3848 Xu et al.
Asian J. Chem.
Catalytic condensation: A 250 mL four-neck round-
Lewis acid sites. The former is due to the presence of oxygen
atoms with low cordination, while the latter toAl3+ cation3,7,14
.
bottom flask equipped with mechanical stirrer and reflux
condenser are charged. 10.5 g (0.125 mol) of cyclopentanone
and 0.4 g of the HTc were added in the round-bottom flask
and 4.3 g (0.05 mol) of n-valeraldehyde was then added
dropwise with stirring slowly while keeping the reaction tempe-
rature at 80 ºC for 11 h. Then, the Mg-Al mixed oxides was
separated by filtration, the filtrate was dried over anhydrous
sodium sulfate and analyzed by gas chromatography on an
Angilent 6890A chromatograph with FID detector and equipped
with a SE-30 column. The desired product of 2-pentylidene-
cyclopentanone (e) was separated by column chromatography
(n-hexane:ethyl acetate = 12:1) and its structure was identified
by 1H NMR spectrum and MS (Trace DSQ-GC-MS). The 1H
NMR spectra were recorded on a Bruker ARX300 instrument
with TMS as the interior standard. The 1H NMR (CDCl3) of
2-pentylidene-cyclopentanone (e): δ 0.866-0.914 (t, 3H, CH3),
1.311-1.455 (m, 8H, 4CH2), 1.890-1.965 (m, 2H, CH2), 2.099-
2.171 (m, 2H, CH2), 2.286-2.338 (t, 2H, CH2), 2.544-2.605 (t,
2H, CH2), 6.533 (t, 1H, -C=C-H). MS (EI, 70 eV): m/z = 151.94
(M+).
The reaction procedure of the aldol condensation
(Scheme-II) is nearly the same as the traditional procedure.
The aldol condensation was carried out on basic sites firstly
by capturing an α-H atom from cyclopentanone. Then the
generated carbanion species will attack the carbonyl group of
valeraldehyde. Finally, the ultimate product (e) was achieved
by dehydrating on the weak acid sites of the HTc (773 K).
Although it is easier to form a carbanion on the cyclopentanone
in the presence of base properties, the weak acid properties
can promote the formation of the protonated carbonyl compound
on valeraldehyde to be attacted by the generated carbanion.
As a result, the catalyst which has acid-base properties is benefit
for the cross-condensation3,15
.
O
O
O
Valeraldehyde
B
+
-BH
O
O
O
O
OH
+BH
_
B
-H O
2
RESULTS AND DISCUSSION
Scheme-II: Procedure of the cross-condensation between cyclopentanone
and valeraldehyde
The catalyst of HTc (773 K) used in the aldol condensation
between valeraldehyde and cyclopentanone was achieved by
calcinating hydrotalcite precursor HT (Mg/Al = 3) at 773 K.
The XRD powder patterns of HT (a) and HTc (773 K) (b)
were shown in Fig. 1. The XRD patterns indicated that the
lamellar structure of the HT (a) was changed. Moreover, the
obvious characteristic peaks of MgO (200) and Al2O3 (135)
appeared in the XRD patterns.
In order to get a better catalytic performance, reaction
temperature was taken into account firstly in our experiments.
Varying temperature of 60, 80 and 100 ºC, respectively were
carried out with a valeraldehyde/cyclopentanone molar ratio
of 1/5 and without solvent. Entries 4, 7, 8 (Table-1) indicated
that with the temperature up to 100 ºC, the valeraldehyde
conversion was increased. However, the selectivity of e was
the best when the temperature at 80 ºC. Due to low temperature
couldn't activate the carbonyl of cyclopentanone and the
catalysts efficiently, the lower temperature could result in low
valeraldehyde conversion and selectivity to e. On the contray,
a product g appeared that isomerizing from e when the reaction
temperature reached 100 ºC. 2-Cyclopenten-1-one (g) was
more thermodynamically stabler than 2-pentylidene-cyclo-
pentanone (e) because the conjugate between the carbonyl and
cyclic olefinic bond was more easier and stabler. Higher
temperature could favour to activate the catalyst and the
procedure of isomerization.
(003)
(a)
(006)
(012)
(015)
(110)
(018)
(112)
(200)
(135)
(b)
The reaction was also carried out over the different amount
of catalyst. From the entries 4, 9, 10, we could see that the
valeraldehyde conversion wouldn't increase with the HTc (773
K) used from 0.4-0.6 g. However, the side product g also
appeared when 0.6 g catalyst was used. 0.4 g HTc (773 K)
was enough for the procedure of the reaction under this
reaction condition. While increasing HTc (773 K) would
decrease the selectivity for producing g as a side product. Less
catalyst couldn't activate the substance efficiently and result
in low valeraldehyde conversion and poor selectivity to the
major product e.
0.
10
20
30
40
2θ (º)
50
60
70
80
90
Fig. 1. XRD powder patterns of HT (a), HTc (773 K) (b)
It is well known that the aldol condensation can be
catalyzed by both acid and base10-13. The base catalyst is favour
to the formation of carbanion on the cyclopentanone. However,
the acid catalyst can active the carbonyl group on the
valeralderhyde easily and strengthen the carbocation of the
carbonyl to be attacted by the carbanion species. The catalyst
of HTc (773 K) owned both the acid and base catalyst
excellences simultaneously for its both strong Lewis basic and
The molar ratio between valeraldehyde and cyclopen-
tanone also played an important role in the selectivity between
cross- and self-condensation3,7,9,16. Entries 1-6 (Table-1) showed
that valeraldehyde/cyclopentanone molar ratio of 1/5 was the