4-heptenal is obtained, similarly to the system with only
the phosphite ligand.
To explain these experimental facts 31p-NMR stud-
ies were performed. The results of the measurements
were the following:
a) For the system Rh(acac){P(OPh3}2+ PPh3' re-
gardless of the PPh 3 concentration and reaction time,
only the Rh(acac){P(OPh)3}2 complex was observed (8
123.1 ppm, J(Rh-P) 307 Hz);
b) in the system Rh(acac)(CO)(PPh3)+ p(OPh)3
([P(OPh)3]: [Rh] = 1) immediately after mixing, the
bands typical for Rh(acacXCO)(PPh3) complex (8 48.6
ppm, J(Rh-P) 178 Hz) disappear and the bands, as-
signed for Rh(acac){P(OPh)3}2 appear. After a couple
of hours an equilibrium is established and three com-
plexes Rh(acac)(CO)(Pph3)' Rh(acac){P(OPh)3}2 and
Rh(acac)(CO){P(OPh)3} (8 121 ppm, J(Rh-P) 293 Hz)
are found in the solution;
c) in the system: Rh(acac)(CO)(PPh3)+ P(O-o-Me-
C6H4)3, ([P(O-o-MeC6H4)3]: [Rh] = 2), in spite of the
significant steric hindrance of this phosphite ligand
(O = 141°) it substitutes immediately for both PPh 3
and CO and the only product identified is Rh(acac){P-
(O-o-MeC6H4)a}2 (8 123 ppm, J(Rh-P) = 305 Hz).
From the above experiments, one may conclude that
any phosphite ligand used practically eliminates the
phosphine ligand from the coordination sphere of the
rhodium catalyst precursor at the very beginning of the
reaction. The rhodium catalyst precursor with coordi-