J. A. van Rijn et al.
Table 2. Allylation of BPA in the presence of Ru- or Pd-based catalysts with different solvent systemsa
Conversion of
1
(%) (selectivity for O-allylation, %)b
Entry
Catalyst
Solvent
1 h
3 h
Yield of 4 after 3 h (%)
+
+
+
+
+
+
+
+
1
2
3
4
5
6
7
8
9c
[RuCp(PPh3)2]
[RuCp(PPh3)2]
[RuCp(PPh3)2]
[RuCp(PPh3)2]
[RuCp(PPh3)2]
[RuCp(PPh3)2]
[RuCp(PPh3)2]
[RuCp(PPh3)2]
Allyl alcohol
0 (−)
47 (100)
86 (85)
95 (81)
96 (68)
55 (91)
80 (92)
78 (93)
12 (100)
0 (−)
54 (94)
95 (82)
95 (72)
96 (64)
80 (86)
98 (84)
90 (88)
28 (100)
0
9
Diallyl ether (DAE)
DAE : toluene = 2 : 1
DAE : toluene = 1 : 1
DAE : toluene = 1 : 2
DAE : heptane = 2 : 1
DAE : heptane = 3 : 1
DAE : heptane = 4 : 1
DAE : toluene = 2 : 1
50
51
46
23
49
38
Pd(OAc)2 + dppdmp
2 (24)
a
◦
Reaction conditions: ratio BPA : allyl alcohol : [RuCpCl(PPh3)2] : AgOTs : HOTs = 500 : 2000 : 1 : 2 : 20, 60 C, total solvent volume = 2.5 ml.
Selectivity towards O-allylation indicated in brackets. O-allylation = 3 + 4; C-allylation = 5–7 + trisallylated compounds.
b
c
◦
Reaction conditions: ratio BPA : allyl alcohol : Pd(OAc)2 : dppdmp = 500 : 2000 : 1 : 4, 100 C, total solvent volume = 2.5 ml. Yield of 4 in parentheses
determined after 20 h reaction time. Selectivity for O-allylation remains 100%.
Allylating Agents as Solvent
be considered. Owing to the thermodynamic preference of C-
allylation over O-allylation of phenols, the reaction eventually will
build up C-allylated side products, of which the concentration
depends on a combination of catalyst structure and reaction time
and is independent on the allylating agent. It is therefore of key
importance that the reaction is halted before C-allylated products
form when performed in a batch reaction. In a continuous process
both water, forming a separate phase in the reaction mixture,
and the desired product needs to be efficiently removed from
the reaction mixture while feeding it with new starting materials.
The very low polarity of product 4 compared with 1 and water
could be used to separate these compounds by extraction. Diallyl
ether should be used as (co-)solvent, which can be efficiently
synthesized from allyl alcohol; with the use of [RuCp(PPh3)2](OTs)
The reaction with [RuCp(PPh3)2](OTs) as the catalyst in the
presence of acid and with diallyl ether as the allylating agent gave
the highest yield of 4 (30% after 3 h). The selectivity for O-allylation
is, however, not very high and a large amount of C-allylated
products is formed. In an attempt to improve the selectivity of
the reaction, different solvent systems were investigated and the
results are shown in Table 2.
When the reaction is performed in allyl alcohol as the solvent,
no conversion of 1 is observed (entry 1) and only formation of
diallyl ether is detected. With diallyl ether as the solvent (entry
2), the reaction proceeds very selectively, but mainly product 3
is formed and only 9% of 4 is formed after 3 h reaction time.
When the reaction medium is made more apolar by using a
mixture of diallyl ether and toluene (entry 3), conversion of 1
and yield of 4 is increased in a major way and 50% of 4 (based
on 1) is formed, a very high yield for a product that is formed
via two equilibrium reactions. Making the solvent more apolar
by increasing the amount of toluene on diallyl ether causes a
decrease in selectivity (entries 4 and 5). Also n-heptane was used
as the apolar component in the reaction mixture. When the results
from entries 6–8 are compared with that of entry 3, it appears that
slightly less n-heptane than toluene should be used for an optimal
selectivity for O-allylation, which obviously can be related to the
+
HOTs as the catalytic system, extremely high turnover numbers
can be achieved based on allyl alcohol (>200 000), as has already
been demonstrated.[
16]
A schematic representation of a possible continuous process is
shown in Fig. 2. In an ideal case, diallyl ether should be synthesized
from pure allyl alcohol, catalyzed by the Ru-catalyst, forming only
water as co-product (reactor 1: R1 in Figure 2). The resulting
mixture is then separated in a separation system (S2); a suitable
method would be distillation. The isolated diallyl ether is used
as allylating agent (in excess) in the O-allylation of BPA (reactor
2, R2), catalyzed by the same catalyst present in reactor 1. An
inert solvent (like n-heptane) could be added during, but also
after, the reaction to create an apolar system from which the
phenolic products and catalyst would precipitate, occurring in
S2. This separation is believed to be the bottleneck of such a
process, since many compounds are present in the mixture from
R2 and in particular products 3 and 4 proved to be difficult to
separate. A bleed of C-allylated products would be necessary, in
order to prevent accumulation of these compounds. However, the
catalystshouldberecycledandthereforeaheterogeneouscatalyst
would be favored.[ If the catalyst was homogeneous, it would
also be removed from the process, which is only commercially
acceptable when the bleed is very small or the catalyst is highly
active with high turnover numbers. Compounds containing two
phenol moieties hardly dissolve in heptanes and are therefore
less difficult to retrieve from the reaction mixture. However, the
selective separation of C-allylated product from 3 is expected to be
+
lower polarity of n-heptane. Finally, besides the [RuCp(PPh3)2]
catalyst, the Pd-containing catalytic system proved to be highly
selective for O-allylation. When a diallyl ether–toluene mixture
is used as the solvent, the reaction is completely selective for
O-allylation; however, conversion of BPA after 3 h is considerably
lower than in the Ru-based catalytic system. After 20 h, only O-
allylated products are detected while the yield for 4 increases to
2
4% based on 1. Longer reaction times did not result in higher
conversion, indicating complete deactivation of the catalyst. This
deactivation also prevents possible C-allylation, as C-allylation
mostly occurs to an appreciable extent later in the reaction, when
a high concentration of O-allylated product is reached.
18]
Industrial Application
When the described allylation reaction with BPA as the substrate
is implemented in an industrial process, several things should
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Appl. Organometal. Chem. 2011, 25, 207–211