Method for separating and recovering carbon nanotubes
11440800 · 2022-09-13
Assignee
Inventors
Cpc classification
C01B2202/20
CHEMISTRY; METALLURGY
B82Y30/00
PERFORMING OPERATIONS; TRANSPORTING
B82Y40/00
PERFORMING OPERATIONS; TRANSPORTING
International classification
B82Y30/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The invention has for its object to provide an aqueous solution for structural separation capable of acting on carbon nanotubes (CNTs) having a specific structure thereby separating them with high accuracy, a separation and recovery method capable of allowing the aqueous solution to act on CNTs having a specific structure thereby separating and recovering them, and CNTs obtained by the separation and recovery method. According to the invention, it is possible to separate CNTs having a specific structure with high accuracy by solubilizing lithocholic acid or a lithocolic acid isomer that has high hydrophobicity and is insoluble in water by itself, and a carbon nanotube obtained by using an aqueous solution containing lithocholic acid or a lithocholic acid isomer, each solubilized, as an aqueous solution for structural separation of CNTs.
Claims
1. A method for separating and recovering carbon nanotubes, comprising; eluting carbon nanotubes having a diameter of 1 nm or less from a gel on which carbon nanotubes are adsorbed, by using an aqueous solution containing at least one selected from the group consisting of solubilized lithocholic acid and solubilized lithocholic acid isomer.
2. A method for separation and recovery of carbon nanotubes as recited in claim 1, wherein said lithocholic acid, and said lithocholic acid isomer are solubilized by another surfactant.
3. A method for separation and recovery of carbon nanotubes as recited in claim 2, wherein said another surfactant is sodium dodecyl sulfate and/or sodium cholate.
4. A method for separation and recovery of carbon nanotubes as recited in claim 1, further comprising, after eluting carbon nanotubes having a diameter of 1 nm or less, eluting carbon nanotubes remaining in the gel with a diameter of larger than 1 nm.
5. A method for separation and recovery of carbon nanotubes as recited in claim 1, wherein said lithocholic acid and said lithocholic acid isomer are solubilized by another surfactant.
6. A method for separation and recovery of carbon nanotubes as recited in claim 5, wherein said another surfactant is sodium dodecyl sulfate and/or sodium cholate.
7. A method for separating and recovering carbon nanotubes as recited in claim 1, wherein the carbon nanotubes with a different chiral index are selectively eluted from the gel on which the carbon nanotubes are adsorbed.
8. A method for separation and recovery of carbon nanotubes as recited in claim 7, wherein said lithocholic acid and said lithocholic acid isomer are solubilized by another surfactant.
9. A method for separation and recovery of carbon nanotubes as recited in claim 8, wherein said another surfactant is sodium dodecyl sulfate and/or sodium cholate.
10. A method for separation and recovery of carbon nanotubes as recited in claim 1, wherein the aqueous solution containing the at least one selected from the group consisting of solubilized lithocholic acid and solubilized lithocholic acid isomer is prepared to obtain an aqueous solution for separation; preparing the gel containing carbon nanotubes; mixing the gel and the aqueous solution for separation to elute the carbon nanotubes; and separating the carbon nanotubes.
Description
BRIEF EXPLANATION OF THE DRAWINGS
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MODES FOR CARRYING OUT THE INVENTION
(36) The present invention will now be explained below.
(37) Lithocholic acid is of high hydrophobicity and substantially insoluble in water because of having hydrophilic hydroxyl groups less than those of cholic acid or deoxycholic acid having a similar steroid skeleton. The solubility of lithocholic acid in water is 0.000002%, and isomers having a hydroxyl group at 3β rather than 3α position, or 7α or 7β position have a low solubility value as well (Non-Patent Publication 11).
(38) While some surfactants in a monomolecular form are insoluble in water, they may be soluble in water because of forming a micelle having a plurality of associated molecules. However, lithocholic acid has a micelle formation temperature of higher than 65° C., meaning that it cannot form any micelle at room temperature. A lithocholate that is a salt of lithocolic acid is also not used for CNT dispersion due to its slight solubility in water (Non-Patent Publication 2). Thus, lithocholic acid has also not been used as any surfactant for separation.
(39) On the other hand, cholic acid, deoxycholic acid, taurocholic acid, and taurodeoxycholic acid having a similar steroid skeleton form a micelle at room temperature, and become soluble in water by itself, and salts thereof are soluble in water as well so that they are widely used as surfactants for dispersion and separation of CNTs.
(40) According to the invention, lithocolic acid and its isomers that have hardly be used so far because of high hydrophobicity and insolubility in water in a single form are made soluble in water under proper conditions, providing an aqueous solution for structural separation capable of accurately separating CNTs having a specific structure.
(41) In place of the aqueous solution of mixed SDS/SC/DOC surfactants set forth in Non-Patent Publication 9, an aqueous solution containing lithocolic acid or a lithocholic acid isomer solubilized according to the invention was used in the elution step of CNTs adsorbed to a gel. As a result, the aqueous solution has been found to have the following functions.
(42) Function (1): only CNTs having a diameter of smaller than 1 nm are eluted for separation and recovery in descending order of diameter.
(43) Function (2): only CNTs having a specific structure inclusive of (9,1), (10,0), (8,3) and (9,2) are eluted under a specific surfactant condition for separation and recovery in descending order of diameter.
(44) Function (3): any CNTs having a diameter of larger than 1 nm are not eluted so that only CNTs remaining in the column with a diameter of larger than 1 nm are eluted by an aqueous solution of mixed SDS/SC/DOC surfactants for separation and recovery of single-structure CNTs.
(45) Three such novel functions make it possible to separate single-structure CNTs that could not be isolated by use of an aqueous solution of conventional surfactants, resulting successfully in exhaustive separation from the raw material of 22 species of semiconducting CNTs having a diameter in the vicinity of 1 nm, inclusive of 16 species of high-purity, single-structure CNTs. Metallic CNTs can also be recovered after the separation of semiconducting CNTs.
(46) Three such functions as provided by an aqueous solution for structural separation containing lithocholic acid solubilized according to the invention are quite different from those provided by a conventional aqueous solution for structural separation containing SC or DOC, as described below.
(47) In other words, a prior art aqueous solution for structural separation containing SC or DOC has acted on both CNTs having a diameter of smaller than 1 nm and CNTs having a diameter of larger than 1 nm, preventing an enhancement in the accuracy of separation thanks to such incomplete diameter selectivity. On the contrary, an aqueous solution for structural separation containing lithocholic acid or lithocholic acid isomer solubilized according to the invention is of complete diameter selectivity in the sense of acting on only CNTs having a diameter of smaller than 1 nm, thereby making accurate separation possible. From the previous report (Non-Patent Publication 10), it has been expected that a surfactant whose hydrophobicity is higher than that of DOC would act mainly on the separation of CNTs having a diameter of smaller than 1 nm; however, the complete diameter selectivity of acting on only CNTs having a diameter of smaller than 1 nm is a function that cannot be predicted from the previous report whatsoever. Lithocholic acid and its isomers are of extremely high hydrophobicity and hardly soluble in water; there is none of the cases where lithocholic acid and its isomers are used for an aqueous solution for CNT separation or an aqueous solution for CNT dispersion. For this reason, the method of the invention, wherein lithocholic acid or its isomer is solubilized to provide unprecedented functions, is quite unique, and the method for separation and recovery of CNTs using an aqueous solution for separation containing lithocholic acid solubilized according to the invention ensures that the species of single structures to be separated reach a maximum in number among all existing separation/recovery methods.
(48) Lithocholic acid used herein, the surfactants needed for solubilization and bases are inexpensive, commercially available chemicals. They are combined with separation methods using gels (Non-Patent Publication 9 or the like) so that a large amount of CNTs can automatically be separated in inexpensive installation for a short period of time with high purity, which is extremely useful for mass production of single-structure CNTs on an industrial scale. As described above, it is known that methods for separation of CNTs using gels are carried out according to similar principles using a common surfactant: they may be applied not only to separation by gels but also to separations such as density gradient ultracentrifugation separation, and liquid/liquid two-phase separation.
(49) The present invention will now be explained in further details.
(50) Lithocholic Acid and Lithocholic Acid Isomers
(51) Among cholic acids having a steroid skeleton, lithocholic acid used herein has only one hydroxyl group, as represented by 3α-hydroxy-5β-cholic acid and its enantiomer.
(52) Lithocholic acid may include an isomer having only one hydroxyl group. Typically, the isomer comprises diastereomer wherein the hydroxyl group is located in 3β position rather than 3α position and its enantiomer, diastereomer wherein the hydroxyl group is located in 7α position rather than 3α position and its enantiomer, or diastereomer wherein hydrogen is located in 5α position rather than 5β position and its enantiomer (see Non-Patent Publication 11).
(53) Having very similar physicochemical qualities such as solubility in water, these isomers are all capable of solubilization, but commercially available 3α-hydroxy-5β-cholic acid is preferred in view of cost.
(54) Lithocholic acid turns into a lithocholic acid salt by way of neutralization reaction with a base. For instance, when it undergoes neutralization reaction with sodium hydroxide, there is sodium lithocholate salt obtained. When there is lithocholic acid or the lithocholate salt in water, the proportion of lithocholic acid grows high under acidic conditions whereas the proportion of lithocholate salt grows high under alkaline conditions. This is also true of lithocholic acid isomers.
(55) Therefore, the lithocholic acid and lithocholic acid isomer solubilized according to the invention include their salts.
(56) Any base may be used for neutralization of lithocholic acid and a lithocholic acid isomer, in which any lithocholate salt and any lithocholic acid isomer may be used. However, it is understood that the lithocholate salt and lithocholic acid isomer salt are preferably of the same type as the surfactant to be mixed with the inventive aqueous solution for structural separation. For instance, sodium salts such as sodium dodecyl sulfate and sodium cholate are primarily used for the dispersion and separation of CNTs. It is then preferable to use a sodium salt obtained by using sodium hydroxide as the base to be added to lithocholic acid.
(57) Solubilization
(58) In one embodiment of solubilizing lithocholic acid and lithocholic acid isomer according the invention, they are solubilized by way of neutralization reaction in an aqueous solution of other surfactant, and the resulting aqueous solution for separation containing lithocholic acid and lithocholate salt is used.
(59) Specifically, lithocholic acid and its isomer that are each insoluble in water by itself are first mixed with an aqueous solution of other surfactant, and then solubilized under pH control.
(60) For the other surfactant used for solubilization of lithocholic acid and its isomer, any of anionic surfactants, cationic surfactants, amphoteric surfactants, and nonionic surfactants may be used with the proviso that they can solubilize lithocholic acid and its isomer. These surfactants may be used alone or in admixtures. Note here that the surfactant needed for structural separation of CNTs contains an alkyl sulfate having 10 to 14 carbon atoms, dodecane sulfonic acid, dodecanoylsarcosine, dodecanoic acid, cholic acid, n-dodecylphosphocholine and so on, among which sodium dodecyl sulfate (SDS) and sodium cholate (SC) are most preferable in view of versatility because they are used with a variety of CNT separation processes inclusive of separation using gels, density gradient ultracentrifuge separation, and liquid/liquid two-phase separation.
(61) These surfactants used for solubilization of lithocholic acid and its isomer may be used in combination with other materials such as high-molecular polymers, DNAs, proteins, alcohols and organic solvents.
(62) In the invention, while the concentrations of the surfactants used for solubilization vary with the types and concentrations of the CNTs used, the types of the surfactants used, the separation methods used, and so on, it is understood that they may be used in 0.01% to 25% as an example.
(63) Referring to the solubilization of lithocholic acid and its isomer, pH control is needed for the solubilization of lithocholic acid and its isomer that are each insoluble in water by itself; it is carried out by the addition of a base. The base may be added before or after the mixing of lithocholic acid and its isomer with an aqueous solution of other surfactants. While any base may be used as that base, it is understood that a base that forms a sodium salt to be used for structural separation of CNTs is preferred in view of versatility.
(64) Aqueous Solution for Structural Separation
(65) Any concentration may be used as the concentrations of lithocholic acid and lithocholic acid isomer solubilized in the inventive aqueous solution for structural separation; a preferable concentration varies with the species and concentrations of the CNTs used, the types of the surfactants used, the separation processes used, and so on. For instance, when so-called HiPco CNT species are separated in an aqueous solution of mixed SC/SDS, practically all CNTs may be separated in a range of 0.005% to 0.4%.
(66) Separation of CNTs Using the Inventive Aqueous Solution for Structural Separation
(67) In the present invention, there is no limitation imposed on the processes and means using the inventive aqueous solution for structural separation. For instance, CNTs and a density gradient agent may be added to the inventive aqueous solution for structural separation of CNTs due to density differences. Alternatively, the inventive aqueous solution for structural separation may be allowed to act on two types of liquids to undergo phase separation thereby causing separation of CNTs contained in the aqueous solution for structural separation or separation of CNTs dispersed in the two liquids. Yet alternatively, the inventive aqueous solution for structural separation may be allowed to act on a gel for separation of CNTs contained in the aqueous solution for structural separation or separation of CNTs adsorbed to the gel.
(68) While the separation temperature varies with the type of surfactant used, the separation process used and so on, it is understood that any temperature may be used. Note here that at a temperature of higher than 30° C., the solubilized lithocholic acid would also act on CNTs having a diameter of larger than 1 nm, ending up with a loss of the complete diameter selectivity: a temperature of less than 30° C. is preferred.
(69) In the invention, it does not matter whether or not the inventive aqueous solution for structural separation contains CNTs. Thus, it may also be used as a CNT-containing dispersion aqueous solution or a CNT-free aqueous solution dedicated to separation alone. With a mixed SDS/SC/DOC surfactant having the same surfactant concentration, similar effects have actually been obtained at the time when a CNT-containing aqueous solution is allowed to act on a column and at the time when a CNT-free aqueous solution is allowed to act on a column to which CNTs are adsorbed (Non-Patent Publication 9).
(70) When the inventive aqueous solution for structural separation is used for separation using gels, it may be employed in both an adsorption step to a gel and an elution step from the gel. In the adsorption step, the inventive aqueous solution for structural separation having CNTs dispersed in it is added to a column for selective adsorption of CNTs having a specific structure. Because, in this case, the separation by the inventive aqueous solution for structural separation takes place in the adsorption step, what will happen in the subsequent elution step does not matter. When the inventive aqueous solution for structural separation is used in the elution step, it is added to a column to which CNTs are adsorbed for selective elution of CNTs having a specific structure. Because, in this case, the separation by the inventive aqueous solution for structural separation takes place in the elution step, what happened in the previous adsorption step does not matter. Note here that in the adsorption and elution steps, there is preferably no variation of other components than the lithocholic acid and lithocholic acid isomer solubilized according to the inventive aqueous solution for structural separation. This helps prevent elution of CNTs due to a change in other components to make use of only an effect arising from a change in the solubilized lithocholic acid or lithocholic acid isomer. A merit of using the inventive aqueous solution for structural separation in the elution step is that after its addition, an aqueous solution for structural separation having an increased surfactant concentration is added so that CNTs incapable of elution under the previous conditions can be eluted, making it possible to use a single column for separation under a plurality of conditions. If changes in the concentration of the surfactant added to the aqueous solution for structural separation are kept small, even CNTs hard to separate under similar conditions can then be accurately separated.
(71) Gel Used Herein
(72) The gels used herein may be well-known glucide or saccharide-based gels such as dextran-based gels (Sephacryl: a homopolymer of allyl dextran and N,N′-methylenebisacrylamide made by GE Healthcare), agarose gels, starch gels, acrylamide gels, and so on. The gel used herein may comprise a mixture of such gels, or a mixture or compound of gel constituents with other substances.
(73) The gel concentration may be set such that the final concentration will be 0.01% to 25%.
(74) When the inventive method for separation and recovery of CNTs is in the form of a gel separation process, it may be applied not only to a column process but also to a batch process. For the separation using a column, a liquid may be fed to the column while a solvent falls down due to gravity in an open column or, alternatively, a solution may be fed by a pump to a closed column. In the separation process using a pump, a flow rate may be increased for mass processing. Automatic separation may also be carried out using chromatography equipment.
(75) In the method for separation and recovery of CNTs according to the invention, the conditions under which the functions work (conditions for preparation of a solubilized lithocholic-acid-containing aqueous solution for structural separation, and concentrations and temperatures of surfactants) are set in the examples described below. Note here that such conditions are provided for predetermined environments concerning the species of CNTs used, the species of gels used or the like, but they may otherwise be varied depending on the environments.
(76) It is here noted that CNTs “having a specific structure” to be separated and recovered according to the invention include those having a specific structure defined by diameter, chirality, local radius of curvature, and a combination thereof, and have characteristic features based on that structure, which features may be clearly distinguished from those of CNTs before the separation operation by measurements of ultraviolet/visible/near-infrared light absorption spectra, fluorescence spectra, Raman spectra, etc. Therefore, such CNTs obtained after separation and recovery with a specific structure may comprise a mixture having two or more species extracted as the specific structure, to say nothing of CNTs composed substantially of a single-structure. Within a range where the fact that such CNTs having a specific structure are selectively separated and recovered can be confirmed based on such measurements as mentioned above, the CNTs may comprise a mixture including a slight amount of other arbitrary structures.
(77) The present invention is applied to a mixture containing metallic CNTs and semiconducting CNTs (hereafter simply called the CNTs) or a mixture of semiconducting CNTs having varying structures, and relates to a method for separating the mixture into metallic and semiconducting CNTs, and separating semiconducting CNTs having varying structures, or a method for separating CNTs having varying structures.
(78) In the method for separating CNTs having varying structures according to the invention, the aqueous solution for structural separation containing a solubilized lithocholic acid or a solubilized lithocholic acid isomer is added to a column having CNTs adsorbed to it for selective elution of CNTs having a specific diameter and chiral angle or, alternatively, the CNTs remaining in the column are then used.
(79) Any CNTs may be used for the inventive separation without giving rise to problems in terms of production processes, shapes (such as diameter and length), structures (such as single and double layers), and so on.
(80) Preparation of the CNT Dispersion Liquid
(81) Synthesized CNTs are usually in the form of dozens to hundreds of bundles containing both metallic CNTs and semiconducting CNTs. Prior to separation of metallic CNTs and semiconducting CNTs or separation of CNTs due to structure, it is of importance that they are dispersed and solubilized into an isolated state for each bundle so that they can exist stably over an extended period of time.
(82) More specifically, the mixture of CNTs is added to a solution to which surfactants are added as a dispersant, and then fully treated with ultrasonic waves to disperse and isolate the CNTs. The solution subjected to this dispersal treatment contains dispersed/isolated CNTs, CNTs that remain bundled because they are not dispersed and isolated, amorphous carbon that is a byproduct of synthesis, metal catalysts, and so on.
(83) The dispersion liquid obtained after ultrasonic wave treatment is centrifuged by a centrifugal separator thereby causing precipitation of CNTs remaining bundled, amorphous carbon and metal catalysts, but isolated CNTs forming micelles with the surfactants can be recovered in a supernatant form. The thus obtained supernatant provides a sample used for separation of CNTs.
(84) Water is most preferable as the solvent used for preparation of CNT dispersion liquids. With this in mind, water is used for preparation of CNT dispersion liquids.
(85) Any of anionic surfactants, cationic surfactants, amphoteric surfactants, and nonionic surfactants may be used with the proviso that they are capable of structural separation of CNTs. These surfactants may be used alone or in admixtures.
(86) Ultraviolet/visible/near-infrared light absorption spectra are measured so as to make an estimation of the ratio between metallic CNTs and semiconducting CNTs.
(87) Here take the results of using CNTs synthesized by the HiPco process (HiPco-CNTs having a diameter of 1.0±0.3 nm) as an example. An absorption wavelength band called M11 (approximately 450 to 650 nm) comes from metallic CNTs. Three absorption wavelength bands: S11 (greater than approximately 900 nm), S22 (approximately 650 to 900 nm) and S33 (less than approximately 450 nm) come from semiconducting CNTs. There are changes of absorption wavelength bands (M11, S11, S22, S33) depending on the average diameter of CNTs measured. As the average diameter decreases, it causes the wavelength band to shift to a shorter wavelength side, and as the average diameter increases, it causes the wavelength band to shift to a longer wavelength side.
(88) Referring here to the measurement of light absorption spectra, the absorptions of CNTs overlap each other with the result that it is impossible to determine whether a single peak comes from a single CNT or from the overlapping of a plurality of varying species of CNTs. Therefore, the measurement of fluorescence spectra capable of detection of semiconducting CNTs for each chiral was also used in combination. The results are depicted in the form of a contour map with excitation wavelength as ordinate, fluorescence wavelength as abscissa, and fluorescence intensity as color density. What spots and then appears is fluorescence coming from a semiconducting CNT having a single chirality. The associated chirality is shown near the spot.
EXAMPLES
(89) By way of example but not by way of limitation, the present invention is now explained in greater details.
(90) Note here that in the following examples, “LC” refers to solubilized 3α-hydroxy-5β-cholic acid, and includes 3α-hydroxy-5β-cholic acid and sodium 3α-hydroxy-5β-cholate.
(91) In the following examples, bear in mind that the “aqueous solution of mixed SDS/SC/LC surfactants” and the “aqueous solution of mixed SDS/SC/DOC surfactants” will be respectively called “SDS/SC/LC” and “SDS/SC/DOC”, and the “elution step using the aqueous solution of mixed SDS/SC/LC surfactants” and the “elution step using the aqueous solution of mixed SDS/SC/DOC surfactants” will be respectively called the “SDS/SC/LC elution” and the “SDS/SC/DOC elution”.
Example 1
(92) In this example, an LC-containing aqueous solution for structural separation was prepared using lithocholic acid insoluble in water.
(93) Preparation of the LC-Containing Aqueous Solution for Structural Separation
(94) An LC-containing aqueous solution for structural separation was prepared by solubilization of lithocholic acid.
(95) In view of cost, 3α-hydroxy-5β-cholic acid, only one commercially available among lithocholic acid isomers was used as the lithocholic acid.
(96) The surfactants and base to be mixed for solubilization of lithocholic acid were selected as follows: in the examples as described later, the aqueous solution for structural separation is used with gel chromatography (Non-Patent Publication 9) that makes it easy to change or vary the surfactant concentration and is dedicated to the search for separation conditions, where an aqueous solution of sodium dodecyl sulfate (SDS) and sodium cholate (SC) is used in the adsorption step of CNTs. It is thus desirable to use the same surfactant in the CNT elution step. For this reason, the mixed SDS/SC surfactants were used as the surfactants mixed herein, and sodium hydroxide was used as the base.
(97) First of all, an aqueous solution of 0.5% SDS/0.5% SC was added to commercially available lithocholic acid (Tokyo Chemical Industry Co., Ltd.) in such a way as to provide a lithocholic acid concentration of 0.1%. Thereafter, an aqueous solution of sodium hydroxide was added such that the molar concentration of lithocholic acid was the same as that of sodium hydroxide, and then fully stirred. The surfactant composition at this time is assumed to be 0.5% SDS/0.5% SC/0.1% LC. Further, similar experiments were repeated in varying SDS concentrations, varying SC concentrations, and varying LC concentrations.
(98) Identification of Solubility
(99) First, an aqueous solution of 0.5% SDS/0.5% SC was added to lithocholic acid in an amount equivalent to 0.1% and fully stirred, yielding a cloudy liquid with lithocholic acid residues observed. An aqueous solution of sodium hydroxide was added to the liquid and fully stirred to form a transparent aqueous solution, identifying that an aqueous solution of 0.5% SDS/0.5% SC/0.1% LC was prepared. For comparisons, on the other hand, similar experimentation was carried out with the addition of deionized water in place of the aqueous solution of SDS/SC, failing to obtain any transparent aqueous solution. From this, it has been found that both the base such as sodium hydroxide and the surfactants such as SDS/SC are required for the preparation of an LC-containing aqueous solution. One possible reason for this is that lithocholic acid insoluble by itself in water turns into a lithocholate salt that is then taken in a micelle of SDS/SC or forms a micelle mixed with SDS/SC thereby rendering lithocholic acid soluble in water.
(100) Then, similar experiments were repeated while the concentration of the SDS/SC solution mixed was varied. The SDS concentration was varied from 0.3% to 0.9%, and the SC concentration was varied from 0.3% to 0.9%. In any SDS concentration and any SC concentration, it has been found that a transparent aqueous solution can be prepared up to the LC concentration of 0.2%. The thus prepared aqueous solution is used as the LC-containing aqueous solution for structural separation.
Example 2
(101) The LC-containing aqueous solution for structural separation obtained in Example 1 was used for separation of CNTs. In this example, gel column chromatography capable of controlling surfactant concentrations as desired was used to search for detailed separation conditions. To make the search for separation conditions efficient and enhance separation accuracy, the LC-containing aqueous solution for structural separation was used in the elution step of CNTs. The LC-containing aqueous solution for structural separation was added to a column to which CNTs were adsorbed, and while the LC concentrations were stepwise varied, CNTs having a specific structure were selectively eluted in the respective concentrations.
(102) Preparation of the CNT Dispersion Liquid
(103) An aqueous solution of 0.5% SC (30 ml) was added to 30 mg of Hipco-CNTs (CNI Co., Ltd.: CNTs synthesized by a chemical vapor deposition process with a diameter of 1.0±0.3 nm). Using a chip type ultrasonic crusher (Sonifier made by Branson Co., Ltd. with a tip diameter of 0.5 inch), this solution was ultrasonically processed for 6 hours at an output of 20 W/cm.sup.2 while it was cooled in cold water. After a dispersion liquid obtained by ultrasonic processing was ultracentrifuged (for two hours at 210,000×g), 80% of the resultant supernatant were recovered. Thereafter, powders of SDS were added to the CNT dispersion liquid to prepare a CNT dispersion liquid of the SDS/SC surfactants. Using powders of SDS and de-ionized water, the concentration of the SDS/SC surfactants was adjusted. In Example 2, the concentrations of the surfactants in the CNT dispersion liquid to be added to the column were adjusted to 0.5% for SDS and 0.5% for SC. This surfactant concentration has been well used as the condition under which semiconducting CNTs contained in Hipco-CNT are adsorbed to the gel (Non-Patent Publication 9).
(104) Preparation of the Column and Separation
(105) Gel beads (Sephacryl S-200 made by GE Healthcare Co., Ltd.) were used for a column carrier. The gel beads were filled up in a plastic column (Terumo syringe made by Terumo) having a capacity of 5 mL in such a way as to provide a volume of about 3 mL. After deionized water passed through the column, it was equilibrated with an aqueous solution of 0.5% SDS/0.5% SC having the same concentration as those of the surfactants in the CNT dispersion liquid, and the CNT dispersion liquid was then added thereto in an amount of 20% based on the gel volume to carry out the CNT elution step. Thereafter, an aqueous solution of 0.5% SDS/0.5% SC was added and the column was washed until the eluted liquid became colorless and transparent. An LC-containing aqueous solution for structural separation was added thereto for carrying out the CNT elution step. In this example, the concentration of SDS and the concentration of SC were kept invariable in the adsorption and elution steps so that CNTs were prevented from further elution due to changes in the SDS and SC concentrations for the purpose of studying contributions only due to changes in the LC concentration. First, an aqueous solution of 0.5% SDS/0.5% SC/0.01% LC was added to recover CNTs eluted out of the column. Similar operations were carried out while the LC concentration was varied at an increment of 0.01% from 0.02% to 0.10% but the SDS concentration and the SC concentration were kept invariable. Such operations for recovering CNTs eluted in the respective surfactant concentrations while the surfactant concentration increased stepwise are herein called stepwise elution. The separation was carried out at 20° C.
(106) Measurement of the Light Absorption Spectra
(107) Given the semiconducting species, the light absorption spectra of CNTs having a single structure have absorption peaks called S.sub.11 and S.sub.22 observed from a long wavelength side. These absorption peaks vary in terms of wavelength depending on diameters, and shift to a long wavelength side in the case of CNTs having a large diameter and to a short wavelength side in the case of CNTs having a small diameter. Synthesized CNTs are in a mixture form having a variety of diameters and chiral angles, and the light absorption spectra are observed while the peaks of such mixtures overlap each other.
(108) The light absorption spectra of an eluate obtained through the SDS/SC/LC elution are shown in
(109) For comparative purposes,
(110) This suggests that the SDS/SC/LC elution is different from the SDS/SC/DOC elution in terms of the CNT species eluted and remaining in the column.
(111) Measurement of the Fluorescence Spectra
(112) With the light absorption spectra, it is unlikely to detect the desired peak due to the overlapping of another absorption peak thereon. Therefore, fluorescence spectra were measured so that discrete chiralities of semiconducting CNTs could be detected while making a distinction between them.
(113) The fluorescence spectra of eluate (corresponding to the sample in
(114) For comparative purposes,
(115) Chirality Distribution and Determination of Separation Order
(116) Absorption peaks called S.sub.11, S.sub.22 and observed in the light absorption spectra may be used for determination of the respective chirality distributions. With use of light absorption spectra alone, chirality distributions were sometimes undeterminable due to the overlapping of absorption peaks of another CNTs or the like. In that case, the chirality distribution was determined using spots observed in fluorescence spectra. First, the absorbances or luminescence intensities of all chiralities included in the respective eluates were calculated. Then, an LC concentration—in which the absorbance or luminescence intensity of a specific chirality becomes highest—was found from all concentration ranges; it is defined as the LC concentration in which the elution of that chirality takes place. Similar operations were carried out for all chiralities to determine the order of separation of chiralities with respect to the LC concentration.
(117) For comparative purposes,
(118) In Example 2, the column used for the SDS/SC/LC elution and the column used for the SDS/SC/DOC elution were operated under the same conditions for the mixed SDS/SC surfactants in the adsorption step; it is understood that the same CNT species are adsorbed to both the columns. In the SDS/SC/DOC elution, however, both CNTs having a diameter of smaller than 1 nm and CNTs having a diameter of larger than 1 nm are eluted whereas in the SDS/SC/LC elution, only CNTs having a diameter of smaller than 1 nm are eluted. From this, it is understood that CNTs having a diameter of larger than 1 nm remain without being eluted. In Example 3 given just below, therefore, separation and recovery of CNTs remaining in the column after the addition of SDS/SC/LC and having a diameter of larger than 1 nm were carried out. Used for separation and recovery was SDS/SC/DOC already found to be capable of elution of CNTs having a diameter of larger than 1 nm.
Example 3
(119) As was the case with Example 2, the SDS/SC/LC elution was followed by the SDS/SC/DOC elution for selective elution of CNTs remaining in the column.
(120) In order to vary concentration in a more accurate manner than in Example 2, high performance liquid chromatography equipment (HPLC) (JASCO Corporation) was used for separation. Gel beads were filled up in a column (Tricorn, GE Healthcare Co., Ltd.) of 5 cm in length and 1 cm in inner diameter in such a way as to provide a height of about 6 cmL followed by equilibration with an aqueous solution of 0.5% SDS/0.5% SC, and a CNT dispersion liquid was then added to the column in an amount of 20% based on the gel volume. After the column was washed with an aqueous solution of 0.5% SDS/0.5% SC, the LC concentration was varied in an increment of 0.005% from 0.005% to 0.100%, while keeping the SDS and SC concentrations invariable, for stepwise elution followed by recovery of CNTs eluted out of the column. Thereafter, the CNTs were again equilibrated with an aqueous solution of 0.5% SDS/0.5% SC, after which the DOC concentration was varied in an increment of 0.005% from 0.005% to 0.100%, while keeping the SDS and SC concentrations invariable, for stepwise elution followed by recovery of CNTs eluted out of the column. The operation was carried out at 20° C.
(121) The light absorption spectra of eluate obtained in the SDS/SC/LC elution are shown in
(122) According to the results of the SDS/SC/LC elution, it is understood that as the LC concentration increases, the absorption peak shifts from a short wavelength side to a long wavelength side as is the case with Example 2, resulting in separation in descending order of diameter. According to the results of the SDS/SC/DOC elution after the addition of SDS/SC/LC, it is found that the short wavelength peak decreases and the long wavelength peak increases as compared with the results of the ordinary SDS/SC/DOC elution of Example 2.
(123) Then, the fluorescence spectra of eluate obtained in the SDS/SC/LC elution are shown in
(124) As is the case with Example 2, the order of separation of chiralities with respect to the LC or DOC concentration was determined from the light absorption spectra or fluorescence spectra.
(125) From the examples described hitherto, it has been found that as the LC-containing aqueous solution for structural separation is added to the column to which CNTs are adsorbed, it causes selective elution of CNTs having a diameter of smaller than 1 nm. Such CNTs having a diameter of smaller than 1 nm would have been further coated with LC added in the elution step, rendering their adsorption to the gel impossible. When a surfactant other than LC is contained in that aqueous solution for separation, on the other hand, that surfactant could also exert some influence on the coating of CNTs. The inventive aqueous solution for separation contains SDS and SC in addition to LC. In the following Examples 4, 5 and 6, for the purpose of going into the influence of the surfactant mixed other than LC, the SDS concentrations and/or the SC concentrations were then systematically varied to make a study of how the SDS/SC/LC elution changes in varying SDS concentrations and/or varying SC concentrations. In order to prevent elution of CNTs due to changes in the SDS and SC concentrations, the SDS and SC concentrations in the adsorption step were identical with the SDS and SC concentrations in the elution step as described hitherto.
Example 4
(126) Similar experimentation as in Example 3 was carried out in two different SDS concentrations: 0.3% and 0.7% while the SC concentration was fixed to 0.5%. The SDS and SC concentrations were varied not only in the elution step but also in the adsorption step (inclusive of dispersion liquid, equilibration, and washing). Note here that there is no experimentation carried out for the SDS/SC/DOC elution after the addition of SDS/SC/LC.
(127) Along with the results of 0.5% SDS/0.5% SC in Example 3,
(128) It is here noted that an LC concentration, in which the absorbances of 7 chiralities (7,3), (9,1), (10,0), (6,5), (8,3), (9,2) and (7,5) have the highest values, was found from all concentration ranges.
Example 5
(129) Similar experimentation as in Example 3 was carried out in two different SC concentrations: 0.7% and 0.9% while the SDS concentration was fixed to 0.5%. The SDS and SC concentrations were varied not only in the elution step but also in the adsorption step (inclusive of dispersion liquid, equilibration, and washing). Note here that there is no experimentation carried out for the SDS/SC/DOC elution after the addition of SDS/SC/LC.
(130) Along with the results of 0.7% SDS/0.5% SC in Example 4,
(131) Here,
Example 6
(132) Similar experimentation as in Example 3 was carried out in two different concentrations: 0.3% and 0.9% while keeping the ratio between the SDS concentration and the SC concentration constant (1:1). The SDS and SC concentrations were varied not only in the elution step but also in the adsorption step (inclusive of dispersion liquid, equilibration, and washing). Note here that there is no experimentation carried out for the SDS/SC/DOC elution after the addition of SDS/SC/LC.
(133) Along with the results of 0.5% SDS/0.5% SC in Example 3 and 0.7% SDS/0.7% SC in Example 5,
Example 7
(134) In the separation method relying upon gels, the separation of CNTs changes with temperatures. Similar experimentation as in Example 3 was carried out while the temperature was changed from 20° C. to two temperatures: 25° C. and 30° C. The temperature is changed not only in the elution step but also in the adsorption step. Note here that there is no experimentation carried out for the SDS/SC/DOC elution after the addition of SDS/SC/LC.
(135) Along with the results of 0.5% SDS/0.5% SC at 20° C. in Example 3,
Example 8
(136) Based on the results of Examples 3, 4 and 5, similar experimentation as in Example 3 was carried out while the SDS and SC concentrations were changed to a high 0.9% SDS and a low 0.3% SC, respectively, expected to make the accuracy of separation higher. The SDS and SC concentrations are changed not only in the elution step but also in the adsorption step (inclusive of dispersion liquid, equilibration and washing). Note here that there is no experimentation carried out for the SDS/SC/DOC elution after the addition of SDS/SC/LC.
(137) From the results of Examples 3, 4 and 5, the LC concentration needed for elution of CNTs is expected to exceed 0.100% in the high SDS concentration and low SC concentration. For this reason, stepwise elution was carried out while the LC concentration was changed in an increment of 0.005% from 0.005% to 0.080% and in an increment of 0.020% from 0.080% to 0.160%. During the stepwise elution, the SDS and SC concentrations remain unchanged.
(138)
(139) As is the case with Example 2, the order of separation of chirality with respect to the LC concentration was determined from light absorption spectra.
Example 9
(140) Based on Example 8, it has been found that under the 3:1 condition CNTs having a specific structure inclusive of (9,1), (10,0), (8,3) and (9,2) are eluted in descending order of diameter, and under the 1:1 condition more species of CNTs are eluted in descending order of diameter. This suggests that when the adsorption of CNTs is maintained under the 3:1 and 1:1 conditions, CNTs having a specific structure inclusive of (9,1), (10,0), (8,3) and (9,2) can first be separated and recovered under the 3:1 condition, and other CNTs can then be separated and recovered under the condition 1:1. Here, the separation of CNTs was carried out while the ratio between the SDS concentration and the SC concentration was changed from 3:1 to 1:1 in a stepwise manner. To be specific, similar experimentation was carried out, first by changing the SDS concentration to 0.9% and the SC concentration to 0.3%, and then by changing the SC concentration to 0.5%, 0.7% and 0.9% in a stepwise manner while fixing the SDS concentration to 0.9% and adjusting the ratio between the SDS concentration and the SC concentration for the SDS/SC/LC elution in the respective SC concentrations. Note here that no SDS/SC/DOC elution was carried out after the addition of SDS/SC/LC.
(141) The concentrations of surfactants in the CNT dispersion liquid were adjusted to 0.9% SDS/0.3% SC. After the column was equilibrated with an aqueous solution of 0.9% SDS/0.3% SC, the dispersion liquid of CNTs was added to the column in an amount of 40% based on the gel volume (first step). After the column was washed with an aqueous solution of 0.9% SDS/0.3% SC, stepwise elution was carried out while changing the LC concentration in an increment of 0.005% from 0.010% to 0.080% and in an increment of 0.020% from 0.080% to 0.160% without varying the SDS and SC concentrations thereby recovering CNTs eluted out of the column (1-1 step). Thereafter, the column was equilibrated with an aqueous solution of 0.9% SDS/0.3% SC and, then, with an aqueous solution of 0.9% SDS/0.45% SC, after which the SDS/SC/LC elution in 0.9% SDS/0.45% was carried out as in the 1-1 step (1-2 step). The subsequent steps were similarly carried out: the SDS/SC/LC elution in 0.9% SDS/0.6% SC in the 1-3 step, and the SDS/SC/LC elution in 0.9% SDS/0.9% SC in the 1-4 step. Throughout the separation at 25° C. the operation was under automated control of HPLC.
(142)
Example 10
(143) From the results of the examples described hitherto, it is found that the LC-containing aqueous solution for structural separation has three functions as summarized below. (1) Function capable of separating and recovering only CNTs having a small diameter, as shown in Examples 2 to 9. (2) Function capable of separating and recovering, with high purity, only CNTs having a specific structure inclusive of (9,1), (10,0), (8,3) and (9,2) under the condition having an SDS to SC concentration ratio of 3:1 as shown in Examples 8 and 9. (3) Function capable of high-purity separation and recovery by way of SDS/SC/DOC elution without giving rise to elution of large-diameter CNTs adsorbed to the gel as shown in Example 3.
(144) In order to study the functions of the LC-containing aqueous solution for structural separation in the examples described hitherto, most semiconducting CNTs were adsorbed to a single column in the adsorption step, and they were then separated in the elution step by selective separation comprising the addition of an LC-containing aqueous solution. Referring here to the subsequent step, there is the mention of a process in which not only the selective elution but also such selective adsorption of CNTs as set forth in Non-Patent Publication 9 are simultaneously carried out as the means for improving on the accuracy of separation of single-structure CNTs. The SDS and SC concentrations were varied in Example 4 to 6 and Example 8 alike, but numerous species of CNTs were still adsorbed in place within such a range. Based on Non-Patent Publication 9, the SDS and SC were herein adjusted to such concentrations as to render adsorption of CNTs more selective, and selective adsorption was then carried out using a plurality of columns. As the SDS concentration increases with the SC concentration fixed to 0.5%, it gives rise to adsorption of only CNTs having a strong adsorption power to the gel (the column to which CNTs having a strong adsorption power are adsorbed is called the first column). As the SDS concentration decreases, it causes unabsorbed CNTs having a weak adsorption power to be again adsorbed to the gel. If the SDS concentration is low enough to again adsorb CNTs to a new column (here called the second column), it is then possible to classify CNTs adsorbed to the column in terms of a difference in the adsorption power to the gel. This difference in adsorption power to the gel is dependent on the chiral angle and diameter of CNTs, and CNTs having a small chiral angle or diameter have a strong adsorption to the gel. The operation for previously separating CNTs via such a difference in adsorption power was carried out up to the fifth column. Further, selective elution was applied to a plurality of columns subjected to selective separation as described just below. First, high-purity separation and recovery of CNTs having a diameter of smaller than 1 nm is carried out using the LC-containing aqueous solution for structural separation. Then, other aqueous solution for structural separation (here a DOC-containing aqueous solution for structural separation) is used for separation and recovery of CNTs remaining in the column with a diameter of larger than 1 nm. Then, because (9,1), (10,0), (8,3) and (9,2) having a small chiral angle have been adsorbed to the first column by way of selective adsorption, those CNTs are separated and recovered by the SDS/SC/LC elution in a high SDS concentration and a low SC concentration. Then, CNTs remaining in the column with a diameter of smaller than 1 nm are separated and recovered by the ordinary SDS/SC/LC elution. Finally, CNTs having a diameter of larger than 1 nm are separated and recovered by the SDS/SC/DOC elution. In this way, selective adsorption was combined with selective elution for high-purity separation of CNTs having multi-structures. Set out below is one specific process.
(145) The surfactant concentration of the CNT dispersion liquid was adjusted to 2% SDS/0.5% SC. There are a plurality of columns provided, each having a length of 20 cm and an inner diameter of 2.6 cm (XK, GE Healthcare) and having gel beads filled up therein in such a way as to have a height of about 6 cm. The CNT dispersion liquid was added to the first column equilibrated with an aqueous solution of 2% SDS/0.5% SC in an amount of 40% based on the gel volume (the first step). Then, the first column was equilibrated with an aqueous solution of 0.9% SDS/0.3% SC for the SDS/SC/LC elution in 0.9% SDS/0.3% SC (the 1-1 step). Then, the first column was equilibrated with an aqueous solution of 0.9% SDS/0.3% SC, an aqueous solution of 0.7% SDS/0.4% SC and an aqueous solution of 0.5% SDS/0.5% SC in this order for the SDS/SC/LC elution in 0.5% SDS/0.5% SC (the 1-2 step). Then, the first column was equilibrated with an aqueous solution of 0.5% SDS/0.5% SC for the SDS/SC/DOC elution in 0.5% SDS/0.5% SC (the 1-3 step). Then, a liquid obtained by dilution of a filtrate (2% SDS/0.5% SC) from the first column with an aqueous solution of 0.5% SC was added to the second column equilibrated with an aqueous solution of 1.5% SDS/0.5% SC for a similar operation as in the first step (the second step). Then, as in the 1-2 step, the SDS/SC/LC elution in 0.5% SDS/0.5% SC was carried out (the 2-1 step) and, as in the 1-3 step, the SDS/SC/DOC elution in 0.5% SDS/0.5% SC was carried out (the 2-2 step). The subsequent columns were operated as in the second step: selective adsorption was carried out in 1% SDS/0.5% SC for the third column, 0.75% SDS/0.5% SC for the fourth column, and 0.5% SDS/0.5% SC for the fifth column, respectively. The respective columns were subjected to the SDS/SC/LC elution and SDS/SC/DOC elution as in the 2-1 step and 2-2 step. The separations were all carried out at 25° C. under the automatic control of HPLC. Shown in
(146)
(147) CNTs having a small chiral angle are adsorbed to the first column for selective adsorption in 2% SDS/0.5% SC (