Dewal S.
Deshmukh
a,
Sanjay
Singh
b,
Kirtikumar C.
Badgujar
c,
Vivek T.
Humne
d,
Gajanan V.
Korpe
*e and
Bhalchandra M.
Bhanage
*f
aDepartment of Chemistry, J. D. Patil Sangludkar Mahavidyalaya, Daryapur, Maharashtra 444803, India
bPandit Deendayal Energy University-PDEU (Formerly PDPU), Knowledge Corridor, Raisan Village, PDPU Rd, Gandhinagar, Raysan, Gujarat 382007, India
cDepartment of Chemistry, SIES College of Arts, Science & Commerce, Mumbai, 400022, India
dDepartment of Chemistry, Shri R. R. Lahoti Science College, Morshi, Maharashtra 444905, India
eDepartment of Chemistry, Shri Shivaji Science College, Amravati, Maharashtra 444603, India. E-mail: korpegv@gmail.com
fDepartment of Chemistry, Institute of Chemical Technology, Mumbai, 400019, India. E-mail: bm.bhanage@ictmumbai.edu.in
First published on 17th April 2025
C–H bond functionalisation is a pivotal approach in contemporary fabrication of organic compounds, and enables straightforward transformation of inert C–H bonds exempt from needing pre-functionalisation. Homogeneous recyclable catalytic systems upsurge sustainability by empowering catalyst recovery and reuse. This review combines the advantages of both these protocols by exploring a range of recyclable catalytic systems for functionalisation of C–H bonds, concentrating on green and sustainable approaches. We delve into the utilisation of various media and catalytic systems, including polyethylene glycols (PEG), ionic liquids (ILs), deep eutectic solvents (DESs), micellar systems, biphasic systems and systems allowing simple filtration or extraction to enhance catalytic efficiency and recyclability. The discussion encompasses a variety of metal-based catalysts, including rhodium (Rh), ruthenium (Ru), palladium (Pd), copper (Cu) and cobalt (Co), as well as catalyst-free approaches. The recyclability potential of most of these catalytic systems has also been explored. The atom economy and environmental advantages of employing these recyclable systems are highlighted in this review by giving an extensive overview of these innovative methods. Also, this seeks to motivate further exploration in the realm of functionalisation of C–H bonds and foster the progress of sustainable and environmentally conscious synthetic methods.
Green foundation1. This review discusses advances in green chemistry through homogeneous recyclable catalytic systems for C–H bond functionalisation, including the use of sustainable media. It highlights efficient recovery and reuse of metal catalysts as well as metal-free methods promoting sustainable organic synthesis.2. The study addresses a critical aspect of modern organic synthesis, C–H bond functionalisation, while emphasising on green and sustainable methodologies. By highlighting homogeneous recyclable catalytic systems that combine the benefits of both homogeneous and heterogeneous catalysis, this review aligns with green chemistry principles by incorporating environmentally friendly media, recyclability, waste minimisation, and atom economy, advancing the field. 3. Although notable homogeneous recyclable catalytic systems for C–H functionalisation have been developed, further work is needed to improve efficiency, scalability, substrate versatility, and the scope for other transition metals. Optimisation for industrial applications, cost-effectiveness, and reduced energy consumption with enhanced catalyst reuse remains a key focus. |
In this regard, C–H activation represents a groundbreaking tactic in the development of organic compounds, allowing straightforward transformation of inactive C–H bonds that do not require pre-functionalisation of substrates (Fig. 1).1–9 Unlike traditional approaches, activation of C–H bonds avoids preliminary functionalisation (for instance, halogenation or borylation) of the target molecules that reduces the number of steps. Ideally, multiple step synthesis could thus be modified into single-step synthesis allowing a straightforward approach to projected frameworks, thus decreasing the quantity of undesirable refuse of multistep transformations. This stands out as a greener and more sustainable tactic in chemical synthesis owing to its inherent alignment with the principles of green chemistry.8 This method significantly improves atom economy and step economy, diminishing the need for pre-functionalised starting materials and their associated waste streams.2,4,8 This decrease in synthetic steps and the avoidance of stoichiometric byproducts directly address the principle of waste prevention.2,8 The current development of catalytic systems based on Earth-abundant metals and the investigation of milder reaction conditions, along with the use of greener solvents, actively endorse the principles of catalysis, energy efficiency design, safer solvents and accident prevention. Practically, the evolution of C–H activation methodologies towards more selective, efficient, and environmentally benign procedures represents a commitment to the core tenets of green chemistry, paving the way for more sustainable chemical transformations.
Transition metal catalysis plays a vital role by enabling precise regioselectivity and reactivity.10–20 This practice has become pivotal for assembling complex molecules in pharmaceuticals, agrochemicals, and advanced materials.21–28 Homogeneous catalytic systems are employed in the majority of these reactions.
Homogeneous catalytic systems offer numerous compensations, with meticulous regulation of reaction parameters, resulting in higher selectivity and yield. They facilitate molecular-level tunability, and often operate under milder conditions. Moreover, they allow better interaction with substrates, attaining transformations not possible with heterogeneous systems.29–32 On account of its remarkable activity and selectivity, homogeneous catalytic systems have several industrial applications and can be significantly more efficient than their corresponding heterogeneous counterparts.33 Conversely, heterogeneous catalysis shows reduced reactivity and selectivity, mainly due to the restricted accessibility of active sites. These confines are associated with steric hindrances imposed by support matrices and mass transport constraints, as active sites are often deeply embedded within these structures, impeding reactant access.34
Although homogeneous catalysis outperforms in reactivity and selectivity, it often faces limitations in catalyst recovery and recycling. In order to get over this, researchers have developed heterogeneous catalytic systems, providing efficient and reusable replacements for chemical transformations including C–H bond functionalisation.35–37 Nonetheless, a significant impediment in the employment of heterogeneous catalytic setups is the potential catalyst percolation into the reaction medium, which consequently limits its applicability. Furthermore, homogeneous catalysts exhibit additional advantages, including markedly elevated turnover number and turnover frequency.
The recyclability constraint in homogeneous catalysis considerably impedes its large-scale application, making it pivotal to enhance the reuse of these catalytic systems. Enhanced recyclability can lower costs and minimize waste, thus encouraging the sustainable production of fine chemicals. Consequently, alternatives that not only enhance catalyst recycling but also maintain its competitiveness with traditional homogeneous and heterogeneous methods are urgently required. Extensive study is underway to advance strategies that integrate the beneficial properties of both catalyst types. The prime aim is to formulate a catalyst that exhibits a high degree of reactivity, complete product selectivity, stability under specific reaction conditions, and the capacity for recyclability. Accomplishing these properties in catalyst designing and fruitfully applying them at both the laboratory and industrial levels will significantly cut the total reaction system expenditure.
To address the demanding challenge of sustainable catalysis, the emergence of homogeneous recyclable catalytic systems has gathered noteworthy attention as a promising and innovative solution.38–46 Homogeneous recyclable catalytic systems represent a substantial development in sustainable catalysis by combining the high activity and selectivity frequently associated with homogeneous catalysts with the ease of separation and reuse conventionally characteristic of heterogeneous catalysts. These systems characteristically involve a catalyst that exists in the same phase as the reactants, enabling close contact and efficient transformations. However, contrasting traditional homogeneous catalysts that are frequently challenging to separate from the reaction mixture, recyclable versions are precisely designed with characteristics that allow for their recovery and subsequent use in multiple catalytic cycles. This recyclability not only diminishes the amount of catalyst needed over time, thus lowering costs and minimising waste generation, but also addresses environmental concerns. By enabling catalyst reuse, these systems contribute to greener and more sustainable chemical procedures, in line with the principles of atom economy, waste reduction, etc. in modern chemical synthesis.
Researchers have made substantial advancements in strengthening the recyclability of these systems through various strategies, including the use of polyethylene glycol (PEG),47–53 ionic liquids (ILs),54–59 micellar catalysis,60,61 deep eutectic solvents (DESs),62–66 nanofiltration,67,68 biphasic systems,69–71 supported catalysts,72 supercritical carbon dioxide73,74etc. all while retaining catalytic activity. By enabling easy separation and reuse, these systems endorse waste minimisation, atom economy, and the employment of environmentally benign solvents, eventually contributing to a more sustainable tactic for chemical processes while reducing waste and cost.
Such homogeneous, recyclable catalytic systems are similarly employed in facilitating C–H functionalisation reactions. This review article provides a summary of current advancements in homogeneous recyclable catalytic systems for C–H bond activations, concentrating on sustainable methodologies and innovative strategies. By highlighting diverse tactics that employ deep eutectic solvents (DESs), ionic liquids, polyethylene glycol (PEG), micellar, biphasic and simple filtration or extraction systems, we aim to illustrate the advancement made toward greener and more efficient synthetic methodologies. By incorporating green chemistry principles, the objective of this review article is to present a cohesive understanding of the breakthroughs in recyclable catalytic systems and their role in promoting environmentally accountable synthetic strategies. The ultimate objective is to recognize trends and investigating the recycling efficiency of various catalytic frameworks for the activation and functionalisation of C–H bonds.
Considering the pre-eminence demonstrated by PEG, an environmentally friendly solvent system, it has been prolifically used as medium in favour of the metal-facilitated cross-coupling reactions in particular Heck reaction,82 Suzuki reaction,83,84 the homocoupling and cross-coupling of aryl halides,85 carbonylative Suzuki coupling,86 carbonylative Sonogashira coupling,76 hydrosilylation of terminal alkynes,87 click reaction of fluorescent organic probes,88 and one-pot synthesis of chromenes89 with solvents and precious metals being easily reusable. A concise overview of the innovative aspects and illustrative examples of recycling methods using PEG media for C–H activation reactions that take account of toxicity, cost-effectiveness, technical utility, and sustainable chemistry has been described here.
:
2) mixture resulted in a significantly improved yield of 95% and reduced the reaction time by half. Furthermore, with an initial Ru catalyst loading of 2 mol%, no additional catalyst was required during the recycling process. A range of derivatives of phthalides can be generated in yields that are good to outstanding during the mild reaction that uses Cu(OAc)2·H2O playing the role of an oxidant while the reaction proceeds at a temperature of 80 °C (Scheme 1).
In an extensive examination of catalyst reusability, 2-methylbenzoic acid and butyl acrylate were employed to evaluate oxa-Michael addition and oxidative alkenylation as a tandem reaction under the influence of [{RuCl2(p-cymene)}2] (2.0 mol%) and Cu(OAc)2·H2O (2 eq.) in a PEG-400/H2O mixture (3
:
2, 5 g) at 80 °C. Having high yields (ranging from 93% to 96%) across every cycle, the catalytic system demonstrated remarkable stability over the course of six successive reaction runs (Fig. 2). Equivalent activity and yields were constantly demonstrated over multiple runs in the reaction between 2,4-dimethylbenzoic acid and acrylonitrile under the same conditions. Ultimately, there was no discernible decrease in catalytic activity during recycling and reusing the catalysts for both of the reactions.
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| Fig. 2 Recycling study of the [{RuCl2(p-cymene)}2]/Cu(OAc)2·H2O/PEG-400/H2O catalytic system designed for the alkenylation reactions. | ||
Zhu and co-workers reported a similar protocol as depicted in Scheme 1 utilising a rhodium catalyst where catalyst recycling was not a priority.91 Their method involved the use of Rh as a catalyst and employed a higher catalyst loading compared to the protocol outlined in Scheme 1. Furthermore, the reported yields were also comparable. An advantage associated with this scheme is the use of water as a green and sustainable solvent.
Later in the subsequent year, Yedage and colleagues defined an effective and sustainable method for annulation and olefination through C–H bond activation employing Ru(II) in PEG-400 as a reusable and green catalytic system.92 They reported oxidation-driven annulations of N-methoxybenzamides 4 and benzoic acids 6 with alkynes catalysed by ruthenium to synthesize isoquinolinones 8 and isocoumarins 10, respectively (Scheme 2). Additionally, they conducted annulation reactions of N-methoxy-N-methylbenzamides 5 catalysed by ruthenium in order to synthesize N-methyl isoquinolinones 9 (Scheme 2). Oxidative olefination of Weinreb amides 11 catalysed by ruthenium was also carried out (Scheme 3). The recyclable solvent system based on PEG-400 proved to be more effective than other tested PEG solvents (PEG-200, PEG-600, PEG-2000, and PEG-6000). Interestingly, the addition of water to PEG-400 did not enhance its performance, and a 3 mol% initial Ru catalyst loading eliminated the need for further additions during recycling. This protocol enables the regioselective and stereoselective formation of fresh C–C, C–O, and C–N bonds through a one-step cleavage of C–H, N–H, O–H and N–O bonds. The established technique reveals key sustainable features, including moderate reaction conditions, high atom economy, and the ability to reuse the expensive ruthenium-based homogeneous catalyst. Significantly, the method is scalable to the gram level with a simple extraction process, making it appropriate for large-scale synthesis.
The reusability of Ru(II) in the PEG-400 catalyst setup was systematically inspected for annulation and ortho-olefination reactions of amides with alkynes and styrenes. During the reaction, a notable colour change from brown to blue directed completion, and phase separation enabled simple catalyst and product recovery. The catalytic system, after being cooled and treated with diethyl ether, was reused for subsequent reaction cycles, representing consistent catalytic activity until the fourth cycle with minimal decrease in yield. For instance, the yields of 8a, 10a, 9a, and 13a remained above 86% after four cycles (Fig. 3).
Guimond and co-workers described a related protocol with Scheme 2 employing a rhodium catalyst,93 but catalyst recovery was not a focus of their work. While their method used rhodium, it required a lower catalyst loading than the procedure detailed in Scheme 2. However, the reported product yields of both the methodologies were broadly similar.
In 2017, Li and co-workers introduced a straightforward and recyclable catalytic framework for activating C–H bonds to directly arylate heteroarenes 14 with aryl chlorides 15, employing RuCl3·xH2O as a cost-effective catalyst and PEG-400 as a sustainable solvent (Scheme 4).94 Initial solvent screening revealed the unsuitability of toluene and water for the generation of the target products. While ethylene glycol afforded a moderate yield of 57%, methanol proved ineffective for direct arylation, likely due to its low boiling point limiting the achievable reaction temperature. Polyethylene glycol (PEG) demonstrated superior performance as a solvent compared to ethylene glycol and offered the additional advantage of recyclability over other tested solvents. Furthermore, the potentially weak interaction between PEG and the ruthenium species might enhance reactivity, drawing a parallel to the coordination effects observed with crown ethers and ruthenium catalysts. The system required no additional ligands or additives showing outstanding compatibility of functional groups, and the ratio of mono- to diarylated products could be effortlessly controlled by regulating reaction parameters. Additionally, the transformation progressed efficiently under ambient air conditions, and the reaction could be scaled up to gram quantities with a minimal loading of the catalyst (0.3 mol%).
The recycling potential of the catalytic system was examined by performing a sequence of recycling experiments. For each cycle, the reaction was executed by stirring a combination of 2-phenylpyridine, 1-chloro-3-fluorobenzenes, and LiOH·H2O in PEG-400 containing 5 mol% RuCl3·xH2O at 120 °C under air for 24 hours. Subsequent to completion, diethyl ether (50 mL) was used to extract the reacting mass when it reached ambient temperature. The recovered PEG solution, comprising the catalyst, was directly reused by adding fresh reactants under similar conditions. Even after six consecutive cycles, the system preserved a high yield of 85%; however a gradual decline in selectivity was detected (Fig. 4).
During the same time, Cai and colleagues again established the competence of a ruthenium-based catalytic system, [Ru2Cl3(p-cymene)2][PF6], during the oxidation-induced annulation of alkynes 19 with N-2-pyrimidyl-substituted anilines 18 to produce indoles 20 (Scheme 5).95 The reaction occurs effectively in a PEG-400 and water mixture at 100 °C, employing Cu(OAc)2·H2O as an oxidising agent. The PEG-400/H2O solvent system demonstrated superior performance compared to other tested systems for these reactions, exhibiting higher product yields and faster reaction times. While using pure PEG-400 as the solvent resulted in a 53% yield of the target product, employing a 3
:
2 mixture of PEG-400 and H2O significantly improved the outcome, yielding 93%. For catalyst recycling, the reaction was initially performed with 3 mol% of Ru catalyst, and subsequent reaction runs were conducted by simply adding fresh substrates without replenishing the catalyst.
To test the robustness of this recyclable system, the annulation of 2-methoxy-N-(2-pyrimidyl)aniline using an internal alkyne (diphenylacetylene) was employed as a prototypical reaction. Product isolation is conveniently attained by extraction with petroleum ether, further contributing to the practicality of the method. Under these conditions, the catalytic system showed outstanding reusability, with both the [Ru2(p-cymene)2Cl3][PF6] catalyst and Cu(OAc)2 oxidising agent being recycled and re-utilised as long as six times without any considerable decline in the performance of the catalyst. Steady yields were obtained over six successive runs (96%, 94%, 96%, 95%, 95%, and 94%, respectively) with minimal variation in reaction time (Fig. 5). This result highlights the stability and efficacy of the catalytic system.
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| Fig. 5 Recycling study of the Ru-catalysed annulation of 2-methoxy-N-(2-pyrimidyl)aniline using an internal alkyne. | ||
Later, a study by the Bhanage group offers an environmentally friendly and sustainable approach in order to generate isoquinoline derivatives 23 employing a homogeneous reusable Ru(II)/PEG-400 catalytic system (Scheme 6).96 This method employs N-tosylhydrazone 21, a seldom utilised directing group, to enable annulation reactions using alkynes 22 through C–H/N–N activation. Initially, 1,2-DCE proved to be an efficient solvent for the proposed protocol giving 76% product yield. However, this solvent could not be applied for recyclability, so in order to achieve recyclability, evaluation of various polyethylene glycols (PEG-200, PEG-600, PEG-2000, and PEG-6000) revealed that only the lower molecular weight PEGs, specifically PEG-200 and PEG-600, were effective in driving the reaction to completion. The reaction proceeded smoothly in biodegradable PEG-400, affording the desired product in a gratifying 74% yield with additional merits of recyclability and greener media.
The main strengths of these procedures encompass a quick reaction period, an easy extraction procedure, extensive variety of substrates and exceptional yields of products, as well as readily accessible substrates. The usage of biodegradable solvents and the scalability of the system to gram levels additionally improve its sustainability and competence.
The potential for the reuse of the Ru(II) in PEG-400 system was thoroughly verified performing the cyclisation reaction of 4-methyl-N′-(1-phenylethylidene)benzenesulfonylhydrazide using diphenylacetylene under standard conditions. With an initial Ru catalyst loading of 5 mol%, subsequent recycling of the catalyst proceeded without the need for any further additions. After the reaction completion, the reaction composition was retrieved using diethyl ether, while the leftover PEG-catalyst layer was reutilised for successive cycles. The catalyst was able to preserve consistent yields (86%, 86%, 85%, and 83%) over four successive cycles with minimal reduction in yield owing to product loss during the work-up (Fig. 6).
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| Fig. 6 Recycling study of the Ru catalyst for annulation reaction of 4-methyl-N′-(1-phenylethylidene)benzenesulfonylhydrazide. | ||
Extending their work, the same research group reported a green and atom-efficient protocol for synthesising isoquinolines 26 and isoquinolinones 28 using a reusable ruthenium catalyst in polyethylene glycol (PEG) solvent, aided by microwave energy.97 Using the proposed catalytic system, ketazines 24 first underwent an annulation reaction with internal alkynes 25 (Scheme 7). Then, a novel approach was employed, utilising dibenzoylhydrazine 27 for the first time as a directing group in the annulation reaction with internal alkynes 25 (Scheme 8). Under comparable reaction conditions, a range of reaction media, such as PEG-200, PEG-600, and ethylene glycol, were evaluated. However, PEG-400 showed superior efficacy. Specifically, employing PEG-400 as the solvent yielded the target product with an 89% yield. In contrast, the utilisation of alternative solvents led to considerably diminished yields or a complete absence of the desired compound. The approach is environmentally gentle, necessitating no external oxidant or silver/antimony salts, and offers high atom economy with an easy extraction procedure. The reaction completes quickly due to microwave assistance, dropping the overall reaction time. It also establishes broad substrate compatibility, gram-scale synthesis potential, and steadily high product yields.
The reusability of the Ru catalyst in PEG-400 media was inspected by performing repetitive annulation reactions of 1,2-bis(1-phenylethylidene)hydrazine and N,N′-dibenzoylhydrazine using an internal alkyne, diphenylacetylene, under optimised conditions. The Ru catalyst, initially loaded at 5 mol%, was successfully recycled in subsequent reactions without requiring an additional catalyst. Upon finishing every cycle, the reaction composition was separated with diethyl ether, and then the remaining catalytic medium, containing RuCl2(p-cymene)2 in PEG-400, was reused after heating to remove remaining ether. The yields across five runs remained high, exhibiting minimal variation: for ketazine, the product (26a) yields ranged from 89% to 83%, and for dibenzoylhydrazine (product 28a), from 74% to 70% (Fig. 7).
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| Fig. 7 Recycling analysis of annulation reactions of 1,2-bis(1-phenylethylidene)hydrazine and N,N′-dibenzoylhydrazine. | ||
Han et al. reported a related protocol with Scheme 7 utilising a rhodium catalyst,98 where, catalyst recovery was not a focus of their study. While their method employed rhodium, it achieved comparable yields to that in Scheme 7 with a lower catalyst loading (2 mol%) and was operated under milder conditions at 25 °C.
Inspired from the earlier studies reported on C–H activation reactions utilising [RuCl2(p-cymene)]2 as a homogeneous reusable catalyst in PEG-400, the Jadhav group proposed a sustainable and effective protocol for the preparation of 1-phenyl isoquinolines 31 (Scheme 9).99 This catalytic system is accompanied by Cu(OAc)2 acting as an oxidising agent and AgSbF6 as an additive. The reaction works through C–H and N–N functionalisation between 1-(diphenylmethylene)hydrazine 29 and aryl-substituted acetylenes 30. Several reaction media were evaluated, including ethanol (EtOH), toluene, and dichloromethane (DCM). Compared to these, PEG-400 not only provided comparable or higher product yields but also offered the key advantage of being a biodegradable and “green” solvent, making it a more environmentally sustainable choice for the reaction medium. This method delivers numerous advantages, including an easy extraction process, the use of an eco-friendly solvent, high atom economy, and a reusable catalytic system. With the catalyst loading of 10 mol%, the approach reveals broad substrate scope, yielding a variety of 1-phenyl isoquinoline derivatives 31 with outstanding efficiency and high yields.
Recently, Li et al. have established a remarkably effective and reusable catalytic system implementing [{RuCl2(p-cymene)}2] in a PEG-400/water mixture for the annulation reaction of N-methoxybenzamides 32 using alkynes 33 to give isoquinolones 34 (Scheme 10).100 This system functions under mild conditions (60 °C) with MesCO2K as a co-catalytic additive and does not necessitate an external oxidant, making it a green and sustainable method.
In the optimisation study, the homogeneous catalytic system PEG-400/H2O showed superiority over other systems for the proposed reaction, as it gave better product yields compared to using PEGs alone. The enhanced effectiveness of the PEG-400/H2O mixture is due to the role of H2O in facilitating the dissolution of the additive (MesCO2K) and the subsequent formation of the active catalytic species. Furthermore, this mixed solvent system also outperformed water alone, providing higher yields. However, this system has a limitation in recyclability. To enhance recyclability, employing a PEG-400/H2O mixture emerged as the optimal choice for the protocol. This protocol yields a range of isoquinolone derivatives with good to outstanding efficacy.
The reusability of this catalytic methodology was confirmed using the reaction of 4-tert-butyl-N-methoxybenzamide and diphenylacetylene, where the [RuCl2(p-cymene)]2 catalyst with an initial catalyst loading of 3 mol%, under the similar conditions, was reused for six cycles without requiring an additional catalyst (Fig. 8). After each cycle, the reaction mixture was isolated using diethyl ether, and inductively coupled plasma (ICP) analysis suggested minimal ruthenium percolation, characterised by a level of 2.7 ppm in the product.
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| Fig. 8 Recycling study of the [RuCl2(p-cymene)]2/PEG-400/H2O catalytic framework for annulation reaction of 4-tert-butyl-N-methoxybenzamide. | ||
These triazoles underwent arylation reactions via Pd-catalysed C–H activation in PEG media, providing an efficient and recyclable approach for the synthesis of arylated triazoles under green and sustainable conditions. The Ackermann group in 2009 proposed an innovative method for Pd-catalysed straightforward arylation reactions of various triazoles bearing directing groups 35 in polyethylene glycol (PEG), contributing to substantial development of user-friendly catalytic systems (Scheme 11).104 This method applied a recyclable palladium(0) complex without the need for phosphine ligands, simplifying the method and making it more sustainable. The palladium-catalysed functionalisations of C–H bonds were conducted under atmospheric air conditions, evading the necessity of an inert atmosphere. The utilisation of carboxylic acid MesCO2H as a co-catalyst further improved the reaction's efficiency.
Various solvent systems were evaluated for this reaction and PEG-20000 showed superior performance as a solvent compared to other systems. While organic solvents like NMP, DMA, and 1,4-dioxane resulted in low conversions, and lower molecular weight PEGs (PEG-400 and PEG-2000) produced products in lower yields, the use of PEG-20000, particularly in combination with the additive MesCO2H, significantly improved catalytic efficacy, leading to a higher product yield of 74%. Furthermore, the non-toxic and non-volatile nature of PEG-20000 contributes to a greener process and facilitates the recycling of the catalyst, a feature not typically associated with organic solvents, thus contributing to a more sustainable process.
A crucial discovery from the research was the reusability of the Pd(0) catalyst using PEG-20000 as the reaction solvent. To examine the recyclability of the initially loaded 5 mol% Pd catalyst, the arylation reaction was realised in order to synthesize product 37c and the researchers could reuse the catalytic system for the further cycles (Fig. 9). Even though the catalytic activity reduced to some extent upon recycling, this characterised the pioneering case of a reusable transition metal-based catalyst employed to achieve straightforward arylations via C–H bond activation.
Ackermann and co-workers, later in 2019, advanced a sustainable methodology for C–H arylation of 1,2,3-triazoles through dehydrogenation using a reusable palladium catalyst in polyethylene glycol (PEG).105 This oxidative palladium-catalysis approach facilitated the formation of functionalised 1,2,3-triazoles with wide compatibility with functional groups and a broad range of substrates.
Various triazole-fused chromenes (Scheme 12), isoindoline-fused triazoles (Scheme 13), phenanthrene-fused triazoles and bio-active triazole compounds (Scheme 12) were synthesised using the proposed protocol. The application of PEG as an environmentally benign solvent highlighted the environmental advantages and also confirmed the competence to reuse both the Pd catalyst and the reaction medium.
Recycling studies of the catalyst were carried out for the synthesis of product 39a which demonstrated that the optimal reaction conditions led to a minor but acceptable decline in catalytic efficacy over consecutive runs (Fig. 10). The catalyst, combined with catalytic amounts of copper acetate and pivalic acid, was reused in at least four successive reactions. To ascertain the catalyst's stability and recovery during the recycling process, the palladium loading within the catalytic system was rigorously analysed. Following the reaction, the solid-phase material (PEG/Pd) was isolated via precipitation, and the palladium content was quantified using ICP-AES. This analysis revealed that the palladium loading remained essentially unchanged throughout the consecutive runs, confirming the catalyst's durability and minimal loss under the reaction conditions.
Besides the methodologies involving C–H arylations of triazoles, in 2018, Kumar and colleagues recognised an effective procedure for producing indolizine/imidazoline-fused heterocycles 44via Pd catalysed activation of C(sp2)–H accompanied by isocyanide 43 incorporation, employing PEG-400 as reusable reaction medium (Scheme 14).106 The authors specifically examined water also as a solvent and found it to be ineffective. This ligand, base, and metal oxidant-free method utilises oxygen as an external oxidant, making the process environmentally friendly.
The recyclability of PEG-400 was examined through reactions of 2-(indolizin-2-yl)phenol with tert-butyl isocyanide. Following initial experimentation, the reaction mixture underwent ether extraction, and the isolated PEG was subjected to a subsequent cycle of C–H activation and isocyanide insertion. This second run involved charging the PEG with the same substrate and introducing additional Pd(OAc)2. The findings indicated that PEG-400 remained effective through three cycles of reuse for the synthesis of 44a with minimal loss in catalytic activity (82%, 80%, and 77%) (Fig. 11).
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| Fig. 11 Recyclability of PEG-400 for reaction between 2-(indolizin-2-yl)phenol and tert-butyl isocyanide. | ||
Additionally, the catalytic system, including CuI and PEG, was effectively retrieved and reused repeatedly avoiding a substantial loss in catalytic efficiency, preserving high productivity across multiple cycles. For instance, the reaction between benzaldehyde, morpholine, and phenylacetylene to produce 48a confirmed that the leftover PEG with CuI has the potential to be reutilised until five repeated cycles with consistent results (Fig. 12). Remarkably, no additional copper salt was required in subsequent cycles, further contributing to the reaction's sustainability.
Later, the Das research group established an efficient and green approach to achieve direct alkynylation of the C–H bonds of 1,3,4-oxadiazoles 49 using 1,1-dibromo-1-alkenes 50, catalysed by 10 mol% CuBr and LiOtBu in PEG-400 at 80 °C (Scheme 16).108 The reaction exhibited high product conversion within 2 hours, with no requirement of additional ligands. When dichloromethane (CH2Cl2) and acetonitrile (CH3CN) were employed as solvents instead of PEG-400, no reaction was observed. Also, PEG-400 acts as a non-toxic, reusable medium, eliminating the necessity for hazardous organic solvents, which highlights its eco-friendly nature. The process is a valuable green synthetic approach that eliminates the use of expensive palladium-based catalysts and works under mild conditions with straightforward procedures. It also offers high efficiency, rapid product formation, and significant sustainability advantages.
Recyclability was verified in the annulation of benzaldehyde with diphenylacetylene in order to synthesize isocoumarin 54a utilising the Cp*Co(CO)I2/CuO/PEG-400 catalytic framework comprising 10 mol% Co catalyst. Over three cycles, the protocol preserved a steady conversion rate without the need to add a fresh catalyst or solvent, only demanding replenishment of oxygen (Fig. 13). Though a minor decrease in yield occurred due to slight cobalt catalyst losses, the system remained efficient, delivering good yields in each cycle.
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| Fig. 13 Recycling study of Co-catalysed production of isocoumarin by annulation of benzaldehyde with diphenylacetylene. | ||
A primary advantage of ionic liquids in catalysis is their ability for reusability.116–119 As homogeneous recyclable catalytic systems, ionic liquids can be conveniently isolated from the reaction composition, for the retrieval and reuse of the catalyst, thus lessening waste and enhancing the overall efficacy of the method. Besides, the capability to modify the physical and chemical characteristics of ionic liquids through careful cation and anion selection allows for the creation of customised catalytic systems for specific reactions.120–124
In the past few years, C–H activation reactions have also been fruitfully described using recyclable ionic liquid catalytic systems. In this section, we focus on the application of homogeneous recyclable ionic liquid systems in C–H activations. For clearness along with inclusive understanding, we have further categorised the discussion into two subsections: (1) C–H bond functionalisation catalysed by transition metals in ionic liquids and (2) ionic liquid catalysed C–H functionalisations.
N–CH2Ph)(cod) for the arylborylation of arenes 59 with bis(pinacolato)diboron 58via C–H activation, in the presence of tetra-2-pyridinylpyrazine (TPy) and an ionic liquid (tributyltetradecylphosphonium dodecylbenzenesulfonate (TBPD)) (Scheme 19).125 This catalytic system accomplished up to 91% isolated yield and confirmed excellent recyclability compared to other systems. In contrast, other systems, such as those involving N-heterocyclic carbene complexes of Ir(I), are found to be not reusable, which increases the cost of such synthetic schemes.
1.5 mol% catalyst was loaded in the starting of the reaction. After each borylation reaction, the solvent was eliminated, and boroxine products were obtained by distillation at reduced pressure. The residual catalyst mixture was reutilised for at least three additional runs without losing activity. Hydrolysis of the distillate yielded the final products, permitting efficient catalyst recovery and reuse.
Ruthenium was also explored as a catalyst for ionic liquid mediated C–H activation reactions. Biletzki and colleagues highlighted a noteworthy development in the catalytic development of chiral 2,3-dihydropyrrolones 62 and 2,3-disubstituted pyrroles 63 through the combination of α,β-unsaturated imines 61, carbon monoxide, and ethylene in the presence of 3 mol% Ru3(CO)12 as a precatalyst.126 This reaction was performed across a variety of ionic liquids, demonstrating improved efficiency compared to that of conventional organic solvents. In particular, optimisation in the ionic liquid [C4mim][BTA] revealed that moderate conditions, with respect to reaction time and gas pressures, yielded better results giving both the products in a 50
:
50 ratio in the first catalytic cycle (Scheme 20).
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| Scheme 20 Ru-catalysed preparation of 2,3-dihydropyrrolones and 2,3-disubstituted pyrroles from α,β-unsaturated imines. | ||
The ruthenium species remained active in the ionic liquid phase, allowing reuse after product extraction without a considerable decrease in catalytic performance or selectivity, particularly in [C4mim][BF4]. However, after 1–3 cycles, the activity began to decline, likely due to the development of ruthenium nanoparticles, as verified by dynamic light scattering study. The gradual transition from homogeneous to heterogeneous catalysis reduced efficiency over time, highlighting the role of nanoparticle formation in deactivating the catalyst.
The study was expanded to a palladium catalyst also. Sutar and co-workers, in the year 2020, established a green protocol for C–H functionalisation of azole-based substrates 64, particularly benzoxazole, benzothiazole, and benzimidazole employing 1-aryltriazenes 65 as arylating agents (Scheme 21).127 The protocol utilises a catalytic system comprising 10 mol% Pd(OAc)2 and CuI in hydrophilic [Bmim][BF4] or hydrophobic [Bmim][PF6] ionic liquid (IL) media, accompanied by [BMIM(SO3H)][OTf] as a booster. This approach facilitates the efficient C2-arylation of azoles, providing 2-aryl-substituted azoles 66 in satisfactory to high yields while exhibiting tolerance to an array of functional groups. Furthermore, the study's objectives of green chemistry are supported by the ionic liquid's recyclable and reusable nature, which provides a sustainable substitute for conventional arylation strategies.
To assess the reusability, a C2-cross coupling between 3,3-diethyl-1-phenyltriaz-1-ene and benzoxazole was performed under optimal conditions using fresh, reused, and recycled ILs. The results, presented in Fig. 14, showed negligible yield loss with reused ILs and a slight decrease in yield for recycled ILs, confirming the reusability of the ionic solvents.
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| Fig. 14 Recycling study for Pd-catalysed C2-cross coupling between 3,3-diethyl-1-phenyltriaz-1-ene and benzoxazole. | ||
A relevant protocol shown in Scheme 21, reported by Zhang's group, also employed a Pd catalyst, albeit without prioritising catalyst recycling.128 This method required similar loadings of Pd and Cu salts but utilised DMF as the solvent and necessitated higher reaction temperatures compared to the IL-based system in Scheme 21.
In Scheme 22, Xu and Kong have used manganese as a catalyst for amidation reactions of C–H bonds in ionic liquids. They presented a novel tactic for the amidation of aromatic oximes 67 through activation of C–H bonds, employing simply accessible sulfonyl azides 68 as reagents for amidation.129 The transformation is enabled using a base-metal catalyst, MnBr(CO)5/[Hmim]OTf with 5 mol% cat. loading, which not only achieves outstanding chemical yields but also shows remarkable regioselectivity and compatibility with functional groups. The catalytic system offers advantages like recyclability compared to other screened systems. This recyclability makes it more practical for large-scale C–H amidation reactions. Ionic liquid: [Hmim]OTf enhances catalytic reactions compared to traditional organic solvents. This is because the weakly coordinating counter anion in the ionic liquid likely interacts with the bromide in MnBr(CO)5, forming a more reactive Mn-catalyst.
The reutilisation of the MnBr(CO)5/[Hmim]OTf framework was systematically studied, revealing its capacity for recycling through a simple phase separation process. Upon accomplishment of the reaction, the catalyst has the potential to be recovered by extracting the reaction composition with solvents like diethyl ether, allowing for efficient isolation of the organic products from the ionic liquid medium containing most of the manganese catalyst. Impressively, the system maintained its catalytic activity across five successive runs, though a decline in performance was observed after this point (Fig. 15), attributed to increased emulsion formation and phase separation difficulties.
Several studies on Rh catalysed functionalisation reactions of C–H bonds in ionic liquids exist in published reports. In an innovative study reported in year 2018, Lv and colleagues presented an innovative Cp*Rh(III)/ionic liquid (IL)-based system (with 5 mol% cat. loading) to achieve the straightforward cyanation of C–H bonds, representing the first fruitful development of this method.130 They prepared aryl nitriles by reacting N-cyano-N-phenyl-p-toluenesulfonamide 71 with 2-phenylpyridines 70 (Scheme 23) and oxime ethers 73 (Scheme 24) in separate reactions. This method is distinguished for its gentle reaction parameters, excellent competence, and recyclability, allowing the generation of aryl nitriles from an extensive array of substrates. The system showed compatibility with numerous directing groups and also tolerated a variety of functional groups, showcasing its versatility in synthetic applications.
The reaction's practicality was also established through a 10-fold scale-up, attaining a remarkable yield of the anticipated molecule 74a, even when cutting down the loading of catalyst to 2.5 mmol%. The study also highlighted the recyclability of the catalyst and the ionic liquid as the reaction medium. After six cycles of reuse without reloading the Rh catalyst, only a minor decline in product yield was observed, emphasising the effectiveness of the IL as a recyclable solvent (Fig. 16).
Concurrently that year, Ma et al. recognised an innovative protocol for Cp*Rh(III) catalysed direct amidation of C–H bonds using ionic liquids, showcasing a highly efficient and environmentally benign technique.131 Various directing group comprising substrates, including synthetically valuable N-containing heterocycles, amides, ketoximes, and N-oxides, were precisely amidated using dioxazolones 76 as shown in Scheme 25. This approach allows the selective amidation of dual C(sp2)–H bonds in (hetero)arenes along with alkenes. Furthermore, the protocol's applicability has been widened to 8-methylquinolines 78 also (Scheme 26), functionalising unactivated C(sp3)–H bonds, achieving outstanding yields accompanied by significant tolerance for various functional groups. The application of the Cp*Rh(III)/[BMIM]BF4 system further enhances the process by excluding the use of harmful organic solvents and allowing for catalyst reuse, promoting sustainability in chemical synthesis.
The study examined the reusability of the Cp*Rh(III)/[BMIM]BF4 system across multiple catalytic cycles specifically in the synthesis of product 77d (Fig. 17). Starting with 5 mol% of catalyst and after completing the reaction, the catalyst and solvent were separated, and the recovered system was employed in subsequent reactions with different substrates without significant loss in activity. Remarkably, the system maintained its efficiency for at least five cycles, enabling fruitful amidation of diverse substrates, including various N-comprising heterocycles.
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| Fig. 17 Reusability of the rhodium catalyst in the C–H amidation reaction involving phenylpyridine and dioxazolone. | ||
The Liu research group, in the subsequent year, has established a robust catalytic protocol for the formation of 1,2-benzothiazines through Rh(III) catalysed activation of C–H bonds and cyclisation of NH-sulfoximines.132 This innovative approach employs a mixture of Cp*Rh(III), AgSbF6, and the ionic liquid [BMIM][PF6], enabling a mild reaction environment that eliminates the need for additional base or acid additives. Various ionic liquids and a deep eutectic solvent were tested in this methodology. The results indicated that using [BMIM][PF6] as the medium yielded the best results. Other ionic liquids did not improve the yield and the deep eutectic solvent, ChCl–EG (1
:
1.5), did not produce the desired product. The protocol shows scope for an extensive range of substrates, encompassing a variety of NH-sulfoximines and coupling partners, and consistently achieves excellent product yields. Diverse coupling partners include diazo compounds 81 (Scheme 27), internal alkynes 83 (Scheme 28), and sulfoxonium ylides 85 (Scheme 29).
To examine the stability and recyclability of this catalytic system, the investigators conducted extensive experimentations with the reaction involving NH-sulfoximine and diazo compound, proving that the [Cp*Rh(III)]/AgSbF6/[BMIM][PF6] system containing 5 mol% Rh catalyst could be effectively reused a minimum of ten times, consistently providing the desired product 82a with over 84% yield in the first ten cycles (Fig. 18). The product separation is simple, relying on ether extraction after the completion of reaction. Other experiments involving sulfoximines and diphenylacetylenes confirmed that the system retains its catalytic efficiency, even with the introduction of the oxidant Cu(OAc)2, attaining moderate to good yields over eight cycles.
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| Fig. 18 Reuse of the [Cp*Rh(III)]/AgSbF6/[BMIM][PF6] catalytic system for the production of product 82a. | ||
In recent times, Rui and colleagues have proposed a novel rhodium(III)-catalysed protocol in order to generate C–S and C–Se bonds utilising acetanilide 87 and diaryl disulfides 88 or diaryl diselenides 90 in an ionic liquid (IL) medium.133 This reaction occurs via activation of C–H bonds, producing the corresponding C–H thiolation (Scheme 30) and C–H selenation products (Scheme 31), respectively. This method is notable for its efficiency and sustainability, as it abolishes the need for additional silver salts as additives. The reactions in non-ionic liquids did not proceed, indicating that ionic liquids were crucial not only as solvents but also as additives to facilitate the reaction. The catalytic system demonstrates excellent compatibility with various functional groups and facilitates the straightforward removal of the directing group.
The investigation also underscores the sustainable application of the ionic liquid and the rhodium catalyst. After the initial reaction with 5 mol% catalyst loading, the product can be retrieved using an organic solvent, allowing the reuse of the IL for subsequent reactions without the necessity for an additional Rh(III) catalyst. Remarkably, the system demonstrated stability across five cycles, with only a gradual reduction in product yield, indicating an effective recycling strategy that preserves precious metal resources.
Du and Yao testified ruthenium and rhodium both for the monitored mono- and diolefination of arenes in ionic liquids. The catalytic systems, precisely [BMIM]NTf2 and [BMIM]PF6, empowered controlled mono- and di-olefination of arenes 92 at ambient temperature by means of activation of C–H bonds.134 This pioneering strategy eliminates the need for heating equipment, representing a substantial energy-saving route for industrial production. Their catalyst screening revealed that 5 mol% [RuCl2(p-cymene)]2 principally produced mono-olefinated products 94 (Scheme 32), while 5 mol% [RhCp*Cl2]2 exclusively produced di-olefinated products 94′ (Scheme 33). The optimised catalytic system provides advantages like recyclability compared to other screened systems, including traditional organic solvents like toluene, CH2Cl2, t-AmOH, HFIP, and DMF, which could not produce the desired reaction products. The utilisation of these green, recyclable ionic liquids not only ensured the absence of volatile and toxic organic solvents but also made the reaction process safer, as it required no pressure-tight apparatus. The protocol showcased an extensive substrate scope, achieving excellent yields and selectivity, yet in gram-scale applications.
For examining the reusability of the catalysts, they employed 2-phenylpyridine and styrene in a prototype reaction. Subsequent to the extraction of the product using diethyl ether, the catalytic systems were recycled for at least six cycles, indicating consistent high yields with only a minor decline in competence.
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| Scheme 34 Ionic liquid enabled C(sp3)–H bond functionalisation of alkyl azaarenes for reaction with aldehyde. | ||
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| Fig. 19 Recycling study of ionic liquid promoted addition reaction of p-nitrobenzaldehyde to 2,6-lutidine. | ||
Later, in order to develop benzyl esters despite the need for metals, Liu and colleagues outlined a heterocyclic ionic liquid-catalysed straightforward oxidative esterification of the benzylic Csp3–H bond in hydrocarbons 99 with carboxylic acids 98 (Scheme 35).136 They provided a novel protocol, utilising 20 mol% 1-butylpyridinium iodide ([BPy]I) as an efficient and recyclable catalyst. Various benzyl ester derivatives 100 could be prepared using the mentioned approach with yields ranging from good to excellent.
The recyclability of the ionic liquid catalyst [BPy]I was testified by the reaction of 2-chlorobenzoic acid and methylbenzene under standard reaction conditions which afforded the product 100a. A minimum of four reaction cycles could be accomplished with this catalyst without a considerable decrease in its activity (Fig. 20). They demonstrated that catalyst retrieval is convenient from the aqueous phase by adding ethyl acetate and water on the completion of the reaction, using 2-chlorobenzoic acid and methylbenzene as representative substrates.
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| Fig. 20 The recyclability of the ionic liquid in the reaction of 2-chlorobenzoic acid and methylbenzene. | ||
Feng et al. reported a pertinent protocol (as in Scheme 35) utilising Bu4NI;137 however, this method did not focus on recycling the reaction medium. Notably, the protocols by Feng et al. and Liu et al. operate at the same reaction temperature and employ identical catalyst loadings, achieving efficient generation of the desired ester products.
The following year, Cirujano and co-workers underscored the significance of catalytic systems competent in being recovered and reused though sustaining the exceptional efficiency and selectivity typical of homogeneous catalysts.138 They demonstrated that enhancing the flexibility of the catalytic environment, such as transitioning from rigid microporous structures to adaptable ionic liquids, increases the catalytic site turnover count. They evaluated the HBr@Bu4PBr ionic liquid system for the green alkylation of indoles 101 with alcohols 102 under gentle, solventless parameters. C3 monoalkylated indole 103 has been generated by this system efficiently (Scheme 36). The HBr@Bu4PBr system demonstrates good catalytic performance and maintains its activity in recycling. Indole derivatives can be easily separated through hydrocarbon solvent extraction in this quasi-homogeneous system, which merges the efficiency of homogeneous catalysts with the recyclability characteristic of heterogeneous ones. This allows for reuse in subsequent reaction cycles. The reusability provides a significant advantage compared to traditional homogeneous catalysts, which often suffer from difficult product recovery, deactivation, and moderate selectivity. Notably, the authors claim that HBr@Bu4PBr is the lone recyclable framework described to date to attain high yields of the large indole derivative 103, with consistent performance across five cycles without any noticeable decline in efficiency.
Afterwards, in Scheme 37, Valiyev and co-workers examine the utilisation of Brønsted acidic ionic liquids (ILs) as catalysts in order to prepare tetrasubstituted imidazoles (PRO1, 106) and pyrazines (PRO2, 107) from 1,2-diketones 104 and aliphatic amines 105 without the use of metals or solvents.139 Among various screened ILs, the most effective were [deaH][HSO4] and [taH4][I4], with [deaH][HSO4] getting a 75% yield of PRO1 and 18% yield of PRO2 at 90 °C in an hour. The IL catalyst's robustness has been shown by catalyst recycling tests (Fig. 21), where PRO1 yields remained steady over three reuses. Surprisingly, PRO2 yields varied very little over the course of eight reuses, indicating that during brief reaction times, its formation is less dependent on the catalyst.
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| Fig. 21 Recycling test of the IL [deaH][HSO4] for the synthesis of tetrasubstituted imidazoles and pyrazines. | ||
In recent work, Chu et al. designed an electrochemical approach that uses aryl tetrafluoroborate diazonium salts 109 in an ionic liquid [EMIM]BF4 (1-ethyl-3-methylimidazolium tetrafluoroborate) (2
:
1) as the electrolyte to directly arylate quinazolinones 108.140 Moderate to good yields of 2-arylquinazolinones 110 were effectively produced using this green, catalyst-free process (Scheme 38). Using [EMIM]BF4 (2
:
1) as the electrolyte, a number of reaction cycles were executed to investigate the reusability of the ionic liquid medium. The mixture was extracted following each reaction, and the ionic liquid was preserved for use in later cycles. Over the course of four cycles, the system remained effective with the accumulation of impurities leading to only a slight yellowing of the ionic liquid. The electrochemical process in ionic liquids avoids the addition of a supporting electrolyte due to their inherent conductivity. This non-volatile system not only replaces the traditional organic solvent/supporting electrolyte system but also simplifies the product separation process, making it an ideal medium for electrochemistry.
Recent years have seen the successful demonstration of C–H activation reactions with recyclable deep eutectic solvent (DES) catalytic devices. The implementation of homogeneous recyclable DES systems in C–H activation methods is emphasised in this section. We have separated the discussion into two subsections for the sake of simplicity and complete interpretation: (1) DES mediated C–H functionalisations catalysed by transition metals and (2) C–H functionalisation catalysed by deep eutectic solvents.
A hydrogen bond donor and an acceptor—choline chloride in this instance—combine to form DESs, which are well-known for their biodegradability and low toxicity. Palladium-catalysed dehydrogenation–aldol condensation was effectively mediated by the DES, which improved the process's atom efficiency and chemoselectivity.
This DES system's reusability is one of its main benefits; several reaction cycles were conducted without significant reduction in catalytic efficiency. Following the reaction, the DES could be recovered using a simple aqueous workup, in which the products were precipitated by diluting the reaction composition with water. After that, the filtrate was removed by evaporation to recover the remaining DES-catalyst composition, subsequently utilised for additional reactions. Through the use of dichloromethane or ether to extract it from the aqueous phase, the DES itself was recycled, and FT-IR analysis was employed to confirm its functional integrity.
In deep eutectic solvents (DESs), palladium acetate (10 mol%) acts as the central catalyst in Marset's catalytic framework for the Csp3–H activation of aliphatic amides.152 In the DES [ChCl
:
acetamide (1
:
2) or betaine
:
HFIP (1
:
2)] under an air atmosphere, they reported an arylation reaction integrating aryl halides 118 and amides derived from 8-aminoquinoline 117 (Scheme 41). In contrast to traditional organic solvents, the optimised catalytic system using deep eutectic solvents (DESs) provides improved yields, safer solvent options, and enhanced reactivity. The reaction conditions are more cost-effective and sustainable because of this novel system's elimination of the need for Ag salts, which are frequently employed in similar transformations. The catalyst can be reused, further emphasising the environmental and economic advantages of this approach, because of the DESs, which also maximise reaction yields.
Upon the reaction's completion, the system is brought to a lower temperature, and then two immiscible phases are generated by the addition of 2-MeTHF, a green solvent. The palladium catalyst and the DES stay in the reaction vessel, while the organic phase containing the product is isolated. For two more cycles, the reaction can be restarted with new starting materials without the need for extra palladium or ligand.
A robust approach to generate spiro[indoline-3,3′-pyrrolizin] was described by Pavithra et al. in the year 2020. The dehydrogenative Friedländer annulation catalysed by Cu(OAc)2/TEMPO, followed by sp3 C–H functionalisation and regioselective 1,3-dipolar cycloaddition, yielded the compound spiro[indoline-3,3′-pyrrolizin]-2′-yl)-4-phenylquinoline-3-carboxylate 125 (Scheme 42).153 2-Amino-5-chlorobenzhydrol 120, benzyl alcohols 121, and methyl or ethyl acetoacetate 122 are the starting materials employed in this reaction.
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| Scheme 42 Cu-TEMPO catalysed generation of spiro[indoline-3,3′-pyrrolizin]-2′-yl)-4-phenylquinoline-3-carboxylate. | ||
At first, the dehydrogenative Friedländer annulation is performed in a deep eutectic solvent using Cu(OAc)2/TEMPO with 10 mol% Cu catalyst, bipy, KOtBu, and ethyl or methyl acetoacetate 122. The resulting 2-styrylquinolines, generated in situ, then undergo 1,3-dipolar cycloaddition under the influence of isatin 123 and L-proline 124, yielding the final product, spiro[indoline-3,3′-pyrrolizin]-2′-yl)-4-phenylquinoline-3-carboxylate 125.
The application of 1,3-dimethyl urea-tartaric acid offers multiple benefits, including minimal toxicity, affordability, biodegradability, and reusability. The stability of the DES was shown by its infrared (IR) spectra before and after the reaction, which additionally verified the preservation of hydrogen bonding and catalytic activity. There were no significant modifications in the key stretching and bending vibrations.
In order to facilitate greener Ru-catalysed C–H functionalisation transformations, González-Gallardo and coworkers recently proposed deep eutectic solvents (DESs).154 Using sodium acetate as an additive and a DES consisting of ethylene glycol and choline chloride (in a 1
:
2 ratio), the group carried out a model Ru-catalysed C–H functionalisation reaction of N-methoxybenzamides 126 in the presence of internal alkynes 127. Derivatives of isoquinolones 128 were generated as an outcome of this protocol (Scheme 43). Acyclic and cyclic products were generated when they investigated the reactivity of N-methoxybenzamides with electron-deficient olefins under the same conditions.
Furthermore, the DES system was replaced with betaine
:
HFIP (with a ratio of 1
:
2) to test another C–H functionalisation reaction. C–H activation of N-phenoxyacetamide with diphenylacetylene was performed to give the corresponding disubstituted benzofuran with 70% product yield.
Using copper(II) acetate as an additive, the team then turned its focus to the C–H activation of benzoic acid 129 to react with internal alkynes 127, which generated isocoumarin derivatives 130 in high to outstanding yields with high efficiency (Scheme 44). They additionally examined how benzoic acid 129 reacted with different electron-deficient olefins 131, resulting in both cyclic and acyclic products (Scheme 45). It is worth mentioning that, depending on the substrate used, methyl acrylate reactions can yield both acyclic and cyclic products.
Shang and co-workers also described a related protocol (as in Scheme 44) using a similar Ru catalyst.155 While this method, unlike the one in Scheme 44, did not address reaction medium recycling, it offered the advantages of milder temperatures and the use of water as a sustainable solvent, with air as the sole oxidant. It is worth noting, however, that this protocol required a higher catalyst loading compared to that in Scheme 44.
Following that, investigations have been carried out with an array of electron-deficient olefins 131 and 2-thiophenecarboxylic acid, which successfully produced cyclic products. In Scheme 46, the group explored the reactivity of aryl pyrazole derivatives 134 with electron-deficient olefins 131 in a further extension of their research. Both saturated 135 and unsaturated compounds 136 were produced by this reaction. It is interesting to point out that minor amounts of monoalkenylated target molecules were seen along with the double addition products 137 when alkyl acrylate derivatives were employed.
Their straightforward approach efficiently produces fascinating heterocyclic compounds by activating a broad array of aromatic reactants. On employing a commercially available ruthenium catalyst, the method works well with both internal and external oxidants, including atmospheric oxygen, and achieves similar or better results compared to previous techniques. The advantages of DESs are emphasised during the investigation, particularly their efficiency and recyclability. Recycling the DES is made feasible by the extraction of the organic products from each reaction using a solvent derived from biomass. Even though yields begin to drop after the fifth cycle, the method can support gram-scale reactions that require fewer purification steps, which minimises wasteful solvent use.
A model reaction, involving arylation of benzoxazole with benzaldehyde to generate arylated benzoxazoles 140a, was employed to test the DES's recyclability, with the catalyst being used five times in sequence (Fig. 22). Utilising diethyl ether, the final product was separated from each reaction, and the DES was separated, vacuum-dried, and re-used with little to no decrease in activity. Just a minor quantity of zinc leaching (0.08 ppm) was noticed during the work-up process by inductively coupled plasma mass spectrometry (ICP-MS), while IR spectroscopy confirmed that there was no apparent structural degradation of the DES after recycling. Though there was a small drop in catalytic activity following several recycling cycles, this study highlights the effectiveness, durability, and sustainability of the DES, establishing it as a sustainable replacement for the C2-arylation of benzoxazoles and benzothiazoles.
Through a three-component reaction featuring 1H-pyrazol-5-amine 141, isatin 142, and an enolisable C–H activated compound 143, Zhang and colleagues later established a sustainable protocol in order to synthesize pyrazolo[3,4-b]quinoline spirooxindoles 144 by a one pot approach (Scheme 48).157 The optimised catalytic system using a natural deep eutectic solvent (NADES) offers advantages over organic solvents by providing higher product yields, facilitating a cleaner and more cost-effective reaction, simplifying the procedure, and allowing for reusability. The reaction becomes easier by microwave irradiation in a natural deep eutectic solvent (NADES) comprising choline chloride and lactic acid, which is biodegradable, recyclable, and reusable. The technique is distinctive in that it does not require chromatography and is straightforward, scalable, high-yielding, and clean. Excellent yields were maintained when the model reaction was tested on a 100 mmol scale to establish the reaction's robustness and scalability.
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| Scheme 48 Preparation of pyrazolo[3,4-b]quinoline spirooxindoles in a ChCl/Lac deep eutectic solvent. | ||
The assessment of the NADES's recyclability was examined in the synthesis of product 144a which demonstrated that, regardless of eight recycling cycles, the system retained a 78% yield of the desired compound (Fig. 23). The reason for this insignificant yield drop is believed to be a small amount of solvent lost during the work-up process.
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| Fig. 23 Recyclability of the NADES catalytic system in the synthesis of pyrazolo[3,4-b]quinoline spirooxindole (144a). | ||
In 2021, Nguyen et al. have shown that the catalytic system [CholineCl][ZnCl2]3 is successfully recyclable when applying 2-naphthol 145, benzaldehyde 146, and benzamide 147 in the multi-component preparation of 1-amidoalkyl naphthols 148 (Scheme 49).158 The applied DES system showed higher efficiency (94% yield) than metal catalysts like ZnCl2 (61%), FeCl2 (65%), and AlCl3 (74%) for the proposed protocol. This process is a sustainable substitute for traditional methods since it works at low temperatures, has short reaction times, and does not need volatile or hazardous organic solvents. The DES affects product selectivity in addition to enabling the reaction with high yields. With the addition of aldehydes 149, dimedone 150, ethyl acetoacetate 151, and ammonium acetate, the proposed catalytic system has been further expanded for the generation of polyhydroquinolines 152 (Scheme 50). The catalyst [CholineCl][ZnCl2]3 has outstanding recyclability; it could be reused thrice without going through substantial performance loss while retaining high catalytic activity. After every reaction cycle, the catalyst's structure remained largely unchanged, as determined by FT-IR analysis. The FT-IR spectra of the fresh and recovered catalysts indicated nearly identical results, suggesting that the deep eutectic solvent (DES) had been effectively recovered and employed again in later runs. This minimal structural degradation highlights the stability and durability of the [CholineCl][ZnCl2]3 system in multicomponent reactions.
A primary benefit of micellar catalysts is its competence to be readily retrieved and reutilised, which can substantially contribute to the environmental friendliness of chemical processes.162,163 Micellar catalysts, identical to heterogeneous catalysts, can be easily recovered using straightforward tactics, like centrifugation or extraction, and then reintroduced into the reaction system, making them a financially and environmentally sound choice.
The development of micellar catalysts as an effective replacement for traditional homogeneous and heterogeneous catalysts has risen in significance as the demand for efficient and sustainable chemical processes keeps rising. Micellar catalysts can also be effectively employed for C–H functionalisation reactions.164,165 This section emphasizes the implementation of protocols involving homogeneous recyclable micellar catalytic systems for the functionalisation of C–H bonds.
In accordance with Scheme 51, Ping et al. developed a benign and competent Ru(II)-catalysed ortho-oxidative alkenylation of 2-arylbenzo[d]thiazoles 153, which comprises the activation of two C–H bonds.166 The catalytic system uses 10 mol% ruthenium complex in conjunction with an aqueous solution of the anionic surfactant sodium dodecylbenzenesulfonate (SDBS). Among other screened phase transfer catalysts, SDBS (sodium dodecylbenzenesulfonate) was found to be the most effective, yielding the desired product with the highest yield. This ecologically benign setup utilises aqueous solvent and activated olefins 155 as coupling partners. Remarkably, this transformation progresses under mild conditions (80 °C) and requires a catalytic quantity of the inexpensive oxidant Cu(OAc)2·H2O. The application of SDBS improves the effectiveness and selectiveness of the alkenylation, facilitating the reaction on a gram scale with high regioselectivity toward ortho-C–H bond activation. Moreover, the system is applicable to a broad array of substrates, comprising both 2-arylbenzo[d]thiazoles 153 and 2-arylthiazoles 154, and generates alkenylated products with high yields.
The reusability of this Ru-catalyst was also studied, indicating robust performance over three successive cycles with negligible decline in performance. Specifically, the alkenylation of 2-(o-tolyl)benzo[d]thiazole using n-butyl acrylate was carried out under ambient conditions to synthesize product 156a in order to assess the recyclability (Fig. 24). The results established the efficiency and sustainability of the Ru/SDBS system, which retained its catalytic activity throughout the trials.
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| Fig. 24 Recycling study of the ruthenium catalyst in the alkenylation of 2-(o-tolyl)benzo[d]thiazole. | ||
Miura and his team also reported a related approach (as illustrated in Scheme 51) for synthesising compounds 156 using a similar ruthenium catalyst.167 Although this alternative method, unlike the previously mentioned protocol in Scheme 50, did not incorporate reaction medium recycling, it boasted a shorter reaction time. However, achieving this outcome necessitated higher temperatures and the inclusion of a silver salt.
The Kumar research group in the year 2019 employed a micellar catalysis strategy to establish a sustainable and selective arylation of C–H bonds in indoles 158.168 They performed this by employing a palladium catalyst known as [(Cinnamyl)PdCl]2 (1 mol%) and the third-generation designer surfactant SPGS-550-M. Fundamental principles of green chemistry are achieved by this catalytic system, facilitating the selective arylation of indoles at either the C-2 or C-3 position under mild conditions. In order to direct the site-selectivity and promote arylation at C-3 (Scheme 52) and C-2 (Scheme 53), correspondingly, the selection of phosphine ligands—specifically, DPPF and DPPP—was critical. Using water as the solvent, the reaction demonstrates high chemo- and regio-selectivity and can tolerate an extensive range of functional groups.
The reusability of the catalyst has been accessed in the synthesis of 160a. Yields would not be impacted by repeated applications of the surfactant-containing aqueous micellar solution (Fig. 25). Each reaction cycle enabled easy separation of the SPGS-550-M-containing aqueous layer from organic residues, allowing it to be reused in later batches without suffering a significant decrease in conversion efficiency.
In the same year, with the support of micellar catalysis, the Ackermann group established a chemoselective C–H arylation approach applying a single-component ruthenium catalyst.169 Through weak chelation assistance, this innovative strategy achieved a broad range of C–H arylated ferrocenes 164 with a high compatibility for an array of functional groups. The homogeneous catalysis in aqueous media was facilitated by the properties of [Ru(p-cymene)(O2CAd)2] and [Ru(OAc)2(PPh3)2] in the ruthenium(II)-catalysed C–H arylation system. By utilising micellar systems, this technique was able to exhibit outstanding sustainability and maintain high reactivity and selectivity, even with sensitive functional groups. The wide-ranging C–H arylation enabled by ruthenium failed to be exclusive to mono-substituted ferrocenes. In fact, it emerged that ferrocenes could also be employed as effective substrates to develop the arylated products 164 (Scheme 54). Furthermore, in the scope of the Ru-catalysed C–H activation protocol, it was found that differently substituted arenes 165 were also arylated (Scheme 55). The used micellar system enables C–H arylations with high chemoselectivity and broad functional group tolerance, demonstrates high catalytic performance and water stability, allows for catalyst recycling, and provides a more sustainable process with a low E factor.
A recycling study of the surfactant has been performed in the synthesis of 164f and the fact that it could be recycled up to four times without going through an apparent reduction in catalytic efficiency highlights the method's practical and environmental advantages (Fig. 26). After the reaction ended, ethyl acetate was introduced, and the solution was gently agitated over five minutes. A centrifuge was then utilised to separate the organic layer, and the solvent was concentrated while the pressure was decreased. The anticipated product was obtained through column chromatography purification. Without the need for an extra surfactant, the aqueous layer that was left over after separation was kept for additional recycling research.
Recently, the employment of these systems to C–H activation reactions has shown substantial potential. With the combination of biphasic systems with C–H activation protocols it was intended to take advantage of the distinguished reactivity and efficiency of homogeneous catalysis accompanied by the practical benefits of heterogeneous systems, such as recyclability and ease of separation. This review section will focus on the advancement of homogeneous recyclable biphasic catalytic systems for C–H activation transformations, highlighting the recyclability of the proposed systems.
By utilising a polyoxometalate catalyst, namely H5PV2Mo10O40, to oxygenate methylarenes 168, Neumann's research team, during the year 2015, created a highly effective technique for synthesising benzaldehyde derivatives 169 (Scheme 56).193 Since it prevents the excessive waste produced by traditional techniques and avoids over-oxidation to benzoic acids, this reaction is highly interesting. It also has a 100% atom economy. Utilising an aqueous sulphuric acid solvent in a biphasic mode, the system makes it easier to recover and recycle the catalyst while also facilitating the catalytic reaction. Aiming to promote the selective conversion of methylarenes 168 into benzaldehyde derivatives 169, the polyoxometalate is protonated by the acid solvent. This allows for subsequent proton and electron transfers. This method releases H2 during electrolysis and permits additional reaction cycles. It additionally yields over 95% and allows multiple catalytic cycles with almost no waste.
Using substrates such as toluene and its derivatives, the polyoxometalate catalyst's recyclability was thoroughly evaluated in multiple cycles, showing its stability and efficiency over five oxygenation–electrolysis cycles. The biphasic aqueous sulphuric acid medium enabled the catalyst's easy reoxidation and recovery without requiring removal, leading to high conversion rates and product selectivity with only minor variations of ±3% between cycles.
Later in 2016, a promising catalytic system to achieve C–H bond functionalisation of arylalkane 170 and substrates with an array of methylene groups was contributed by Hossain and Shyu's work.194 As shown in Scheme 57, the method transforms the substrates into the corresponding ketones 171. tert-Butyl hydroperoxide (TBHP), an environmentally harmless solvent, is used as the oxidant in water to catalyze the reaction, which is mediated by 5 mol% copper salts. The reaction conditions have been rendered easier by not using phase-transfer catalysts or bases, and the process is conducted at room temperature. Its ability to tolerate an array of functionalised arylalkanes and activate C–H bonds outside of the usual benzylic methylene positions is one of its primary advantages. The ease with which products can be separated, without requiring chromatographic workup, enhances its applicability in synthetic applications.
The catalyst's ability to be recycled over multiple reaction cycles attested its sustainability. After every reaction, the product was transferred to the organic layer using ethyl acetate, retaining the copper catalyst in the aqueous phase. The catalyst remained stable and active since there was no apparent percolation of the neocuproine ligand inside the organic medium. The system is highly recyclable as it can be used until seven times without compromising catalytic efficacy. In addition, it proved that the catalytic process is scalable, showing consistent performance in reactions at the gram scale, underscoring its potential for use in industrial settings.
In the subsequent year, Mamlouk et al. showed how to successfully use PIB oligomers functionalised with bipyridine (bpy) ligands and iridium complexes derived from Ir(I) precursors as recyclable catalysts to achieve the borylation of arenes 172 with bis(pinacolato)diboron 173 (Scheme 58).195 This oligomer-supported catalyst generated a variety of arylboronates 174 under mild operating conditions that were identical to those from its non-recyclable counterparts. The system's creative design and efficient biphasic separation made it feasible to recover the catalyst with very little iridium leaching in the first cycle and almost none in the second and third. The catalyst demonstrated outstanding stability for up to eight cycles, allowing high yields of arylboronate products 174 without requiring further purification.
A simple extraction technique was employed to carry out the recycling process, by making use of the PIB-bound iridium complex's differing solubilities in nonpolar solvents like heptane, while the arylboronate products were extracted into acetonitrile. The method guaranteed full catalyst recovery for future applications and high product purity (>97%). Approximately 90% of the 1,2-dichlorobenzene and 84% of the 1,3-dichlorobenzene borylation yields were retained in subsequent catalytic runs, proving the robustness and generality of the recycling process.
This section highlights such homogeneous recyclable catalytic systems for C–H functionalisation reactions, where catalysts are dissolved in media and used for unambiguous separation and reuse on completion of the reaction.
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1). The LDH nanosheets specifically substitute α-amino acid (AA) ligands, ensuring precise regioselectivity and a highly effective system for selective C–H activations.
The regioisomeric ratio remained constant, but the rhodium(III) catalyst having delaminated Mg/Al-Ala-LDHs showed limited recyclability (Fig. 27), with yields descending from >99% to 63% in the 2nd cycle and 19% in the 3rd cycle. Yields were boosted to 86% in the fourth cycle and 74% in the fifth by adding new Mg/Al-CO3-LDHs. Decreased reusability was not caused by rhodium leaching, as proven by the minimal amount (<3.2%); rather, hydroxyl groups on the LDH layers were probably consumed. The reintroduction of LDHs led to partial regeneration.
Guimond and his team also explored a similar strategy, depicted in Scheme 59, to synthesize compounds 177 and 178 using the same rhodium catalyst.204 While this alternative method shared identical catalyst loading and temperature, and comparable reaction times with the previously described protocol in Scheme 59, it lacked the reaction medium recycling capability. Thus, the earlier protocol outlined in Scheme 59 offered an additional advantage of catalyst recycling.
In the successive year, Jones and co-workers synthesised and characterised four novel water- and air-stable organometallic Rh(III) complexes, namely: trans-RhIII(α-diimine)(CO)MeI2 (complex A), [RhIII(α-diimine)(H2O)3(C(O)Me)][BF4]2 (complex B), [RhIII(α-diimine) (H2O)3Me][BF4]2 (complex C), and RhIII(α-diimine)(H2O)(C(O)Me)(OC(O)CF3)2 (complex D), where α-diimine refers to 1,4-bis(Ar)-2,3-dimethyl-1,4-diaza-1,3-butadiene and Ar = 3,5-dimethylphenyl. With 4 mol% of the complex, complex C showed significant catalytic activity in order to achieve the H/D exchange among benzene 179 and TFA-d1, attaining 98% conversion with 91% deuterium incorporation in 24 hours (Scheme 60).205 Complex C retained its catalytic activity, according to recycling experiments (Fig. 28), but its efficiency reduced with each cycle owing to the generation of breakdown products and low water solubility, which prevented complete recovery. Water was additionally found to slow down the rate of reaction, suggesting that aquo ligand fragmentation is necessary to maintain catalytic activity.
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| Scheme 60 Catalytic activity of complex C containing Rh towards the H/D exchange among benzene and TFA-d1. | ||
Using rhodium catalysis, Meng et al. recently established a highly competent and sustainable C–H activation followed by [4 + 2] annulation of aryl amides 181 with propargyl alcohols 182 in order to prepare isoquinolones 183 (Scheme 61).206 Screening a range of transition-metal catalysts, including MnBr(CO)5, Pd(OAc)2, Cp*Co(CO)I2, [Ru(p-cyeme)Cl2]2, and [Cp*RhCl2]2, in the presence of NaOAc at room temperature revealed that only [Cp*RhCl2]2 efficiently catalysed the reaction. The desired product was also obtained through simple filtration in various solvents, including ethyl acetate, methanol, DCE, MeCN, THF, and DCM. Given the environmental friendliness and efficiency of ethanol in this reaction, it was selected as the preferred solvent. The reaction exhibited unique characteristics, such as outstanding regioselectivity and the utilisation of ethanol as a green solvent that reacts both with water and air. Surprisingly, the reaction proceeds under mild conditions, could be scaled up to gram levels, and has a lower rhodium catalyst loading (0.5 mol%). The study indicates that propargyl alcohol moieties, the hydroxy group, and the pivaloyl fragment in the substrates are crucial for controlling chemoselectivity. This process makes simple product purification feasible, and also does not depend on a metal oxidant.
The recycling study of the catalytic framework was performed in the preparation of product 183a (Fig. 29). When the reaction was completed, Na2CO3 granules were removed using a Pasteur pipette, and the product readily solidified, which could enable easy separation employing filtration. The precipitate was rinsed with ethanol and dried in vacuo. Throughout ten cycles, the filtrate, which was concentrated and reused without an extra rhodium catalyst, was consistent. Without having a substantial depletion of activity, the catalytic system showed outstanding recyclability. Isoquinolone synthesis remained ecologically sound and cost-effective over a three-day period.
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| Scheme 62 C–H/N–H activation of acetanilides catalysed by a Pd(II) pincer type complex to form functionalised carbazoles. | ||
The recycling study of the catalyst was performed in a reaction of acetanilide and phenylboronic acid. On termination of the reaction, the solid product underwent filtration, and the resulting filtrate was diluted with ethyl acetate to separate the catalyst and inorganic salt as a by-product. After being dried, the recycled catalyst was used in further cycles with similar reaction parameters. The remarkable recyclability of the catalytic system, which maintains activity over six successive runs, is an important aspect of this work. Melting point data, TLC analysis results, and 1H NMR spectroscopy results all confirm the stability of the recovered catalyst, despite a progressive decline in efficiency with each cycle. This feature emphasises the methodology's practicality by facilitating the generation of biologically relevant carbazoles in a simple and environmentally friendly way without requiring tedious column chromatography for product isolation.
Building on the exploration of palladium-catalysed reactions in aqueous media, Bhatt and colleagues later fruitfully developed three novel, air- and moisture-insensitive palladium(II) complexes, two of which contained an S,CNHC half-pincer ligand, while the third featured the first Se,CNHC,S-type pincer ligand.208 These complexes showed outstanding thermal stability and resistance to moisture and air, rendering them predominantly suitable for the regioselective C–H bond arylation of imidazoles under gentle reaction parameters. Remarkably, the complex [Pd(L3-HBr)Cl]BF4 (complex F), characterised by S,CNHC,Se coordination, exhibited excellent catalytic activity, enabling the C-5 arylation of imidazoles 189 with aryl bromides 190 in the vicinity of K2CO3 and pivalic acid (Scheme 63). It attained yields up to 97% within 12 hours, using only 0.5 mol% of catalyst. The methodology was established to be highly versatile, with remarkable functional group compatibility across an extensive variety of substrates, confirming broad applicability and high efficiency.
The reusability of complex F was examined in the arylation of 1-methyl-1H-imidazole with 1-bromo-4-nitrobenzene. Following the accomplishment of maximum conversion in the initial reaction cycle, fresh aliquots of initial reactants, K2CO3, and pivalic acid were incorporated into the reaction vessel for succeeding cycles. Complex F exhibited admirable recyclability over the following five reaction cycles, revealing only an insignificant reduction in catalytic competence thereafter.
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| Scheme 64 Cu-catalysed chemo- and regioselective benzylic C(sp3)–H oxidation of biaryl substrates bearing methyl and carboxylic acid. | ||
The heterogeneous catalyst is subsequently precipitated out and collected for application in the following processes via straightforward filtration, leveraging the merits of both homogeneous and heterogeneous catalysts. By repeating the procedure with a copper catalyst and di-tert-butyl peroxide (DTBP) in four separate runs without adding more copper catalyst, the yields of the anticipated product 193a were 82%, 75%, 66%, and 48%, respectively (Fig. 30). Likewise, the catalysts with Rose bengal were also recycled and reused in the Cu/O2 system (condition B).
However, no system follows 100% of the 12 principles of green chemistry, and certain green chemistry principles are still challenging to address and “can be” addressed in near future to make the homogeneous recyclable catalytic system a complete “green and sustainable system for C–H activation and functionalisation”.
Table 1 provides a concise overview of various catalytic systems employed for C–H bond functionalisation reactions, with an emphasis on their recyclability and key features. Several catalytic systems, including polyethylene glycols (PEG), ionic liquids (ILs), deep eutectic solvents (DES), micellar systems, biphasic systems, and systems allowing simple filtration or extraction, have verified efficiency in supporting a range of metal catalysts such as Ru, Rh, Pd, Cu, Co, Ir, and Mn.
| Entry | Catalytic system type | Metal catalyst(s) | Recyclable system/medium | Number of recycles | Key features |
|---|---|---|---|---|---|
| 1 | Polyethylene glycol (PEG) | Ru, Pd, Cu, Co | PEG-400, PEG-400/H2O, PEG-20000 | 3–6 | Negligible vapor pressure, inexpensive, thermally stable, biodegradable |
| 2 | Ionic liquids (ILs) | Ir, Ru, Pd, Mn, Rh | TBPD, [C4MIM][BF4], [BMIM][BF4], [BMIM][PF6], [HMIM]Otf, [BMIM]NTf2, [BMIM]Otf, [Hmim][H2PO4], [BPy]I, HBr@Bu4PBr, [deaH][HSO4], [EMIM]BF4:H2O | 3–10 | Chemically and thermally stable, strong solvation capabilities, less volatility and vapor pressure, high polarity and conductivity |
| 3 | Deep eutectic solvents (DESs) | Pd, Cu, Ru | ChCl : malonic acid, ChCl : acetamide, betaine : HFIP, DMU : tataric acid, ChCl : ethylene glycol, betaine : HFIP, [ZnCl2][ethylene glycol]4, ChCl/Lac, [CholineCl][ZnCl2]3 |
3–8 | Excellent solubility, broad viscosity range, low toxicity, simple recoverability |
| 4 | Micellar systems | Ru, Pd | SDBS, SPGS-550-M-water, TPGS-750M/H2O | 4–5 | Capability to solubilise both polar and non-polar reactants, ability to be readily recovered and reused |
| 5 | Biphasic systems | Cu, Ir | Aqueous biphasic medium, heptane : acetonitrile |
5–8 | Simple separation and recycling, potential for continuous operation |
| 6 | Systems allowing simple filtration or extraction | Rh, Pd, Cu | Extraction or filtration of products | 3–11 | Minimal work-up requirements, simple separation and recycling, potential for continuous operation, reduction of metal contamination |
Each catalytic system presents exclusive merits. For instance, PEG-based systems show negligible vapor pressure, cost-effectiveness, thermal stability, and biodegradability, making them environmentally benign substitutes. Ionic liquids are characterised by their chemical and thermal stability, strong solvation capabilities, low volatility, and high polarity and conductivity, offering a versatile medium for numerous reactions. Deep eutectic solvents exhibit excellent solubility, a broad viscosity range, low toxicity, and simple recoverability, in line with green chemistry principles. Micellar systems can solubilise both polar and non-polar reactants and are easily recoverable and reusable. Biphasic systems enable simple separation and recycling, with potential for continuous operation, enhancing process efficacy. Lastly, systems allowing simple filtration or extraction minimize work-up requirements, simplify separation and recycling, and reduce metal contamination, contributing to cleaner product development.
The number of recycles attained diverges across the systems, ranging from 3 to 11, demonstrating the potential for prolonged use and reduced waste generation. While this highlights the key features and recyclability of these catalytic systems, a more in-depth analysis of their catalytic activity, substrate scope, reaction kinetics, and long-term stability would provide a more comprehensive understanding of their applicability and limitations in different C–H bond functionalisation reactions.
Recyclability and product selectivity are the major advantages of the homogeneous recyclable catalytic systems for C–H functionalisation reactions. However, loss of catalytic activity/rate is a possible penalty attributed to catalyst deactivation during the reaction or isolation process. Basically, the catalyst reduces the activity due to chemical, mechanical, physical and thermal deactivation. Apart from this, metal leaching is a notable cause for the decrease of catalytic activity which involves escaping of the metal from the complex system. Above all, penalties are very common in the use of the recyclable catalytic system for C–H activation which may result in the decrease of the catalytic activity, selectivity, conversion efficiency and yield of the reaction. Nevertheless, it is important to mention that, catalyst deactivation is more simply prohibited by controlling reaction conditions and temperature. The mild reaction conditions are more favorable for retaining the catalytic activity for the next recycle which is a characteristic feature of recyclable homogeneous catalytic systems for C–H activation compared to heterogenous systems.
Sometimes, to retain the maximum catalytic activity various regeneration and rejuvenation strategies are applied which are beyond the scope of the present review. Another strategy to maintain optimal reaction performance in the recycling process is to compensate the loss of catalyst loading during recyclability by adding a fresh catalyst which in turn increases the process economics. However, a question arises about the quantity of fresh catalyst to be added for the next cycle which is to be determined. Hence, two parameters, namely, the turnover number (TON) and turnover frequency (TOF) are crucial to assess the recyclability of the catalytic system. TON mentions the catalyst's life-time and sturdiness before losing its activity while TOF mentions the efficiency and activeness of the reusable catalyst. Higher values of the TON and TOF are desirable for the subsequent recycling of the catalyst.
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60.222 Homogeneous catalysis is still facing several challenges considering catalyst stability, large-scale applicability and profitability at the industrial level.
Considering the green aspects, although biomass-derived solvents for transition metal catalysed sustainable C–H activation offer a promising direction,223 more challenges and opportunities remain, particularly in the development of homogeneous recyclable catalytic systems for C–H activation. Looking at the goal of green chemistry and sustainability to synthesize the fine chemicals at the industrial scale, the first major contribution towards green chemistry is attributed to “generation of NO waste” which is closely associated with the factor “selectivity” (one product–NO waste). This selectivity factor is very genuine during the C–H activation reactions attributed to homogeneous reactions, since a number of C–H bonds are available at the organic reacting substrate. Furthermore, another most important factor towards green chemistry is recyclability that ultimately makes the process industrially feasible which is the real challenge for the development of homogeneous recyclable C–H activation systems. Hence, catalyst designing needs special attention in developing catalytic systems for sustainable homogeneous recyclable C–H activation reactions which involve catalyst designing with (i) appropriate selectivity, (ii) catalytic reaction rate (iii) recyclability and (iv) stability to the reaction environment and conditions.222,224,225
More commonly, homogeneous catalysts decompose at higher temperature, whereas C–H activation is carried out at elevated temperature and hence a temperature sensitive catalyst may decompose during the reactions which cannot be isolated/recycled. Under such conditions, attention should be paid during catalyst designing so that the catalyst is stable towards higher temperature and can be easily recycled without modification after higher temperature exposure to C–H activation reaction. Heterogenisation of a homogeneous catalyst with appropriate use of a solid recyclable support is a new strategy that can be used to obtain a recyclable homogeneous catalytic system.226–228 The support material for anchoring of the catalyst plays a crucial role in the development of the catalyst.41,196,229 Designing of the heterogenised supported homogeneous catalyst is a tedious concept but can be helpful for achieving the goal of green chemistry and sustainability. Furthermore, the anchoring support should be free from the active C–H groups, completely inert to reaction media and easily isolatable from the reaction media. The linkages of the active catalyst and support should be strong enough to avoid the leaching of catalysts.
Apart from this, the catalyst must be sufficiently stable to inhibitory substances formed during the reaction. Separation strategies are essential to consider, since those of a homogeneous catalyst may result in the physical disintegration of the catalyst and hamper further catalyst reusability. Many times, such separation strategies completely decay the catalyst which involves vacuum distillation, evaporation and other sophisticated downstream treatments. It is advisable that, a minimum number of downstream processing steps (such as extraction, precipitation, crystallisation, separation, and distillation) should be performed to retain the catalyst reusability and economic viability. Since isolation of the homogeneous catalyst is the key to obtain further recyclable systems, the use of biphasic media or a phase enhancing solvent system or a co-solvent to precipitate the catalyst/separate products is another approach. Furthermore, the use of a neutral inert solvent is essential to recover the catalyst from the reaction phase, because reactive or nucleo-/electro-philic solvents during subsequent processing steps may cause catalyst leaching and disintegration or catalyst derivatisation or deactivation through blocking of active catalytic sites. Hence, the catalyst designing can be modified for scale-up after knowing or optimising the requisite reaction conditions at the lab scale. Such a kind of strategy of knowing reaction specifications and then fabrications of the catalyst may have a great impact on the development of a recyclable homogeneous catalyst.
The barrier between homogeneous and heterogeneous catalysis for C–H activation can be crossed by the use of several novel strategies involving the use of polyethylene glycol, biphasic media, fluorous solvent/ionic liquid/supercritical fluids, insoluble supports, micellular media, soluble–precipitating supports, nanoparticles as a support/catalyst, magnetically separable nano-particles and nano-filtration which can be applied to successfully obtain recyclable homogeneous C–H activation catalytic systems. Various ideas of catalyst designing and C–H activation reaction from the academics can be tested at the lab scale wherein the catalyst can be further modified as per the reaction requisite for the successful implementation of process scale up and industrial applications. The union of the academia and industry and collaborations can be helpful in crossing over hurdles to obtain a stable, robust, efficient and green homogeneous reusable catalytic C–H activation system.
While substantial development has been made, further research is advantageous for the progress of further robust, selective, and efficient catalytic systems. Discovering novel catalyst designs, optimising reaction conditions, and expanding the scope of functionalisation reactions are crucial areas of future research. By continuing to revolutionize in this field, we can reveal the complete potential of C–H bond functionalisation and contribute to the progress of sustainable and environmentally friendly synthetic approaches.
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