# An Improved Protocol for the Aldehyde Olefination Reaction Using  (bmim) (NTf2) as Reaction Medium

Authors: Vivek Srivastava
Journal: Journal of Chemistry
 (2013)

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## Abstract

[Ru(COD)Cl2]/CuCl2·2H2O/LiCl catalytic system works efficiently in ionic liquid media for aldehyde olefination reaction. It offers good yield and selectivity with the added advantage of 5 times recyclability for [Ru(COD)Cl2] /CuCl2·2H2O/LiCl catalytic system. We also successfully reduced the reaction time from 12 hours to 9 hours for the aldehyde olefination reaction.


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## Body

## 1. Introduction

Carbonyl olefination reaction is one of the convenient and universal methods for the preparation of alkenes (C=C) [1, 2]. Although Wittig reaction [2–5] as well as its modified versions like Horner-Wadsworth-Emmons reaction [6–8], Kocienski-Julia reaction [8], and Peterson reaction [9–11] offers its effective and alternative method [6–14] to produce highly reactive carbanion these above-discussed reactions suffer from atom economy [15]. Transition-metal-catalyzed decarbonylation reaction of aldehydes is an attractive subject that has been studied for decades [1–14]. However, very limited research has focused on decarbonylative addition reactions. Recently [Ru(COD)Cl2]/CuCl2·2H2O/LiCl catalytic system was reported as an efficient combination for aldehyde olefinationvia decarbonylation addition pathway [15]. This catalytic system was found active for various substrates in terms of yield and selectivity but it suffers from long reaction time and recyclability of catalyst.Ionic liquids are well documented as solvent for different type of transition-metal-catalyzed organic transformations with the added advantage of catalyst recyclability [16–20]. Here, we are reporting first time ionic liquid mediated [Ru(COD)Cl2]/CuCl2·2H2O/LiCl catalytic system for aldehyde olefination reaction via decarbonylation addition pathway.


## 2. Experimental Procedure

All the chemicals were purchased from Sigma Aldrich and SD fine chemicals. All the solvents were dried according to the standard procedure and all the reactions were performed under argon in a sealed tube. The work-up and purification procedures were carried out with reagent-grade solvents. NMR spectra were recorded on standard Bruker 300 WB spectrometer with an advance console at 300 and 75 MHz for1H and 13C NMR, respectively.


### 2.1. Typical Experimental Procedure

The reaction tube was charged with [Ru(COD)Cl2] (0.01 mmol), CuCl2·2H2O (0.03 mmol), and LiCl (2 equivalent) along with p-anisaldehyde (0.2 mmol ) and 1-decyne (0.8 mmol) in ionic liquid (1 mmol) or dry toluene (1 mL). Further, the reaction tube was sealed under argon and the resulting reaction mixture was heated for 9 hours at 120°C. Later, the reaction mixture was allowed to cool up to room temperature. Isolation of corresponding reaction product was isolated according to the solvent system as described below.While using toluene as a solvent, the reaction mixture was first filter though silica plug with dicloromethane and then the organic solvent was evaporated in vacuo. The residue was further purified by column chromatography (Petroleum ether : Ether = 100 : 1) to recover pure reaction product.In case of Ionic liquidas a reaction medium, the reaction product was extracted with ether (5×2 mL) and the combined ether extract was evaporated in vacuo. Later the residue was further purified by column chromatography (Petroleum ether : Ether = 100 : 1) to isolate the pure reaction product.


## 2.1. Typical Experimental Procedure

The reaction tube was charged with [Ru(COD)Cl2] (0.01 mmol), CuCl2·2H2O (0.03 mmol), and LiCl (2 equivalent) along with p-anisaldehyde (0.2 mmol ) and 1-decyne (0.8 mmol) in ionic liquid (1 mmol) or dry toluene (1 mL). Further, the reaction tube was sealed under argon and the resulting reaction mixture was heated for 9 hours at 120°C. Later, the reaction mixture was allowed to cool up to room temperature. Isolation of corresponding reaction product was isolated according to the solvent system as described below.While using toluene as a solvent, the reaction mixture was first filter though silica plug with dicloromethane and then the organic solvent was evaporated in vacuo. The residue was further purified by column chromatography (Petroleum ether : Ether = 100 : 1) to recover pure reaction product.In case of Ionic liquidas a reaction medium, the reaction product was extracted with ether (5×2 mL) and the combined ether extract was evaporated in vacuo. Later the residue was further purified by column chromatography (Petroleum ether : Ether = 100 : 1) to isolate the pure reaction product.


## 3. Results and Discussion

We selected one model reaction betweenp-anisaldehyde and 1-decyne using [Ru(COD)Cl2]/CuCl2·2H2O/LiCl catalytic system with three different types of ionic liquid (1 mmol), that is, [bmim] [Cl], [bmim] [PF6], and [bmim] [NTf2]. Among these three ionic liquids, [bmim] [NTf2] mediated olefination of p-anisaldehyde offers a good yield (88%) and selectivity (E/Z 10 : 1) (Scheme 1, Table 1).Table 1
Aldehyde olefination reaction in different solvent systems.
Entry
Ionic liquid (1 mmol)
Yield (%)a
E/Zb
1
(bmim)(Cl)
70
3 : 1
2
(bmim)(PF6)
75
5 : 1
3
(bmim)(NTf2)
88
10 : 1
4
Toluene
73
6 : 1
aYield was calculated after column chromatography.
bAll E/Z ratios were calculated by 1HNMR.Scheme 1After getting delightful results with [bmim] [NTf2], we optimised the quantity of Ru (II) catalyst along with CuCl2 and LiCl. Only 0.01 mmol of Ru (II) catalyst with 0.03 mmol hydrated CuCl2 and 2 equivalents of LiCl  are found sufficient to offer the olefination reaction product 1 in terms of  yield (85%) and selectivity (E/Z ratio 10 : 1). While in toluene, the above optimised quantity of [Ru(COD)Cl2]/CuCl2·2H2O/LiCl catalytic system, that is, Ru (II) catalyst 0.01 mmol, 0.3 mmol of hydrated CuCl2, and 2 equivalent LiCl,  gives corresponding olefinated product 1 with lower yield (52%)  and  decreased selectivity (E/Z  ratio 2 : 1) (Figure 1).Figure 1
Olefination ofp-anisaldehyde in different solvent mediaLater, we screened  different aromatic aldehydes and alkynes using optimized proportion for [Ru(COD)Cl2]/CuCl2·2H2O/LiCl catalytic mixture with 1 mmol of [bmim] [NTf2], and we observed in our study that aromatic aldehydes with more electron-donating groups give a much better yield with respect to aromatic aldehydes carrying electron withdrawing group (Table 2). In most of the cases, we obtained more than 60% yield with acceptable E/Z ratio (Scheme 2, Table 2: Entry 1–7).Table 2
Decarbonylative addition reaction using different substrates.
Entry
Aldehydes (RCHO)
Isolated yield (%)a
E/Zb
1
70
6 : 1
2
85
10 : 1
3
65
5.5 : 1
4
75
4 : 1
5
70
7 : 1
6
60
4 : 1
7
95
5 : 1
aYield was calculated after column chromatography.
bAll E/Z ratios were calculated by 1HNMR.Scheme 2To make [Ru(COD)Cl2] catalytic system more cost-effective for olefination reaction, we extended our work towards recycling study of this catalytic system. In that context, after completion of the reaction, the product was extracted from the reaction mixture using ether washing.  The rest of the catalytic mixture along with ionic liquid was dried for 1 hour under high vacuum. Further, this used catalyst was recycled to the next batch of same olefination reaction. In the same way, we recycled  [Ru(COD)Cl2]/CuCl2·2H2O/LiCl catalytic system, 5 times and we obtained the corresponding olefinated product 1 with acceptable yield and selectivity (Scheme 3, Table 3).Table 3
Recyclability test forp-anisaldehyde olefination reaction.
Recyclability run
Isolated yield (%)a
(E/Z)b
1
85
10 : 1
2
80
8 : 1
3
78
7.5 : 1
4
71
6.5 : 1
5
72
6.5 : 1
aYield was calculated after column chromatography.
bAll E/Z ratios were calculated by 1HNMR.Scheme 3


## 4. Conclusion

In summary, we extended the application of ionic liquids as a reaction medium for transition-metal-catalysed olefination of aldehydes using decarbonylation pathway. We obtained not only good yield and selectivity for different types of aromatic aldehyde, but we also optimised successfully the quantity of [Ru(COD)Cl2]/CuCl2·2H2O/LiCl catalytic system. The most important thing is that we successfully reduced the reaction time from 16 hours to 9 hours and we also recycled the catalytic system (5 times) along with acceptable yield and selectivity in order to make them nearer to their industrial application.



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*Source: 439673-2012-11-05.xml*