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Proceeding Paper

Sulfur-Containing Homo- and Methanofullerenes: Synthesis and Study of Tribological Properties †

Institute of Petrochemistry and Catalysis, Ufa Federal Research Center of the Russian Academy of Sciences, Ufa 450075, Russia
*
Author to whom correspondence should be addressed.
Presented at the 26th International Electronic Conference on Synthetic Organic Chemistry, 15–30 November 2022; Available online: https://sciforum.net/event/ecsoc-26.
Chem. Proc. 2022, 12(1), 25; https://doi.org/10.3390/ecsoc-26-13537
Published: 14 November 2022

Abstract

:
The data obtained by the authors in the field of carbon cluster chemistry, namely the catalytic cycloaddition of sulfur-containing diazo compounds to C60-fullerene under the action of complex Pd catalysts, are summarized. Cycloaddition reactions of diazoalkanes, diazoketones, and diazothioates with C60-fullerene, catalyzed by Pd(acac)2–PPh3–Et3Al, with the selective formation of new sulfur-containing methano-, homo-, and pyrazolinofullerenes, are promising as modern nanosized additives in oils for highly loaded mechanisms.

1. Introduction

Since the discovery of fullerenes, a new form of carbon existence, the chemistry of carbon clusters has become an independent branch of the organization of chemistry. Along with the study of the chemical properties of fullerenes, much attention is paid to determining possible areas of their application.
The interest in sulfur-containing fullerenes is due to the possibility of their application in medicine [1,2,3,4] and electronics and nonlinear optics [5], as well as solar energy photoconverters [6,7] and supramolecular dyes [8,9]. We assume that the spherical structure of the molecules of the simplest C60- and C70-fullerenes will play the role of nanobearings, which will allow them to be used as oil additives.
By the time we started our research, in the world literature, methods for the synthesis of sulfur-containing derivatives were described, focusing on C60-fullerene, with the most attractive synthetic point of view being a method based on the thermal interaction of carbon clusters with diazo compounds [10,11]. However, the main disadvantage of the specified method is the low selectivity of the reaction. Meanwhile, it has recently been shown [12] that the introduction of methods such as metal complex catalysis in the reaction of fullerenes with diazo compounds allows one to achieve selective homo- or methanofullerenes.
In this regard, the use of metal complex catalysts in the reactions of sulfur-containing diazo compounds with fullerenes, as we assume, will allow us to develop highly selective and efficient catalytic methods of synthesis for sulfur-containing homo-, methane-, or pyrazolinofullerenes of a given structure, which will allow us to create, on their basis, promising nanocomponent additives for lubricating oils and highly loaded mechanisms.

2. Results and Discussion

As a follow-up to the ongoing work in our group [13,14,15,16,17,18,19,20] related to the selective functionalization of C60-fullerene with diazo compounds, we studied the catalytic cycloaddition reaction of sulfur-containing diazoalkanes generated in situ by the oxidation of hydrazones of the corresponding ketosulfides with MnO2 to C60. Of the tested catalysts based on salts and compounds of Cu, Pd, and Rh, the three-component catalyst prepared in situ from Pd(acac)2, PPh3, and Et3Al, taken in a ratio of 1:2:4, respectively, showed the highest activity in the reaction of diazoalkanes and C60-fullerene. In this regard, all experiments on the study of the reaction of the catalytic cycloaddition of sulfur-containing diazoalkanes to C60-fullerene were carried out in the presence of this catalytic system.
It was found that in the interaction of C60-fullerene with a 1.5–fold excess of 2–diazo-3–(pentylthiomethyl)– or 2–diazo–3–(cyclohexylthiomethyl)butane, generated in situ by the oxidation of hydrazones of the corresponding ketones, in the presence of 20 mol% of the three–component catalyst Pd(acac)2–PPh3–Et3Al (1:2:4) at room temperature (18–20 °C) in chlorobenzene, the corresponding homofullerenes 1 and 2 are formed in 1 h with a yield of ~50% [21] (Scheme 1).
Under the developed optimal conditions (~20–22 °C, 1 h, 20 mol% Pd(acac)2–PPh3–Et3Al (1:2:4)), the cycloaddition of sulfur-containing diazoalkanes generated in situ from hydrazones of 4–methylthiobenzaldehyde and 2–acetylthiophene to C60-fullerene leads to compounds 3 and 4 in 50 and 45% yields, respectively (Scheme 2).
Analysis of the 1H and 13C Nuclear Magnetic Resonance (NMR) spectra, as well as the UV spectra, of compound 4 showed that the reaction of C60 with a diazo compound containing a thienyl fragment resulted in the formation of only a [2+1]–cycloadduct of a closed structure.
Similarly, the cycloaddition of a diazoalkane generated from thiochroman–4–one hydrazone [22] to C60 under the conditions developed above (20 °C, 1 h, 20 mol% Pd(acac)2–2PPh3–4Et3Al) leads to the formation of spiro-methanofullerene 5 in a ~50% yield. When using a cyclic ketone hydrazone that does not contain a heteroatom in the cyclic fragment for example, o-methylsulfanylcyclohexanonehydrazone individual spiro-homofullerene 6 is formed in the reaction under discussion. We assume that the formation of methanofullerenes, in the case of heterocyclic diazo compounds, is due to the stabilization of the corresponding carbenes formed during the reaction due to the delocalization of unpaired electrons with an aromatic nucleus [22] (Scheme 3).
According to the literature [23], substituted homofullerenes can be quite easily isomerized into the corresponding methanofullerenes. In this regard, and also in order to obtain previously undescribed sulfur-containing methanofullerenes, we carried out the thermal isomerization of the synthesized [5,6]–open cycloadducts 1–3, 6. As a result of refluxing the indicated homofullerenes in 1,2–dichlorobenzene (o–DCB) for 15 h, individual [6,6]–closed isomers 7–10 were obtained in high yields of ~100% (Scheme 4).
In the UV spectrum of individual methanofullerenes 7–10, a narrow, low–intensity absorption band is observed in the region of 427–430 nm, which is a fairly simple and reliable characteristic of the formation of [6,6]–closed cycloadducts.
In order to obtain C60 adducts containing sulfoxide or sulfone groups, we oxidized the cycloadducts 1–3, 5–10, synthesized by us, which contain sulfide sulfur. It has been shown that the treatment of sulfides with 1–3, 5–10 equimolar amounts of m–CPBA leads to the formation of the corresponding individual sulfoxides 11–19 in quantitative yields (controlled by HPLC and 1H NMR). An increase in the amount of m–CPBA relative to the initial sulfide 1–3, 5–10 to 3:1 leads to the formation of individual sulfones 20–28, which are characterized by an even longer retention time (Scheme 5).
In order to develop our research, we carried out the catalytic cycloaddition of sulfur-containing diazoketones to C60 under these conditions (~80 °C, 1.5 h, chlorobenzene or 1,2 dichlorobenzene) and only methanofullerene 29 was formed, with a yield of ~70%. An increase in the reaction time to 2 h leads to the formation of dicycloadducts. Homofullerene and fullerodihydrofuran, which are usually formed under the conditions of the thermal reaction of C60 with diazoketones, were not found in our experiments (Scheme 6).
In order to study the effect of the structure of the starting diazoketone on the course and direction of the reaction under discussion, we studied the cycloaddition of diazoketones containing methylthiopyridyl and mercaptoaryl substituents to C60. It has been shown that under the previously developed conditions (80 °C, 1.5 h, o–dichlorobenzene), these aromatic diazoketones react with C60-fullerene in the presence of a three-component catalyst, Pd(acac)2–PPh3–Et3Al (1:2:4), to give the corresponding methanofullerenes 30 and 31 with a yield of ~55 and 60%, respectively (Scheme 7).
In order to develop effective methods for the synthesis of functionally substituted sulfur-containing C60-carbon clusters, we, for the first time, carried out the interaction of C60 with diazothioates under the conditions of thermal and catalytic reactions [24]. Diazo compounds synthesized on the basis of α–amino acids (glycine, alanine, leucine, and methionine) and alkyl mercaptans were chosen as initial diazothioates.
It was found that diazothioate 32 quite easily reacted with C60 (20 °C, 7 h, solvent chlorobenzene) to form pyrazolinofullerene 33 in a ~28% yield. An increase in the reaction temperature to 40 °C leads to the target [3+2]–cycloadduct 33 in the same yield in 2 h. An increase in the reaction time at 40 °C to 4 h makes it possible to synthesize pyrazolinofullerene 33 in a ~43% yield (Scheme 8).
Boiling pyrazolinofullerene 33 in 1,2–dichlorobenzene led to the extrusion of the N2 molecule from the pyrazoline fragment and the quantitative formation of the corresponding methanofullerene 34.
In order to study the influence of the structure of the initial diazothioate on the course and direction of the reaction, the cycloaddition of α-substituted diazothioates to C60-fullerene was carried out.
Thus, we found that, in contrast to the reaction of C60-fullerene with unsubstituted diazothioates, the interaction of C60 with thiopentyl–2–methyl–2–diazothioate in chlorobenzene takes place at 40 °C for 1 h, with the formation of an individual [5,6]–open fullerene adduct 35 with the arrangement methyl group at the bridging carbon atom above the plane of the five-membered fragment of the fullerene core (Scheme 9).
Subsequent experiments showed that the use of a 20 mol% three-component catalyst based on the Pd phosphine complex (Pd(acac)2–PPh3–Et3Al) with a component ratio of 1:2:4 in the reaction of C60-fullerene with thiopentyl–2-methyl–2–diazothioate makes it possible to direct it towards the formation of an individual [6,6]–closed cycloadduct 36 with a yield of ~47%.
Later, we studied the effect of the size of the alkyl substituent in the α–position of the diazo compound on the yield and selectivity of the formation of C60-fullerene cycloadducts, using the example of diazothioates synthesized from amyl mercaptan, leucine, and methionine. It was established that, under the developed conditions (40 °C, 1 h) C60 reacts with the indicated diazo compounds (molar ratio 1:5) in the absence of a catalyst, forming a mixture of the corresponding stereoisomerichomofullerenes 37a,b (55%) and 38a,b (48%). Heating a mixture of homofullerenes 37a,b and 38a,b in toluene (80 °C) for 4 h leads to the isomerization of [5,6]–open cycloadducts into [6,6]–closed 39a,b, respectively (Scheme 10).
Carrying out the above reaction under catalytic conditions (40 °C, 1 h, 20 mol% Pd(acac)2–2PPh3–4Et3Al) leads to the production of exclusively methanofullerenes 39a,b in 54–60% yields. Similar results were obtained using isopropyl, cyclohexyl, and benzyl diazothioates. In all experiments using the Pd(acac)2–2PPh3–4Et3Al catalytic system, the corresponding methanofullerenes 40–42 are formed (Scheme 11).
Using the example of methanofullerene 39b, we observed the possibility of the selective oxidation of sulfide sulfur to sulfoxide and the sulfone treatment of the starting compound with an equimolar amount or a three-fold excess of m–CPBA (Scheme 12).
Thus, for the first time, we performed the cycloaddition of diazothioates to C60-fullerene under the conditions of thermal and catalytic reactions. We determined that the interaction of C60 with α–substituted diazothioates in the presence of a three-component catalyst based on Pd leads to the selective formation of the corresponding methanefullerenes, while, in the absence of a catalyst, only homofullerenes are formed.
Considering that the majority of additives currently used in industry are sulfur-containing compounds, it can be assumed that oil-soluble sulfur-containing fullerenes are promising as new functional nanomaterials to improve the lubricating and antifriction properties of additives, as well as materials with significantly improved extreme pressure and anti-wear properties.
In this regard, within the framework of this work, we studied the anti-wear and extreme pressure properties of oils containing the synthesized C60 derivatives, the structure of which contains sulfur atoms of various nature, as well as various functional groups [25]. The following compounds were chosen as model sulfur-containing C60 adducts (Figure 1):
Compound 2 is practically insoluble in industrial oils, as well as in known sulfur-containing additives, as a result of which we attempted to carry out the polyaddition of the corresponding diazoalkane generated in situ by the oxidation of hydrazone (cyclohexylthiomethyl)–2–butanone with MnO2, to C60, taken in a ratio of 50:1, respectively, in the presence of 20 mol% Pd(acac)2–2PPh3–4Et3Al catalyst, hoping to obtain polycycloadducts with good solubility (Scheme 13). Under these conditions, a mixture of regioisomeric cycloadducts 2′ is formed, which are built from one C60-fullerene molecule and five molecules of residues of the initial sulfur-containing diazoalkane. The fullerene C60 conversion in this experiment is ~100%.
The regioisomeric mixture of cycloadducts 2′ synthesized by us, as well as monoadducts 12, 21 and 30, did not dissolve in I–20A industrial oil, so we attempted to dissolve them in a well-known PRP additive, which is a sulfided propylene tetramer. The additive compositions obtained in this way were easily dissolved in industrial oil I–20A in an amount of 5 wt% with vigorous stirring under the given conditions (4 h, 60 °C), which made it possible to compare the effectiveness of the prepared additives with known samples.
The study of the obtained additives for extreme pressure properties was carried out on a four-ball friction machine, ChMT–1 (State Standard 9490–75). When tested on the ChMT, balls were used according to State Standard 3722–81, made of steel, with a diameter of 12.7 mm, and with a degree of accuracy of 20. We evaluated the welding load (Pw), which characterizes the maximum performance of the lubricant under test conditions, and the critical load (Pcr), as well as the wear diameter (dws), which determines the ability of the lubricant to prevent the occurrence of scuffing of rubbing surfaces and to provide anti-wear properties. The results of the tests carried out are presented in Table 1.
As can be seen from the data in Table 1, the obtained new compositions of additives, in comparison with the original (STP), have better anti-wear and extreme pressure properties and good compatibility with industrial oils, which makes it possible to reduce the consumption of the sulfur-containing extreme-pressure and anti-wear additives currently used and produced by the industry by eight times. They can be used as additives for highly loaded machines and mechanisms, while maintaining their efficiency, as well as to expand the range of new domestic multifunctional additives. It should be noted that C60 adducts containing sulfoxide, sulfone, or sulfide and carbonyl groups have better solubility in the STP additive, in contrast to monocycloadducts containing only a sulfide group. Methanofullerene 31 does not dissolve in oil and STP additive, as a result of which the tribological properties of this compound could not be studied.
When preparing composite oils for the study of the tribological properties, we found that monoadduct 39b, in contrast to the compounds 2′, 12, 21, 30 used above, dissolves well directly in industrial oil I–20A, as a result of which the addition of STP, in this case, was not carried out.
As a result of the research, it was shown that the industrial oil I–20 A, containing 0.005 wt% adduct C60 with a thioate group, significantly exceeds the weldability load of oils containing 40 wt% STP (Pw > 1000 kgf); however, it has a low Pcr index (45 kgf).
The low critical load is likely due to the low sulfur content of the test samples, as we abandoned the use of 5 wt% STP. In this regard, we assumed that an increase in the number of fragments attached to the fullerene molecule would lead to an increase in the critical load index. To confirm our idea, we synthesized a model polyadduct 39b′, which is an analogue of monoadduct 39b and contains three to five attached cyclopropane fragments.
The test of the prepared composition consisting of industrial oil I–20 A and 0.005 wt% compound 39b′ showed that, indeed, an increase in the number of attached fragments contributes to an increase in the critical load (Pcr) from 45 to 63 kgf, while the welding load (Pw) slightly decreases to 942 kgf.
Using an electron microscope, as well as using atomic force microscopy (AFM), it was established that the introduction of sulfur-containing C60-fullerene derivatives into industrial oil I–20A leads to the smoothing of the steel ball surface at the wear spot after tribocontact.

3. Conclusions

Thus, for the first time, we have developed effective methods for the synthesis of fullerene derivatives containing sulfur atoms of various nature by the cycloaddition of sulfur-containing diazo compounds to C60-fullerene in the presence of the Pd(acac)2–PPh3–Et3Al three-component catalytic system, which provides a fairly simple and effective method for the synthesis of homo- and methanofullerenes—effective additives to oils for highly loaded machines and mechanisms.

Author Contributions

Conceptualization, U.M.D., A.R.T. and A.A.K.; methodology, validation, and execution of chemistry experiments, A.A.K.; manuscript preparation, A.A.K. and A.R.T. All authors have read and agreed to the published version of the manuscript.

Funding

This work was supported by the Ministry of Science and Higher Education within the State Assignments of the Institute of Petrochemistry and Catalysis of RAS (FMRS–2022–0075).

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

Not applicable.

Acknowledgments

The structural studies of the synthesized compounds were performed with the use of the Collective Usage Centre “Agidel” at the Institute of Petrochemistry and Catalysis of RAS.

Conflicts of Interest

The authors declare no conflict of interest.

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Scheme 1. Catalytic cycloaddition of sulfur-containing diazoalkanes to C60-fullerene.
Scheme 1. Catalytic cycloaddition of sulfur-containing diazoalkanes to C60-fullerene.
Chemproc 12 00025 sch001
Scheme 2. Cycloaddition of sulfur-containing diazoalkanes to C60-fullerene generated in situ.
Scheme 2. Cycloaddition of sulfur-containing diazoalkanes to C60-fullerene generated in situ.
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Scheme 3. Formation of spiro-methane and spiro-homofullerenes.
Scheme 3. Formation of spiro-methane and spiro-homofullerenes.
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Scheme 4. Thermal isomerization of [5,6]–open cycloadducts.
Scheme 4. Thermal isomerization of [5,6]–open cycloadducts.
Chemproc 12 00025 sch004
Scheme 5. Oxidation of C60 adducts containing sulfide sulfur to sulfoxide or sulfonic.
Scheme 5. Oxidation of C60 adducts containing sulfide sulfur to sulfoxide or sulfonic.
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Scheme 6. Catalytic cycloaddition of sulfur-containing diazoketones to C60-fullerene.
Scheme 6. Catalytic cycloaddition of sulfur-containing diazoketones to C60-fullerene.
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Scheme 7. Catalytic cycloaddition of sulfur-containing diazoketones to C60-fullerene.
Scheme 7. Catalytic cycloaddition of sulfur-containing diazoketones to C60-fullerene.
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Scheme 8. Cycloaddition of diazothioates to C60-fullerene.
Scheme 8. Cycloaddition of diazothioates to C60-fullerene.
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Scheme 9. Cycloaddition of α–substituted diazothioates to C60-fullerene.
Scheme 9. Cycloaddition of α–substituted diazothioates to C60-fullerene.
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Scheme 10. Catalytic cycloaddition of α-substituted diazothioates to C60-fullerene.
Scheme 10. Catalytic cycloaddition of α-substituted diazothioates to C60-fullerene.
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Scheme 11. Catalytic cycloaddition of isopropyl, cyclohexyl, benzyl diazothioates to C60-fullerene.
Scheme 11. Catalytic cycloaddition of isopropyl, cyclohexyl, benzyl diazothioates to C60-fullerene.
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Scheme 12. Selective oxidation of sulfide sulfur compound 39b to sulfoxide and sulfonic.
Scheme 12. Selective oxidation of sulfide sulfur compound 39b to sulfoxide and sulfonic.
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Figure 1. Selected C60-fullerene adducts for the study of antiwear and extreme pressure properties of oils.
Figure 1. Selected C60-fullerene adducts for the study of antiwear and extreme pressure properties of oils.
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Scheme 13. Obtaining a sulfur-containing polycycloadduct of fullerene C60.
Scheme 13. Obtaining a sulfur-containing polycycloadduct of fullerene C60.
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Table 1. Testing oils containing C60-fullerene cycloadducts 2′, 12, 21, 30.
Table 1. Testing oils containing C60-fullerene cycloadducts 2′, 12, 21, 30.
Test SamplesPcr, kgfPw, kgfdws, mm
1Industrial oil + 5 wt% STP * + 0.005 wt% of compound 2′715960.73
2Industrial oil + 5 wt% STP + 0.005 мас.% of compound 1275>10000.76
3Industrial oil + 5 wt% STP + 0.005 мас.% of compound 2171>10000.74
4Industrial oil + 5 wt% STP + 0.005 мас.% of compound 3071>10000.51
5Industrial oil + 5 wt% of sulfidized tetramers of propylene (STP) (Control sample)793980.93
6Industrial oil + 40 wt% of sulfidized tetramers of propylene (STP) (Control sample)1005960.75
* STP—sulfidized tetramers of propylene.
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MDPI and ACS Style

Khuzin, A.A.; Tuktarov, A.R.; Dzhemilev, U.M. Sulfur-Containing Homo- and Methanofullerenes: Synthesis and Study of Tribological Properties. Chem. Proc. 2022, 12, 25. https://doi.org/10.3390/ecsoc-26-13537

AMA Style

Khuzin AA, Tuktarov AR, Dzhemilev UM. Sulfur-Containing Homo- and Methanofullerenes: Synthesis and Study of Tribological Properties. Chemistry Proceedings. 2022; 12(1):25. https://doi.org/10.3390/ecsoc-26-13537

Chicago/Turabian Style

Khuzin, Artur A., Airat R. Tuktarov, and Usein M. Dzhemilev. 2022. "Sulfur-Containing Homo- and Methanofullerenes: Synthesis and Study of Tribological Properties" Chemistry Proceedings 12, no. 1: 25. https://doi.org/10.3390/ecsoc-26-13537

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