It has been discovered that differences in electronic structure of fullerenes of various types permit separation and purification of different types of fullerenes based on chemical reactivity.
For example, C60 and C70, other fullerenes and various classical metallofullerenes contain a type of 6:6 ring junctions where two six-member rings are joined by two five-member rings. These 6:6 ring junctions form a pyracylene region or Stone-Wales patch, as shown in
The reactivity of C60 is similar to a localized, electron-deficient polyolefin, because of its isolated double bonds. Addition reactions described by A+B=C (such as Diels-Alder reactions) primarily occur at the 6:6 junctions having these localized double bonds. For example, cycloaddition reactions occur preferentially and relatively quickly at the 6:6 junctions of C60 and C70 fullerenes. Additions occur so as to minimize the formation of energetically unfavorable 5:6 double bonds. Under preferable conditions, a substantial degree of control and predictability of such reactions can be achieved.
As a contrasting example, in reactions that favor the pyracylene-type 6:6 junction, trimetallic nitride endohedral metallofullerenes, e.g., A3-nXnN@Cm fullerenes having m=80, show a tremendously reduced reaction rate relative to C60 and other fullerenes. The cage of A3-nXnN@C80 differs significantly from that of other fullerenes. (Olmstead, M. M., et. al. J. Am. Chem. Soc., 122:12220-12226, 2000) The Ih (icosahedral) C80 cage lacks the 6:6 junction sites found in C60 and C70. Localized double bonds, which favor Diels-Alder type cycloaddition reactions, do not appear to be present on the C80 cage. Further, the distribution electric charge on the surface of trimetallic nitride endohedral metallofullerenes is also affected by the caged trimetallic nitride group, promoting increased stability and reduced reactivity relative to other fullerenes.
Exploiting the differences in chemical reactivity between different types of fullerenes, a chemical method of separating different types of fullerenes from each other and/or from various contaminants can comprise: contacting a mixture comprising different fullerenes with a reagent that reacts at different rates or to a different extent with different types of fullerene in the mixture and separating at least one type of fullerene from the mixture based upon the extent of reaction between the fullerene and the reagent.
In preferred examples, a mixture of different fullerenes can comprise the soot produced in a Kratschmer-Huffman type reaction or can be the product of a solvent extraction and/or another procedure that substantially separates fullerenes from non fullerene components of soot. A mixture of different fullerenes can include two or more fullerenes of formula Cm, such as C60, C70, C80, C84, higher cage fullerenes, metallofullerenes with various carbon numbers, and trimetallic nitride endohedral metallofullerenes (e.g. A3-nXnN@Cm; where m can be typically 80 and/or 84) and may include various contaminants. Preferably, the mixture comprises A3-nXnN@Cm, where m is 80 and/or 84, and one or more of C60, C70, and metallofullerenes with various carbon numbers. Alternatively, or in addition, the mixture may comprise a fullerene and one or more contaminants, where at least one contaminant reacts with the reagent at a different rate than the fullerene, thereby permitting separation of the fullerene from the contaminant.
In preferred examples, the reaction of the reagent with a fullerene comprises formation of a covalent bond or bonds, and in more preferred examples the reaction comprises reversible formation of a covalent bond or bonds. In preferred examples, reaction comprises simultaneous formation of two covalent bonds. For example, the reaction may comprise a Diels-Alder type reaction. In a preferred embodiment, the reaction comprises a reversible Diels-Alder type cycloaddition reaction.
Where the reaction is a Diels-Alder type reaction, the reagent can comprise any diene that will convey a property to the fullerenes with which it reacts that can be used to separate those fullerenes from the mixture. As examples, the reagent can comprise cyclopentadiene, a cyclopentadiene derivative, a substituted cyclopentadiene comprising one or more substituents, cyclohexadiene, a cyclohexadiene derivative, a substituted cyclohexadiene comprising one or more substituents, or the like, including molecules such as furan. Alternatively, the reagent can comprise a substrate functionalized with a diene, such as a cyclopentadiene, a cyclopentadiene derivative, a substituted cyclopentadiene comprising one or more substituents, a furan, a cyclohexadiene, a cyclohexadiene derivative, a substituted cyclohexadiene comprising one or more substituents, or the like.
Without limitation, preferred reagents for use in these methods may include structures exemplified by formulas I, II or III where R1 and R2 can be the same or different. R1 and/or R2 are preferably chosen to convey a property to fullerenes with which the reagent reacts. As an example R1 and/or R2 may be —COOCH3 which can be converted to —COO− following reaction with a mixture of fullerenes to convey solubility in aqueous solution to those fullerenes with which it reacts, or may comprise a perfluorocarbon moiety, which can convey solubility in a perfluorinated hydrocarbon solvent. In various alternatives, R1 and/or R2 can convey affinity to a substrate, may cause aggregation of reacted fullerenes, or may link the diene to a substrate such as a silica gel or polymer resin. It should be noted that the arrangement and number of substituent groups need not be as illustrated in the examples, that is, in a substituted cyclopentadiene or hexadiene there may be one or more than one Ri, and the Ri may be bonded to any carbon of the ring.
As another example, in a variation of the method utilizing fluorous substituted diene as a reagent, the reaction can be performed in a vessel containing two immiscible solvents such as perfluorocarbon and toluene. Unreacted fullerenes are soluble in toluene.
Accordingly, a method of separating different types of fullerenes from each other and/or from various contaminants can comprise: contacting a mixture comprising different types of fullerene with a reagent that reacts at different rates or to a different extent with different types of fullerene in the mixture where the reagent conveys a property to a fullerene with which it reacts that can be used to separate reacted from unreacted fullerene. The method can further comprise separating the fullerenes based upon the extent of reaction between each type of fullerene and the reagent. In a simple example, the reagent conveys a change in solubility upon those types of fullerene that react with the reagent and the types of fullerene can be separated using phase extraction. In alternative methods, the reagent reacts to a different extent with different types of fullerene, for example as a function of the number of pyracyclene units, and the types of fullerene can be separated based upon the extent of reaction, e.g. the number of adduct groups per fullerene.
The methods described herein can further comprise preparing a mixture of fullerenes from soot produced in a in a Kratschmer-Huffman reactor by solvent extraction. For example, a mixture of fullerenes produced in the Kratschmer-Huffman reaction can be extracted in o-xylene prior to contacting the mixture with a reagent. The methods may further comprise one or more additional purification steps, such as a chromatographic separation before or after contacting the mixture with a reagent and separating at least one type of fullerene based on the extent of reaction with the reagent.
Attachment of fullerenes to solid substrates comprises an alternative approach to chemical separation of classical Cm fullerenes such as C60 and higher carbon number empty-cage and metallofullerenes from A3-nXnN@Cm. Classical fullerenes such as C60 and C70 can react with polymer-supported dienes. These addition reactions occur at room temperature and are reversible. Thermally stable silica-supported dienes prepared as in
Accordingly, a method of separating different types of fullerenes from each other and/or from various contaminants can comprise: contacting a mixture comprising different fullerenes with a functionalized substrate that reacts at different rates or to a different extent with different types of fullerenes in the mixture such that the reacted fullerene is physically removed from the solution. Such a reaction can be conducted in a batch vessel or in a continuous flow vessel. In a continuous flow vessel the mixture may be flowed through a bed of functionalized substrate or contacted in a continuous countercurrent arrangement.
As has been illustrated, separating the reacted material can comprise separation based on solubility, and/or physical separation such as where the reagent is attached to a substrate. In various embodiments, other separation techniques may be utilized, such as any affinity and chromatographic separation methods that may be facilitated by selection of an appropriate substrate. In preferred embodiments, substantially all of at least one type of fullerene is removed from the mixture.
In preferred embodiments, after separation the method further comprises causing the reaction of reagent and fullerene to be reversed. In some embodiments, this permits recovery of reacted fullerene and/or reuse of the reagent.
As a way of illustrating methods of removing one or more types of fullerene from a mixture of fullerene molecule, the foregoing examples illustrate the use of Diels-Alder type reactions that occur at a faster rate to C60 over C80 fullerenes and which do not occur to any significant extent to trimetallic nitride endohedral metallofullerenes such as A3-nXnN@C80. To illustrate an alternative approach, a reagent may be chosen that reacts at a higher rate with fullerenes of type A3-nXnN@Cm than other types of fullerenes. One such reagent can be a redox reagent or electrons having an appropriate potential which can selectively react with fullerenes of type A3-nXnN@Cm, preferably permitting separation of fullerenes of type A3-nXnN@Cm from a mixture while leaving empty-cage fullerenes.
It has been discovered that, while photo-induced energy and electron transfer for trinitiride endohedral metallofullerenes (e.g., of formula A3-nXnN@Cm) are similar to that for the empty cage fullerenes, the energies are different enough to allow selective electrochemical and photochemical reactions.
Without wishing to be bond by theory, the following theoretical and experimental discussion may help explain and illustrate the physical basis underlying this discovery. The low-lying empty orbitals of C60 lead to high electron affinity and a particularly long-lived triplet excited state as well as ready participation as the acceptor component in donor-acceptor dyads. An electron affinity of about 2.60-2.80 eV for C60 has been estimated from photoelectron spectra. Moreover, C60 can accept up to six electrons, giving rise to the ions C60-n (n=1-6). The vertical electron affinity for C60 was computed to be 2.85 eV, a value that is in excellent agreement with the experimental data. The empty cage C80 molecule of Ih symmetry has an even larger vertical electron affinity of 3.75 eV. By comparison, A3-nXnN@Cm undergoes modification of its electron affinity due to electron acceptance from the captured trimetallic structure. For example, Sc3N@C80 undergoes modification of the highest occupied molecular orbitals (HOMO)/lowest unoccupied molecular orbitals (LUMO) due to the formal transfer of six electrons from the Sc3N unit to the cage, which reduces the electron affinity of this compound to 2.99 eV, comparable to the measured value of 2.81 eV. Theoretical electron acceptance values for several nanocompounds are shown in Table 1.
Based on the difference in the first oxidation potential between empty C60 and the Ih and D5h isomers of Sc3N@C80 (about 300 mV), it is possible, in an exemplary preferred method, to extract the Ih only Sc3N@C80. In preferred embodiments, the reaction can be accomplished by electrochemical means or by using redox reagent such as a chemical oxidant.
Electrochemical studies have been carried out on various fullerenes of type A3-nXnN@Cm. The cyclic voltammogram of Sc3N@C80 illustrated in
As an example, soot containing Sc3N@C80 obtained from Luna Innovations was pre-purified by recrystallization from hot o-xylene. 1.0 mg of the resulting mixture of fullerenes Sc3N@C80 was dissolved in 1.0 mL of dry 0.05 M TBAPF6 (tetrabutylammonium hexafluorophosphate) solution in o-dichlorobenzene. A platinum working electrode (1 mm), platinum wire counter electrode, and an Ag/Ag+ reference electrode in an 0.1 M TBAPF6/0.01 M AgNO3 CH3CN solution was used to examine the electrochemical properties of Sc3N@C80.
The cyclic voltammogram of Sc3N@C80 illustrated in
The first anodic peak of Sc3N@C80 appears to be a well-behaved electrochemically reversible peak. (
A Diels Alder-SC3N@C80 derivative was prepared as described by E. B. Lezzi et al., J. Am. Chem. Soc., 2002, 124, 524. The derivative is shown in
As illustrated, fullerenes of various types can be subjected to electrochemical reactions or redox reactions which occur at different rates or to a different extent depending on the type of fullerene. Thus, a method of separating one or more types of fullerenes from a mixture of different types of fullerenes can comprise contacting the mixture of fullerenes with a reagent that reacts with one or more types of fullerene in the mixture at a different rates or to a different extent than one or more other types of fullerene in the mixture and separating one or more types of fullerene on the basis of whether or to what extent the fullerenes have reacted with the reagent. In preferred embodiments, the reagent can be a charged moiety, such as an electron, or a chemical redox reagent, for example a chemical reducing agent or a chemical oxidation agent. Alternatively, or in addition to the modes of separation that have been described above, separating reacted fullerenes may include separation on the basis of redox state or ionization, for example by electrochemical means, affinity to an electrode, differences in solubility of charged species, and the like.
For example, a method can comprise contacting a mixture of fullerenes with electrodes at a potential selected to preferentially change the redox state of one or more types of fullerenes, such as fullerenes of type A3-nXnN@Cm. Fullerenes of a type preferentially oxidized or reduced at the selected potential can be separated based upon ionization. As another example, a method can comprise contacting a mixture of fullerenes with a chemical redox reagent, such as a chemical oxidizer, having an appropriate redox potential to preferentially oxidize or reduce one or more type of fullerene. In preferred embodiments, differences in ionization potential and electron affinity of types of fullerenes can be exploited to choose a potential where fullerene of type A3-nXnN@Cm is reacted but fullerene of type Cm is not reacted. In other preferred embodiments, a potential is chosen where a fullerene of type X3N@C80 of Ih symmetry reacts but X3N@C80 and X3N@C78 of D5 symmetry do not react. In preferred embodiments, the reaction is an electrochemical oxidation reaction, or a chemical oxidation reaction. In preferred embodiments, the reaction may be reversed after separation.
As used herein the word “or” between two things includes a combination of the things, the word “and” includes the alternative, and singular terms include the plural unless the context in which these words are used indicates otherwise. A reversible reaction is understood to be a reaction that can be reversed by application of conditions such as heat, light, pH, reagents, and the like, which results in substantially restoring at least one of the starting materials of the reversible reaction to its state before the reversible reaction or a functionally similar state. For example, a reaction is reversible if a covalent bond or bonds formed in the reaction can by broken by application of an amount of heat that does not destroy the restored starting material. That a reagent has a reaction rate with a material includes the case of no reaction or substantially no reaction unless otherwise indicated. Separating a component of a mixture from the mixture includes any process wherein a substantial majority of the component is removed from the mixture. Separating substantially all of a component from a mixture means that more than about 90%, and preferably more than 95% of the component is removed from a mixture.
While the invention has been described in detail with reference to preferred embodiments thereof, it will be apparent to one skilled in the art that various changes can be made, and equivalents employed, without departing from the scope of the invention.
This application claims the benefit of U.S. Provisional Application No. 60/640,234, filed on Jan. 3, 2005, the entire contents of which are hereby incorporated herein by reference in their entirety.
Work described herein was supported by the NSF under Grant #DMI-0232204, Grant # DMI-0321630, and Grant #DMI-0349691. The U.S. Government may have certain rights in the invention.
Number | Date | Country | |
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60640234 | Jan 2005 | US |