A series of 20 one chiral epoxides were obtained with excellent yields (up to 99%) and enantioselectivities (up to >99% ee) using hybrid amide-based Cinchona alkaloids. Our method is characterized by low catalyst loading (0.5 mol %) and short reaction times. Moreover, the epoxidation process can be carried out in 10 cycles, without further catalyst addition to the reaction mixture. This methodology significantly enhance the scale of the process using very low catalyst loading.
A series of 20 one chiral epoxides were obtained with excellent yields (up to 99%) and enantioselectivities (up to >99% ee) using hybrid amide-based Cinchona alkaloids. Our method is characterized by low catalyst loading (0.5 mol %) and short reaction times. Moreover, the epoxidation process can be carried out in 10 cycles, without further catalyst addition to the reaction mixture. This methodology significantly enhance the scale of the process using very low catalyst loading.
Catalytic enantioselective epoxidation
of allylic alcohols, introduced by Sharpless[1] in the 1980s, has been recognized as one of the most significant
tools in asymmetric synthesis, since epoxides are considered versatile
building blocks and intermediates in asymmetric organic transformations.[2,3] This fundamental discovery has significantly expanded over the last
40 years, especially in the field of metal catalysis[4] and organocatalysis.[5] With the
growing demand for green and sustainable chemistry, the development
of environmentally benign and cheap catalysts remains a great challenge
in stereocontrolled organic synthesis.[6] In this area, phase-transfer catalysis (PTC) has become established
as a comprehensive method,[7] owing to mild
reaction conditions, operational simplicity, and no use of heavy metals.
Particular attention in such work has been devoted to the asymmetric
epoxidation of α,β-unsaturated ketones,[3a,8−10] as an extension of the pioneering work by Wynberg
et al.[11] on epoxidation of E-chalcones using quinine salts as catalysts. However, successful
examples of highly enantioselective synthesis of epoxyketones still
remain few in number. The most representative continuations of Wynberg’s
discovery were published in the 1990s by the Lygo[12] and Corey[13] groups. Alternative
methods to improving the abilities of Cinchona-based
catalysts were presented by the Park[14] and
Siva[15] groups, who showed that adding surfactants
to reaction mixtures or using ultrasound support increased the enantiomeric
excess of products formed. On the other hand, Maruoka et al.[16] introduced efficient, but expensive, BINOL-based
catalysts. Furthermore, other types of PTC catalysts, such as macrocyclic
compounds, peptides, guanidine salts, prolines, etc., have also been
used, albeit without high enantioselectivities.[17]Despite recent spectacular progress in asymmetric
epoxidation of E-chalcones, there are several issues
that prevent their
general applicability. The main disadvantages of the methods discussed
are as follows: multistep synthesis of catalysts, high catalyst loading,
a frequent necessity to use special techniques, and long reaction
times. Therefore, there is a strong need for research on rationally
designed and efficient PTC catalysts, especially chiral ones, which
meet additional requirements related to the possibility of their reuse.
Herein, we report our own approach to enantioselective epoxidation
by introducing a readily available and finely tunable library of hybrid Cinchona alkaloid-based catalysts, the potential application
of which we have previously demonstrated in studies on alkylation
of imino glycine esters.[18]We began
the present study with epoxidation of model E-chalcone S1 using cinchonidine-based catalyst C1, leading
to product P1 with high yield (91%),
but low enantioselectivity (29% ee), as shown in Scheme . Next, we carried out catalyst
screening under the given conditions, and we found that compound C5 allows the desired epoxides to be obtained with high yield
(99%) and promising enantiomeric excess (71% ee). Also, reactions
with catalysts based on the other Cinchona alkaloids
give the desired products with excellent yield, but in racemic form.
Scheme 1
Scope of Hybrid Cinchona-Based Catalysts
The ee values were determined
by HPLC analysis using a chiral column Kromasil OD-H or Chiralcel
AD-H and OB-H.
Scope of Hybrid Cinchona-Based Catalysts
The ee values were determined
by HPLC analysis using a chiral column Kromasil OD-H or Chiralcel
AD-H and OB-H.Subsequently, we started to
optimize the reaction conditions using C5 as the catalyst,
and we noted that the ratio of hydrogen
peroxide and aqueous solution of NaOH strongly affected the enantioselectivity.
We postulate that the oxidant/base ratio affects the rate of hydrogen
peroxide decomposition and formation of the reactive HOO– ion. Moreover, instead of toluene we found that a mixture of Et2O/toluene (1:1) was the best solvent for most of these reactions.
Finally, we showed that epoxidation of chalcone S1 under
the newly found conditions was very efficient and proceeded for 1
h with an excellent enantiomeric excess (99% ee), using only 0.5 mol
% of catalyst at 5 °C temperature. Lower catalyst loading resulted
in decreased yield and ee value. All details of the optimization process
are presented in the Supporting Information (Tables S2–S6). Under such optimal conditions we examined the
reactivity and selectivity of α,β-unsaturated ketones S1–S21 as shown in Scheme .
Scheme 2
Asymmetric Epoxidation of α,β-Unsaturated
Ketones S1–S21 Using Catalyst C5
The ee values were determined
by HPLC analysis using a chiral column Kromasil OD-H or Chiralcel
AD and OB-H.
The ee values
were determined by HPLC analysis using a chiral column Kromasil OD-H
or Chiralcel AD and OB-H.
Reactions were carried out in toluene, and 1 mol % of C5 was used.
Asymmetric Epoxidation of α,β-Unsaturated
Ketones S1–S21 Using Catalyst C5
The ee values were determined
by HPLC analysis using a chiral column Kromasil OD-H or Chiralcel
AD and OB-H.The ee values
were determined by HPLC analysis using a chiral column Kromasil OD-H
or Chiralcel AD and OB-H.Reactions were carried out in toluene, and 1 mol % of C5 was used.All of the epoxides P1–P21 were
obtained from the corresponding substrates S1–S21 with both excellent yield and excellent enantioselectivity.
For substrates S1–S13, with various
electron-differentiating substituents on the carbonyl group side,
no significant changes in the extremely high selectivities (95–99%
ee) were observed. Due to lower solubility of epoxides P6, P10, and P12 in the diethyl ether, reactions
should be carried out longer (up to 48 h). Slightly lower enantiomeric
excesses were noted for epoxidation of E-chalcones
with an electron-differentiating substituents in the phenyl ring on
the double bond side S14–S17. In
those four cases, achievement of complete conversion required the
use of 1 mol % of the catalyst and the reactions were carried out
in toluene (P13–P16 marked green, Scheme ), but we noted very
high yields and ee values (92–99%, 90–96% ee). With
more challenging substrates S18–S21 we performed the epoxidation reactions with 3 mol % of the catalyst C5 and also in these cases we choose toluene as an optimal
solvent (P18–P21 marked purple, Scheme ). Epoxidation of S20 was conducted 72 h leading to product with moderate yield
71% and high enantiomeric excess 97% ee. It is worth mentioning the
great results obtained for (2E,4E)-1,5-diphenylpenta-2,4-dien-1-one S18 (95% yield, 96%
ee) and α,β-unsaturated ketone S21 containing
aliphatic substituent (98% yield, 99% ee). In addition, all epoxides,
except P20, can be isolated from organic layer using
simple filtration by silica gel pad. Such results indicate a fairly
universal character of the developed method, and to the best of our
knowledge it is a first example of successful epoxidation such substrates
using organocatalysts.The obtained results may indicate a competitive
π-stacking
effect originating from the phenyl system on the double bond side,
which may adversely affect the formation of the diastereomeric complex
with the catalyst C5. In order to explain such high selectivity,
we obtained monocrystals of C5 by slowly evaporation
of its saturated solution in wet acetone. Next, we performed a successful
single-crystal X-ray diffraction analysis of catalyst C5 (for details see the Supporting Information), which revealed its distinctive three-dimensional structure (Figure ).
Figure 1
X-ray structure of selected
molecule of catalyst C5. The solvent molecules, anions,
and nonacidic protons were omitted
for clarity, and thermal ellipsoids are drawn at the 50% probability
level.
X-ray structure of selected
molecule of catalyst C5. The solvent molecules, anions,
and nonacidic protons were omitted
for clarity, and thermal ellipsoids are drawn at the 50% probability
level.Let us consider one of the catalyst
molecules as it occurs in a
single crystal. The C5 molecule has an aromatic ring
stacked in the direction determined by the amide function. Importantly,
the arrangement of the phenyl group in the amide arm is nearly perpendicular,
this conformational information creating an attractive chiral reaction
cavity around the amide function. This strongly implies that the expected
hydrogen-bonding interaction would indeed bring an enone inside the
cavity to provide an ideal proximity to the hydrogen peroxide ion.
This hypothesis is supported by studies with N-methylated
catalyst C5 in which we obtained a racemic epoxide P1. Our proposed model of the transition state (Figure ) posits that the chalcone
substrate is stabilized by the hydrogen bond from the amide function
of a catalyst.
Figure 2
Proposed transition-state model for catalyst C5 with E-chalcone.
Proposed transition-state model for catalyst C5 with E-chalcone.A key element determining the high enantioselection of the reaction
is the phenyl ring from the amide arm which has a π–π
stacking interaction with the β-phenyl group of substrate. Such
interactions block one of the E-chalcone faces. Moreover,
the hydroxyl group of the catalyst forms an ionic pair with the hydrogen
peroxide ion (HOO–) via a hydrogen bond. Consequently,
the hydrogen peroxide can reach the β-carbon atom of an enone
exclusively from above to afford the αS,βR-product of epoxidation.The above results turned
our attention to the possibility of further
improving our reaction. After confirming the stability of catalyst C5 under PTC-epoxidation conditions, we decided to investigate
the possibility of its reuse. Scheme presents our concept of conducting 10 epoxidation
cycles under subsequent conditions. The chalcone S1,
in the presence of 1 mol % of catalyst C5, was used for
the first reaction cycle.
Scheme 3
Multigram Synthesis of Epoxide P1 Using Subsequent Epoxidation
Reactions
After completion of the reaction,
another portion of hydrogen peroxide
and aqueous NaOH, accompanied by chalcone S1 were added
(the second cycle). This procedure was repeated after each reaction
cycle in order to maintain full conversion of the reaction. Thus,
we were able to carry out epoxidation of chalcone S1 on
a 5 g scale, after 10 reaction cycles, and the product was obtained
in total with 97% yield and >99% ee. Note that during eight reaction
cycles, the model catalytic reaction did not lose any efficiency or
enantioselectivity; however, we terminated the experiment after the
tenth cycle due to the slightly lowering of the conversion (to 97%).
Given that the epoxidation reaction is very clean, after isolation
of the desired product P1, we were also able to recover
the catalyst C5 from a postreaction mixture with 99%
efficiency, simply by precipitating it with the addition of diethyl
ether. Given these advantages, the discussed procedure is an excellent
solution for epoxidation on a multigram scale, as only 0.1 mol % of
the catalyst was used, based on the final amount of the product obtained.
Note that when such catalyst loading under classical batch conditions
(without sequential addition of reagents) was used, the products were
obtained in the form of a racemate with low yield. Such high efficiency
of sequential addition of reagents is observed due to the continuous
presence of 1 mol % of catalyst in the reaction mixture, which does
not lose its activity over time or in the presence of the product.In summary, we have developed an efficient method for the preparation
of enantiomerically pure epoxyketones using hybrid amide-based Cinchona alkaloids as catalysts under PTC conditions. The
low loading (0.5 mol %) of highly effective catalysts allowed us to
obtain a wide range of such chiral epoxyketones with very high yields
and with excellent enantioselectivity (up to 99% and 99% ee, respectively).
To the best of our knowledge, these are unique results as compared
to those obtained with application of known catalysts, while maintaining
such low catalyst loading. Additionally, for the first time we presented
the possibility of reusing Cinchona derivatives in
the synthesis of optically pure epoxy ketones by follow-up epoxidation
cycles without adding a fresh portion of catalyst between subsequent
reactions. This approach could be highly valuable in the synthesis
of potential building blocks in the field of medicinal, agrochemical,
and material chemistry on a large scale. Further work on applying
our catalyst library to asymmetric epoxidation with other enones is
in progress.