1. Introduction
Alkenes belong to a chemical functional group that is omnipresent in literally all natural products. Interestingly, since the early times when organic synthesis slowly became a ‘useful’ scientific discipline, many synthetic strategies have focused on the stereoselective synthesis of these structural motives. Especially, methods that allow for the connective stereoselective introduction of the olefin moiety have become very valuable tools for this achievement. Over the past 100 years, many different connective olefination methods have been developed, but many of them follow the same retrosynthetic pathway [
1] - they are based on the reunion of α-negative charge stabilizing reagents
1 with aldehydes or ketones
2 (
Table 1).
Since the introduction of the Wittig reaction[
7,
8] in the late 1950s of the twentieth century, Wittig,[
3] Horner-Wadsworth-Emmons,[
4] Johnson,[
2] Peterson,[
5] and Julia olefination[
1] established themselves as the most widely used olefination protocols. Each of these methods has, of course, its advantages and drawbacks that change over time because each of the methods went through a long and interesting development since its original disclosure. In this review, we wish to focus on the so-called modified Julia reaction,[
1,
9,
10,
11,
12,
13,
14,
15,
16] also known as the Julia one-pot, Silvestre-Julia, or Julia-Kocienski olefination, and its development in terms of the reaction mechanism and selectivity.
2. Origins and Mechanism of the Julia-Kocienski Olefination Reaction
2.1. Julia-Lythgoe Olefination vs. Julia-Kocienski Olefination: A Comparison
Classical Julia olefination, also known as Julia-Lythgoe olefination, was described for the first time in 1973 by (Mark) Julia and Paris[
17] and was later developed by Kocienski and Lythgoe[
18]. The original protocol was soon expanded for the beneficial
O-derivatization step and thus consisted of four distinct stages carried out commonly in the two-pot protocol (
Scheme 1): (1) metalation of an alkylarylsulfone
4, (2) addition of the resulting carbanion species
5 to an aldehyde or ketone
6, (3)
O-acylation (sulfonylation) of the adduct
7, and (4) reductive-elimination of the β-acyl (sulfonyl) oxysulfone
8 intermediate. The addition of
5 to
6 typically yields product
7 as a mixture of all possible diastereoisomers; however, this is not of consequence because the stereochemical information encoded in
7 (or
8) is lost during the reductive elimination step. A common feature of Julia-Lythgoe olefination is its high (
E)-stereoselectivity[
1] – a consequence of the various radical mechanisms that operate in the final stage of reductive elimination[
19].
The main drawbacks of Julia-Lythgoe olefination, namely the steric requirement-driven (
E/Z)-selectivity, and the two-pot protocol, were in 1993 overcome by Silvestre Julia[
20,
21] (brother of Mark Julia). Their modification of the standard Julia-Lythgoe olefination protocol was based on the replacement of the phenylsulfonyl group with the benzo[
d]thiazol-2-ylsulfonyl (BT) group (
Scheme 2). The common feature of the new transformation with Julia-Lythgoe olefination are the first two steps: (1) metalation and (2) addition of metalated sulfone
11 to aldehyde
12. Since in this case the aryl group in the alkyl aryl sulfone is an electron-acceptor, the initially generated
β-alkoxy sulfone adduct
13 can undergo to spontaneous Smiles rearrangement (S to O migration of the heteroaryl group) to yield adduct
15. Subsequent
β-elimination of SO
2 (
18) and of an aryloxide anion (
17) in
15 directly forms olefin
16.
As mentioned above, Silvestre Julia introduced the BT-group as the only electron-acceptor aryl group suitable for the Julia-Kocienski olefination reaction. But this situation did not last long, and many other research groups introduced several different heteroaryl groups such as pyridine-2-yl (
PYR),[
20,
22] 1-phenyl-1H-tetrazole-5-yl (
PT),[
23] 1-tert-butyl-1H-tetrazole-5-yl (
TBT),[
24] and 3,5-bis(trifluoromethyl)phenyl (
BTFP)[
25] and others[
20,
26]. Interestingly, only the
PT group introduced by Kocienski
et al.[
13,
24] possessed sufficiently interesting properties (diminished side reactions such as homocoupling[
13], high (
E)-selectivity) that remained along with the original BT group as the most widely used heteroaryl acceptor groups explored in olefination reactions.
The generalized scopes and limitations and the achieved (
E/Z) selectivities observed for Julia-Lythgoe and Julia-Kocienski olefination are summarized in
Table 2.
.
2.2. Reaction Mechanism and Its Impact on the Selectivity of Julia-Kocienski Olefination
The Julia-Kocienski reaction mechanism was intensively studied by Silvestre Julia[
20,
21] and the study was further extended by P. Kocienski and R. Blackmore.[
11,
12,
13,
24] Based on these excellent mechanistical works, the reaction mechanism could be established with respect to the stereochemical outcomes of the reaction (
Scheme 3). There are three important features of this mechanism that deserve a brief comment.
- (1)
The addition step of metalated sulfone
11 to aldehyde
12 can provide
anti-adduct
anti-
19 via
TS1 or
syn-adduct
syn-
19 via
TS2 (
Figure 2). The selectivity in this step is extremely important since all subsequent transformations of intermediate
19, Smiles rearrangement and
β-elimination, are stereospecific. Thus, the
syn/anti-selectivity of the addition step determines the final (
E/Z)-olefin ratio. Therefore, in theory, the (
E/Z)-selectivity of the reaction could be swapped from (
E) to (
Z) if proper reaction conditions are applied.
- (2)
When stabilized metalated sulfonyl anions
11 (R
1 = Ph, alkenyl, etc.) are used, the addition step of
11 to
12 becomes reversible (
Scheme 3, path A). In this case, the original kinetically driven
syn/anti-ratio of adduct
19 becomes less important in comparison with the Smiles rearrangement reaction rates (transformation of
19 to
22). In such cases, the rearrangement of
anti-
19 adduct leading to (
E)-olefin
16 is slower compared to the rearrangement of
syn-
19 to olefin (
Z)-
16 due to repulsive 1,2-interactions in the transition state (see
cis-
20).
- (3)
For the elimination step, two borderline mechanisms are generally accepted. In the first, which is the most common, the rearranged intermediate 22 undergoes β-elimination. The elimination is stereospecific, and the syn-19 adduct rearranged intermediate syn-22 furnishes (Z)-olefin and the anti-19 adduct rearranged intermediate, compound trans-22 (trans refers to the arrangement of R1 and R2 within the intermediate cycle), yields (E)-olefin. Alternatively, when (hetero)aryl aldehydes 12 (R2 = (hetero)aryl) an alternative elimination pathway (path B) was postulated to occur. In this case, the elimination pathway should proceed through the formation of intermediate carbocation 23. The steric requirements of R1 and R2 then play a crucial role in the final (E/Z)-selectivity of the reaction. Path B was used to explain the unexpected (E)-selectivity of the coupling reactions carried out using (hetero)aryl aldehydes 12 as substrates.
Recently, our group, in collaboration with Robiette’s group, proposed an alternative explanation for the observed (
E) selectivity of these reactions. Our explanation is based on a combined experimental and theoretical study that revealed that the key role in the elimination step plays the rearrangement product
22a (
Scheme 4).[
14] In general, both the
anti and
syn intermediates
22a, can adopt the
cisoid and
transoid conformation. Conformational equilibrium is strongly influenced by the steric requirements of the R
1 and Ar groups, and in the case of the
anti-
22a intermediate, the
transoid is preferred, while in the case of
syn-22a, the
cisoid is preferred. Advanced experimental and theoretical study then suggested that in the case of a
cisoid conformation, competitive
syn elimination can occur,[
14] explaining almost exclusive formation of (
E)-olefins observed in the case of olefins of general structure
16a.
Theoretical studies also suggested that the
syn elimination process should be more favored when the aryl substituent R
2 has electron-donating substituents and disfavored when an electron-deficient substituent is present. The postulated prediction was then evaluated using a stereodefined intermediate
24 that was selectively transformed in situ to the corresponding lithiated anion
25 that was allowed to undergo an elimination process. The generated anion cannot undergo the retroaddition process (it is an intermediate after the rearrangement step) and the nucleophile generated in situ (thiolate anion) is not basic enough to trigger the epimerization process of any of the two epimerizable stereogenic centers. Thus, only (
Z) olefin (
Z)-
26 should be produced as the main product of the transformation. If the reaction should proceed through the carbocation-type intermediate of the
23 type (see
Scheme 3), an approximately 50:50 ratio of the (
E/Z)-isomeric mixture was expected. In all tested cases, the (
E)-isomer (
E)-
26, the product of the
synperiplanar elimination process was produced as the main product of the reaction, strongly suggesting that the
syn elimination process is the main process that operates during the Julia-Kocienski olefination reaction of alkyl sulfones with aryl aldehydes. The observed stronger preference for electron-donating group containing intermediates to undergo preferentially
synperiplanar elimination was also in agreement with the DFT calculation-based prediction.
Scheme 5.
2.3. Recent Achievements in the Reaction Selectivity Improvements
Reaction mechanism studies carried out by S. Julia and P. Kocienski, which were later confirmed by our own studies, implies that the reaction selectivity is directly linked with the initial syn/anti-selectivity of the addition step. The adduct ration further directly influences the selectivity (E/Z) of the overall reaction regardless of whether the reaction proceeds through the antiperiplanar elimination (for R1 and R2 = alkyl), or mixed antiperiplanar and synperiplanar (for R1 and/or R2 = (hetero)aryl) elimination in the final step. Not surprisingly, then, most of the methods developed to influence the reaction selectivity in favor of one of the two isomers focus on the key addition step.
2.3.1. Solvent Effect
The most important and most straightforward way to influence the
syn/anti-selectivity of the addition step is to choose the right solvent for the transformation. When polar solvents such as THF, DME, or DMF are used,
anti-adduct
anti-
19 is the preferred product of the addition due to solvent stabilization (
Scheme 6A). On the contrary, when nonpolar solvents such as toluene are used, the reaction proceeds via a
closed transition state (
Scheme 6B) and
syn adduct
syn-
19 is preferred.
It should be noted that, even though such an approach is generally applicable and correct, the role of the solvent might be altered by several factors that cannot be removed from the reaction mixture and which will be discussed in the following two sub-sections.
The metal cation, which is always present in the reaction mixture as a ‘residue’ after the deprotonation step, has a key influence on the selectivity of the reaction. In general, cations with the character of a hard Lewis acid such as, e.g., Li
+ favor the formation of the (
E) olefins. It is assumed that the observed (
E) selectivity is caused by a better stabilization of the generated anion
11 that can further add due to its lower reactivity to the aldehyde
12 with a better selectivity that favors the
anti-adduct
anti-
19. On the contrary, when a large cation is used, such as K
+, the reaction can proceed preferentially either via
closed TS or the solvent can increase the dissociation of the cation from the anion
11 and thus increase the reactivity of it. The first case is typical for nonpolar solvents (e.g., toluene), since the solvent does not provide additional stabilization to the reagents and/or reaction intermediates. In the latter case, dissociation of the cation from reagent
11 increases the reactivity of the anion and leads to the faster production of the kinetic product of the addition step,
anti-isomer
anti-
19. However, it should also be noted that an increase in anion
11 reactivity can also inevitably lead to the undesired self-dimerization of reagent
11 (
Scheme 7); thus, a compromise between selectivity and reactivity has to be searched.
The addition of the co-solvents to the reaction mixture can also be beneficial when (E)-selectivity is searched. It was observed that the addition of co-solvents such as DMPU or HMPA to the reaction mixtures carried out in the THF or DMF leads to an increase in the (E)-olefin selectivity of the desired product. It is believed that the co-solvent role is in metal cation scavenging with an impact similar to that described in the previous section (increased reactivity that favors the anti-adduct formation).
2.3.2. Additives
Another way to increase the (E/Z) selectivity of the Julia-Kocienski reaction is the addition of additives to the reaction mixture. Over the years, many various additives have been used for such purposes; however, only a few of them have had a significant effect. The relevant ones are listed below.
As mentioned in the previous section, the role of (co-)solvent was shown to have a tremendous effect on the reaction yield and selectivity. As a
modus operandi, it was postulated that polar solvents increase the reactivity of anion
11 due to a cation/anion separation (reaction kinetic) that leads to the preferential formation of
anti-adduct (polar solvents) or
syn-adduct (nonpolar solvents). As a disadvantage, self-condensation of metalated sulfone
11 (
Scheme 7) was observed. The use of specific cation-chelating co-solvents such as HMPA or DMPU met only with limited success even though in several cases it led to the diminished formation of self-condensation products and an increase in the (
E) selectivity.
Based on the same logic, to increase the reactivity of metalated sulfone
11 and thus increase
anti-adduct formation (kinetic product), an excess of crown ethers (18-crown-6 for K
+; 12-crown-6 for Li
+)[
27] can be used during the reaction as demonstrated in several recent total syntheses of natural products (
e.g., zeaenol,[
28] paecilomycins E and F,[
29] amphidinolide E,[
30] and salarins A and C[
31]).
However, it should be noted that if metalated sulfone
11 is used with a group in the lateral chain (R
1) that is capable of stabilizing the generated anion, the addition of generated anion
11 to aldehyde
12 is reversible. Consequently, the
syn/anti-ratio of adducts
19 is in equilibrium and (
Z)-olefin (
Z)-
16 is formed preferentially due to a faster (
kanti <
ksyn) Smiles rearrangement step.[
32]
Scheme 8.
The use of ammonium salts proved to be also beneficial and in several cases of highly complex molecular scaffolds led to an increase in the observed reaction yield and (
E)-selectivity.[
33,
34] It is believed that the role of ammonium salts is in the activation of aldehyde
12, where, due to its steric requirements, increases the
anti-selectivity of the addition step. It should also be noted that the role of counter anion of the ammonium salt is not innocent. The best (
E) selectivity was observed when potassium-containing metalated sulfone
11 was reacted in the presence of TBAB (
tetra-butylammonium bromide) and lithium-containing metalated sulfone
11 was reacted in the presence of TBAC (
tetra-butylammonium chloride). Such observations suggest the beneficial formation of KBr and LiCl salts during the reaction.
Similarly, metal cations as e.g., CeCl
3,[
35,
36] MgCl
2,[
37] ZnCl
2, and LiBr, can be used to activate aldehyde
12 during the reaction. The addition of such salt generally results in an increase in the reaction yield of the transformation. The (
E/
Z) selectivity of the transformation is influenced only if aldehydes bearing
α-alkoxy substituents[
37] are used in the presence of an excess of MgCl
2 or ZnCl
2 (addition via the Cram-chelate transition state).[
38]
3. Julia-Kocienski Olefination – Extension to Carboxylic Acid Derivatives
All the above-mentioned olefination methods are based on the reunion of the metalated sulfone
11-type intermediate and a carbonyl-containing intermediate
12 (
Scheme 2). The overall transformation can thus be regarded as an addition/rearrangement/elimination sequence, where the final (
E/Z)-selectivity of the newly olefinic bond is determined by the addition step. Therefore, the stereoselectivity is dictated by the reaction kinetic of the addition step (kinetic conditions) or by the kinetic of the rearrangement step (the addition step is in equilibrium) (
Scheme 3).
However, recently this paradigm changed since we have introduced ‘reaction work-up driven selectivity’ for the Julia-Kocienski reaction.[
39] In analogy to the famous Peterson olefination reaction,[
5] we have designed and optimized the new Julia-Kocienski protocol that allows the selective (
E) or (
Z) olefin formation by a simple change in the reaction work-up procdure. Our protocol is based on the seminal work of Jørgensen et al.[
40,
41] that demonstrated that
β-keto BT sulfones
33 can be successfully transformed into the corresponding olefins
34 in high yields and (
E)-stereoselectivity.
Scheme 9.
On the basis of these results, we have designed a novel type of the Julia-Kocienski reaction that allows the synthesis of the desired olefins
16 starting from the metalated sulfone
11 and acyl halides
35 (
Scheme 10). In this sequence, the reunion of the two reagents (compounds
11 and
35) is carried out using previously described protocol.[
42,
43] The generated adduct
36 is then quenched in situ with the external source of the proton (protic solvent, e.g., MeOH) and
β-keto sulfone
36 is formed. Compound
36 is present in the reaction mixture as a dynamic mixture of its keto and enol derivatives. Compound
36 is present in the reaction mixture as a dynamic mixture of its keto and enol derivatives. When an external mild reducing agent (e.g., NaBH
4) is added, the keto-form of
keto-36 is selectively reduced, and the nucleophilic hydride approach is directed according to the Felkin-Ahn model[
44] (
Scheme 11). Carbonyl reduction preferentially generates a
syn derivative of β-hydroxy sulfone
syn-
19, and compound
syn-
19 is further converted via the Smiles rearrangement/
β-elimination sequence of the Julia-Kocienski olefination reaction to olefin (
Z)-
16. However, if chelating salts such as ZnCl
2 are added to the reaction mixture prior to NaBH
4, the reduction proceeds through the Cram-chelate model and the
anti-
β-hydroxy sulfone
anti-
19 is formed. Consequently, compound
anti-
19 furnishes after the Smiles rearrangement/
β-elimination sequence (
E)-olefin (
E)-
16.
Although only preliminary scope and limitations of the transformation were established (28 examples), the method was successfully applied in the context of the (nitro)fatty acid synthesis.[
39]
4. Conclusions
Since its first dissemination in 1993 the reaction sequence that is now referred to as the Julia-Kocienski reaction has become very popular late-stage connective method in natural product synthesis, because it combines highly efficient (reaction yield) and selective (predominantly (E)-selective) connective method that proceeds in one-pot protocol and under mild reaction conditions and with broad substrate and functional group tolerance. The past 30 years of reaction development have also identified key mechanistic properties that allow better control of reaction selectivity. Moreover, we have recently introduced a novel modification of the Julia-Kocienski reaction that not only increases the starting material scope since it allows for the use of previously inaccessible carboxylic acid derivatives as substrates but also allows for the selective (E) or (Z)-olefin formation. In addition, this method allows for the first time in the development of the Julia-Kocienski olefination reaction an independent formation of (E) or (Z) olefins starting from the same starting materials by simple reaction work-up protocol alternation.
Author Contributions
Conceptualization and methodology, C.D. and J.P.; writing: preparation, review and editing of the original draft, C.D. and J.P. All authors have read and agreed to the published version of the manuscript.
Funding
This research was funded by the Internal Grant agency of Palacky University, grant number IGA_PrF_2024_007 and IGA_PrF_2024_028.
Conflicts of Interest
The authors declare no conflicts of interest.
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