Nian
Li
a,
Yunyun
Ning
a,
Xiaopeng
Wu
a,
Jin
Xie
*ab,
Weipeng
Li
*a and
Chengjian
Zhu
*ac
aState Key Laboratory of Coordination Chemistry, Jiangsu Key Laboratory of Advanced Organic Materials, Chemistry and Biomedicine Innovation Center (ChemBIC), School of Chemistry and Chemical Engineering, Nanjing University, Nanjing 210023, China. E-mail: xie@nju.edu.cn; lwp1989@nju.edu.cn; cjzhu@nju.edu.cn
bAdvanced Catalytic Engineering Research Center of the Ministry of Education, Hunan University, Changsha 410082, China
cState Key Laboratory of Organometallic Chemistry, Shanghai Institute of Organic Chemistry, Shanghai 200032, China
First published on 3rd March 2021
In this paper, we report a mild and practical method for precise deuteration of aliphatic carboxylic acids by synergistic photoredox and HAT catalysis. The reaction delivers excellent D-incorporation (up to 99%) at predicted sites even in substrates bearing reactive C–H bonds or versatile functional groups. The use of a recirculation reactor with a peristaltic pump supports a scalable preparative ability (up to 50 mmol) under very mild reaction conditions. The practical and precise deuteration of readily available complex carboxylic acids makes this protocol promising for the preparation of deuterium-labelled compounds.
Fig. 1 Classical deuteration strategies and decarboxylative deuteration approaches. (a) Classical ionic strategies. (b) Pioneering works. (c) This work. |
Carboxylic acids are common commercially available feedstocks.6 Decarboxylative strategies enable carboxylic acids to serve as traceless linkers with which to construct C–C and C–X bonds (X = F, Cl, N3).7 In view of the diverse skeletons of carboxylic acids, this type of reaction could significantly enhance the development of a useful library of deuterated organic molecules. In contrast with well-developed radical dehalogenative deuteration of organic halides,8 decarboxylative deuteration represents an elegant access to deuterated molecules from commercially available starting materials. For example, in 2004, Oshima et al.9a reported Pd-catalyzed decarboxylative deuteration of aliphatic carboxylic acids at 250 °C and 5 MPa. In 2010, Hatanaka et al.10 employed a 400 W high-pressure mercury lamp and a stoichiometric photosensitizer for the deuteration of alkyl carboxylic acids. Later, Gooßen et al.9b disclosed Cu or Ag-catalyzed decarboxylative deuteration of (hetero)aromatic carboxylic acids at elevated temperatures. Recently, deuteration of oxime carboxylate was developed by Glorius and coworkers.11
Despite these great efforts, the development of a scalable, practical and site-specific decarboxylative deuteration strategy is still highly desired. Pursuant to our previous work on synergistic catalysis,12 we designed a new strategy to achieve precise deuteration with D2O of a wide array of readily available acids via synergistic thiol and photoredox catalysis (Fig. 1c), efficiently affording structurally diverse deuterated molecules with up to 99% deuterium incorporation. We have explored the practicality of the method via recirculation reactors, developing a protocol which is easily scalable (up to 50 mmol) in laboratories.
As shown in Fig. 2b, the alkyl carboxylic acid (1a) does not have an oxidation potential in the range of 0–2 V, but a significant peak at 0.74 V vs. SCE (the oxidation potential of a carboxylate) is seen when a stoichiometric inorganic base, especially CsOH is added. It was presumed that the use of CsOH could benefit the formation of cesium carboxylate, which can undergo single electron oxidation and be decarboxylated. Radical trapping experiments with 2,2,6,6-tetramethylpiperidinooxy (TEMPO) and EPR results showed that the radical pathway was highly likely, consistent with the proposed mechanism shown in Fig. 2a.
Initially, we selected cesium 4-(4-methoxyphenyl)butanoate (1a-Cs) as a model substrate, and it is readily available from the corresponding carboxylic acid in almost quantitative yield (Table 1). The optimized conditions include the use of 1 mol% [Ir(dF(CF3)ppy)2(dtbbpy)]PF6 [PC-III, 1/2Ered(*IrIII/IrII) = +1.21 V vs. SCE]17 as the photocatalyst, thiol (2a) as the HAT catalyst, DCM/D2O as the mixed solvent and irradiation of blue LEDs at ambient temperature (entry 1). The reaction delivered the desired 1-methoxy-4-(propyl-3-d)benzene (3a) in 75% yield and with up to 96% deuterium incorporation. The substrate cesium 4-(4-methoxyphenyl)butanoate (1a) has a weak benzylic C–H site, but the site remained intact during the decarboxylative deuteration. To our knowledge, C–H sites of this type are challenging in H/D exchange strategies.5c If sodium or potassium salts were used instead of cesium carboxylate, it was found that the D-incorporation was notably decreased (entries 2 and 3). However, the formation of the corresponding cesium carboxylate in situ from a carboxylic acid and CsOH gives a moderate yield and D-incorporation (entry 3). The use of other photocatalysts such as PC-I or PC-II and thiols (2b–2c) reduces the reaction efficiency (entries 5–9). Control experiments suggest that the photocatalyst, thiol HAT catalyst and light irradiation are key factors contributing to the success of the reaction (entries 10 and 11). On the other hand, we found that aliphatic acids such as 2-(4-(benzyloxy)phenyl)acetic acid (1b), which are stabilized by heteroatomic or aryl substitution, can directly react under modified optimized conditions when using Mes-Acr-Me (PC-I) as shown in Fig. 3 (see the ESI† for optimization details). This can precede the precise decarboxylative deuteration and afford the desired product (3b) in 97% yield and 95% D-incorporation. We envisioned that the strong oxidative ability of photoexcited *Mes-Acr-Me [1/2Ered(*PC/PC˙−) = +2.08 V vs. SCE]18 would facilitate the SET oxidation of carboxylic acid in the presence of an organic base. Interestingly, we found that the initial reaction rate of this decarboxylative deuteration was heavily light-dependent since a dramatically decreased rate was observed when only one LED lamp was used rather than two lamps (see the ESI† for details). This encouraged us to use a recirculation reactor to address the efficiency of the reaction.
Entry | Variation of standard conditions | Yieldb | D-Inc.c |
---|---|---|---|
a 1a-Cs (0.2 mmol), PC-III (1 mol%), 2a (10 mol%), DCM/D2O (4:1, v/v; 2 mL, 110 eq. of D2O), 45 W blue LEDs, room temperature, 18 h. b Measured by GC using acetophenone as the internal standard due to the high volatility. c Deuterium incorporation was determined by HRMS-ESI. d Sodium 4-(4-methoxyphenyl)butanoate. e Potassium 4-(4-methoxyphenyl)butanoate. f CsOH (2.0 equiv.) as the base. DCM = dichloromethane, N.D. = not detected. | |||
1 | None | 75% | 96% |
2 | With 1a-Nad | 75% | 77% |
3 | With 1a-Ke | 75% | 83% |
4 | 4-(4-Methoxyphenyl)butanoic acid and CsOHf | 57% | 60% |
5 | PC-I instead of PC-III | 4% | — |
6 | PC-II instead of PC-III | 3% | — |
7 | 2b instead of 2a | Trace | — |
8 | 2c instead of 2a | 23% | 96% |
9 | 2d instead of 2a | 14% | 96% |
10 | Without PC-III or light | N.D. | — |
11 | Without 2a | 5% | — |
With the optimized decarboxylative deuteration conditions in hand, we investigated the scope of the aliphatic carboxylic acids. As shown in Fig. 4, a wide variety of primary, secondary and tertiary carboxylic acid derivatives can smoothly undergo the decarboxylative deuteration, affording the products (3c–3s) in moderate to good yields with excellent (up to 99%) D-incorporation. The benzylic and α-heteroatom carboxylic acids (3c–3e, 3g–3k, 3n, 3q and 3r) can be directly employed under optimized reaction conditions A with Mes-Acr-Me (PC-I) as the photocatalyst. The reactive benzylic and α-amino C–H bonds, for which H/D exchange under photocatalysis has been reported,2a were not structurally affected by the reaction. The unactivated cesium carboxylates were employed under optimized conditions B, affording the desired products (3f, 3l, 3m, 3o, 3p and 3s) in satisfactory yields and with good D-incorporation. As shown in Fig. 4, the decarboxylative deuteration protocol has good functional group compatibility. Several relatively sensitive but versatile functional groups, such as a weak benzylic C–H bond (3c, 3d, 3l–3n and 3q), an α-amino C–H bond (3d, 3l–3n, 3q and 3u), heteroaryl (3j and 3k), boronic ester (3e), ketone (3o) or strained small rings (3r), survived the conditions well, which suggests promising applications in synthetic and medicinal chemistry. The synthetic robustness of the reaction was further illustrated by the decarboxylative deuteration of complex carboxylic acids such as erdosteine (3u), ambrisentan (3y), gemfibrozil (3aa) and oleanic acid (3cc). The resulting deuterated products (3t–3ee) are difficult to prepare from other available starting materials, such as organic halides which are usually prepared from acids by reduction and subsequent halogenation under harsh conditions. However, aromatic acids are unsuccessful examples in this decarboxylative protocol possibly because the radical decarboxylation of aromatic substrates is a kinetically less favoured pathway.11
Although several important radical deuteration syntheses of various compounds have been established, a scalable and practical strategy remains a problem.8 Flow chemistry has significant advantages in terms of scalability, safety and productivity, and has been recently applied in photocatalyzed organic transformations.19 In general, the mesoscale two-phase photoreaction could be improved through the use of a flow reactor setup, allowing for a larger illumination area and liquid–liquid interfacial area. Consequently, we sought to develop scalable decarboxylative deuteration in flow reactors. However, we immediately found that the use of a continuous-flow micro-tubing reactor employing a syringe pump to deliver the reaction liquid decreased the D-incorporation ratio of products, such as 3b, to less than 40%. Inspired by the well-established continuous-flow technology, we designed a batch recirculation reactor with a peristaltic pump to transfer the reaction mixture (the detailed setup is shown in the ESI†); the enhanced mixing effect and mass transfer between two phases of our equipment improved the interfacial area20 of DCM and D2O, and this increased the D-incorporation ratio of 3b from 37% to 95% (see the ESI† for details).
As shown in Fig. 5, the decarboxylative deuteration assisted by our recirculation arrangement could be scaled up with 5.0 mmol of carboxylic acid. A wide range of aliphatic carboxylic acids are effective substrates, affording the desired products (3ff–3uu) in acceptable yields without decreasing the D-incorporation or the chemoselectivity. Furthermore, although the cesium carboxylate is not soluble well in recirculation reactors, it can also furnish the decarboxylation product (3hh) in 71% yield and 97% D-incorporation upon addition of 18-crown-6 as an additive with 0.5 mol% photocatalyst. The use of recirculation reactors can allow for 50.0 mmol scale-up ability to produce 3b (8.6 g) and 3vv (13.0 g) without compromising the reaction efficiency and D-incorporation (>95%). With this protocol, we were able to easily prepare 18 kinds of different deuterated compounds on a 2–50 mmol scale from readily available starting materials under mild reaction conditions.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/d1sc00528f |
This journal is © The Royal Society of Chemistry 2021 |