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Review

Keggin Heteropolyacid Salt Catalysts in Oxidation Reactions: A Review

by
Marcio Jose da Silva
*,
Alana Alves Rodrigues
and
Neide Paloma Gonçalves Lopes
Chemistry Department, Federal University of Viçosa, Viçosa 36590-000, Brazil
*
Author to whom correspondence should be addressed.
Inorganics 2023, 11(4), 162; https://doi.org/10.3390/inorganics11040162
Submission received: 12 February 2023 / Revised: 25 March 2023 / Accepted: 27 March 2023 / Published: 11 April 2023

Abstract

:
Keggin heteropolyacids (HPAs) are metal–oxygen clusters with strong Bronsted acidity. The conversion of HPAs to metal salts can result in Lewis acidity, improving their performance in oxidation reactions. In this review, the main routes for the synthesis of Keggin-type heteropolyacids salts, as well their use as catalysts in oxidation processes of a plethora of substrates, such as monoterpenes, olefins, aldehydes, terpene alcohols, and aromatics, are described. Green reactants such as hydrogen peroxide and molecular oxygen are used as oxidants. These reactions are of interest to several industries because they can be used to produce drugs, additives, fragrances, and fine chemicals. The high efficiency of Keggin HPA with green oxidants contributes to a reduction in the environmental impact of these processes, as preconize the principles of green chemistry. Moreover, Keggin HPAs can be converted to bifunctional catalysts by the modification of their structure, total or partial replacement of their protons with Lewis acid metal cations, or the introduction of these cations into the Keggin anion structure, replacing the addenda atoms (i.e., W and Mo). Aspects linked to the synthesis and characterization of these catalysts are discussed herein, with emphasis on infrared spectroscopy and powder XRD patterns. The most recent advances achieved in the development of catalytic oxidation systems based on Keggin HPA salts are also addressed.

Graphical Abstract

1. Introduction

The development of bifunctional catalysts has attracted attention for economic and environmental reasons [1]. Many bifunctional catalysts have either Lewis or Brønsted acidity functionality, which can promote either acidic or oxidative transformations [2]. Another possible use of the term “bifunctional” is concerning catalysts that can promote hydrogenation and dehydrogenation [3]. Catalysts that can promote reactions for which the main steps require Lewis or Brønsted acid sites are still scarce. Although it is expected that these two types of active sites catalyze different elementary steps within an overall reaction, it is also possible that they participate in the same step.
There are various types of bifunctional catalysts, such as bimetallic catalysts [4]. Normally, these catalysts comprise noble metals as nanoparticles, solid-supported catalysts, and metal oxides [5]. In general, these catalysts have active hydrogenation or oxidation sites [6]. Perovskite oxides are bifunctional catalysts with the general formula ABO3 or A2BO4, where A sites normally represent rare-earth, alkaline-earth, or other large metal cations, while the B sites are transition metal cations. These compounds have been demonstrated to be a class of effective bifunctional catalysts due to their plentiful stoichiometries and crystal structures, as well as multimetal active centers [7]. Bifunctional catalysts frequently combine active metal sites for hydrogenation/dehydrogenation and active acidic sites for protonation/deprotonation steps [8]. Salts containing different counterions can also be used as bifunctional catalysts [9,10].
Keggin heteropolyacids are compounds belonging to the polyoxometalate class that can also be used as bifunctional catalysts [11,12]. Their strong acidity and their structural properties make them easily modulable. Keggin HPAs are solid metal–oxygen clusters with a high strength of Brønsted acidity, and consequently, they can be used as heterogeneous acid catalysts [13,14]. Although soluble in polar solvents, the exchange of HPA protons with large radium cations makes them heterogeneous catalysts. Moreover, their doping with transition metals results in Lewis acidity or redox potential, which are adequate properties for use in acid-catalyzed or oxidative processes [15,16,17,18]. Consequently, Keggin HPA salts have been used in both homogeneous and heterogeneous catalytic reactions [19].
The most widely studied heteropoly catalysts have anions with a typical Keggin structure, as represented by the formula (XM12O40)n−, where X is the central heteroatom (i.e., Si or P), and tetrahedrally is surrounded with oxygen atoms, which are in octahedral environmental coordination with addenda metal atoms, usually Mo6+ or W6+ [20].
In this review, various procedures to prepare Keggin HPA salts are addressed, with an emphasis on those involving unsupported catalysts and a focus on lacunar heteropoly salts, transition metal cation-exchanged salts, and transition metal-doped salts. Beyond synthesis and characterization, special attention is dedicated to describing their applications as catalysts in oxidation and acid-catalyzed reactions.

2. Main Routes to Synthesize POMs Salts

2.1. Synthesis of Metal-Exchanged Phosphotungstic, Phosphomolybdic, and Silicotungstic Acid Salts

Transition metal cation-exchanged salts can be easily synthesized starting from the metathesis of Keggin HPA solution with another solution containing the metal chloride with adequate stoichiometry, according to literature (Scheme 1) [21,22]. In this process, the metal chloride solution is slowly dropped into the Keggin HPA solution; afterwards, the mixture is heated to release water and HCl, resulting in a solid salt, which is dried in an oven at 423 K.
When the metal cation has large ionic radium such as K+, Rb+, or Cs+ ions, the metal-exchanged Keggin HPA salt is precipitated into the reaction solution. Other cations such as ammonium and tetrabutylammonium have been widely used to synthesize the insoluble HPAs [23]. Consequently, when the HPA is insoluble, it is separated through a filtration step [24]. However, if the metal cation has an ionic radium smaller than 1.3 Angstroms, the HPA salt is water-soluble; therefore, separation requires the vaporization of the solvent [25,26].
Figure 1 shows the yield achieved in the syntheses of the metal-exchanged silicotungstic acid salts [27]. In almost all cases, high yields were attained, demonstrating that this is an attractive route to obtain these HPA salts.

2.2. Synthesis of Phosphotungstic, Phosphomolybdic, and Silicotungstic Acids Lacunar Salts

Lacunar Keggin anions are obtained from hydrolyzes of the pristine Keggin HPAs or their salts [28]. The hydrolysis reaction occurs when a NaHCO3 solution is added to the HPA solution. This is a key step because the pH control is straightly linked to the number of MO units removed from the Keggin anions (Scheme 2).
However, this synthesis route requires the presence of the pristine HPA or their salt, which has a saturated anion. Alternatively, it is possible to obtain the Keggin HPA and afterwards their lacunar salt through the one–pot procedure. To do it, solutions containing the synthesis precursors in stoichiometry amount should be gently mixed and then the pH should be adjusted with NaHCO3 solution, resulting in the lacunar heteropolyanion salt. Scheme 3, Scheme 4 and Scheme 5 show these procedures.
It is noteworthy that the lacunar HPAs can be obtained as soluble or insoluble salts, depending on the ionic radius of the metal cation that replaces the protons [29,30].

2.3. Synthesis of Metal-Substituted Lacunar HPA Salts

The doping of lacunar salts with transition metal cations is an efficient strategy to convert these salts into highly active catalysts in oxidation reactions with hydrogen peroxide. Copper, nickel, manganese, vanadium, zinc, and iron are the most common dopants [31,32]. Scheme 6 describes how converting the saturated Keggin heteropolyanion to a lacunar anion and posteriorly to a metal-doped anion.
Charge balancing is done by the counter-ion, which was omitted for clarity. Once more, the solubility of these salts may vary according to the size of the cation. The pH control is a key step herein. An excessive increase in the pH may promote successive hydrolysis of the Keggin anion, and di-or tri-lacunar species can be obtained.

3. Characterization Techniques of Keggin HPA Salts

There are several techniques used to characterize Keggin HPA salts, however, we will emphasize only those more frequently used [33]. Most results were previously obtained by us and the references were adequately cited [26,27,28,29,30,34,35].

3.1. Infrared Spectroscopy

Infrared spectroscopy gives information on the primary structure of Keggin HPAs (i.e., heteropolyanion) [34]. The fingerprint region shows the typical absorption bands assigned to the vibration of chemical bonds involving Si-O, W-Ob-W, W-Oc-W, and W = Od atoms. The subscript distinguishes the oxygen atoms in the function of the position occupied in the heteropolyanion [27].
The profile of infrared spectra of silicotungstate anion remained intact after the protons exchange with metal cations (Figure 2). This indicates that the Keggin structure was preserved after the synthesis of heteropoly salts.
Figure 3 shows a comparison of infrared spectra of pristine HPAs (i.e., H3PW12O40, H3PMo12O40, and H4SiW12O40) and their aluminium-exchanged salts.
The main absorption bands assigned to the vibrations of chemical bonds of Keggin anion seen in the infrared spectra of pristine HPAs were also observed in the spectra of aluminium salts.
The same comparison was also performed with infrared spectra of iron heteropoly salts (Figure 4).
As verified in the infrared spectra of aluminium-exchanged salts, the Keggin anion structure was preserved after the synthesis of the iron-exchanged salts [36].

3.2. Powder X-rays Diffraction Patterns

While infrared spectroscopy provides information about the primary structure of Keggin HPAs (i.e., heteropolyanion), the powder XRD patterns give information on the secondary structure, which comprises the tridimensional arrangement of Keggin heteropolyanions surrounded by cations (i.e., hydronium, di-hydronium, metals) and water molecules [34,35,36,37,38]. Figure 5 displays the primary, secondary, and tertiary structures of the metal-doped heteropoly salts.
The Bragg equation describes the relation between interplanar distance “d” and scattering 2 θ angles.
sin θ = n λ/ 2d
An increase in metal cation radium led to a greater “d” value, consequently, it is expected that 2 θ angle values become smaller than scattering angles of pristine HPA. However, this distance is impacted too by the water molecules. Therefore, ionic radium is not the only aspect to be considered.
Figure 6 presents the powder XRD patterns of silicotungstic acid and their metal-exchanged cations. Diffractograms of the metal cation-exchanged silicotungstic acid salts have some typical diffraction peaks. The main appears at low 2 θ angles (i.e., 6° to 9°), 15° and 30° 2 θ angles. In particular, the diffractograms of trivalent cation salts (i.e., Fe3+, and Al3+ ions) have more well-defined and more intense diffraction peaks. The differences observed between XRD patterns of silicotungstic acid, and their metal-exchanged salts can be a consequence of different hydration levels (Table 1), as well as the different sizes of ionic radium of metal cations.
Figure 7 shows a comparison between the powder XRD patterns of pristine HPAs (i.e., H3PW12O40, H3PMo12O40, and H4SiW12O40) and their aluminium-exchanged salts.
The comparison of powder XRD patterns of tungsten HPAs with their aluminium salts showed that at 2 θ angles greater than 50°, the diffractogram of acids displays diffraction lines present more intensity than their salts. This did not occur with molybdenum HPAs. Moreover, diffractograms of tungsten heteropoly acids had a more significant peak number. The different ionic radium of W6+ and Mo6+ cations and the distinct hydration levels affect the diffraction patterns of these acids and their heteropoly salts. Moreover, Al3+ and H3O+ or H5O2+ have ionic radium with different sizes, triggering thus change in the diffraction patterns. Although XRD patterns can give important information about the secondary structure, it is unable to distinguish the different isomeric structures of the Keggin anion. However, due to the difficulty to isolate Keggin isomers and evaluate separately their catalytic activity, most of the time these aspects are not addressed.

3.3. Acidity Properties

Potentiometric titration is a technique that allows estimating the number of acid sites, from the plateau region of titration curves. Moreover, it can be determined from the titration curve’s first-derived curve. The strength of acidic sites is estimated from the initial value of electrode potential (Ei). They are classified as follows: E > 100 mV (very strong sites), 0 < E < 100 mV (strong sites), −100 < E < 0 (weak sites), and E < −100 mV (very weak sites) [38]. However, this technique did not distinguish the nature of acid sites (i.e., Lewis or Brønsted).
It is important to note that although the chemical formulae of salts suggest that there is no proton, a residual amount remains still. Moreover, the literature describes that Lewis acid metal cations can react with the hydration water molecules giving H3O+ ions, which consume n-butylamine. Moreover, the transition metal cations can themself react with the nitrogen of the base [27]. Therefore, the titrant n-butylamine is still consumed when the salts are titrated.
Figure 8 displays the potentiometric titration curves of silicotungstic acid and their silicotungstate salts. All the salts presented very strong acid sites (Ei > 100 mV). However, the profile of M2+ and M3+ cation salts titration curves differed. Typically, the titration of Al4/3SiW12O40 and Fe4/3SiW12O40 solutions gave curves with a well-defined plateau, likewise the pristine H4SiW12O40. Conversely, the titration of Cu2SiW12O40, Ni2SiW12O40, and Co2SiW12O40 solutions resulted in curves with two plateaus. The profile of these three last curves suggests that there are acid sites with distinct strengths of acidity [27].

4. Keggin HPA Salts as Catalysts in Oxidation Reactions

Keggin HPAs such as phosphomolybdic acid are active in oxidation reactions even in the absence of metal as countercations or dopants. However, depending on the selected substrate (i.e., aldehydes, alcohols, olefins), the presence of cation metal may trigger a synergism and increase its efficiency. From a practical viewpoint, most of the reactions require an initial screening to select the most active Keggin HPA salt. The catalytic activity of HPA salts can be linked to the electronic aspects, which are modified in the presence of metal cations in determined positions.
Aluminium or copper salts of the phosphotungstic and silicotungstic acids were synthesized and used as catalysts in 2-methoxynaphthalene acylation [39]. These catalysts were compared and the main results are in Figure 9.
The highest conversion and selectivity toward acyl methoxy naphthalene were reached in the AlPW12O40-catalyzed reaction. Keggin HPA iron salts were evaluated in etherification reactions of β-pinene with alkyl alcohols [34]. Salts of three Keggin HPAs were synthesized containing aluminium or transition metal cations. Among them, FePW12O40 was the most efficient catalyst converting the β-pinene mainly to α-terpinyl alkyl ether (Scheme 7). The secondary products were fenchyl and bornyl alkyl ethers resulting from the carbon skeletal rearrangement reaction of β-pinene followed by the nucleophilic addition of alkyl alcohol.
Those authors compared the effect of the Keggin anion on the catalytic activity of iron salts in the reaction of β-pinene with methyl alcohol. Figure 10 displays the main results.
Although the reactions in the presence of iron silicotungstate or phosphotungstate have achieved almost the same conversion, this last was the most selective toward the goal product (i.e., α-terpinyl methyl ether). In Figure 11, the activity of FePW12O40 was compared to the other Lewis acid metal cations (i.e., Cu2+ and Al3+).
The highest activity of the FePW12O40 catalyst was attributed to its highest Lewis acidity, which promotes the reaction of carbon skeletal of β-pinene and gives the α-terpinyl carbocation, the most probable reaction intermediate.
The impact of the size of the carbon chain was also evaluated in reactions with C1-C4 alcohols and β-pinene (Scheme 8) [34].
An increase in the carbon chain size and steric hindrance of the hydroxyl group may leave to a lower conversion and ether selectivity. However, herein, high conversions were attained regardless of alcohol. The conversions achieved in the reactions with methyl ethyl, propyl and butyl alcohols were 95%, 80,%, 85%, and 83%, respectively. Therefore, although these three last conversions have been lower than reached in the reaction of methyl alcohol, this effect was less pronounced herein. Conversely, the selectivity to α-terpinyl alkyl ether was 70%, 41%, 45%, and 41%, in the reactions with methyl ethyl, propyl and butyl alcohols, respectively. Thus, it suggests that only methyl alcohol shows a high selectivity. The other alcohols, regardless of the size of the carbon chain have similar reactivity. Due to the steric hindrance, isopropyl alcohol was the less reactive, reaching the lowest conversion and ether selectivity [34].
Aluminium heteropoly salts were evaluated in oxidation reactions of camphene, another monoterpene [35]. In that work, the aluminium silicotungstate salt (i.e., Al4/3SiW12O40) was the most active and selective toward the formation of borneol. Nonetheless, the novelty was the formation of two novel products: 1-(3-(2-hydroxy propan-2-yl) cyclopentyl) ethan-1-one, and 3-(3-hydroxy cyclopentyl)-3-methyl butan-2-one. Scheme 9 shows the conversion and selectivity achieved in the presence of aluminium-exchanged Keggin HPAs salts.
Remarkably, the Al4/3SiW12O40 salt provided the highest selectivity toward the two novel products. The authors attributed this to the greatest Lewis acidity of the catalyst. After carrying out reactions with Al(NO3)3 salt and H43SiW12O40 acid, those authors demonstrated that a synergism occurs between the Al3+ cation and silicotungstate anion [35].
Metal-exchanged silicotungstic acid salts were evaluated as catalysts in furfural oxidation reactions with hydrogen peroxide [27]. Furfural-derived products such as furfuryl ester and dimethyl acetal are valuable compounds for bioadditives formulation.
In this one-pot process, furfural was selectively oxidized to acid and esterified in the presence of methyl alcohol (Scheme 10). Copper silicotungstate was the most effective catalyst, which was more efficient than other Lewis’s acid catalysts also tested such as aluminium or iron silicotungstate. Therefore, it can be concluded that different from verified in the reactions of carbon skeletal rearrangement followed by the oxidation of camphene (see ref. [33]), where the Lewis acidity was a key aspect to explain the highest activity of Al3+ phosphotungstate, herein other aspects can be also important. For instance, the nature of heteropolyanion plays an essential role in these reactions.
The Cu2SiW12O40-catalyzed oxidative esterification of furfural was carried out with hydrogen peroxide in the presence of different alkyl alcohols (Scheme 11).
Scheme 11 shows the yield only to alkyl esters. An increase in the size of the carbon chain of alcohol harmed ester yield. This may be a consequence of hydrophobic forces, which increase with the size of the carbon chain.
Although all salts evaluated have been soluble in the reaction medium, a recycling process was developed to recover and reuse the catalyst (Figure 12).
After the catalytic run, the solvent of the reaction is removed in a rotatory evaporator, and the neat remaining is extracted with a mixture of water/ethyl acetate. The Keggin HPA salt catalyst is soluble in water, which is evaporated, giving the solid catalyst. Afterwards, it is weighted and used in another catalytic cycle. Table 2 shows the conversion and recovery rates obtained after the successive cycles of recovery/reuse.
In oxidation reactions with molecular oxygen, molybdenum HPAs have been more active than tungsten. Cobalt cations-doped catalysts have been active in oxidation reactions [30,40]. Swericka et al. studied the effect of the Co position within the Keggin anion of the catalysts, using cyclooctane as a model molecule [41].
Scheme 12 shows the main results achieved in these reactions. Cyclooctane was preferentially oxidized to cyclooctanol, cyclooctenone, and cyclooctane peroxide, regardless of the catalyst. However, the oxygenates yield was higher in the reactions carried out in the presence of molybdenum HPA or their salts if compared to the tungsten catalysts. The reactions with cobalt as a counterion or as a dopant of heteropolyanion achieved the same oxygenate yields. The same happened with tungsten salts that had Co as a counterion. However, while phosphomolybdic acid reached the same yield as their cobalt salts, the phosphotungstic acid-catalyzed oxidation of cyclooctane achieved the lowest oxygenate yield [41].
Lacunar salts have been effective catalysts in oxidation reactions of terpene alcohols with hydrogen peroxide, even as undoped salts. Vilanculo et al. explored these catalysts in various reactions like these. Scheme 13 displays the main products obtained in Na7PW11O39-catalyzed linalool oxidation with hydrogen peroxide [30].
Linalool is an unsaturated tertiary alcohol, which may be epoxidized generating mono or diepoxides. However, herein it was cyclized generating furane and pyrane derived, which were isolated and spectroscopically characterized [30]. Those authors assessed the effect of Keggin heteropolyanion in this reaction and the main results are shown in Figure 13.
The saturated salt Na3PW12O40 was inactive, reinforcing that the presence of vacancy in the anion is an essential aspect of the activity of these catalysts. The lacunar tungsten sodium salt catalysts were more efficient than molybdenum, being the lacunar sodium phosphotungstate salt the most active, achieving the highest conversion and selectivity toward furan-derived (Figure 13).
Da Silva et al. investigated the activity of these sodium HPA salts in oxidation reactions of nerol, an allylic terpene alcohol. Hydrogen peroxide was the oxidant and acetonitrile was the solvent [26]. Figure 14 describes the results obtained using different sodium salts, the main products, and a probable reaction pathway.
As verified in the linalool oxidation, lacunar tungsten salt catalysts were more efficient than molybdenum ones. Again, saturated salt was inactive. Different from linalool, which undergoes a cyclization reaction, the nerol was preferentially epoxidized giving monoepoxide as the main product, diepoxide, and aldehyde as secondary products [26,30]. Those authors demonstrated that this epoxidation of allylic alcohols is a hydroxy group-assisted reaction.
Figure 15 describes the probable reaction pathway. According to this proposal, the lacunar heteropolyanion is peroxidized, generating intermediate 1, which transfers the oxygen atom to the substrate, releasing water and the oxidation product [26,30].
Transition metal cations-doped silicotungstic acid salts were evaluated as catalysts in oxidation reactions with hydrogen peroxide [42]. In these reactions, borneol, a terpene alcohol was selectively converted to camphor, a product with wide application in the pharmaceutic and fragrancies industries. Figure 15 exhibits the main results achieved in reactions where the vacancy of lacunar salt K8SiW11O39 was filled with a transition metal cation.
Only the nickel and iron-doped potassium silicotungstate salts achieved a camphor yield equal or superior to that reached by the lacunar potassium silicotungstate salt. However, while the K8SiW11O39-catalyzed reaction attained the maximum conversion after 2 h of reaction, in the presence of the K6SiW11NiO39 catalyst it was achieved within the first hour of reaction. Interestingly, when the copper acted as a countercation of silicotungstate salt, it was the best catalyst in furfural oxidation [27]. Herein, as a dopant, the copper was the worst catalyst, achieving the lowest camphor yield on the borneol oxidation (Figure 14) [42].
Another successful example of metal-doped Keggin HPA potassium salts was described by da Silva et al., which assessed their use in benzaldehyde oxidation reactions with hydrogen peroxide [43]. Scheme 14 describes the yield of benzoic acid achieved in the reactions with various metal-doped catalysts.
A noticeable result is that in general, the yields achieved in the reactions with the Keggin HPAs or cobalt-doped potassium salts were poor, varying from 18 to 39%, being reaction yields with cobalt salts lower than pristine HPAs. The remarkable exception was the K6SiW11CoO39-catalyzed reaction, which achieved the highest yield (i.e., 91%) [43].
Da Silva et al. investigated the oxidation of benzylic alcohol with hydrogen peroxide over metal-doped phosphotungstic acid potassium salts [30]. Figure 16 displays the main results.
Different than found in the benzaldehyde oxidation [43], where the cobalt-doped potassium phosphotungstate salt was the most active catalyst, herein, the reactions carried out over the nickel-doped potassium phosphotungstate salt were those that achieved the highest conversion and selectivity to carboxylic alcohol (benzylic acid) [30]. Patel et al. have found a similar result, where nickel-doped phosphotungstic acid salt was the most efficient catalyst in oxidation reactions of aldehydes and alcohols, however, those authors used the catalyst supported on the zirconia [44].
Serwicka et al. investigate the Keggin salts in Baeyer Villiger oxidation of cyclohexanone [12]. Partially exchanged salts with cobalt, manganese, or iron cations were the catalysts (Figure 17 and Figure 18).
Among the evaluated salts, it is possible to observe that while the reactions in the presence of cobalt or manganese salts achieved almost the same conversion and selectivity, regardless of Keggin anion, the reactions with iron as the dopant were the most efficient (Figure 17 and Figure 18). However, the H2Fe0.33PW12O40-catalyzed reaction achieved the highest conversion and lactone selectivity if compared to the reaction in the presence of H2Fe0.33PMo12O40 [43].
The performance of silicotungstic acid and its saturated or lacunar salts of tert-butylammonium was evaluated in the oxidation reaction of cyclopentene [45]. Scheme 15 shows the main results of conversion and selectivity. Cyclopentene was selectively converted to cyclopentanediol and 1,5-diketone.
All the silicotungstate salts were very efficient catalysts, except the tert-butylammonium silicotungstate saturated salt. Once more the importance of the presence of a vacancy on the Keggin structure of heteropolyanions was demonstrated. Although the silicotungstic acid had achieved a high conversion, the selectivity to oxidation products was poor. The performance of di-lacunar salt was superior to the mono-lacunar silicotungstate.
Tahar et al. prepared nickel or ammonium salts of phosphomolybdic acid replacing partially their protons and evaluated its catalytic activity in reactions of oxidative cleavage of cyclohexanone to adipic acid [46]. Nickel performance is depicted in Scheme 16 and Scheme 17.
Those authors verified that 14 h was time enough to achieve a good conversion. They investigated the effect of catalyst load, and the main results are in Scheme 18.

5. Conclusions

The synthesis routes of a series of Keggin heteropolyacid (HPAs) salts were described. Infrared, powder XRD patterns and measurements of the acidity strength of these salts were discussed. The Keggin HPA salt catalysts are used in the oxidation processes of monoterpenes, aldehydes, alcohols, and olefines to produce valuable fine chemicals. Herein, the most significant results were described. Lacunar HPA salts and metal-doped HPA salts were the focus and had their activity compared in several oxidative processes. A comparison of the main results of these two types of processes showed that the Keggin heteropolyacid salts are efficient catalysts, with performance superior to the conventional catalysts used in oxidation processes, either with hydrogen peroxide or molecular oxygen. Commonly, noble metal catalysts such as Au, Ag, and Pd are used in oxidation processes. However, they decompose hydrogen peroxide and are incompatible with this oxidant. Even when used with molecular oxygen, frequently they require high oxygen pressure, hampering the processes. Therefore, Keggin HPA salts are efficient and cheaper than these noble metals. Moreover, hydrogen peroxide is a nonflammable oxidant and easier to handle than molecular oxygen.

Author Contributions

Conceptualization, M.J.d.S.; methodology, M.J.d.S.; software, M.J.d.S., N.P.G.L. and A.A.R.; investigation, M.J.d.S., N.P.G.L. and A.A.R.; resources, M.J.d.S., N.P.G.L. and A.A.R.; writing—original draft preparation, M.J.d.S.; writing—review and editing, M.J.d.S.; supervision, M.J.d.S. All authors have read and agreed to the published version of the manuscript.

Funding

Aperfeiçoamento de Pessoal de Nível Superior—Brasil (CAPES—Finance Code 001).

Data Availability Statement

Not applicable.

Acknowledgments

The authors are grateful to the Brazilian research agencies, CAPES, FAPEMIG and CNPq for the financial support.

Conflicts of Interest

The authors declare no conflict of interest.

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Scheme 1. Synthesis of metal-exchanged phosphotungstic, phosphomolybdic, and silicotungstic acid salts.
Scheme 1. Synthesis of metal-exchanged phosphotungstic, phosphomolybdic, and silicotungstic acid salts.
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Figure 1. The yield of synthesis of the metal-exchanged silicotungstic acid salts [27].
Figure 1. The yield of synthesis of the metal-exchanged silicotungstic acid salts [27].
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Scheme 2. Synthesis of phosphotungstic (a), silicotungstic (b), and phosphomolybdic acid (c) lacunar salts.
Scheme 2. Synthesis of phosphotungstic (a), silicotungstic (b), and phosphomolybdic acid (c) lacunar salts.
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Scheme 3. One–pot synthesis of phosphotungstic acid lacunar salt.
Scheme 3. One–pot synthesis of phosphotungstic acid lacunar salt.
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Scheme 4. One–step synthesis of silicotungstic acid lacunar salt.
Scheme 4. One–step synthesis of silicotungstic acid lacunar salt.
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Scheme 5. One–step synthesis of phosphomolybdic acid lacunar salt.
Scheme 5. One–step synthesis of phosphomolybdic acid lacunar salt.
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Scheme 6. Synthesis of metal-doped phosphotungstate, phosphomolybdate, and silicotungstate heteropolyanions.
Scheme 6. Synthesis of metal-doped phosphotungstate, phosphomolybdate, and silicotungstate heteropolyanions.
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Figure 2. Infrared spectra of metal-exchanged silicotungstic acid salts (adapted from ref. [27]).
Figure 2. Infrared spectra of metal-exchanged silicotungstic acid salts (adapted from ref. [27]).
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Figure 3. Infrared spectra of phosphotungstic, silicotungstic, and phosphomolybdic acids and their aluminium-exchanged salts (adapted from refs. [34,35]).
Figure 3. Infrared spectra of phosphotungstic, silicotungstic, and phosphomolybdic acids and their aluminium-exchanged salts (adapted from refs. [34,35]).
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Figure 4. Infrared spectra of phosphotungstic, silicotungstic, and phosphomolybdic acid and their iron-exchanged salts (adapted from refs. [34,35]).
Figure 4. Infrared spectra of phosphotungstic, silicotungstic, and phosphomolybdic acid and their iron-exchanged salts (adapted from refs. [34,35]).
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Figure 5. Primary, secondary, and tertiary structures of Keggin anion.
Figure 5. Primary, secondary, and tertiary structures of Keggin anion.
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Figure 6. Powder XRD patterns of silicotungstic acid and their metal-exchanged cations (adapted from ref. [27]).
Figure 6. Powder XRD patterns of silicotungstic acid and their metal-exchanged cations (adapted from ref. [27]).
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Figure 7. Powder XRD patterns of phosphotungstic, silicotungstic, and phosphomolybdic acid and their aluminium-exchanged salts (adapted from refs. [34,35]).
Figure 7. Powder XRD patterns of phosphotungstic, silicotungstic, and phosphomolybdic acid and their aluminium-exchanged salts (adapted from refs. [34,35]).
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Figure 8. Potentiometric titration curves of silicotungstic acid and their metal-exchanged salts (adapted from ref. [27]).
Figure 8. Potentiometric titration curves of silicotungstic acid and their metal-exchanged salts (adapted from ref. [27]).
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Figure 9. 2-Methoxynaphthalene acylation using aluminium or copper salts of phosphotungstic silicotungstic acids as catalysts (adapted from ref. [39]) a. a Reaction conditions: time: 65 min, temperature: 373 K.
Figure 9. 2-Methoxynaphthalene acylation using aluminium or copper salts of phosphotungstic silicotungstic acids as catalysts (adapted from ref. [39]) a. a Reaction conditions: time: 65 min, temperature: 373 K.
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Scheme 7. The main products of the iron phosphotungstate-catalyzed reactions of β-pinene with alkyl alcohol (adapted from ref. [34]).
Scheme 7. The main products of the iron phosphotungstate-catalyzed reactions of β-pinene with alkyl alcohol (adapted from ref. [34]).
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Figure 10. Impacts of Keggin anion on the conversion and selectivity of Keggin HPA iron salts phosphotungstate-catalyzed reaction of β-pinene with methyl alcohol (adapted from ref. [34]) a. a Reaction conditions: β-pinene (3.8 mmol), CH3OH (14.3 mL), temperature (333 K), catalyst (0.50 mol%), volume (10 mL).
Figure 10. Impacts of Keggin anion on the conversion and selectivity of Keggin HPA iron salts phosphotungstate-catalyzed reaction of β-pinene with methyl alcohol (adapted from ref. [34]) a. a Reaction conditions: β-pinene (3.8 mmol), CH3OH (14.3 mL), temperature (333 K), catalyst (0.50 mol%), volume (10 mL).
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Figure 11. Impacts of metal cation on the conversion and selectivity of phosphotungstate-catalyzed reaction of β-pinene with methyl alcohol (adapted from ref. [34]) a. a Reaction conditions: β-pinene (3.8 mmol), CH3OH (14.3 mL), temperature (333 K), catalyst (0.50 mol%), volume (10 mL).
Figure 11. Impacts of metal cation on the conversion and selectivity of phosphotungstate-catalyzed reaction of β-pinene with methyl alcohol (adapted from ref. [34]) a. a Reaction conditions: β-pinene (3.8 mmol), CH3OH (14.3 mL), temperature (333 K), catalyst (0.50 mol%), volume (10 mL).
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Scheme 8. FePW12O40-catalyzed-etherification of β-pinene with different alkyl alcohols (adapted from ref. [34]).
Scheme 8. FePW12O40-catalyzed-etherification of β-pinene with different alkyl alcohols (adapted from ref. [34]).
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Scheme 9. Effect of Keggin anion on conversion and selectivity of Al3+ heteropoly salts-catalyzed camphene oxidation by hydrogen peroxide in CH3CN (adapted from ref. [35]).
Scheme 9. Effect of Keggin anion on conversion and selectivity of Al3+ heteropoly salts-catalyzed camphene oxidation by hydrogen peroxide in CH3CN (adapted from ref. [35]).
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Scheme 10. Metal-exchanged silicotungstic acid salts-catalyzed reactions of furfural with hydrogen peroxide (adapted from ref. [26]) a. a Reaction conditions: furfural (2.5 mmol), CH3OH (9.4 mL, 231 mmol), H2O2 (5.0 mmol), temperature (323 K), catalyst (1.0 mol%, 25.0 μmol), volume (10 mL).
Scheme 10. Metal-exchanged silicotungstic acid salts-catalyzed reactions of furfural with hydrogen peroxide (adapted from ref. [26]) a. a Reaction conditions: furfural (2.5 mmol), CH3OH (9.4 mL, 231 mmol), H2O2 (5.0 mmol), temperature (323 K), catalyst (1.0 mol%, 25.0 μmol), volume (10 mL).
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Scheme 11. Impact of alcohol on the Cu2SiW12O40-catalyzed oxidative esterification of furfural with hydrogen peroxide (adapted from ref. [27]) a. a Reaction condition: furfural (2.5 mmol), alky alcohol (9.4 mL), H2O2 (5.0 mmol), temperature (323 K), catalyst (1.0 mol%, 25.0 μmol), reaction volume (10 mL).
Scheme 11. Impact of alcohol on the Cu2SiW12O40-catalyzed oxidative esterification of furfural with hydrogen peroxide (adapted from ref. [27]) a. a Reaction condition: furfural (2.5 mmol), alky alcohol (9.4 mL), H2O2 (5.0 mmol), temperature (323 K), catalyst (1.0 mol%, 25.0 μmol), reaction volume (10 mL).
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Figure 12. Procedure to recover and reuse the soluble catalyst [27].
Figure 12. Procedure to recover and reuse the soluble catalyst [27].
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Scheme 12. Oxidation of cyclooctane with molecular oxygen in the presence of phosphotungstic or phosphomolybdic acids or their cobalt salts (adapted from ref. [41]).
Scheme 12. Oxidation of cyclooctane with molecular oxygen in the presence of phosphotungstic or phosphomolybdic acids or their cobalt salts (adapted from ref. [41]).
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Scheme 13. Main products of Na7PW11O39-catalyzed linalool oxidation with hydrogen peroxide (adapted from ref. [30]).
Scheme 13. Main products of Na7PW11O39-catalyzed linalool oxidation with hydrogen peroxide (adapted from ref. [30]).
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Figure 13. Impact of heteropolyanion on the efficiency of Keggin HPA sodium salts (adapted from ref. [30]).
Figure 13. Impact of heteropolyanion on the efficiency of Keggin HPA sodium salts (adapted from ref. [30]).
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Figure 14. Impact of heteropolyanion on the efficiency of Keggin HPA sodium salts, main oxidation products of nerol a probable reaction pathway (adapted from ref. [26]).
Figure 14. Impact of heteropolyanion on the efficiency of Keggin HPA sodium salts, main oxidation products of nerol a probable reaction pathway (adapted from ref. [26]).
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Figure 15. Conversions and selectivity achieved on the borneol oxidation with hydrogen peroxide over transition metal cations -doped potassium silicotungstate salts (adapted from ref. [42]).
Figure 15. Conversions and selectivity achieved on the borneol oxidation with hydrogen peroxide over transition metal cations -doped potassium silicotungstate salts (adapted from ref. [42]).
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Scheme 14. Benzaldehyde oxidation with hydrogen peroxide over Keggin HPAs or their cobalt-doped Keggin HPA potassium salts (adapted from ref. [43]).
Scheme 14. Benzaldehyde oxidation with hydrogen peroxide over Keggin HPAs or their cobalt-doped Keggin HPA potassium salts (adapted from ref. [43]).
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Figure 16. Benzylic alcohol oxidation with hydrogen peroxide over aluminium or transition metal-doped lacunar phosphotungstic acid potassium salts (adapted from ref. [30].
Figure 16. Benzylic alcohol oxidation with hydrogen peroxide over aluminium or transition metal-doped lacunar phosphotungstic acid potassium salts (adapted from ref. [30].
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Figure 17. Baeyer Villiger oxidation of cyclohexanone with hydrogen peroxide over partially exchanged-phosphotungstic acid salts (adapted from ref. [12]).
Figure 17. Baeyer Villiger oxidation of cyclohexanone with hydrogen peroxide over partially exchanged-phosphotungstic acid salts (adapted from ref. [12]).
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Figure 18. Baeyer Villiger oxidation of cyclohexanone with hydrogen peroxide over partially exchanged-phosphomolybdic acid salts (adapted from ref. [12]).
Figure 18. Baeyer Villiger oxidation of cyclohexanone with hydrogen peroxide over partially exchanged-phosphomolybdic acid salts (adapted from ref. [12]).
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Scheme 15. Conversion and selectivity of silicotungstate-catalyzed oxidation of cyclopentene with hydrogen peroxide (adapted from ref. [45]) a,b. a Reaction conditions, catalyst (0.03 mmol), CH3CN (4 mL), cyclopentene (25 mmol), H2O2 (30% (mass)) 30 mmol); stirring speed: 500 r·min−1. b Conversions and selectivity values were expressed only with one or two significant figures.
Scheme 15. Conversion and selectivity of silicotungstate-catalyzed oxidation of cyclopentene with hydrogen peroxide (adapted from ref. [45]) a,b. a Reaction conditions, catalyst (0.03 mmol), CH3CN (4 mL), cyclopentene (25 mmol), H2O2 (30% (mass)) 30 mmol); stirring speed: 500 r·min−1. b Conversions and selectivity values were expressed only with one or two significant figures.
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Scheme 16. Partially exchanged acid phosphomolybdic acid nickel salts as catalysts in oxidative cleavage of cyclohexanone to give adipic acid (adapted from ref. [45]).
Scheme 16. Partially exchanged acid phosphomolybdic acid nickel salts as catalysts in oxidative cleavage of cyclohexanone to give adipic acid (adapted from ref. [45]).
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Scheme 17. Partially Ni-exchanged ammonium phosphomolybdate salts as catalysts in oxidative cleavage of cyclohexanone to give adipic acid (adapted from ref. [46]).
Scheme 17. Partially Ni-exchanged ammonium phosphomolybdate salts as catalysts in oxidative cleavage of cyclohexanone to give adipic acid (adapted from ref. [46]).
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Scheme 18. Effect of catalyst load on the oxidative cleavage of cyclohexanone to adipic acid over nickel phosphomolybdate salts (adapted from ref. [46]).
Scheme 18. Effect of catalyst load on the oxidative cleavage of cyclohexanone to adipic acid over nickel phosphomolybdate salts (adapted from ref. [46]).
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Table 1. Hydration water molecules were determined through thermal analysis (DTG) [27].
Table 1. Hydration water molecules were determined through thermal analysis (DTG) [27].
CatalystWater/Catalyst mol
H4SiW12O4011
Ni2SiW12O407
Cu2SiW12O407
Co2SiW12O4010
Fe4/3SiW12O4013
Al4/3SiW12O408
Table 2. The recovery rates and conversions achieved in the reuse of Cu2SiW12O40 catalyst in oxidative esterification reactions of furfural with hydrogen peroxide [27].
Table 2. The recovery rates and conversions achieved in the reuse of Cu2SiW12O40 catalyst in oxidative esterification reactions of furfural with hydrogen peroxide [27].
CycleCatalyst Recovery
(%)
Conversion
(%)
19297
29293
39292
49194
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da Silva, M.J.; Rodrigues, A.A.; Lopes, N.P.G. Keggin Heteropolyacid Salt Catalysts in Oxidation Reactions: A Review. Inorganics 2023, 11, 162. https://doi.org/10.3390/inorganics11040162

AMA Style

da Silva MJ, Rodrigues AA, Lopes NPG. Keggin Heteropolyacid Salt Catalysts in Oxidation Reactions: A Review. Inorganics. 2023; 11(4):162. https://doi.org/10.3390/inorganics11040162

Chicago/Turabian Style

da Silva, Marcio Jose, Alana Alves Rodrigues, and Neide Paloma Gonçalves Lopes. 2023. "Keggin Heteropolyacid Salt Catalysts in Oxidation Reactions: A Review" Inorganics 11, no. 4: 162. https://doi.org/10.3390/inorganics11040162

APA Style

da Silva, M. J., Rodrigues, A. A., & Lopes, N. P. G. (2023). Keggin Heteropolyacid Salt Catalysts in Oxidation Reactions: A Review. Inorganics, 11(4), 162. https://doi.org/10.3390/inorganics11040162

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