Yunxiang
Qiao†
a,
Enting
Shi†
b,
Xinjia
Wei
b and
Zhenshan
Hou
*b
aMax-Planck-Institut für Kohlenforschung, Kaiser-Wilhelm-Platz 1, 45470 Mülheim an der Ruhr, Germany
bState Key Laboratory of Green Chemical Engineering and Industrial Catalysis, Research Institute of Industrial Catalysis, School of Chemistry & Molecular Engineering, East China University of Science and Technology, Shanghai 200237, People's Republic of China. E-mail: houzhenshan@ecust.edu.cn; Tel: +86 21 64251686
First published on 5th April 2024
Metal oxoclusters constitute a dynamic and expanding domain of research with versatile applications in catalysis, materials science, medicine, and beyond. Particular attention has been given to their potential utility due to their distinctive properties. The incorporation of ionic liquid (IL) environments into metal oxocluster (MOC) systems offers numerous advantages, including higher stability, tunable coordination to metal sites, and the capability to dissolve diverse substrates for catalytic applications. Although IL-stabilized MOCs (IL–MOCs) are still in the developmental phase, their potential to revolutionize catalysis is substantial. As research progresses, IL–MOCs will likely play an increasingly important role in catalysis. This perspective article focuses on the preparation methods of IL–MOCs, how the MOCs are stabilized/regulated by ILs or even PIL (polymeric ILs), as well as their catalytic applications, including oxidation, epoxidation, oxidative desulfurization, biomass oxidation, hydroxylation of benzene, acid catalysis, CO2 activation and utilization, carbonylation, hydrogenation/hydrolysis, electrochemistry, etc. IL–MOCs have played a crucial role in the development of sustainable chemistry in the light of the potential opportunities and challenges. The unique advantages make IL–MOCs outstanding candidates for industrial catalysts.
Common examples of MOCs include polyoxometalates (POMs), MOCs with organic ligands (e.g. ILs) or metalloenzymes etc. POMs, a specific class of MOCs, are composed of early transition metals, such as molybdenum, tungsten, and vanadium, in their highest oxidation states.11–13 Various POM structures have been determined, with the most known ones being the Keggin, Dawson, Anderson, Lindqvist, Siverton and Wauth structures, etc. (Fig. 1). For instance, Keggin-POM clusters, featuring 12 metal atoms and 40 oxygen atoms, while Lindqvist-POM clusters, comprising 6 metal atoms and 18 oxygen atoms, both show a cage-like structure and share similar applications.
On the other hand, ionic liquids (ILs) are a class of non-volatile, non-flammable, and tunable solvents, which are made up of ions. They can be tailored to have specific properties, such as polarity, viscosity, and acidity, making them unique media for a wide variety of catalytic reactions and the synthesis of a wide range of MOCs. IL-stabilized MOCs (IL–MOCs) are a new class of catalysts that have shown great promise for a variety of applications in catalysis, electrochemistry, energy production, and materials science.14–17 One of the key advantages of IL–MOCs is their high catalytic activity. This is due to the unique structure of these catalysts with the presence of the exposed metal sites, which allows for close contact between the highly exposed metal atoms and the reactants, thus facilitating the transfer of electrons and the formation of chemical bonds, which are essential for catalysis. ILs could not only stabilize MOCs, but also regulate MOCs through a combination of interactions, e.g. ionic and electrostatic forces, tuning of hydrophilicity or hydrophobicity, and facilitating redox processes. The careful selection of IL components and design considerations can tailor the IL environment to enhance the stability and catalytic properties of MOCs in catalytic applications.
Several research groups actively work on the use of IL–MOCs. In recent years, our group not only designed different IL–MOCs (especially POM-based ILs, POM–ILs), but also utilized them for catalytic epoxidation, oxidation, esterification, and carbonylation/carboxylation, etc. This perspective article aims to provide a brief overview of the development and catalytic applications of IL–MOCs, with a focus on the reports from our own research group and recent contributions from the other groups. Herein, we also briefly discuss the advantages, opportunities, challenges, and the developmental direction of IL–MOCs for the catalytic applications.
The more widely researched examples are the anion-exchange of PILs by POM anions, a process similar to that of monomeric ILs, except the cation is PIL.21–23 PILs are the polymeric products of IL monomers, composed of polymeric backbones with IL species in each repeating unit, forming a network structure.24 Mixing a PIL solution in a miscible organic solvent (often ethanol) with a MOC aqueous solution forms the desired PIL–MOC, which can be separated normally by filtration. As such, PIL–MOCs in this article refer to MOCs serving as anions of PILs. PILs exhibit properties similar to traditional ILs but possess additional characteristics stemming from their polymeric nature. These materials often feature high thermal stability, tunable mechanical properties, compatibility with various solvents and substrates, and more easily tunable amphiphilicity, etc. These characteristics make them similar to, but slightly different from monomeric IL–MOCs. PIL–MOCs are also widely used in various catalytic reactions, which is illustrated in the following sections.
IL–MOCs | POM precursor | IL | T/°C | t | Ref. |
---|---|---|---|---|---|
(R3R′P)2W6O19 | Na2WO4 | R3R′PBr | — | — | 27 and 28 |
[EMIm]4[β-Mo8O26] | Na2MoO4·2H2O | [EMIm]BF4 | 170 | 24 h | 29 |
[EMIm]8Na9[WFe9(μ3-O)3(μ2-OH)6O4H2O(SiW9O34)3]·7H2O | Na10[SiW9O34]·16H2O, Fe(NO3)3·9H2O | [EMIm]Br | 150 | Three days | 30 |
[EMIm]4[SiMo12O40]·12H2O | Na2MoO4·2H2O, Na2SiO3·9H2O | [EMIM]Br | 150 | Three days | 30 |
[BMIm]3NH4[Mo8O26] (crystal) | Ammonium molybdate, La(OH)3, 2-pyridinecarboxylic acid | [BMIm][BF4] | 140 | Six days | 31 |
[BMIm]4[PMoVMo11O40] (crystal) | (NH4)6Mo7O24·4H2O, La(OH)3, NH4H2PO4 | [BMIm][BF4] | 135 | Six days | 31 |
[BMIm]3[PMo12O40] (crystal) | Sodium molybdate, copper chloride, phosphoric acid, water | [BMIm][BF4] | 150 | Seven days | 31 |
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Fig. 2 Schematic diagram of preparation principle to the POM/PIL/Gr hybrids. Adapted from ref. 36 with permission from Elsevier, copyright 2020. |
One way is by forming hybrids with MOCs that act directly as ILs’ anions.17 The unique combination of IL cations and MOC anions can be used to tune the activity and selectivity of IL–MOC/PIL–MOC catalysts. This type of hybrids is the focus of this perspective article, especially their design and catalytic application under green chemistry conditions (Scheme 2A).
Another way is by forming strong bonds with the metal atoms.41–43 ILs are composed of cations and anions. The specific charge distribution on IL components can interact with charged sites on MOCs through electrostatic forces, and also their polar functional groups, such as nitrogen, oxygen, and sulfur atoms. This coordination can help to protect the MOCs from the environment, strengthen the bonds within the MOCs, and make them more stable, thus preventing them from decomposition (Scheme 2B).
To some extent, the universal solvent property of ILs can be ascribed to the strong bonds formed between the ILs and MOCs. So-called task-specific ILs, which are ILs with a functional group covalently tethered to the cation or anion, are being developed to increase the solubility of metal compounds in these solvents. The functional group that has the ability to coordinate with the metal ion, preferably as a bidentate or a polydentate ligand, facilitates the dissolution of MOCs. Taking deprotonated betaine Me3N+CH2COO− as an example, the carboxylate group on one end of the molecule can act as a bridging ligand providing super-exchange pathways between metal ions, while the large trimethylammonium part on the other end behaves like a spacer that can separate adjacent chains.26 And the protonated betaine (also called betainium) exhibits a higher acidity (pKa 1.83) than alkanoic acids like acetic acid (pKa 4.75) or propionic acid (pKa 4.87), it is the higher acidity of the betainium ion improved an enhanced solubilizing ability for MOCs.
Yet another way is ILs can dissolve MOCs that are insoluble in traditional solvents and prevent them from aggregating.44–46 ILs have the ability to dissolve a wide range of compounds, polar and non-polar, which is why they are often referred to as “universal solvents.” This ability to dissolve a wide range of compounds makes ILs ideal for stabilizing MOCs, which can be quite complex and diverse in their structure and composition. Thus, ILs can provide a solvation environment that prevents the MOCs from aggregating and further improves the stability of the cluster (Scheme 2C).
Overall, ILs could stabilize the MOCs through ionic or electronic interactions, or by solubilization. In a sense, ILs could also regulate the stability and structural integrity as well as the catalytic activity of the MOCs within the IL environment. On one hand, ILs can be tailored to have varying degrees of hydrophilicity or hydrophobicity by selecting specific cation and anion combinations. This allows for the adjustment of the IL environment to match the hydrophilic or hydrophobic nature of MOCs, optimizing their interactions. On the other hand, ILs with appropriate structures can enhance the accessibility of catalytic active sites on MOCs. The unique architecture of ILs can act as a scaffold, providing an environment that facilitates interactions between reactants and the catalytic centers of MOCs. Furthermore, ILs often exhibit unique thermophysical properties, such as low volatility and high thermal stability. These characteristics can create a stable environment for MOCs, influencing their behavior, especially in high-temperature or high-pressure catalytic reactions.
Type of MOCs | IL–MOCs | Application | Ref. |
---|---|---|---|
Peroxotungstate anion-based IL | [HDIm]2[{W![]() |
Epoxidation | 47 |
MNP-[HDMIM]2[W2O11], MNP-[SDMIM]2[W2O11] | Epoxidation | 48 | |
Imidazolium–tungsten peroxo complex | Oxidative desulfurization | 49 and 50 | |
[BPy]4W10O32, [BMIm]4W10O32 | Alcohol oxidation | 51 | |
(P6,6,6,14)4[W10O32] | Olefin/alcohol oxidation | 52 and 53 | |
(P6,6,6,14)4[W10O32] | Selenoether oxidation | 54 | |
Peroxoniobate anion-based ILs | [DMIm]0.1·Nb2O7·2H2O; [TTA]0.08·Nb2O7·2H2O. | Epoxidation | 55 |
[A+][Nb![]() |
Epoxidation | 56 | |
[TBA][NbO(OH)2(R)] (TBA = tetrabutylammonium; R = lactic acid, glycolic acid, malic acid) | Epoxidation | 57 | |
[TBA][LA]-stabilized Nb oxoclusters | Epoxidation & sulfide oxidation | 58 | |
Nb-OC@TBAF-0.5 | Epoxidation | 59 | |
18-Crown-6 and ammonium peroxoniobate (NH4–Nb) | Epoxidation | 60 | |
Peroxotantalum anion-based ILs | [P4,4,4,n]3[Ta(O)3(η-O2)], P4,4,4,n = quaternary phosphonium cation, n = 4, 8, and 14 | Epoxidation | 61 |
[P4,4,4,4]3[Ta(η2-O2)3(CO4)] | Epoxidation | 62 | |
Peroxovanadium anion-based ILs | ([TBA][Pic])-stabilized vanadium oxo-clusters (Pic = picolinate ions) | Alkane oxidation | 63 |
[BIm][Pic](Bim = 1-butylimidazolium)-stabilized vanadium oxo-cluster | Selective oxidative cleavage of β-O-4 lignin model compounds | 64 | |
Peroxotitanium anion-based ILs | Ti oxo-HSO4 | Oxidative desulfurization | 65 |
Keggin structure POM-based IL | [PEG-containing quaternary ammonium][PW12O40] | Electrochemistry | 20 |
[Tetraalkylphosphonium] Keggin | Electrochemistry | 27 and 28 | |
[MIMPS]3[PW12O40], [PyPS]3[PW12O40], [TEAPS]3[PW12O40] | Esterification | 66 | |
[BMIm]3[PW12O40] | Epoxidation | 67 | |
[Dopy]3[PW12O40] | Epoxidation | 68 | |
[DEDSA]3[PW12O40] [DEDSA]3[PMo12O40] | Oxidation of alcohols | 69 | |
Chiral IL-[PW12O40] | Asymmetric oxidation | 70 | |
[Im-PEG-Im]1.5[PW12O40] | Oxidation of benzyl alcohol | 71 | |
[Im-PEG-Im][HPW12O40] | Esterification | 72 | |
[Im-PEG-Im]1.5[PO4(W(O)(O2)2)4] | Epoxidation | 73 | |
[BMIm]3[PO4(W(O)(O2)2)4] | Oxidation of alcohols | 74 | |
Ni[MIMPSH][PW12O40] | Acetalization of benzaldehyde with ethylene glycol | 75 | |
[n-C16H33N-(CH3)3]4Na3PW11O39 | Epoxidation | 76 | |
[C12MIm]5PTiW11O40, [CTA]5PTiW11O40, [TBA]5PTiW11O40 | Epoxidation | 77 | |
(ODA)4PMo11VO40 | Oxidation of benzyl alcohol | 78 | |
[MIMPS]NH4−NPMo11VO40 (N = 1–4), [PyPS]3HPMo11VO40, [TEAPS]3HPMo11VO40, and [BMIm]3HPMo11VO40 | Cellulose into formic acid | 79 | |
[HC4Im]3PMo12O40, [HC4Im]5PV2Mo10O40, [HC2Im]5PV2Mo10O40, [HC4Im]4SiMo12O40 | Lignin depolymerization | 80 | |
[PyBS]5PV2Mo10O40 | Cellobiose to formic acid and levulinic acid | 81 | |
Pyridinium cation-PMo10V2O40 | Alkane oxidation | 82 | |
[BMIm]4[Ti(H2O)TiMo11O39] | Degradation of polyethylene terephthalate | 83 | |
[BMIm]4[Ti(H2O)TiMo11O39] | Transesterification | 84 | |
Co4PW–PDDVAC (a porous POM-based composite) | Isolation of proteinase K | 85 | |
Lindqvist structure | [Tetraalkylphosphonium] Lindqvist | Electrochemistry | 28 |
[TBA]2Mo6O19 and [TBA]2W6O19 | Electrolytes | 86 | |
[tBu-Hptz]2[Mo6O19] | Epoxidation | 87 | |
POM–IL-anchored single-atom | [(n-C4H9)4N]6[SiW11O39Pd], [(n-C4H9)4N]5[PW11O39Pd] | Hydrocarboxylation of olefins | 88 |
[TOMA6SiW11O39Ru(dmso)], TOMA = methyltrioctylammonium | N-Formylation of amines with CO2 and H2 | 89 | |
Supported POM–IL | [α-PW12O40]3− immobilized on IL-modified polystyrene resin beads (PS–IL–PW) | Alcohol oxidation | 90 |
[PW12O40]3− immobilized on dual amino-functionalized IL-modified MIL-101(Cr) | Alcohol oxidation | 91 | |
PEG–PW11–CMC (carboxymethyl cellulose) | Epoxidation | 92 | |
P8W48@PIL–G | Electrocatalysts | 93 and 94 | |
AILs/POM/UiO-66-2COOH | Esterification | 95 | |
PMo10V2-ILs@MIL-100(Fe) | Epoxidation | 96 |
Peroxoniobates, a noteworthy class of MOC materials, have gained attention for their structural diversity and high nucleophilicity, making them promising catalyst candidates for environment-friendly applications.97 Consequently, a series of Nb-based ILs have been constructed in Hou's group, such as niobium peroxides modified with IL-type 1-dodecyl-3-methylimidazolium hydroxide,55 the first proposed novel Nb-based IL, assigned as [A+][NbO(O–O)(OH)2] (A+ = ammonium cation),56 and a series of Nb-based ILs coordinated by organic carboxylic acid,57 and then a new class of carboxylate ILs-stabilized Nb oxoclusters58 were reported. Moreover, Nb oxoclusters can also be stabilized/modified by readily available organic fluoride salts.59 Furthermore, supramolecular complexations between 18-crown-6 and ammonium peroxoniobate can lead to the supramolecular IL catalysts with suitable hydrophobicity by a direct mixing of 18-crown-6 and NH4–Nb ((NH4)3[Nb(O2)4]) in methanol, which provides a much simpler approach, as compared with that of the previous Nb-based ILs.60
Hou's group also pioneered the development of early examples of ILs based on monomeric peroxotantalate anions.61 Similar to other active POM–ILs, the Ta-based ILs ([P4,4,4,n]3[Ta(O)3(η-O2)], P4,4,4,n = quaternary phosphonium cation, n = 4, 8, and 14) underwent a structural transformation in the presence of H2O2. Pressurization of [P4,4,4,4]3[Ta(O)3(η2-O2)] with CO2 in the presence of H2O2 produced a new class of Ta-based peroxocarbonate IL ([P4,4,4,4]3[Ta(η2-O2)3(CO4)]), which was found to be more superior towards epoxidation to the monomeric peroxotantalate analogs, and the transformation between Ta-peroxocarbonate and peroxotantalate anions was completely reversible, leading to an excellent regeneration of IL catalysts.62
Vanadium oxoclusters have been synthesized through the condensation of peroxovanadium species in the presence of the functionalized IL [TBA][Pic] (TBA = tetrabutylammonium; Pic = picolinate ions) with tunable IL/V molar ratios.63 Similarly, imidazolium IL [BIm][Pic] (BIm = 1-butyl-imidazolium)-stabilized vanadium oxocluster catalysts were prepared as well.64
Ti oxoclusters stabilized by carboxylic acid-functionalized imidazolium-based IL were also fabricated via a solvothermal method.65 Characterization indicated that Ti oxoclusters (Ti oxo-HSO4) existed in the form of subnanosized structure, uniformly dispersed with an average particle size of ca. 1 nm due to the protection role of the ILs. It was found that the coordination of the carboxylic acid functional group of IL with Ti sites could prevent the Ti oxo-HSO4 from aggregation, and on the other hand, HSO4− could play an additional role in stabilizing the subnanosized Ti oxo-HSO4 cluster via electrostatic interaction.
A series of transition-metal (M = Mn, Fe, Co, Ni, Cu) ion-exchanged H3PW12O40-based IL catalysts were synthesized by integrating metal and methylimidazolium propyl sulfobetaine (MIMPS) zwitterionic IL precursors onto H3PW12O40.75 Hybrids comprising a lacunary-type phosphotungstate anion [PW11O39]7− and (PEG-containing) ammonium cations were also investigated.76 Additionally, Ti-substituted POMs ([C12MIm]5PTiW11O40, [CTA]5PTiW11O40, and [TBA]5PTiW11O40) were synthesized and characterized.77 Keggin type H5PV2Mo10O40 and H4PVMo11O40-based POM–ILs were investigated as well due to their wide and high catalytic activity.78,79,81
Combining a Keggin [PW12O40]3− (or Lindqvist ([W6O19]2−)) anion with an appropriate tetraalkylphosphonium can produce POM-based ILs, exhibiting comparable conductivity and viscosity to a previously described inorganic–organic POM–IL hybrid but possess enhanced thermal stability.28 Furthermore, [TBTP]4PW11VO40 and [TBTP]4PMo11VO40 (TBTP = tributyl-tradecylphosphonium), composed of Keggin POMs and tetraalkylphosphonium cation have been synthesized.98 They show layered structures due to the self-assembly of cations and anions through electrostatic interactions and van der Waals forces, and especially they also display reversible phase transformation process below 100 °C. It was indicated that the oxidability of the Mo-containing POM is greater than that of the W-containing analog from the electrochemical study, which provides valuable insight into the further development of POM–ILs.
Besides recent advancements in POM–SACs, several POM–IL–SACs systems were reported also in Hou's group, such as POM–IL–Rh SAC,100 POM–IL Pd SAC,88 and POM–IL–Ru SAC89 catalytic systems. In these materials, the isolated single metal atoms were proved to be incorporated into the POM structure according to analysis. The bulky IL cations, on one hand, function as stabilizers of the single atoms and thus avoid the usage of the organic phosphine ligands; on the other hand, they prevent the aggregation and leaching of the isolated metal atoms. These POM–IL–SACs displayed a unique “pseudo-liquid-phase” behavior and showed efficient activity for catalytic carbonylation reactions. The detailed discussion of Rh-catalyzed hydroformylation to produce aldehydes, Pd-catalyzed hydrocarboxylation to yield carboxylic acids, and Ru-catalyzed N-formylation of CO2 to generate N-formyl compounds will be given in Section 5.4.
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Fig. 3 The combination of the POM with the chiral IL for the asymmetric styrene oxidation with H2O2. Adapted from ref. 70 with permission from Elsevier, copyright 2020. |
Various IL–MOCs, such as peroxotungstate anion- and Keggin structure-based POM–ILs, have shown particular efficiency in catalyzing the epoxidation of olefins. Most of them show reaction-induced phase-separation properties with the system transitioning from a tri-phase to an emulsion and eventually self-precipitating at the reaction's end, facilitating catalyst recovery and reuse.73 To better reuse the hybrid material, the POM–ILs could be immobilized on support materials to get magnetically separable catalysts exhibiting constant activity over at least ten cycles in the epoxidation of olefins with H2O2.48
Ti-substituted POMs ([C12mim]5PTiW11O40, [CTA]5PTiW11O40, and [TBA]5PTiW11O40) were also efficient for catalyzing the epoxidation of various olefins and the heterogeneous nature of catalysis in ethyl acetate media was confirmed by a hot catalyst filtration test.77 It was found the organic countercations significantly affected the catalytic activity, and the stable Ti-based peroxo structure serves as the active species, allowing for multiple catalytic runs without notable loss of activity.
Similar high activity also applies to polyoxoniobate-based POM–ILs. Niobium peroxides modified with IL-type 1-dodecyl-3-methylimidazolium hydroxide demonstrated excellent yields (80–99%) for the epoxidation of allylic alcohols to their epoxides even if the reaction was performed without any other solvent under ice bath conditions.55 The first proposed novel Nb-based POM–IL, designated as [A+][NbO(O–O)(OH)2] (A+ = ammonium cation), showed excellent catalytic activity and recyclability in epoxidizing various allyl alcohols under solvent-free, ice bath conditions using H2O2 as the oxidant.56 It was observed that the formation of an [Nb(O–O)2(OOH)2]− active center promoted the whole reaction through a homogeneous process and also facilitated the recyclability. To broaden the substrate scope from allyl alcohols to more challenging-to-convert olefins, a series of Nb-based POM–ILs coordinated by organic carboxylic acids were designed.57 Subsequently, a new class of carboxylate ILs-stabilized Nb oxoclusters was reported.58 They had an average particle size of 2–3 nm and exhibited extremely high catalytic activity for the epoxidation of olefins and allyl alcohols, using only 50 ppm of catalyst (0.065 mol%), with turnover number (TON) values exceeding 1000, outperforming the same transition metal catalyst (Scheme 3). Furthermore, organic fluoride salts were found to be able to stabilize or modify Nb oxoclusters due to their strong coordination interaction with Nb sites.59 The F atoms also form a hydrogen-bond interaction with the –OH group of the allylic alcohol, favoring the epoxidation reaction. Notably, the supramolecular complexations between ammonium peroxoniobate and 18-crown-6 were designed, demonstrating high catalytic activity and recyclability for olefin epoxidation.60 These supramolecular IL catalysts provide easy access to hydrophobic substrates and represent a novel approach to selective olefin epoxidation.
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Scheme 3 The proposed reaction route for selective oxidation of sulfides and olefins with IL-stabilized Nb oxocluster catalysts. Adapted from ref. 58 with permission from Wiley-VCH Verlag GmbH, Weinheim, copyright 2019. |
Recently, the Lindqvist-type POM [tBu-Hptz]2[Mo6O19] (tBu-Hptz = 2-tert-butyl-5-(2-pyridyl)tetrazole) was studied as epoxidation catalysts using readily available and relatively eco-friendly hydroperoxide oxidants (hydrogen peroxide and tert-butyl hydroperoxide).87 This POM acted as a homogeneous catalyst and could be recycled by employing an IL solvent. It was found that the type of anion of the IL could affect the catalytic performance. Besides, the presence of water in the ILs (in different amounts) is often unavoidable, which may also influence the level of hydration of the anions, the strength of the anion–cation interactions, and the viscosity of the IL medium. On the other hand, one cannot exclude the possibility that ion-exchange might occur between [tBu-Hptz]2[Mo6O19] and the IL, depending on the type of IL.
Meanwhile, the POM-supported IL@core–shell polymer nanoparticles (PS–ImCn–PW4) have been established to offer an efficient Pickering emulsion catalytic system (Scheme 4).102 A series of PS–ImCn–PW4 nanospheres were prepared with cross-linked polystyrene as the core and POM–IL as the shell. Allyl chloride and H2O2 can be emulsified by these nanospheres. The surface properties of the nanospheres can be modulated by changing the carbon chain length of IL, which in turn affects the properties and catalytic performance of the Pickering emulsion. Interestingly, C2–C6 can stabilize O/W-type emulsion, while C8–C12 refers to W/O-type emulsion. This catalytic system can be used for the epoxidation of allyl chloride with low-concentration (9.6 wt%) H2O2 under solvent-free conditions.
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Scheme 4 Epoxidation of allyl chloride with H2O2 on PS–ImCn–PW4 catalyst. Adapted from ref. 102 with permission from American Chemical Society, copyright 2023. |
Overall, the effectiveness of POM–IL-catalyzed epoxidation reactions stems from the cooperative interactions between POMs and ILs, enabling a catalytic system that is efficient, selective, and environmentally friendly.
For example, pairing the task-specifically designed IL-cation of N,N-bis-2-aminoethyl-4,4-bipyridinium with the Keggin-structured vanadium-substituted POM anion [PMo10V2O40]5− can result in organic–inorganic hybrid catalyst, which is a catalytically active and recyclable catalyst for cyclohexane oxidation with H2O2, giving KA oil (a mixture of cyclohexanol and cyclohexanone).82 Another example of alkane oxidation using IL–MOCs was reported in Hou's group. Vanadium oxoclusters were synthesized through the condensation of peroxovanadium species in the presence of a functionalized IL [TBA][Pic] (Pic = picolinate ions) with adjustable IL/V molar ratios.63 The picolinate anion of the IL acted as a ligand to stabilize the oligomeric vanadium oxocluster by coordinating with the vanadium sites, while the cation of the IL played a dual role in charge balancing and fine-tuning the miscibility of the oxocluster in solvents. The molar ratio of IL to V influenced the oligovanadate structure, with the appropriate ratio forming active trimer and dimer configurations. These vanadium oxoclusters exhibited remarkable efficiency as catalysts for the oxidation of cyclohexane, utilizing H2O2 as the oxidant. Notably, a significant 30% total yield of KA oil was achieved without the need of additional co-catalysts, and the catalyst demonstrated recyclability due to the incorporation of the IL component. Further studies on the reaction mechanism indicated that the HO˙ radicals are formed from the adduct of H2O2 and vanadium complex, and then the HO˙ radicals react with alkanes to afford the oxidation products (Fig. 4).
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Fig. 4 IL-stabilized vanadium oxo-clusters catalyzing alkane oxidation. Adapted from ref. 63 with permission from Royal Society of Chemistry, copyright 2020. |
Looking forward, IL–MOC holds promise for alkane oxidation reactions which involve in electron transfer processes, while POMs are well known for their superior redox properties. In the presence of H2O2 or molecular O2, the oxidation of alkanes often proceeds via a radical mechanism. POMs could affect reaction kinetics and selectivity by regulating radical pathway of alkane oxidation. Further research to fully understand these mechanisms and optimize POM utilization in alkane oxidation is still underway.
Early in 2005, the catalytic efficiency of POM–IL [BMIm]3[PO4(W(O)(O2)2)4] in alcohol oxidation using IL [BMIm][BF4] as a solvent was reported.74 The system exhibited several advantages, including a homogeneous reaction mixture, high product yields, minimal solvent consumption, facile product separation, and the ability to recover and recycle the catalyst without a significant reduction in product yield. Later, Keggin-type H3PW12O40-based di-imidazolium IL hybrids were prepared and exhibited reaction-controlled phase transfer properties with the catalysts precipitated from the aqueous system upon the consumption of H2O2 and could be reused several times without loss of activity and selectivity.71 Similar POM–ILs [DEDSA]3[PW12O40] and [DEDSA]3[PMo12O40] (DEDSA = diethyldisulphoammonium) with solvent-responsive self-separative characteristic were investigated for the oxidation of organic alcohols using hydrogen peroxide as an oxidizing agent.69 Due to the varied solubility of the hybrids in different solvents, they can effectively catalyze the oxidation reaction in homogenous conditions and then switch back to the heterogeneous system, finally self-precipitate upon the addition of a suitable solvent at the end of the reaction. This special property makes this method an environment-friendly and simpler way for the oxidation of alcohols to aldehydes and ketones. Additionally, [PW12O40]3− immobilized on IL-modified polystyrene resin beads,90 and into the nanocages of a dual amino-functionalized IL-modified MIL-101(Cr) framework were reported.91 In the latter case, the dual amino-functionalized IL not only enhances the oxidant accessibility due to the formed hydrogen bonds but also results in increased thermal stability.
V-containing Keggin H4PMo11VO40 was functionalized with ammonium cations with different carbon-chain lengths to form a series of POM-based amphiphilic catalysts.78 Their catalytic activities were evaluated in the selective oxidation of benzyl alcohol to benzaldehyde using H2O2 under organic solvent-free conditions. Among the investigated catalysts, (ODA)4PMo11VO40 (ODA: octadecylmethylammonium) exhibited the highest catalytic efficiency for the selective oxidation with a maximum 61% conversion of benzyl alcohol and a 99% selectivity of benzaldehyde, also offering excellent reusability. Besides, the complexes of decatungstate combined with N-butylpyridinium ([BPy]4W10O32) and 1-butyl-3-methylimidazolium ([BMIm]4W10O32) were synthesized in high yields directly from bisulfate-based ILs and used as novel catalysts in the selective oxidation of alcohols to aldehydes or ketones with H2O2.51 Combined with phosphorous cation, the hybrid (P6,6,6,14)4[W10O32] also demonstrated to be a very promising and recyclable catalytic material for alcohol oxidation with acids as the main products under fixed reaction conditions.52,53
POM–IL (P6,6,6,14)4[W10O32] was also proved to be an efficient catalyst for oxidizing perfluoroalkyl selenoethers.54 A series of perfluoroalkyl selenoxides, selenones, and selenoximines were prepared, with the separation and characterization of enantiomers in some cases. The use of Oxone® as an oxidant allowed the production of perfluoroalkyl selenoxides with electron-withdrawing or donating substituents in different positions (ortho, meta, or para). The reaction also works with various perfluoroalkyl chains and substituents with satisfactory to excellent yields. Overall, the use of POM–IL as a catalyst provides access to the underexplored perfluoroalkyl selenoxides. This study represents the first comprehensive report on the preparation of the perfluorinated selenoximine family with good yields.
Thioether oxidation was achieved by carboxylate IL-stabilized Nb oxoclusters.58 These clusters, dispersed in polar organic solvents, exhibited “pseudo” liquid phase behavior, enhancing substrate accessibility to catalytic sites. Specifically, [TBA][lactate]-stabilized Nb oxoclusters demonstrated exceptional activity, with TONs more than 56000 at catalyst loading as low as 0.0033 mol% (1 ppm), which is superior to other Nb-based catalysts. The clusters’ flexibility and swelling behavior in polar solvents facilitated substrate access and product diffusion, showcasing their potential as high-performance catalysts for thioether oxidation and beyond.
It has been demonstrated that POMs can effectively promote the dissolution of wood in ILs while concurrently reducing the lignin content in the resultant cellulose-rich pulp.103,104 It's noteworthy that POMs do not completely degrade lignin into low molecular weight fragments, and they can be reoxidized under mild conditions in IL, albeit with some loss in POM and activity. Importantly, different POM species affect significantly the efficiency of delignification. For instance, [BMIm]3[PW12O40] not only dissolves approximately 30 wt% of cellulosic biomass but also converts biomass into commodity monosaccharides like glucose and xylose.105 Some examples of biomass oxidation using IL–MOCs as catalysts are shown in Table 3.
IL–MOCs | Solvent | Starting material | Products | Ref. |
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[EMIm]4H[PV2Mo10O40] | [EMIm]OAc | Lignocellulosic biomass | Cellulose-rich pulp | 103 |
[BMIm]3[PW12O40] | None | Biomass | Monosaccharides such as glucose and xylose | 105 |
H5PV2Mo10O40 | [HC4Im][HSO4] | Lignin samples extracted from pine and willow | Vanillin and syringaldehyde | 106 |
[HC4Im]3PMo12O40, [HC4Im]5PV2Mo10O40, [HC2Im]5PV2Mo10O40, [HC4Im]4SiMo12O40 | Acidic IL | Alkali lignin | Various aromatic compounds | 80 |
HPMoV–C4C1Im–SO3H | DMSO | 2-Phenoxy-1-phenylethanol | Benzoic acid and phenol | 107 |
[C2COOHC1IM]4H[PV2Mo10O40] | Deionized water | Carbohydrates | Glycolic acid | 108 |
BetH5V2Mo18 | None | Native lignocellulose of pinewood and poplar wood | Ethyl vanillate, ethyl syringate, vanillin, and syringaldehyde | 109 |
[BIm][Pic]-stabilized V2O5 | MeOH | β-O-4 lignin model compounds | Phenols, eaters, and acids | 64 |
[BSmIm]CuPW12O40 | Ethanol–water mixture | Wheat stalk lignin | Diethyl maleate | 110 |
[BSmIm]CuPW12O40 | Ethanol | Raw lignocellulosic biomass | Diethyl maleate | 111 |
[PyBS]5PV2Mo10O40 | H2O | Cellobiose/cellulose | Formic acid and levulinic acid | 81 |
[MIMPS]3HPMo11VO40, [PyPS]3HPMo11VO40, [TEAPS]3HPMo11VO40, [BMIm]3HPMo11VO40 | H2O | Cellulose | Formic acid | 79 |
Since lignin is resistant to conversion due to its complex structure and stable linkages, acid-catalyzed lignin degradation to phenolic monomers has gained great interest due to its potential for producing biofuels and chemicals.112 Back in 2016, Welton et al. used acidic H5PV2Mo10O40 as a catalyst coupled with protic IL [HC4Im][HSO4] as the solvent, together with molecular oxygen and hydrogen peroxide to depolymerize lignin samples extracted from pine and willow.106 Besides phenols and functionalized aromatics, vanillin and syringaldehyde were the main products extracted from the IL. This system succeeds in the synergistic properties of ILs to depolymerize lignin and the remarkable properties of the POM to oxidize the lignin fragments into useful platform chemicals. Exchanging the protons with imidazolium cations produced [HC4Im]5PV2Mo10O40 and [HC2Im]5PV2Mo10O40 hybrids, which also showed high efficiency in the oxidation of lignin fragments into platform compounds in aqueous acidic ILs solutions.80 Lignin conversion could reach to 76% with 77% selectivity of ketone products (acetovanillone, 3-methoxyphenol, and 4-methylcatechol). With [HC4Im]3PMo12O40 as a catalyst produced phenolic products (mainly m(p)-cresol, veratrole, vanillin). It was found the POM–IL type and the IL acidity had a big influence on the reaction process. The lignin molecule not only had intermolecular hydrogen bonds and π–π stacking with the imidazole ring, but also formed stronger hydrogen bonds with POM anions, thus making the lignin structure more flexible and easier to depolymerize. Later, a series of POM–ILs were reported for the selective cleavage of the β-O-4 linkage to value-added aromatic chemicals under mild conditions. Lv and Yang et al. reacted H5PV2Mo10O40 with 1-methyl-3-(4-sulfobutyl)-1H-imidazolium (C4C1Im–SO3) zwitterions to form the HPMoV–C4C1Im–SO3H POM–IL assembly,107 which could also selectively and effectively convert various β-O-4 lignin models into aromatic acids and phenols under mild homogeneous conditions. It could be precipitated by the addition of ethyl acetate to the homogeneous post-reaction solution, thus could be reused for five runs. Similarly, IL [C2OHC1Im]Br (1-(hydroxyethyl)-3-methylimidazole bromide) was assembled with H5PVnMo12−nO40 (n = 1–3) to form POM–ILs with different V molar ratios.108 Among them, [C2COOHC1Im]4PVMo11O40 could oxidize glucose and its upstream biomass derivatives to glycolic acid under O2 with 88% conversion and 61% selectivity, which is even applicable to the oxidation of raw lignocellulose.
Deep eutectic solvent cation betaine was combined with Dawson-type H6V2Mo18O62 to form BetH5V2Mo18O62 material, and it could be used as a trinitarian catalyst for one-pot lignocellulose transformation.109 The incorporation of Bet+ cation with POM anion not only increases the activity due to the strong hydrogen bonding interactions between the Bet+ cation and substrate 2-phenoxy-1-phenylethanol but also forms a micro-environment that concentrates solid lignocellulose to overcome mass-transferring barriers. Furthermore, the Bet+ endowed H6V2Mo18O62 with temperature responsibility, ensuring the recyclability of BetH5V2Mo18O62.
Besides acidic HPMoV, neutral vanadium pentoxide stabilized by IL is also efficient for biomass oxidation. Hou et al. used imidazolium IL [BIm][Pic] to stabilize the vanadium oxocluster catalysts, and the catalyst showed superior activity for one-step selective oxidation to cleave the β-O-4 linkage of lignin model compounds to phenols, eaters, and acids.64 It was found the presence of mixed-valence state of V4+ and V5+ in V oxocluster catalysts was crucial for enhancing the catalytic activity, and the oligomeric states of V species could be tuned by adjusting the molar ratio of IL [Bim][Pic] to V. Especially, 1-butylimidazolium also played a facilitating role in the cleavage of C–O bonds by the action of the protonated IL cations. Notably, the catalyst can be recycled with the catalytic activity did not decrease significantly even after five cycles (Fig. 5). This catalytic system demonstrates a new approach for the selective aerobic oxidation of β-O-4 lignin without any co-catalysts.
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Fig. 5 IL-stabilized vanadium oxocluster catalysts for selective oxidative cleavage of β-O-4 lignin model compounds. Adapted from ref. 64 with permission from American Chemical Society, copyright 2023. |
Meanwhile, POM–IL [BSmIm]CuPW12O40 catalytic systems have been developed for the production of diethyl maleate in Li's group.110,111 Under optimized conditions, 94% wheat stalk lignin was oxidized with 73% diethyl maleate selectivity over [BSmIm]CuPW12O40via oxidative ring cleavage of lignin, followed by in situ esterification in one pot.110 A series of phenol, guaiacol, syringol, and their derivatives could be oxidatively converted into diethylmaleate. Later, to broaden the substrate scope, a one-step selective conversion of raw lignocellulosic biomass directly to diethyl maleate over the [BSmIm]CuPW12O40 catalyst was proposed.111 All major fractions of lignocellulose could be converted simultaneously into diethyl maleate with high selectivity. It was found that the relatively low incorporation of the Cu2+ sites in [BSmIm]CuPW12O40 (in comparison with that of CuHPW12O40) gives vacant orbitals for molecular oxygen, which is responsible for the excellent catalytic activity. Additionally, the [BSmim]CuPW12O40 could be easily recovered from the mixture after the reaction by simple temperature control.
One-pot transformation of cellulose directly into formic acid (FA) and levulinic acid (LA) is possible via vanadium-containing POM–IL catalysts.113 A relatively high selectivity of LA (46.3%) and FA (26.1%) together with 100% cellobiose conversion could be obtained by using [PyBS]5PV2Mo10O40 as a catalyst.81 It could be easily recycled four times without a significant loss of activity. Meanwhile, a similar POM–IL [MIMPS]3HPVMo11O40 was applied in the conversion of cellulose into FA with over 50% FA yield and a high FA concentration of ∼10% in aqueous solution.79 Notably, these POM–ILs acted as bifunctional catalysts, with –SO3H functionalized cations catalyzing cellulose hydrolysis to glucose and POM anions catalyzing glucose oxidation to FA.
Overall, acidic IL–MOC materials are efficient for biomass oxidation, representing an innovative approach with significant implications for sustainable energy and chemical production. The synergistic effect between the IL cation and MOC anion facilitates the controlled oxidation of biomass components, such as lignocellulosic materials, under mild conditions to value-added products without any additives.
Recently, Hou's group developed novel carboxylic acid-functionalized imidazolium IL-stabilized Ti oxoclusters.65 These oxoclusters, well stabilized in ILs and highly dispersed in methanol, showed excellent desulfurization efficiency under mild conditions. Complete removal of sulfur compounds from model oil was achieved using the Ti oxo-HSO4 catalyst, with methanol identified as the most effective extractant. It was indicated that Ti–OOH species were indeed the active species and responsible for the sulfur removal on the Ti oxocluster catalysts. Moreover, the HSO4− anion could activate the Ti–OOH species by forming hydrogen bonds, facilitating the electrophilic oxygen transfer in the ODS reaction. This strategy provides an alternative and green route for constructing stable MOC catalytic systems (Scheme 5).
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Scheme 5 Proposed mechanism for the extraction and catalytic oxidative desulfurization (ECODS) system catalyzed by Ti oxocluster catalyst. Adapted from ref. 65 with permission from American Chemical Society, copyright 2022. |
Several review papers focusing on ODS reactions using POM–ILs as catalysts have been published, including works by Yu et al.,116 Zhao et al.,117 Ong et al.,118 and Anbia et al.119 Specifically, the reported examples until March 2021 are detailedly summarized by Anbia et al.119 Beyond the commonly studied tungstenphosphoric or phosphomolybdenum-based POM–(P)ILs,120,121 tungstovanadate-based POM–IL [C2(MIm)2]2VW12O40 (MIm = 1-methylimidazolium) was also investigated as a catalyst in ODS with 100% sulfur removal efficiency and sulfone product selectivity in 20 min, with a high turnover frequency (TOF) value (53.2 h−1).122
In addition, the heterogeneous carboxyl-functionalized bilayer POM–IL catalysts were also developed, demonstrating superior activity for ODS (Scheme 6).123 The optimized catalyst, SiO2 (50 nm)–BiIL–PW (Keggin-type), exhibits good amphiphilicity for both sulphur-containing compounds and hydrogen peroxide, thereby providing a quasi-homogeneous microenvironment for the heterogeneous catalysis. Complete sulfur removal can all be achieved for four model fuels free of extractant. It was demonstrated that POM and carrier have significant effects on the catalytic activities. Notably, no decrease in catalytic efficiency was observed even after the eight cycles in scale-up experiments. These results make the catalyst promising for industrial application.
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Scheme 6 The diagram of ODS catalyzed by SiO2–BiIL–CO2H–POM. Adapted from ref. 123 with permission from Elsevier, copyright 2023. |
Besides, SiO2, graphene oxide (GO) was also used as a supported material for POM–IL in ODS reactions.124,125 One example involves the synthesis of POM–ILs with monomer, dimer, and poly IL, and then further loaded on the surface of GO.124 The influences of IL type and carrier on ODS activity were thoroughly investigated. The other example is the covalent immobilization of POM–IL on the amine-modified magnetic GO (APTES-mGO).125 The employed ILs were imidazolium cation-based, with varying alkyl chain lengths (Cn[MIm]Cl, n = 4, 8, 12, and 16). Among these, [C12MIm]5PV2Mo10/APTES-mGO, with a C12 alkyl length chain, showed the highest sulfur removal percentage due to its desirable amphiphilicity, which facilitated a stable Pickering emulsion system, enhancing the contact area between phases and overcoming mass transfer resistance. The emulsion breakage and the catalyst recycling can be achieved using a permanent magnet. Notably, the designed catalyst could be recovered 8 times without significant loss of its catalytic activity.
Phosphovanadomolybdate (V-POM) in other compositions (H7[P2Mo17VO62], H8[P2Mo16V2O62] and H9[P2Mo15V3O62]) were combined with amphiphilic PIL (Scheme 7).21 These composites served as efficient heterogeneous catalysts for the direct hydroxylation of benzene to phenol with H2O2 in the liquid phase. The synergistic catalytic effect between the V-POM anion and carboxylic acid-functionalized PIL cation framework contributed to the high catalytic performance. Meanwhile, H2PMo11VO402− anion-based imidazolium IL was also employed as a catalyst for the hydroxylation of benzene by H2O2 without using a solvent.134 The homogeneous emulsion formed by the catalyst and substrates during the reaction facilitated the catalytic process. After the reaction, the catalyst could self-precipitate from the reaction media and proved to be recyclable. Moreover, mesoporous MCM-41135 and functionalized chloromethylated polystyrene136 were employed as supported materials for V-POMs to enhance the recyclability of the active species.
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Scheme 7 Direct hydroxylation of benzene to phenol with H2O2 catalyzed by three porous functionalized PIL/phosphovanadomolybdate ionic composites. Adapted from ref. 21 with permission from Wiley-VCH Verlag GmbH, Weinheim, copyright 2020. |
In addition to V-POMs, vanadium oxocluster itself is also effective for hydroxylation of benzene. For example, VxOy supported on PIL (VxOy/PIL) demonstrated much higher catalytic performance than the analogous catalyst VxOy/P, prepared with only the polymer support (P), without the IL. The superior catalyst performance of VxOy/PIL might be assigned to a higher specific surface area, stronger absorbent ability, and more active sites than the smooth and bulky VxOy/P.137 Furthermore, the hydrophobic side chain of the IL in the catalyst was beneficial for the access of benzene and the removal of the generated phenol from the surface of the catalyst, which also played an important role in improving the catalytic performance. In addition, the catalyst is highly stable and recycled at least three times without a significant decline in the phenol yield.
Meanwhile, POM–IL immobilized on MOF was prepared and applied for the esterification of acidic vegetable oil.95 MOFs (UiO-66-2COOH) were functionalized with Keggin-type POM acids first and then further incorporated with sulfonated acidic ILs. The resulting ILs/POM/UiO-66-2COOH solid catalyst combines Brønsted and Lewis acid sites, exhibiting a high surface area, increased acidity, and exceptional catalytic activities with long-term stability and reusability for one-pot biodiesel production via esterification of the low-cost acidic oils. Therefore, this solid catalyst has potential for practical application in the catalytic biodiesel production, and would provide a guide for selecting suitable POM–ILs for the preparation of solid acid catalysts.
Catalysts | Amount/g | T/°C | t | Conv./% | Yield/% | Reuse cycles | Ref. | ||
---|---|---|---|---|---|---|---|---|---|
Cat. | Sub. | Sol. | |||||||
Substrate: polyethylene terephthalate (PET), product: bis(hydroxyethyl) terephthalate (BHET), solvent: ethylene glycol. | |||||||||
Na12[WZn3(H2O)2(ZnW9O34)2] | 0.025 | 5.0 | 20.0 | 190 | 40 min | 100 | 84 | Four | 138 |
[PyPs]6[WZn3(H2O)2(ZnW9O34)2] | 0.04 | 5.0 | 20.0 | 195 | 0.5 h | 100 | 85 | Five | 139 |
[BMIm]4[Ti(H2O)TiMo11O39] | 0.21 | 5.0 | 30.0 | 190 | 5 h | 100 | 85 | Six | 83 |
Polyethylene terephthalate (PET) is widely used in daily life, particularly in food packaging. To decrease environmental pollution and resource wastage issues, PET degradation is of great significance. Compared with the physical and hydrolysis methods, PET alcoholysis is a more favored degradation approach. Lu et al. found that transition-metal-substituted POMs Na12[WZnM2(H2O)2(ZnW9O34)2] (M = Zn2+, Mn2+, Co2+, Cu2+, Ni2+) can efficiently catalyze PET alcoholysis,138 with superior activity than transition single-substituted catalyst K6SiW11ZnO39(H2O) due to their specific sandwich structure, increased active sites, and outstanding coordination ability with PET carbonyl oxygen. Then they synthesized a series of POM–ILs with different anion–cation molar ratios to investigate the possible impact of the layer spacing of the catalyst on PET degradation since polymer degradation simultaneously requires the active site of the catalyst to match multiple reaction sites in the polymer long chain (Scheme 8).139 It was found that the adjustable layer spacing (1.00–1.63 nm) in these POM–ILs, achieved by incorporating [WZn3(H2O)2(ZnW9O34)2]12 anion with organic cations such as pyridinium (Py), 3-(pyridine-1-ium-1-yl)propane-1-sulfonate (PyPs), 1-(3-sulfonic group) trimethylamine (TEAPs), and 1-methyl-3-(3-sulfopropyl)imidazolium (MIMPs), was a crucial parameter. When the catalyst layer spacing was adjusted to coincide with the spacing of 1.32 nm between the carbonyl active sites on both sides of the PET benzene ring, the active sites of the catalyst (Zn atom in the POM and N atom in the pyridine ring) corresponded exactly to the reactive sites in PET's long chain. This enabled the shearing of the carbonyl functional group at a fixed point on the nanoscale, promoting fast and complete reaction. Thus the transformation of POM into POM–IL not only enhances thermal stability but also introduces anionic and cationic synergistic catalysis. Under optimal conditions, the proposed catalytic strategy achieved complete PET degradation in just 30 minutes, with a remarkable 85% yield of bis(hydroxyethyl) terephthalate (BHET). Impressively, the BHET yield remained consistently above 85% even after five cycles, highlighting the sustainability and robustness of the approach. This innovative strategy of precisely modulating the spacing of the catalytic active site represents a significant advancement in the field of PET alcoholysis, which also provides a new approach for designing functional catalytic materials tailored for depolymerizing waste plastics into high value-added chemicals.
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Scheme 8 The schematic illustration of the possible mechanism of PET alcoholysis with POM–IL. Adapted from ref. 139 with permission from Wiley-VCH Verlag GmbH, Weinheim, copyright 2023. |
Furthermore, titanium-centered POM–ILs, denoted as [BMIm]4–6[M(H2O)TiMo11O39] (M = Cu2+, Fe2+, Pb2+, Ti4+, and Zn2+), were evaluated in the alcoholysis of bottle-grade PET, using waste mineral water bottles as samples.83 Among the catalysts, [BMIm]4[Ti(H2O)TiMo11O39] exhibited optimal catalytic efficacy, achieving a 100% alcoholysis rate and a 85% BHET yield with a catalyst dosage of 0.6% at 190 °C for 5 hours. Impressively, even after six cycles, the alcoholysis rate remained as high as 94% with 76% BHET yield. These findings highlight the potential of the prepared POM–IL catalysts in catalyzing the degradation of bottle-grade PET, offering a promising avenue for sustainable waste management. Meanwhile, this POM–IL [BMIm]4[Ti(H2O)TiMo11O39] behaved as a phase transfer catalyst for the transesterification reaction between dimethyl carbonate and phenol to synthesize diphenyl carbonate.84 Under optimized conditions, the phenol conversion reached 46%, and the overall selectivity of mono- and di-phenyl carbonate products was 99%. Moreover, the catalyst could be reused four to five times due to its characteristic of a “homogeneous phase at high temperature and separation at low temperature”.
The POM–IL catalytic systems demonstrate the ability to activate CO2 through cooperative interactions between the POM and IL components. The POM acts as a redox-active entity, facilitating electron transfer during the activation of CO2, while the IL provides a stabilizing medium for the POM and influences the solubility and reactivity of CO2. The catalytic transformations of CO2 using POM–IL catalytic systems have been summarized previously,140,141 which demonstrates the advantages of POM-based ILs in the emerging field of CO2 utilization, e.g. CO2 capture, the cycloaddition of CO2 to epoxides, and reduction of CO2. Here, we mainly focus on new catalytic designing and new catalytic effects in CO2 utilization by POM–IL catalytic systems in recent three years.
Catalytic hydroformylation is a pivotal industrial process in which alkenes react with carbon monoxide and hydrogen, typically in the presence of a transition metal catalyst like rhodium, to yield aldehydes. The POM–IL–Rh SAC (MTOA)5[SiW11O39Rh] (MOTA = methyltrioctylammonium cation) is active for the hydroformylation of alkenes to produce aldehydes at an ultralow loading of Rh (ca. 3 ppm) (Fig. 6), displaying exceptional catalytic activity and long storage stability.100 For styrene hydroformylation, both the conversion and the aldehyde yield can reach almost 99%, and a TOF as high as 9000 h−1 was obtained without using any phosphine ligand. This IL catalyst, miscible with n-hexane at reaction temperatures, contributed to the exceptionally high activity, while the bulk organic cation not only prevented active Rh species from leaching during reactions but also stabilized Rh1 species from reducing into Rh0 species.
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Fig. 6 Ionic liquid-immobilized rhodium single-atom catalyst for hydroformylation. For the ball-and-stick structure of the [SiW11O39Rh(H2O)]5− framework: Si, W, O, Rh and H atoms are shown in pink, blue, red, green and gray spheres, respectively (inset). Adapted from ref. 100 with permission from Wiley-VCH Verlag GmbH, Weinheim, copyright 2022. |
Catalytic hydrocarboxylation is a transformative process wherein alkynes or alkenes undergo carboxylation in the presence of carbon monoxide and water, typically facilitated by transition metal catalysts like nickel or palladium. The Keggin-type POM–IL–Pd SACs [(n-C4H9)4N]6[SiW11O39Pd] and [(n-C4H9)4N]5[PW11O39Pd], with Pd atoms incorporated into the POM structure, exhibited high efficiency in the olefin hydrocarboxylation reaction under two-phase conditions, achieving up to 95% conversion of styrene and 95% carboxylic acid yield at 110 °C.88 The tetrabutylammonium cation played a crucial role in stabilizing the Pd catalyst, allowing for easy storage and consecutive catalytic recycling. Mechanistic studies revealed a reaction pathway proceeding through the “Pd–H” pathway, with the Pd SAC system exhibiting superior performance and stability even without phosphine ligands. This catalytic system offers advantages such as broad substrate suitability and easy quantitative recovery, with ongoing efforts to further enhance its efficiency.
The catalytic N-formylation of CO2 involves the incorporation of CO2 into organic substrates to form N-formyl compounds. The POM–IL–Ru SAC ([TOMA6SiW11O39Ru(dmso)], TOMA = methyltrioctylammonium) with the single-atom Ru, confirmed to be anchored into the framework of the POM, demonstrated high efficiency in the N-formylation of amines with CO2 and H2 in toluene-IL biphasic media (Fig. 7).89 The binary IL system, involving the POM-based IL and [BMIm]OAc, exhibited a sponge-like structure, ensuring efficient contact between catalytic sites and substrates. Experimental results and the DFT calculations indicated a pathway that involves formate intermediates, and the process is a three-component (morpholine, Ru–POM–IL, and BMImOAc) synergistic process, which significantly reduces the reaction energy barrier and enhances the conversion and yield, showcasing the catalytic system's advantages in terms of high efficiency, robustness, and recyclability in N-formylation reactions.
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Fig. 7 Ruthenium single-atom anchored in POM–ILs for N-formylation of amines with CO2 and H2. Adapted from ref. 89 with permission from American Chemical Society, copyright 2023. |
Additionally, Hou's group developed new-type organic ammonium cation-stabilized Nb oxoclusters, which can efficiently catalyze the reductive amination of CO2 with amines using PhSiH3 as a reducing agent.142 The reaction proceeds smoothly under ambient conditions and affords formamides with excellent selectivity. Notably, the Nb oxocluster catalysts showed good recyclability in consecutive recycles and wide substrate suitability. Mechanistic studies suggest that the N-formylation reaction proceeds via a silyl formate reaction path. The organic methyltrioctylammonium cation could not only prevent Nb oxoclusters from aggregation, but also provide the suitable hydrophobic environment to accelerate the accessibility of organic reactants to the catalytic active centers. As a result, the POM–IL catalyzed CO2 activation showcases the potential for developing sustainable and environmentally friendly processes for utilizing CO2 as a carbon source, contributing to the field of green chemistry and carbon capture and utilization.
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Fig. 8 Schematic illustration of the process for the synthesis of multifunctional catalyst Pd/POM–IL@SiO2 (Pd/Hx[OMIM]3−xPW12O40@SiO2, x = 1, 2, 3) and its structure. Adapted from ref. 150 with permission from Royal Society of Chemistry, copyright 2018. |
In quinoline hydrogenation, our recent investigation demonstrates that the POM anion-stabilizing Pt nanocatalysts can greatly facilitate to forming oxygen vacancies adjacent to Pt0 species on POM catalysts.147 The oxygen vacancy concentration of the POM catalyst exhibited a decisive role in the catalytic hydrogenation of quinoline in the aqueous media. Further studies indicated H2O actually participated in the hydrogenation and acted as an indirect hydrogen source. Especially, H2O was adsorbed at oxygen vacancies and underwent homolytic cleavage into OH− and H− species, and the forming interfacial platinum–hydroxyl species can efficiently promote the heterolytic H2 dissociation for hydrogenation. It was noteworthy that organic cations exert a remarkable impact on oxygen vacancy density, which implies that the catalytic performance enables it to be tuned by the cation structure.
POM–ILs based on the phosphomolybate anion [PMo12O40]3− and organic imidazolium, pyridinium, and phosphorous cations were prepared and used as electrochromic materials with deep eutectic solvents as electrolytes to design efficient electrochromic devices.155 Additionally, Mo-based electrodes derived from POM–IL, denoted as N/P-MoO2@carbon, were designed and exhibited advanced electrochemical performance.156 The contents of C, N, P, and the pore geometry of N/P-MoO2@carbon networks can be easily tailored by adjusting the precursor's cyano group position, resulting in enhanced lithium storage performance. Moreover, composite catalysts composed of Pd, POM–IL, and N,P-codoped coal-based carbon fibers have been developed, exhibiting superior activity for formic acid electrooxidation compared to non-enhanced Pd/N, P–C composites.157 This enhanced performance is attributed to the synergistic effects of the POM anion and the longer alkyl chains in the imidazole IL, leading to smaller catalyst particles and increased active sites being exposed, thus better electrochemical performance.
Furthermore, a Co-based CoW12–IL–graphene oxide system was reported as an efficient electrocatalyst for water oxidation in neutral pH conditions (Scheme 9).158 This new hybrid material was prepared by covalent attachment of IL species to graphene oxide and then electrostatic interaction of supported imidazolium cations with Keggin type [CoW12O40]6− polyanions, it is the strong electrostatic interaction between imidazolium cations and CoW12 species prevents the leaching of catalytically active species into the solution. It exhibited remarkable stability which demonstrated the efficiency and stability of the oxygen evolution reaction process in neutral pH.
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Scheme 9 Schematic exhibition of the preparation of CoW12–IL–graphene oxide hybrid nanomaterial. Adapted from ref. 158 with permission from Elsevier, copyright 2022. |
Overall, the tunable nature of IL–MOCs allows for precise control over the electrochemical properties, making them suitable for applications such as energy storage devices, sensors, and electrocatalysis. The synergistic effects between the IL environment and the MOCs enhance the stability and conductivity of the electroactive materials, paving the way for advancements in electrochemical technologies with improved efficiency and performance.
ILs can not only stabilize but also regulate MOC structure, reactivity, and catalytic performance. By interacting with MOCs, ILs can alter MOCs’ coordination environment, structural arrangement and even oxygen vacancy density. This interaction may lead to changes in the size, shape, and surface properties of MOCs. Additionally, ILs can affect the redox behavior of MOCs by donating or accepting electrons, and they can also modify the acidity, basicity, hydrophilicity or hydrophobicity. Meanwhile, it has been proved that the composition and morphology of MOCs are quite significant factors affecting the catalytic efficiency. Thus ILs can ultimately influence MOCs’ catalytic activity and selectivity. Furthermore, ILs provide a unique solvent environment that surrounds MOCs, influencing their solubility, stability, and accessibility to reactants. The solvation effects of ILs can enhance the dispersion of MOCs, increase their surface area, and facilitate the diffusion of reactant molecules to active sites.
IL–MOCs offer higher catalytic efficiency with increased reaction rates, higher selectivity, and overall improved performance in catalytic processes. They also exhibit improved stability due to the high thermal stability and non-volatility characteristics of ILs, allowing for easy separation and better recyclability. Additionally, the versatility and flexibility of IL–MOCs, stemming from ILs’ tunability, make them applicable for various types of catalytic reactions, while their green solvent properties reduce environmental impact by simplifying reaction conditions, minimizing waste generation, and lowering overall costs. Moreover, ILs are non-volatile, which means they are less likely to evaporate than traditional solvents. This makes them safer and more attractive to use than traditional solvents, particularly in industrial applications where solvent loss is a concern.
However, there are still some challenges to overcome, such as the cost and availability of ILs, as they are currently more expensive than traditional solvents. Further research is needed to develop new ILs with the desired properties. Additionally, there is still a need for a better understanding of the underlying chemistry of IL–MOCs. Especially, understanding the role of IL in stabilizing/regulating MOCs will foster new discoveries of catalytic reactions that are accelerated by IL–MOC catalysts. This will be essential for developing new and improved IL–MOCs for a wider range of applications. Despite these challenges, IL–MOCs are a promising new class of catalysts with a wide range of potential applications.
In summary, IL–MOCs are a fascinating class of materials with promising catalytic applications. The unique combination of MOCs and ILs brings forth several noteworthy advantages in various chemical transformations. As researchers continue to explore the potential of IL–MOCs, we can anticipate even more remarkable applications in the near future. For example, new IL–MOC combinations could be explored to expand the catalytic scope and improve efficiency. This involves synthesizing and characterizing a diverse range of IL–MOCs to identify promising candidates for various chemical transformations. Meanwhile, detailed mechanistic studies are essential to understand the reaction pathways and active sites involved in IL–MOC catalysis. Techniques such as spectroscopy, microscopy, and computational modeling can provide valuable insights into the fundamental processes occurring at the molecular level, aiding in catalyst design and optimization. Moreover, the stability and recyclability of IL–MOC catalysts could be further enhanced for practical applications and sustainability. Beyond catalytic oxidation reactions, IL–MOCs already offered exciting opportunities for emerging applications such as biomass conversion, CO2 utilization, and renewable energy storage. Future studies should explore these novel application areas and assess the feasibility and potential impact of IL–MOC catalysis. Although the field of IL–MOC hybrids is still young and there are still some challenges to overcome, the utilization of IL–MOCs is preferable from the viewpoint of both industry and society as they align more closely with the principles of green chemistry.
IL | Ionic liquid |
MOC | Metal oxocluster |
IL–MOCs | IL-stabilized metal oxoclusters |
PIL | Polymeric ionic liquid |
POMs | Polyoxometalates |
POM–ILs | POM-based ILs |
HPAs | Heteropoly acids |
PEG | Polyethylene glycol |
[Hbet][NTf2] | Protonated betaine bis(trifluoromethylsulfonyl)imide |
EMIm | 1-Ethyl-3-methylimidazolium |
BMIm | 1-Butyl-3-methylimidazolium |
Gr | Graphene |
HDIm | Protic N-dodecylimidazolium |
MNP | Magnetic nanoparticles |
BPy | N-Butylpyridinium |
P4,4,4,n | Quaternary phosphonium cation |
DMIm | 1-Dodecyl-3-methylimidazolium |
TTA | Tetradecyl trimethyl ammonium |
TBA | Tetrabutylammonium |
NH4–Nb | Ammonium peroxoniobate |
Pic | Picolinate ions |
Bim | 1-Butylimidazolium |
MIMPS | Methylimidazolium propyl sulfobetaine |
Py | Pyridinium |
PyPS | 3-(Pyridine-1-ium-1-yl) propane-1-sulfonate |
TEAPS | 1-(3-Sulfonic group) trimethylamine |
Dopy | N-n-Dodecylpyridinium |
Im-PEG-Im | PEG-functionalized alkylimidazolium |
C12MIm | 1-Dodecyl-3-methylimidazolium |
CTA | Cetyltrimethyl-ammonium |
ODA | Octadecylmethylammonium |
Co4PW–PDDVAC | A porous POM-based composite |
t Bu-Hptz | 2-tert-Butyl-5-(2-pyridyl)tetrazole |
TOMA | Methyltrioctylammonium |
PS–IL–PW | [α-PW12O40]3− Immobilized on IL-modified polystyrene resin beads |
CMC | Carboxymethyl cellulose |
AIL | Acidic IL |
SACs | Single-atom catalysts |
POM-SACs | POM-supported SACs |
MOFs | Metal–organic frameworks |
DEDSA | Diethyldisulphoammonium |
BSmIm | –SO3H-functionalized imidazolium cation |
[C2OHC1Im] | 1-(Hydroxyethyl)-3-methylimidazole |
POMs-ILs@MOFs | MOF encapsulated POMs-based ILs |
TON | Turnover number |
TOF | Turnover frequency |
HPMoV | H5PMo10V2O40 |
FA | Formic acid |
LA | Levulinic acid |
ODS | Oxidative desulfurization |
PET | Polyethylene terephthalate |
BHET | Bis(hydroxyethyl) terephthalate |
Footnote |
† These authors contributed equally to this work. |
This journal is © The Royal Society of Chemistry 2024 |