WO2009003357A1 - Procédé de décoration de nanotubes de carbone au moyen d'un cristal polymère - Google Patents

Procédé de décoration de nanotubes de carbone au moyen d'un cristal polymère Download PDF

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WO2009003357A1
WO2009003357A1 PCT/CN2008/001061 CN2008001061W WO2009003357A1 WO 2009003357 A1 WO2009003357 A1 WO 2009003357A1 CN 2008001061 W CN2008001061 W CN 2008001061W WO 2009003357 A1 WO2009003357 A1 WO 2009003357A1
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polymer
organic solvent
carbon nanotubes
pressure
solution
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PCT/CN2008/001061
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French (fr)
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Qun Xu
Zhiwei Zhang
Zhimin Chen
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Zhengzhou University
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B82—NANOTECHNOLOGY
    • B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00—Manufacture or treatment of nanostructures
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B82—NANOTECHNOLOGY
    • B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/15—Nano-sized carbon materials
    • C01B32/158—Carbon nanotubes
    • C01B32/168—After-treatment
    • C01B32/174—Derivatisation; Solubilisation; Dispersion in solvents
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2202/00—Structure or properties of carbon nanotubes
    • C01B2202/20—Nanotubes characterized by their properties
    • C01B2202/28—Solid content in solvents
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

Definitions

  • the present invention relates to a method for modifying carbon nanotubes by polymer crystallization, and more particularly to a method for modifying a polymer crystal by using supercritical or compressible carbon dioxide as an antisolvent.
  • Carbon nanotubes are crystalline carbons whose walls are the same as those of graphite.
  • low-volume nanomaterials produced in large quantities have many defects and poor dispersion.
  • the surface structure of carbon nanotubes often affects many properties such as electrical, mechanical and optical properties. These factors reduce the superior performance of carbon nanotubes as nanomaterials and affect the application of carbon nanotubes.
  • surface modification methods are generally used to improve the dispersibility, stability and compatibility with other substances, giving them new physical, chemical, mechanical properties and new functions. .
  • surface modification methods can be divided into organic non-covalent bonding modification and organic covalent bonding modification.
  • the organic non-covalent bonding modification allows the surface of the carbon nanotube to carry a large amount of organic functional groups without destroying the large ⁇ bond electrons of the graphite sheet itself.
  • the interaction between this surface-modified functional group and the surface of the broken nanotube is not high.
  • the organic covalent bond modification destroys the original structure of the carbon nanotube due to the existence of the covalent bond, and the original excellent electrical properties of the carbon nanotube. And mechanical properties have been reduced.
  • Supercritical or compressive carbon dioxide has a high solubility in most organic solvents, resulting in a decrease in solvent strength of organic solvents. For many solutes, especially high polymers, the solvent strength of supercritical or compressive carbon dioxide is much weaker than that of organic solvents, thus demonstrating its solvent resistance.
  • Some nanomaterials such as C 60 /(CO 2 ) have been prepared using this property of SC-C0 2 . 95 (NF Christian, AH Paul, MW Jeremy, HG Duncan, JT Jeremy, P. Martyn, J. Am. Chem. Soc. 2000, 122, 2480), Eu 2 0 3 coated multi-walled carbon nanotubes (L Fu, Z. Liu, Y. Liu, B. Han, J. Wang, P.
  • the solvent strength of supercritical or compressible carbon dioxide can be varied by adjusting its pressure or temperature. Therefore, by controlling the pressure or temperature, it is possible to selectively separate polymers of different molecular weights, which are precipitated and crystallized.
  • supercritical or compressible carbon dioxide to resist solvent to achieve polymer-modified carbon nanotubes.
  • No other use of supercritical or compressible carbon dioxide as an anti-solvent to induce epitaxial crystallization of polymers has been reported. Reported in the literature.
  • the object of the present invention is to provide a method for modifying carbon nanotubes by polymer crystallization, in particular, using supercritical or compressible carbon dioxide as an anti-solvent, the method is simple and environmentally friendly, and the prepared polymer crystal modified carbon nanotube surface is modified.
  • the interaction between the functional group and the surface of the carbon nanotube is strong, and does not affect the original electrical and mechanical properties of the carbon nanotube.
  • the technical solution adopted by the present invention is as follows:
  • a method for modifying carbon nanotubes by using polymer crystallization preparing a solution of a polymer dissolved in an organic solvent at a temperature not lower than a temperature of 20 ° C below the melting temperature of the polymer; at a temperature higher than room temperature, The carbon nanotubes are uniformly: in the same organic solvent, the system 2 is obtained; the solution 1 and the system 2 are mixed according to a certain ratio, and the final concentration of the polymer and the carbon nanotubes in the organic solvent after mixing is respectively 0.002 ⁇ 0.02wt%, wait for the equilibrium of the system after mixing to obtain system 3; transfer system 3 to the closed reactor, and pass the carbon dioxide at the same temperature as the preparation solution 1 to the reactor at a pressure of 5 ⁇ 25MP and keep 0.5 ⁇ 7h, after falling to normal pressure, the polymer crystal modified carbon nanotubes are obtained, and the organic solvent is diphenylbenzene, dichlorobenzene, triacetin or isopropanol, and the polymer is crystalline or Semi-crystalline polymer.
  • the temperature of the constant temperature is not lower than 20 ° C below the melting temperature of the selected polymer. For example, if the polymer melting temperature selected is 120 ° C, the constant temperature is not lower than 100 ° C.
  • the temperature is preferably 35 to 60 ° C, more preferably 45 to 50 ° C; the carbon nanotubes should be as homogeneous as possible in the organic solvent, such as ultrasonic ⁇ :.
  • This method is suitable for single Wall carbon nanotubes are also suitable for multi-walled carbon nanotubes.
  • the concentration of the polymer in the organic solvent is 0.006 to 0.04% by weight.
  • the organic solvent is preferably p-xylene or 1,2-dichlorobenzene.
  • the polymer is preferably polyethylene, polypropylene or nylon 66, nylon 6, polytetrahydrofuran, polyethylene oxide, polyvinyl alcohol, polyacrylonitrile or polyurethane.
  • carbon dioxide can be introduced at a flow rate of 150 to 250 mL/h, and the pressure in the reactor after the introduction is preferably 7 to 22 MPa.
  • the closed reactor can be used in a high pressure reactor.
  • the preparation of the solution 1 is preferably carried out at a constant temperature in the range of 100 to 120 °C.
  • the method for modifying carbon nanotubes by using polymer crystallization can be carried out according to the following steps:
  • the polymer is dissolved in an organic solvent at a constant temperature to obtain a solution 1 at a temperature not lower than 20 ° C below the melting temperature of the polymer; the carbon nanotubes are uniformly homogenized in the same organic solvent at 45 to 50 ° C to obtain a system 2 Mixing solution 1 with system 2, so that the final concentration of the polymer and carbon nanotubes in the organic solvent after mixing is 0.006-0.04% and 0.002-0.02% by weight, respectively, waiting for the equilibrium of the system after mixing to obtain system 3,
  • the organic solvent is p-nonylbenzene or 1,2-dichlorobenzene;
  • the present invention has the following advantages:
  • the method has simple process and convenient operation, and the effect is remarkable; the supercritical carbon dioxide is a green solvent and is environmentally friendly; the microscopic morphology of the prepared polymer crystallized carbon nanotubes is a “mutton string structure”, which retains the original carbon nanotubes. It has excellent electronic and mechanical properties, and solves the problem that the interaction between the modified carbon nanotubes and the surface of the carbon nanotubes is not strong, and the compatibility of the carbon nanotubes with the polymer is increased, which can be widely used for preparation. Nanocomposite of polymer/carbon nanotubes.
  • FIG. 1 is a scanning electron micrograph of a polymer crystal-modified carbon nanotube prepared in Example 1 of the present invention
  • FIG. 2 is a transmission electron micrograph of the polymer crystal-modified carbon nanotube prepared in Example 1 of the present invention.
  • HDPE high-density polyethylene
  • the HDPE/SWNTs p-benzoquinone solution is quickly transferred to a high-pressure reactor at 110 ° C constant temperature; C0 2 to 9 MPa is injected into the autoclave, and the high pressure is maintained for 3 h, and finally the pressure is gradually reduced to At normal pressure, all products are taken out of the kettle, which is a high density polyethylene modified carbon nanotube.
  • the amount of HDPE used was 0.5 mg, and the concentration of HDPE finally formed was 0.01 wt%, the same as in Example 1.
  • the HDPE dosage was changed to 0.3 mg, and the final HDPE concentration was 0.006 wt%, the same as in Example 1.
  • the HDPE dosage was changed to 2.0 mg, and the final HDPE concentration was 0.04 wt%, which was the same as in Example 1.
  • the HDPE dosage was changed to 5.0 mg, and the final HDPE concentration was 0.1 wt%, the same as in Example 1.
  • Example 7 The pressure of C0 2 was introduced to 7 MPa, and the same as in Example 1.
  • HDPE IOO'C 1mg of high-density polyethylene HDPE IOO'C is dissolved in 4g of 1,2-dichlorobenzene at a constant temperature, and at the same time, ultrasonically dispersed in lg of 1,2-dichlorobenzene at 45 ° C ⁇ 50 ° C 0.3mg of single-walled carbon nanotube SWNTs, after the HDPE is completely dissolved, and the SWNTs are completely dispersed, the SWNTs/l,2-dichlorobenzene dispersion is mixed with the HDPE 1,2-dichlorobenzene solution at 100 °C, and finally The concentration of HDPE formed was 0.02 wt%, and the concentration of SWNTs was 0.006 wt%.
  • the HDPE/SWNTs 1,2-dichlorobenzene solution is quickly transferred to a high-pressure reactor at a constant temperature of 100 °C; C0 2 to 16 MPa is injected into the autoclave, and the high pressure is maintained for 3 hours, and finally slow. Down to normal pressure, open all the products, that is, high density polyethylene modified carbon nanotubes.
  • the amount of SWNTs was 0.5 mg, and the concentration of the resulting SWNTs was 0.01 wt%, otherwise the same as in Example 9.
  • the amount of SWNTs was 1.0 mg, and the concentration of the finally formed SWNTs was 0.02% by weight, otherwise the same as in Example 9.
  • HDPE high-density polyethylene
  • 4 g of p-benzoquinone at the same time, at 45 ° C ⁇ 50.
  • the system was mixed with a 100 ° C HDPE p-biphenyl solution, the final HDPE concentration was 0.006 wt%, and the MWNTs concentration was 0.002 wt%.
  • the p-diphenylene solution of HDPE/MWNTs is quickly transferred to a high-pressure reactor with constant temperature of 100'C; C0 2 to 9 MPa is injected into the autoclave, and the high pressure is maintained for 3 h, and finally the pressure is gradually reduced to At normal pressure, all products are taken out of the kettle, which is a high density polyethylene modified carbon nanotube.
  • the multi-walled carbon nanotubes were dispersed in p-nonylbenzene at 30 ° C, and the same as in Example 14.
  • the multi-walled carbon nanotubes were dispersed in p-terpene benzene at 60 Torr, and the same as in Example 14.
  • Example 17 The organic solvent was 1,2-dichlorobenzene, and the pressure of C0 2 was passed to 16 MPa, and the same as in Example 14

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Description

一种利用聚合物结晶实现碳纳米管修饰的方法
(一 )技术领域
本发明涉及一种利用聚合物结晶实现碳纳米管修饰的方法， 特别涉及利 用超临界或压缩性二氧化碳作为抗溶剂诱导聚合物结晶进行修饰的方法。
(二）背景技术
碳纳米管属于晶态碳， 其管壁与石墨结构一样。 通常， 大批量生产的低 维纳米材料本身存在着许多缺陷， 分散性也比较差。 特别是碳纳米管的表面 结构往往影响电学、 力学和光学等诸多性能。 这些因素降低了碳纳米管作为 纳米材料的优越性能，影响了碳纳米管的应用。为了改善碳纳米管表面结构， 一般采用表面修饰方法， 从而改善碳纳米管的分散性、 稳定性以及与其他物 质之间的相容性， 赋予其新的物理、 化学、 机械性能和新的功能。 目前， 表 面修饰的方法可以分为有机非共价键化修饰和有机共价键化修饰两大类。有 机非共价键化修饰， 可使碳纳米管表面带有大量有机官能团， 且不破坏石墨 片层自身的大 π键电子。但是这种表面修饰的官能团与破纳米管表面之间的 作用力不高。有机共价键化修饰虽然功官能团与碳纳米管表面之间的作用力 比较强， 但因共价键的存在破坏了碳纳米管的原有结构， 使得碳纳米管原有 的优良的电性能和机械性能都有所降低。
超临界或压缩性二氧化碳在大多数有机溶剂中都有很高的溶解度，致使 有机溶剂的溶剂强度降低。 对于许多溶质尤其高聚物来说，超临界或压缩性 二氧化碳的溶剂强度要比有机溶剂弱的多，从而表现出来它的抗溶剂性。利用 SC-C02的这种性能已经制备出了一些纳米材料， 比如 C60/(CO2)。.95 ( N. F. Christian, A. H. Paul, M. W. Jeremy, H. G. Duncan, J. T. Jeremy, P. Martyn, J. Am. Chem. Soc. 2000， 122， 2480 )， Eu203涂附多壁碳纳米管 （ L. Fu, Z. Liu, Y. Liu, B. Han, J. Wang, P. Hu, L. Cao, D. Zhu, Adv. Mater. 2004, 16, 350 ) ,铂 /碳 纳米管纳米复合材料 ( J. J. Watkins, J. M. Blackburn, T. J. McCarthy, Chem. Mater. 1999, 11, 213 ) ,金属纳米线填充纳米管的纳米复合材料（ X. R. Ye, Y.
1
确认本 Lin, C. Wang, C. M. Wai, Adv. Mater. 2003, 15, 316 )和聚 2，4-己炔 -1,6-二醇酯 / 碳纳米管纳米复合材料 ( X. Dai, Z. Liu, B. Han, Z. Sun, Y. Wang, J. Xu, X. Guo, N. Zhao, J. Chen, Chem. Commun. 2004, 2190 )。
超临界或压缩性二氧化碳的溶剂强度可以通过调节其压力或温度来得 到改变。 因此通过控制压力或温度,可以选择分离不同分子量的聚合物，使其 析出并结晶。 但到目前， 尚未有关利用超临界或压缩性二氧化碳抗溶剂性实 现聚合物修饰碳纳米管的文献报道， 亦未见有其它利用超临界或压缩性二氧 化碳作为抗溶剂， 诱导聚合物附生结晶的文献报道。
(三）发明内容
本发明的目的在于提供一种利用聚合物结晶修饰碳纳米管的方法，特别 利用超临界或压缩性二氧化碳作为抗溶剂， 方法简单、 环保， 制备出的聚合 物结晶修饰的碳纳米管表面修饰的官能团与碳纳米管表面之间的作用力较 强， 又不影响碳纳米管原有的电性能和机械性能。 本发明采用的技术方案如下：
一种利用聚合物结晶实现碳纳米管修饰的方法：在不低于聚合物熔 温 度以下 20°C的温度条件下恒温制备聚合物溶于有机溶剂的溶液 1 ; 高于室温 的温度条件下， 将碳纳米管均匀^：于同种有机溶剂中， 得到体系 2; 按照 一定的比例混合溶液 1与体系 2， 混合后聚合物与碳纳米管在有机溶剂中的 终浓度分别为
Figure imgf000004_0001
0.002~0.02wt%, 等待混合后的体系平衡得到 体系 3; 将体系 3转移至密闭反应器中， 在与制备溶液 1相同的温度下恒温 通入二氧化碳至反应器中压力为 5~25MP 并保持 0.5~7h, 降至常压后即得 聚合物结晶修饰的碳纳米管， 所述的有机溶剂为二曱苯、 二氯苯、 丙三 或 异丙醇， 所述的聚合物为结晶型或半结晶型高聚物。
制备溶液 1时，恒温的温度只要不低于选用的聚合物的熔融温度以下 20 °C即可。 例如， 若选用的聚合物熔融温度为 120°C， 只要恒温的温度不低于 100'C即可。
制备体系 2时， 温度优选为 35~60°C , 更优选为 45~50°C ; 碳纳米管应 尽量均匀^^于有机溶剂中， 如可采用超声 ^：的方式。 本方法既适用于单 壁碳纳米管， 也适用于多壁碳纳米管。
较好的， 体系 3中， 聚合物在有机溶剂中的浓度为 0.006~0.04wt%。 进一步， 所述的有机溶剂优选对二甲苯或 1， 2-二氯苯。 所述的聚合物 优选为聚乙烯、 聚丙烯或尼龙 66、 尼龙 6、 聚四氢呋喃、 聚环氧乙烷、 聚乙 烯醇、 聚丙烯腈或聚亚氨酯。
在密闭反应器中可按照 150~250mL/h的流速通入二氧化碳，通入后反应 器中的压力优选在 7~22MPa。 所述的密闭反应器使用高压反应釜就可以。
进一步， 当选择高密度聚乙烯时， 在 100~120°C范围内恒温进行溶液 1 的制备较好。
具体的， 所述的利用聚合物结晶实现碳纳米管修饰的方法， 可按照以下 步骤进行：
1 ) 恒温将聚合物溶于有机溶剂中得到溶液 1 , 温度不得低于聚合物的 熔融温度以下 20°C ;在 45~50°C将碳纳米管均匀^于同种有机溶剂中得到 体系 2; 混合溶液 1与体系 2， 使得混合后聚合物与碳纳米管在有机溶剂中 的终浓度分别为 0.006~0.04 ％与 0.002~0.02wt%，等待混合后的体系平衡得 到体系 3， 所述的有机溶剂为对二曱苯或 1 , 2-二氯苯；
2 )将体系 3转移至恒温的高压反应釜中， 温度与制备溶液 1时的温度 相同；
3 )在高压反应釜中以 150~250mL/h的流速通入二氧化碳至压力为
7~22MPa, 保持 l~4h后降压至常压， 即得聚合物结晶修饰的碳纳米管。
本发明相对于现有技术， 有以下优点：
本方法工艺简单， 操作筒便， 成效显著； 超临界二氧化碳是绿色溶剂， 环保； 制得的聚合物结晶修饰的碳纳米管微观形态均为 "羊肉串儿结构"， 既 保留了碳纳米管原有优良的电子和机械性能， 又解决了同类碳纳米管修饰基 团与碳纳米管表面间作用力不强的问题， 增大了碳纳米管与聚合物的相容 性， 可广泛用于制备聚合物 /碳纳米管的纳米复合材料。
(四） 附图说明
图 1为本发明实施例 1制备的聚合物结晶修饰的碳纳米管的扫描电镜图； 图 2为本发明实施例 1制备的聚合物结晶修饰的碳纳米管的透射电镜图。
(五）具体实施方式： 以下以具体实施例来说明本发明的技术方案，但本发明的保护范围不限 于此： 实施例 1
将 l.Omg的高密度聚乙烯（HDPE ) 110°C恒温溶解在 4g的对二曱苯中， 与此同时， 于 45°C ~ 50°C在 lg的对二甲苯中超声^ L O.lmg的单壁碳纳米 管 SWNTs, 待 HDPE完全溶解， SWNTs完全分散后， 混合 110°C的 HDPE 的对二曱苯溶液与 SWNTs/对二曱苯分散体系， 最后形成的 HDPE的浓度为 0.02wt% , SWNTs的浓度为 0.002wt%。 待体系平衡后， 将 HDPE/SWNTs的 对二曱苯溶液迅速转移至已 110°C恒温的高压反应釜中； 向高压反应釜中注 入 C02 至 9MPa， 并保持高压 3h， 最后緩慢降压至常压， 开釜取出所有产 物， 即为高密度聚乙烯修饰的碳纳米管。
实施例 2
HDPE用量为 0.5mg， 最后形成的 HDPE的浓度为 0.01wt%， 其他同实 施例 1。
实施例 3
HDPE用量改为 0.3mg，最后形成的 HDPE的浓度为 0.006wt%，其他同 实施例 1。
实施例 4
HDPE用量改为 2.0mg， 最后形成的 HDPE的浓度为 0.04wt% , 其他同 实施例 1。
实施例 5
HDPE用量改为 5.0mg，最后形成的 HDPE的浓度为 0.1wt%，其他同实 施例 1。
实施例 6
通入 C02压力至 5MPa, 其他同实施例 1。
实施例 7 通入 C02压力至 7MPa， 其他同实施例 1。
实施例 8
通入 C02压力至 13MPa， 其他同实施例 1。
实施例 9
将 lmg的高密度聚乙烯 HDPE IOO'C恒温溶解在 4g的 1， 2 -二氯笨中， 与此同时， 于 45°C ~ 50°C在 lg的 1， 2 -二氯苯中超声分散 0.3mg的单壁碳 纳米管 SWNTs, 待 HDPE完全溶解， SWNTs完全分散后， 将 SWNTs/l， 2 -二氯苯分散体系与 100°C的 HDPE的 1， 2 -二氯苯溶液混合， 最后形成的 HDPE的浓度为 0.02wt%， SWNTs的浓度为 0.006wt%。 待体系平衡后， 将 HDPE/SWNTs的 1， 2 -二氯苯溶液迅速转移至已 100 °C恒温的高压反应釜 中； 向高压反应釜中注入 C02至 16MPa， 并保持高压 3h， 最后緩慢降庄至 常压， 开釜取出所有产物， 即为高密度聚乙烯修饰的碳纳米管。
实施例 10
SWNTs用量为 0.5mg， 最后形成的 SWNTs的浓度为 0.01wt% , 其他同 实施例 9。
实施例 11
SWNTs用量为 1.0mg， 最后形成的 SWNTs的浓度为 0.02wt%， 其他同 实施例 9。
实施例 12
通入 C02压力至 22MPa, 其他同实施例 9。
实施例 13
通入 C02压力至 25MPa， 其他同实施例 9。
实施例 14
将 0.3mg的高密度聚乙烯 HDPE 100 °C恒温溶解在 4g的对二曱苯中，与 此同时， 于 45°C ~ 50。C在 lg的对二曱苯中超声^ It O.lmg的多壁碳纳米管 MWNTs, 待 HDPE完全溶解， MWNTs完全分散后， 将 MWNTs/对二曱苯 体系与 100°C的 HDPE的对二曱苯溶液混合， 最后形成的 HDPE的浓度 为 0.006wt %， MWNTs的浓度为 0.002wt%。待体系平衡后，将 HDPE/MWNTs 的对二曱苯溶液迅速转移至已 100'C恒温的高压反应釜中； 向高压反应釜中 注入 C02至 9MPa， 并保持高压 3h， 最后緩慢降压至常压， 开釜取出所有 产物， 即为高密度聚乙烯修饰的碳纳米管。
实施例 15
在 30°C将多壁碳纳米管分散于对二曱苯中， 其他同实施例 14。
实施例 16
在 60Ό将多壁碳纳米管分散于对二曱苯中， 其他同实施例 14。
实施例 17 有机溶剂为 1， 2 -二氯苯， 通入 C02压力至 16MPa， 其他同实施例 14

Claims

权 利 要 求
1. 一种利用聚合物结晶实现碳纳米管修饰的方法， 其特征在于所述的 于有机溶剂的溶液 1; 高于室温的温度条件下， 将碳纳米管均匀分散于同种 有机溶剂中， 得到体系 2; 按照一定的比例混合溶液 1与体系 2, 混合后聚 合物与碳纳米管在有机溶剂中的终浓度分别为 0.003~0.1^%与
0.002~0.02wt%, 等待混合后的体系平衡得到体系 3; 将体系 3转移至密闭反 应器中，在与制备溶液 1相同的温度下恒温通入二氧化碳至反应器中压力为 5~25MPa并保持 0.5~7h， 降至常压后即得聚合物结晶修饰的碳纳米管，所述 的有机溶剂为二曱苯、 二氯苯、 丙三醇或异丙醇， 所述的聚合物为结晶型或 半结晶型高聚物。
2.如权利要求 1所述的利用聚合物结晶实现碳纳米管修饰的方法， 其特 征在于所述的体系 3中聚合物在有机溶剂中的浓度为 0.006〜0.04wt%。
3.如权利要求 1所述的利用聚合物结晶实现碳纳米管修饰的方法， 其特 征在于所述的体系 2的配制温度为 35~60°C。
4.如权利要求 1所述的利用聚合物结晶实现碳纳米管修饰的方法， 其特 征在于所述的二氧化碳通入的流速为 150~250mL/h。
5.如权利要求 1所述的利用聚合物结晶实现碳纳米管修饰的方法， 其特 征在于通入二氧化碳至反应器中压力为 7~22MPa。
6.如权利要求 1所述的利用聚合物结晶实现碳纳米管修饰的方法， 其特 征在于所述的有机溶剂为对二曱苯或 1， 2-二氯苯。
7.如权利要求 1所述的利用聚合物结晶实现碳纳米管修饰的方法， 其特 征在于所述的聚合物为聚乙烯、 聚^烯、 尼龙 66、 尼龙 6、 聚四氢呋喃； '聚 环氧乙烷、 聚乙烯醇、 聚丙浠腈或聚亚氨酯。
8.如权利要求 1所述的利用聚合物结晶实现碳纳米管修饰的方法， 其特 征在于所述的方法按照以下步骤进行：
1 ) 恒温将聚合物溶于有机溶剂中得到溶液 1， 温度不得低于聚合物的 熔融温度以下 20°C ;在 45~50°C将碳纳米管均匀分散于同种有机溶剂中得到 体系 2; 混合溶液 1与体系 2， 使得混合后聚合物与碳纳米管在有机溶剂中 的终浓度分别为 0.006~0.04\^%与 0.002~0.02wt%,等待混合后的体系平衡得 到体系 3， 所述的有机溶剂为对二曱苯或 1 , 2-二氯苯； 2 )将体系 3转移至恒温的高压反应釜中， 温度与制备溶液 1时的温度 相同；
3 )在高压反应釜中以 150〜250mL/h的流速通入二氧化碳至压力为 7~22MPa, 保持 l~4h后降压至常压， 即得聚合物结晶修饰的碳纳米管。
9.如权利要求 8所述的利用聚合物结晶实现碳纳米管修饰的方法， 其特 征在于所述的聚合物为聚乙浠、 聚丙烯或尼龙 66。
10.如权利要求 8所述的利用聚合物结晶实现碳纳米管修饰的方法，其特 征在于所述的溶液 1的制备为 100~120°C恒温将高密度聚乙烯溶于有机溶剂 中。
PCT/CN2008/001061 2007-07-03 2008-05-30 Procédé de décoration de nanotubes de carbone au moyen d'un cristal polymère WO2009003357A1 (fr)

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