WO2013053250A1 - Method for using graphene sponge - Google Patents

Method for using graphene sponge Download PDF

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Publication number
WO2013053250A1
WO2013053250A1 PCT/CN2012/078045 CN2012078045W WO2013053250A1 WO 2013053250 A1 WO2013053250 A1 WO 2013053250A1 CN 2012078045 W CN2012078045 W CN 2012078045W WO 2013053250 A1 WO2013053250 A1 WO 2013053250A1
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Prior art keywords
graphene sponge
distillation
graphene
adsorption
organic solvent
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PCT/CN2012/078045
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French (fr)
Chinese (zh)
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孙立涛
毕恒昌
谢骁
尹奎波
周奕龙
万树
贺龙兵
徐峰
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东南大学
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Publication of WO2013053250A1 publication Critical patent/WO2013053250A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28042Shaped bodies; Monolithic structures
    • B01J20/28045Honeycomb or cellular structures; Solid foams or sponges
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/32Materials not provided for elsewhere for absorbing liquids to remove pollution, e.g. oil, gasoline, fat

Definitions

  • the invention relates to a method for applying a graphene sponge.
  • adsorbents such as activated carbon have a number of disadvantages, including long adsorption times, poor selectivity, and limited adsorption capacity (D. Cl ifford, S. Subranmonian and TJ Sorg, Environ. Sci. Technol., 1986, 20, 1072.; AB Fuertes, G. Marban and DM Nevskaia, Carbon, 2003, 41, 87.).
  • expanded graphite has a strong adsorption capacity for oil, it does not work for toxic organic solvents. The recovery of expanded graphite is also very difficult.
  • porous materials with pore sizes of nanometers or micrometers L. Feng, Z. Zhong, Z. Mai, B. Liu, L. Jiang and D. Zhu, Angew. Chem., Int. Ed., 2003, 42, 800.; Y. Zhang, S. Wei, F. Liu, Y. Du, S. Liu, Y. Ji, T. Ji, T. Yokoib, T. Tatsumib and FS Xiao, Nano Today, 2009 , 4, 135.
  • nano- and micro-scale porous materials and nanowire films have strong hydrophobic ability and superior lipophilic ability, the separation of organic pollutants and water, grease and water can be achieved well. At the same time, these materials have the characteristics of short adsorption time, high selectivity and high adsorption capacity.
  • nano- and micro-scale porous materials and nanowire films have the disadvantages that the adsorption capacity is not strong enough, the cost is high, and it is not easy to mass-produce.
  • the technical problem to be solved by the present invention is to provide a method for applying a graphene sponge which is used for absorbing organic solvents or fats and has the characteristics of strong adsorption capacity and fast adsorption speed.
  • the technical solution adopted by the present invention is: A method for applying a graphene sponge for absorbing an organic solvent or a grease. Further, after the graphene sponge absorbs the organic solvent or the grease, the decontamination treatment is performed: the decontamination treatment is a method of low-pressure distillation, extraction, or high-temperature distillation, and the organic solvent or grease is removed or recycled from the graphene sponge. .
  • the application method is simple in operation and low in cost, and can be applied to industrial production. Because graphene sponge has excellent water repellency and has strong adsorption capacity and fast adsorption speed for organic solvents and oils, graphene sponge has the advantage of being used for adsorbing organic solvents and greases. In particular, graphene sponges are used in liquid-liquid separation and sewage treatment, and graphene sponges are used to adsorb organic solvents and greases.
  • the graphene sponge can be reused, and the organic solvent and grease can be recycled.
  • the organic solvent and grease adsorbed by the graphene sponge are separated from the graphene sponge by low-pressure distillation, extraction or high-temperature evaporation, and the graphene sponge from which the organic solvent and the grease are removed can be reused.
  • the separated organic solvents and greases can be recycled.
  • the graphene sponge has wide application potential for various separations between different liquids and sewage treatment.
  • Fig. 1 is a graph showing the adsorption ratio of a graphene sponge to an organic solvent and a fat or oil in the present invention.
  • Fig. 2 is a thermogravimetric analysis chart of the graphene sponge of the present invention.
  • Fig. 3 is a view showing the experiment of adsorbing and desorbing toluene using a graphene sponge in Example 1 of the present invention.
  • Fig. 4 is a view showing an experiment of adsorption and desorption of dodecane by a graphene sponge in Example 2 of the present invention.
  • Fig. 5 is a graph showing the adsorption ratio of a porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene benzene, and a porous polymer obtained by polymerizing 1, 4-diethylbenzene to an organic solvent and a fat.
  • the graphene sponge is used for absorbing an organic solvent or a grease.
  • the preparation method of the graphene sponge in the present invention is as follows:
  • the first step 35 ml of a graphene oxide dispersion having a concentration of 2 mg/ml is weighed, and 1 ml of ammonia water is added to form a mixed solution; the concentration of the ammonia water is 30%, which means that 30 g of hydrogen peroxide is contained per 100 g of ammonia water.
  • the mixture is poured into a reaction kettle at a high temperature of 180 ° C for 24 hours, then naturally cooled, and the reaction vessel can be unscrewed. A graphene gel was obtained.
  • the obtained graphene gel is freeze-dried at a low pressure to obtain a porous graphene sponge.
  • the organic solvent or fat includes vegetable oil, crude oil, pump oil, dodecane, n-decane, octane, hexane, phenol, nitrobenzene, chloroform, dichlorobenzene, ethylbenzene, toluene, benzene, Dimethyl sulfoxide, tetrahydrofuran, dimethylformamide, acetone, ethanol, methanol, kerosene, castor oil, heptane, diesel, gasoline, carbon tetrachloride.
  • a graphene sponge is used as an adsorbent.
  • Graphene sponge can be used in the field of liquid-liquid separation or sewage separation.
  • the graphene sponge is used as an adsorbent to absorb organic solvents or grease.
  • the test results are shown in Fig. 1.
  • the abscissa indicates the adsorption rate of the graphene sponge, and the ordinate indicates the organic solvent or grease to be adsorbed.
  • the adsorption rate of graphene sponge to pump oil is 6854%
  • the adsorption rate of graphene sponge to dodecane is 5050%
  • the adsorption rate of graphene sponge to nitrobenzene is 6382%
  • the adsorption of graphene sponge on chloroform The rate is 8612%.
  • the adsorption rate of a porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene and 1, 4-diethylbenzene to a grease or an organic solvent, and an adsorption rate of a graphene sponge For comparison.
  • the abscissa indicates the adsorption ratio of the porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene and the adsorption ratio of the porous polymer obtained by polymerizing 1, 4-diethylbenzene.
  • gray indicates the adsorption rate of the porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene
  • black indicates the adsorption rate of the porous polymer obtained by polymerizing 1, 4-diethylbenzene
  • the ordinate indicates the adsorption to be adsorbed Organic solvent or fat, of which vegetable-oi l : vegetable oil; pump-oi l : pump oil; dodecane: 12th house; decane: nunnery; octane: ⁇ ; hexane : ⁇ ; phenol : ⁇ ; Nitrobenzene: chloroform: chloroform; 1, 2_dichlorobenzene: dichlorobenzene; ethylbenzene: ethylbenzene; toluene: toluene; benzene: benzene; DMS0: dimethyl sulfoxide; THF: tetrahydrofuran; DMF: dimethylformamide; Acetone
  • the adsorption rate of porous polymer obtained by polymerizing 1,3,5-triethylbenzene to vegetable oil is 950-1000%, and the adsorption rate of porous polymer obtained by polymerizing 1, 4-diethylbenzene to vegetable oil is 1000-1100%;
  • 1, 3, 5-triethylbenzene benzene polymerized porous polymer adsorption rate of ethanol is about 1000%, 1, 4-diethylbenzene benzene polymerized porous polymer to ethanol
  • the adsorption rate is 575-625%.
  • the adsorption rate of the graphene sponge is much larger than that of the porous polymer obtained by polymerizing 1,3,5-triethylbenzene.
  • the adsorption rate of a porous polymer obtained by polymerizing 1, 4-diethylbenzene is 725%.
  • the adsorption rate of graphene sponge is 5050%; for nitrobenzene, the adsorption rate of porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene is about 1600%, 1, 4-diethylbenzene The adsorption rate of the polymerized porous polymer is about 1650%, and the adsorption rate of the graphene sponge is 6382%.
  • the adsorption rate of the porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene is 1000%.
  • the adsorption rate of the porous polymer obtained by polymerizing 1, 4-diethylbenzene is about 575-625%, and the adsorption rate of graphene sponge is 5103%.
  • expanded graphite only absorbs oil and does not absorb toxic substances such as toluene, in order to enable it to adsorb toluene, Shande Li (SD Li, SH Tian, CM Du, C. He, CP Cen, Y. Xiong. Chemical Engineering Journal, 2010, 162, 546.), modified expanded graphite with petrolatum.
  • the adsorption rate of adsorbed toluene was 21.3%, which was much lower than that of graphene sponge of 5477. 4%.
  • Figure 1 shows the adsorption rates of graphene sponges for organic solvents and greases.
  • the graphene sponge not only has a strong adsorption force for organic solvents, but also has a strong adsorption force for oils and fats.
  • graphene sponges have different adsorption capacities for different organic solvents or greases. This is the embodiment of graphene sponges with selective adsorption.
  • the graphene sponge is hydrophobic, so that effective removal of organic pollutants can be achieved.
  • the decontamination treatment is a method of low-pressure distillation, extraction, or high-temperature distillation, and the organic solvent or grease is removed or recycled from the graphene sponge.
  • the method of low-pressure distillation is to reduce the boiling point of the adsorbed substance by reducing the gas pressure of the closed container in which the graphene sponge is located, so that the adsorbed substance can be desorbed from the graphene sponge by evaporation.
  • the boiling point of octane is 125. 8 ° C at a pressure of 101. 325 kPa.
  • the octane-absorbing graphene sponge was placed in a flask, and the gas was evacuated by a mechanical pump to reduce the gas pressure in the flask, until the gas pressure was 10.13 kPa, at which point the boiling point of the octane was lowered.
  • the octane is evaporated in a low pressure environment of 10.13 kPa to obtain a clean octane.
  • Low pressure distillation includes vacuum distillation, vacuum distillation, high vacuum distillation, excimer distillation or molecular distillation. The vacuum distillation uses the boiling point of the liquid to change with the external pressure.
  • Vacuum distillation is carried out under reduced pressure, and is generally used to separate substances which are easily decomposed when heated to a boiling point under normal pressure, or in combination with other distillation methods such as steam distillation to lower the distillation temperature and improve the separation efficiency.
  • High vacuum distillation is for compounds with high boiling points or is easily oxidized by atmospheric distillation. Generally, the vacuum is first applied, and the vacuum is stabilized and then heated.
  • Excimer or molecular distillation is a distillation process that operates under high vacuum, where the mean free path of the vapor molecules is greater than the distance between the evaporation surface and the condensation surface, thereby allowing the difference in evaporation rates of the components in the feed liquid to be utilized.
  • the liquid mixture is separated.
  • the extraction is mainly for substances that are not easily volatilized, such as pump oil.
  • the specific process is to place the graphene sponge with non-volatile substances in another organic solvent with a lower boiling point, and the non-volatile substance is easy to dissolve.
  • the organic solvent is then used to displace the non-volatile material, and finally the graphene sponge is subjected to low pressure or high temperature distillation.
  • a graphene sponge with dodecane is placed in a beaker containing 250 ml of ethanol, and the dodecane in the graphene sponge is fully dissolved in ethanol, which is equivalent to replacing the graphene sponge with ethanol.
  • the dodecane at this time, the graphene sponge is heated to 80 ° C, the ethanol can be completely evaporated, thereby obtaining a clean graphene sponge, which can be reused.
  • the high-temperature distillation method is to evaporate an organic solvent or fat by a high temperature, and then recover the organic solvent or fat by condensation.
  • a graphene sponge with dodecane is placed in an Erlenmeyer flask, the Erlenmeyer flask is connected to a condensing device, and then the Erlenmeyer flask is heated to 220 ° C, and the generated dodecane vapor enters the condensing device and becomes Liquid dodecane.
  • the abscissa represents temperature, in units. C, the ordinate represents the weight percentage of the graphene sponge.
  • Figure 3 When the temperature rises to 70 CTC, the graphene sponge does not undergo significant chemical and physical damage, and the weight of the graphene sponge is only reduced by about 17%.
  • the graphene sponge has very good thermal stability. Sex.
  • the characteristics also make it possible to adsorb grease or organic contaminants from high temperature separation graphene sponges (generally the boiling point of organic matter is not high). That is to say, the material adsorbed by the graphene sponge can be desorbed from the graphene sponge by high temperature without affecting the structure of the graphene sponge. Since graphene sponges are resistant to high temperatures, that is, have high thermal stability, high temperature distillation can be used.
  • the graphene sponge to which toluene was adsorbed was subjected to an adsorption and desorption cycle experiment by a method of low-pressure distillation. That is, the same piece of graphene sponge was tested.
  • the specific process is as follows: The graphene sponge to which toluene is adsorbed is placed in a closed container, and then the gas in the container is withdrawn by a mechanical pump to reduce the gas pressure inside the container, and then the toluene is evaporated by means of a graphene sponge. The escape escapes, and after the distillation is completed, the graphene sponge is placed in toluene, reabsorbed, and thus circulated. As shown in Figure 3, the experiment was performed ten times in total.
  • Figure 3 shows the amount of adsorption and desorption of graphene sponge in each experiment.
  • the abscissa indicates the number of cycles of the experiment, a total of ten times;
  • the ordinate indicates the weight of toluene adsorbed by the graphene sponge, the unit is m g ;
  • the curve at the top indicates the weight of the adsorbed toluene, and the curve at the lower indicates the graphite The weight of toluene remaining in the olefin sponge.
  • the abscissa indicates the number of cycles of the experiment, ten times in total; the ordinate indicates the weight of dodecane adsorbed by the graphene sponge in units of mg.
  • the upper curve shows the weight of the adsorbed dodecane, and the lower curve shows the weight of the graphene sponge after the low pressure distillation of dodecane in the graphene sponge.

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Abstract

Disclosed is a method for using a graphene sponge to absorb organic solvents or oils. The method for use is suitable for the fields of sewage treatment or liquid-liquid separation. After the graphene sponge has absorbed organic solvents or oils, a depollution treatment is carried out. The depollution treatment removes or recycles the organic solvents or oils from the graphene sponge, using methods such as distillation at a low pressure, extraction or distillation at a high temperature.

Description

一种石墨烯海绵的应用方法 技术领域  Application method of graphene sponge
本发明涉及一种石墨烯海绵的应用方法。  The invention relates to a method for applying a graphene sponge.
背景技术 Background technique
由于原油的泄露和工业有机溶剂的污染, 全球的水污染问题正变得越来越严重。 为 了克服环境问题, 寻找一种能实现有效吸附油脂和有机污染物, 并最终达到将它们与水 分离的吸附剂变的极为重要 ( J. Yuan, X. Liu, 0. Akbulut, J. Hu, S. L. Suib, J. Kong and F. Stel lacci, Nat. Nanotechnol. , 2008, 3, 332.; M. A. Shannon, P. W. Bohn, M. El imelech, J. G. Georgiadis, B. J. Marinas and A. M. Mayes, Nature, 2008, 452, 301. )。 传统的吸附剂比如活性炭, 存在很多缺点, 包括吸附时间长, 选则性差, 吸附能 力有限 (D. Cl ifford, S. Subranmonian and T. J. Sorg, Environ. Sci. Technol. , 1986, 20, 1072.; A. B. Fuertes, G. Marban and D. M. Nevskaia, Carbon, 2003, 41, 87. )。 膨胀石墨虽然对油有很强的吸附能力, 但是对有毒的有机溶剂却无能为力。 对膨胀石墨 的回收也十分困难。 至于聚合物, 虽然吸附的范围有了较大的增加, 但是一方面它的吸 附能力不足, 另一方面高温易分解, 甚至会形成二次污染。 基于这些缺点, 孔尺寸大小 为纳米或微米级别的多孔材料 (L. Feng, Z. Zhong, Z. Mai, B. Liu, L. Jiang and D. Zhu, Angew. Chem. , Int. Ed. , 2003, 42, 800.; Y. Zhang, S. Wei, F. Liu, Y. Du, S. Liu, Y. Ji, T. Ji, T. Yokoib, T. Tatsumib and F. S. Xiao, Nano Today, 2009, 4, 135. ) 或纳米线薄膜 (Α· Sayari, S. Hamoudi and Y. Yang, Chem. Mater. , 2005, 17, 212. ) 引起了人们的重视。 因为纳米、 微米级别的多孔材料和纳米线薄膜具有很强的憎水能力 和超强的亲油能力, 可以很好的实现有机污染物和水, 油脂和水的分离。 同时, 这些材 料还具有吸附时间短, 选择性强, 吸附能力大的特性。 但是纳米、 微米级别的多孔材料 和纳米线薄膜存在着吸附能力不是足够强、 成本高、 不易大量大块制备的缺点。  Due to the leakage of crude oil and the pollution of industrial organic solvents, global water pollution problems are becoming more and more serious. In order to overcome environmental problems, it is extremely important to find an adsorbent that can effectively adsorb oils and organic pollutants and finally achieve separation from water (J. Yuan, X. Liu, 0. Akbulut, J. Hu, SL Suib, J. Kong and F. Stel lacci, Nat. Nanotechnol., 2008, 3, 332.; MA Shannon, PW Bohn, M. El imelech, JG Georgiadis, BJ Marinas and AM Mayes, Nature, 2008, 452, 301.). Conventional adsorbents such as activated carbon have a number of disadvantages, including long adsorption times, poor selectivity, and limited adsorption capacity (D. Cl ifford, S. Subranmonian and TJ Sorg, Environ. Sci. Technol., 1986, 20, 1072.; AB Fuertes, G. Marban and DM Nevskaia, Carbon, 2003, 41, 87.). Although expanded graphite has a strong adsorption capacity for oil, it does not work for toxic organic solvents. The recovery of expanded graphite is also very difficult. As for the polymer, although the range of adsorption has been greatly increased, on the one hand, its adsorption capacity is insufficient, on the other hand, high temperature is easily decomposed, and even secondary pollution is formed. Based on these shortcomings, porous materials with pore sizes of nanometers or micrometers (L. Feng, Z. Zhong, Z. Mai, B. Liu, L. Jiang and D. Zhu, Angew. Chem., Int. Ed., 2003, 42, 800.; Y. Zhang, S. Wei, F. Liu, Y. Du, S. Liu, Y. Ji, T. Ji, T. Yokoib, T. Tatsumib and FS Xiao, Nano Today, 2009 , 4, 135. ) or nanowire film (Α· Sayari, S. Hamoudi and Y. Yang, Chem. Mater., 2005, 17, 212.) has attracted people's attention. Because nano- and micro-scale porous materials and nanowire films have strong hydrophobic ability and superior lipophilic ability, the separation of organic pollutants and water, grease and water can be achieved well. At the same time, these materials have the characteristics of short adsorption time, high selectivity and high adsorption capacity. However, nano- and micro-scale porous materials and nanowire films have the disadvantages that the adsorption capacity is not strong enough, the cost is high, and it is not easy to mass-produce.
发明内容 Summary of the invention
技术问题: 本发明所要解决的技术问题是, 提供一种石墨烯海绵的应用方法, 该石 墨烯海绵用于吸收有机溶剂或者油脂, 具有吸附能力强、 吸附速度快的特点。  Technical Problem: The technical problem to be solved by the present invention is to provide a method for applying a graphene sponge which is used for absorbing organic solvents or fats and has the characteristics of strong adsorption capacity and fast adsorption speed.
技术方案: 为解决上述技术问题, 本发明采用的技术方案是: 一种石墨烯海绵的应用方法, 所述的石墨烯海绵用于吸收有机溶剂或者油脂。 进一步, 所述的石墨烯海绵吸收有机溶剂或者油脂以后, 进行除污处理: 除污处理 是采用低压蒸馏、 萃取、 或者高温蒸馏的方法, 将有机溶剂或者油脂从石墨烯海绵中清 除或者回收利用。 Technical Solution: In order to solve the above technical problems, the technical solution adopted by the present invention is: A method for applying a graphene sponge for absorbing an organic solvent or a grease. Further, after the graphene sponge absorbs the organic solvent or the grease, the decontamination treatment is performed: the decontamination treatment is a method of low-pressure distillation, extraction, or high-temperature distillation, and the organic solvent or grease is removed or recycled from the graphene sponge. .
有益效果: 与现有技术相比, 本技术方案具有以下有益效果:  Advantageous Effects: Compared with the prior art, the technical solution has the following beneficial effects:
1.该应用方法操作简单、 成本低廉, 可应用于工业生产中。 因为石墨烯海绵具有超 强的憎水性, 对有机溶剂和油脂具有吸附能力强、 吸附速度快的特点, 所以将石墨烯海 绵用于吸附有机溶剂和油脂具有性能上的优势。 尤其是, 将石墨烯海绵应用于液液分离 和污水处理中, 利用石墨烯海绵吸附有机溶剂和油脂。  1. The application method is simple in operation and low in cost, and can be applied to industrial production. Because graphene sponge has excellent water repellency and has strong adsorption capacity and fast adsorption speed for organic solvents and oils, graphene sponge has the advantage of being used for adsorbing organic solvents and greases. In particular, graphene sponges are used in liquid-liquid separation and sewage treatment, and graphene sponges are used to adsorb organic solvents and greases.
2.对石墨烯海绵可以重复利用, 并且对有机溶剂和油脂可实现回收。在本技术方案 中, 利用低压蒸馏、 萃取或者高温蒸发的方法将石墨烯海绵所吸附的有机溶剂和油脂从 石墨烯海绵中分离出来, 同时去除了有机溶剂和油脂的石墨烯海绵可以重复利用。 分 离出来的有机溶剂和油脂可以回收利用。该石墨烯海绵对于不同液体之间的相互分离和 污水处理等多方面具有广泛的应用潜力。 附图说明  2. The graphene sponge can be reused, and the organic solvent and grease can be recycled. In the present technical solution, the organic solvent and grease adsorbed by the graphene sponge are separated from the graphene sponge by low-pressure distillation, extraction or high-temperature evaporation, and the graphene sponge from which the organic solvent and the grease are removed can be reused. The separated organic solvents and greases can be recycled. The graphene sponge has wide application potential for various separations between different liquids and sewage treatment. DRAWINGS
图 1是本发明中的石墨烯海绵对有机溶剂和油脂的吸附率图。  BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a graph showing the adsorption ratio of a graphene sponge to an organic solvent and a fat or oil in the present invention.
图 2是本发明中的石墨烯海绵的热重分析曲线图。  Fig. 2 is a thermogravimetric analysis chart of the graphene sponge of the present invention.
图 3是本发明中实施例 1利用石墨烯海绵对甲苯进行吸附、 脱附循环实验图。 图 4是本发明中实施例 2利用石墨烯海绵对十二烷进行了吸附、 脱附循环实验图。 图 5是 1, 3, 5-三乙块苯聚合而成的多孔聚合物、 1, 4-二乙块苯聚合而成的多孔聚合 物对有机溶剂和油脂的吸附率图。  Fig. 3 is a view showing the experiment of adsorbing and desorbing toluene using a graphene sponge in Example 1 of the present invention. Fig. 4 is a view showing an experiment of adsorption and desorption of dodecane by a graphene sponge in Example 2 of the present invention. Fig. 5 is a graph showing the adsorption ratio of a porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene benzene, and a porous polymer obtained by polymerizing 1, 4-diethylbenzene to an organic solvent and a fat.
具体实施方式 detailed description
下面结合附图, 对本发明的技术方案进行详细的说明。  The technical solution of the present invention will be described in detail below with reference to the accompanying drawings.
本发明的一种石墨烯海绵的应用方法, 所述的石墨烯海绵用于吸收有机溶剂或者油 脂。  In the method for applying a graphene sponge of the present invention, the graphene sponge is used for absorbing an organic solvent or a grease.
本发明中的石墨烯海绵的制备方法如下:  The preparation method of the graphene sponge in the present invention is as follows:
第一步, 量取 35ml浓度为 2mg/ml的氧化石墨烯分散液, 并加入 1ml氨水, 形成混 合液; 氨水的浓度为 30%, 指每一百克氨水中, 含过氧化氢 30克。  In the first step, 35 ml of a graphene oxide dispersion having a concentration of 2 mg/ml is weighed, and 1 ml of ammonia water is added to form a mixed solution; the concentration of the ammonia water is 30%, which means that 30 g of hydrogen peroxide is contained per 100 g of ammonia water.
第二步, 将混合液倒入反应釜中, 180°C高温 24h, 然后自然冷却, 拧开反应釜即可 得到石墨烯凝胶。 In the second step, the mixture is poured into a reaction kettle at a high temperature of 180 ° C for 24 hours, then naturally cooled, and the reaction vessel can be unscrewed. A graphene gel was obtained.
第三步, 将得到的石墨烯凝胶低压冷冻干燥, 即可得到多孔的石墨烯海绵。  In the third step, the obtained graphene gel is freeze-dried at a low pressure to obtain a porous graphene sponge.
所述有机溶剂或者油脂包括植物油、 原油、 泵油、 十二烷、 正十烷、 辛烷、 己烷、 苯酚、 硝基苯、 三氯甲烷、 二氯苯、 乙基苯、 甲苯、 苯、 二甲基亚砜、 四氢呋喃、 二甲 基甲酰胺、 丙酮、 乙醇、 甲醇、 煤油、 蓖麻油、 庚烷、 柴油、 汽油、 四氯化碳。  The organic solvent or fat includes vegetable oil, crude oil, pump oil, dodecane, n-decane, octane, hexane, phenol, nitrobenzene, chloroform, dichlorobenzene, ethylbenzene, toluene, benzene, Dimethyl sulfoxide, tetrahydrofuran, dimethylformamide, acetone, ethanol, methanol, kerosene, castor oil, heptane, diesel, gasoline, carbon tetrachloride.
在该应用方法中, 石墨烯海绵是作为吸附剂来使用的。 石墨烯海绵可以应用于液液 分离, 或者污水分离的领域, 把石墨烯海绵当作吸附剂, 吸取有机溶剂或者油脂。 石墨烯海绵吸附率的测试方法是: 将制备的石墨烯海绵切割成小块, 并称取每块质量, 记为 w , 然后将每块石墨烯海绵放入待吸附的溶剂中, 石墨烯海绵充分吸附待测液, 最 后称取每块石墨烯海绵的重量, 记为 w fi, 则石墨烯海绵的吸附率由下式计算得出: 吸附率 = ^ 湿_ ^ 干 >< 100% 利用上述测试方法, 测试石墨烯海绵对作为所述溶剂的甲醇、 乙醇、 丙酮、 四氢呋 喃、 二甲基亚砜、 甲苯、 乙苯、 二氯苯、 氯仿、 硝基苯、 己烷、 庚烷、 辛烷、 正十烷、 十二烷、 泵油、 煤油、 蓖麻油和豆油的吸附率。 测试结果如图 1所示, 横坐标表示石墨 烯海绵的吸附率, 纵坐标表示待吸附的有机溶剂或者油脂。 例如, 石墨烯海绵对泵油的 吸附率为 6854%, 石墨烯海绵对十二烷的吸附率为 5050%, 石墨烯海绵对硝基苯的吸附 率为 6382%, 石墨烯海绵对氯仿的吸附率为 8612%。 In this application method, a graphene sponge is used as an adsorbent. Graphene sponge can be used in the field of liquid-liquid separation or sewage separation. The graphene sponge is used as an adsorbent to absorb organic solvents or grease. The test method for the adsorption rate of graphene sponge is: cut the prepared graphene sponge into small pieces, and weigh each piece of mass, denoted as w, and then put each graphene sponge into the solvent to be adsorbed, graphene sponge Adequate adsorption of the test solution, and finally weigh the weight of each graphene sponge, denoted as w fi , then the adsorption rate of the graphene sponge is calculated by the following formula: adsorption rate = ^ wet _ ^ dry >< 100% Test method for testing graphene sponge as methanol, ethanol, acetone, tetrahydrofuran, dimethyl sulfoxide, toluene, ethylbenzene, dichlorobenzene, chloroform, nitrobenzene, hexane, heptane, octane as the solvent Adsorption rates of n-decane, dodecane, pump oil, kerosene, castor oil and soybean oil. The test results are shown in Fig. 1. The abscissa indicates the adsorption rate of the graphene sponge, and the ordinate indicates the organic solvent or grease to be adsorbed. For example, the adsorption rate of graphene sponge to pump oil is 6854%, the adsorption rate of graphene sponge to dodecane is 5050%, the adsorption rate of graphene sponge to nitrobenzene is 6382%, and the adsorption of graphene sponge on chloroform. The rate is 8612%.
将 1, 3, 5-三乙块苯聚合而成的多孔聚合物、 1, 4-二乙块苯聚合而成的多孔聚合物对 油脂或者有机溶剂的吸附率, 与石墨烯海绵的吸附率作对比。 如图 5所示, 横坐标表示 1, 3, 5-三乙块苯聚合而成的多孔聚合物的吸附率和 1, 4-二乙块苯聚合而成的多孔聚合物 的吸附率, 其中, 灰色表示 1, 3, 5-三乙块苯聚合而成的多孔聚合物的吸附率, 黑色表示 1, 4-二乙块苯聚合而成的多孔聚合物的吸附率;纵坐标表示待吸附的有机溶剂或者油脂, 其中, vegetable-oi l : 植物油; pump-oi l : 泵油; dodecane: 十二院; decane: 努院; octane: 辛院; hexane : 己院; phenol : 苯西分; nitrobenzene: 石肖基苯; chloroform: 氯仿; 1, 2_dichlorobenzene:二氯苯; ethylbenzene: 乙苯; toluene: 甲苯; benzene: 苯; DMS0 :二甲基亚砜; THF :四氢呋喃; DMF :二甲基甲酰胺; acetone :丙酮; ethanol : 乙醇; methanol : 甲醇; Weight gain:吸附率; CMP- 1 : 1, 3, 5_三乙块苯聚合而成的多孔 聚合物; CMP-2: 1, 4-二乙块苯聚合而成的多孔聚合物。 1, 3, 5-三乙块苯聚合而成的多孔聚合物吸附率的测试方法, 以及 1, 4-二乙块苯聚 合而成的多孔聚合物吸附率的测试方法, 均与石墨烯海绵吸附率的测试方法相同。 本对 比例中利用 1, 3, 5-三乙块苯聚合而成的多孔聚合物、 1, 4-二乙块苯聚合而成的多孔聚合 物分别对植物油、 泵油、 十二烷、 癸烷、 辛烷、 己烷、 苯酚、 硝基苯、 氯仿、 二氯苯、 乙苯、 甲苯、 苯、 二甲基亚砜、 四氢呋喃、 二甲基甲酰胺、 丙酮、 乙醇、 甲醇的吸附率 进行测试。 例如 1,3,5-三乙块苯聚合而成的多孔聚合物对植物油的吸附率为 950-1000% , 1, 4-二乙块苯聚合而成的多孔聚合物对植物油的吸附率为 1000-1100%; 1, 3, 5-三乙块苯聚合而成的多孔聚合物对乙醇的吸附率为 1000%左右, 1, 4-二乙块苯聚 合而成的多孔聚合物对乙醇的吸附率为 575-625%。 The adsorption rate of a porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene and 1, 4-diethylbenzene to a grease or an organic solvent, and an adsorption rate of a graphene sponge For comparison. As shown in FIG. 5, the abscissa indicates the adsorption ratio of the porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene and the adsorption ratio of the porous polymer obtained by polymerizing 1, 4-diethylbenzene. , gray indicates the adsorption rate of the porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene, black indicates the adsorption rate of the porous polymer obtained by polymerizing 1, 4-diethylbenzene; the ordinate indicates the adsorption to be adsorbed Organic solvent or fat, of which vegetable-oi l : vegetable oil; pump-oi l : pump oil; dodecane: 12th house; decane: nunnery; octane: 辛院; hexane : 院院; phenol : 苯西分; Nitrobenzene: chloroform: chloroform; 1, 2_dichlorobenzene: dichlorobenzene; ethylbenzene: ethylbenzene; toluene: toluene; benzene: benzene; DMS0: dimethyl sulfoxide; THF: tetrahydrofuran; DMF: dimethylformamide; Acetone : acetone; ethanol : ethanol; methanol : methanol; weight gain: adsorption rate; CMP-1 : 1, 3, 5 - triethyl benzene polymerized porous polymer; CMP-2: 1, 4- 2 A porous polymer obtained by polymerizing benzene. 1, 3, 5-triethylbenzene benzene polymerization of porous polymer adsorption rate test method, and 1, 4-diethyl benzene polymerization of porous polymer adsorption rate test method, both with graphene sponge The test method for the adsorption rate is the same. In the present comparative example, a porous polymer obtained by polymerizing 1,3,5-triethylbenzene, and a porous polymer obtained by polymerizing 1, 4-diethylbenzene are respectively applied to vegetable oil, pump oil, dodecane, and cesium. Adsorption rates of alkane, octane, hexane, phenol, nitrobenzene, chloroform, dichlorobenzene, ethylbenzene, toluene, benzene, dimethyl sulfoxide, tetrahydrofuran, dimethylformamide, acetone, ethanol, methanol test. For example, the adsorption rate of porous polymer obtained by polymerizing 1,3,5-triethylbenzene to vegetable oil is 950-1000%, and the adsorption rate of porous polymer obtained by polymerizing 1, 4-diethylbenzene to vegetable oil is 1000-1100%; 1, 3, 5-triethylbenzene benzene polymerized porous polymer adsorption rate of ethanol is about 1000%, 1, 4-diethylbenzene benzene polymerized porous polymer to ethanol The adsorption rate is 575-625%.
通过对比表 1和表 5, 可以看出对于相同的待吸附油脂或者有机溶剂, 石墨烯海绵 的吸附率远远大于 1, 3, 5-三乙块苯聚合而成的多孔聚合物的吸附率或者 1, 4-二乙块苯聚 合而成的多孔聚合物的吸附率。 例如, 对于泵油, 1, 3, 5-三乙块苯聚合而成的多孔聚 合物吸附率为 800%左右, 1, 4-二乙块苯聚合而成的多孔聚合物吸附率为 725%左右, 而 石墨烯海绵的吸附率为 5050%; 对于硝基苯, 1, 3, 5-三乙块苯聚合而成的多孔聚合物吸 附率为 1600%左右, 1, 4-二乙块苯聚合而成的多孔聚合物吸附率为 1650%左右, 而石墨 烯海绵的吸附率为 6382%; 对于乙醇, 1, 3, 5-三乙块苯聚合而成的多孔聚合物吸附率为 1000%左右, 1, 4-二乙块苯聚合而成的多孔聚合物吸附率为 575-625%左右, 而石墨烯海 绵的吸附率为 5103%。  By comparing Tables 1 and 5, it can be seen that for the same grease or organic solvent to be adsorbed, the adsorption rate of the graphene sponge is much larger than that of the porous polymer obtained by polymerizing 1,3,5-triethylbenzene. Or the adsorption rate of a porous polymer obtained by polymerizing 1, 4-diethylbenzene. For example, for pump oil, the adsorption rate of porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene is about 800%, and the adsorption rate of porous polymer obtained by polymerizing 1, 4-diethylbenzene is 725%. Left and right, and the adsorption rate of graphene sponge is 5050%; for nitrobenzene, the adsorption rate of porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene is about 1600%, 1, 4-diethylbenzene The adsorption rate of the polymerized porous polymer is about 1650%, and the adsorption rate of the graphene sponge is 6382%. For the ethanol, the adsorption rate of the porous polymer obtained by polymerizing 1, 3, 5-triethylbenzene is 1000%. The adsorption rate of the porous polymer obtained by polymerizing 1, 4-diethylbenzene is about 575-625%, and the adsorption rate of graphene sponge is 5103%.
另外, 对于膨胀石墨而言, 膨胀石墨只吸油不吸甲苯等有毒物质, 为了使它能吸 附甲苯, Shande Li ( S. D. Li, S. H. Tian, C. M. Du, C. He, C. P. Cen, Y. Xiong. Chemical Engineering Journal, 2010, 162, 546. ), 用凡士林修饰膨胀石墨。 经试验, 吸附甲苯的吸附率为: 21. 3%, 远远低于石墨烯海绵的 5477. 4%。  In addition, for expanded graphite, expanded graphite only absorbs oil and does not absorb toxic substances such as toluene, in order to enable it to adsorb toluene, Shande Li (SD Li, SH Tian, CM Du, C. He, CP Cen, Y. Xiong. Chemical Engineering Journal, 2010, 162, 546.), modified expanded graphite with petrolatum. The adsorption rate of adsorbed toluene was 21.3%, which was much lower than that of graphene sponge of 5477. 4%.
图 1列出了石墨烯海绵对于有机溶剂和油脂的吸附率。 从图 1 中可以看出, 石墨 烯海绵不仅对于有机溶剂具有很强的吸附力,而且对油脂类也具有很强的吸附力。但是, 石墨烯海绵对于不同的有机溶剂或油脂的吸附能力是不一样的。这正是石墨烯海绵具有 选择性吸附的体现。另外,石墨烯海绵是憎水的, 因此可以实现有机污染物的有效清除。  Figure 1 shows the adsorption rates of graphene sponges for organic solvents and greases. As can be seen from Fig. 1, the graphene sponge not only has a strong adsorption force for organic solvents, but also has a strong adsorption force for oils and fats. However, graphene sponges have different adsorption capacities for different organic solvents or greases. This is the embodiment of graphene sponges with selective adsorption. In addition, the graphene sponge is hydrophobic, so that effective removal of organic pollutants can be achieved.
进一步, 所述的石墨烯海绵吸收有机溶剂或者油脂以后, 进行除污处理: 除污处理 是采用低压蒸馏、 萃取、 或者高温蒸馏的方法, 将有机溶剂或者油脂从石墨烯海绵中清 除或者回收利用。 低压蒸馏的方法就是通过降低石墨烯海绵所在密闭容器的气压, 从而降低所吸附物 质的沸点, 使得吸附的物质可以通过蒸发的方式, 从石墨烯海绵中脱附出来。 例如, 在 气压为 101. 325kPa时, 辛烷的沸点是 125. 8°C。 将吸有辛烷的石墨烯海绵放入长颈烧瓶 中, 利用机械泵抽出气体, 降低长颈烧瓶中的气压, 直至气压为 10. 13kPa, 此时辛烷的 沸点降低。 辛烷在 10. 13kPa的低压环境中蒸发, 即可得到干净的辛烷。 低压蒸馏包括减 压蒸馏、 真空蒸馏、 高真空蒸馏、 准分子蒸馏或者分子蒸馏。 减压蒸馏是利用液体的沸 点是随外界压力的变化而变化的, 如果借助于真空泵降低系统内压力, 就可以降低液体 的沸点, 这便是减压蒸馏操作的理论依据, 因此它特别适用于那些在常压蒸馏时未达沸 点即已受热分解、 氧化或聚合的物质。 真空蒸馏就是在减压下进行, 一般用于分离在 常压下加热至沸点时易于分解的物质, 或与其它蒸馏方法 (如蒸汽蒸馏) 结合以降 低蒸馏温度并提高分离效率。 高真空蒸馏是针对那些沸点很高的化合物, 或者是常压 蒸馏容易氧化的。 一般先抽真空, 等真空度稳定下来再加热。 当温度接近此真空度下的 沸点时, 再减慢加热的速度。 准分子或分子蒸馏是一种在高真空下操作的蒸馏方法, 这 时蒸气分子的平均自由程大于蒸发表面与冷凝表面之间的距离, 从而可利用料液中各组 分蒸发速率的差异, 对液体混合物进行分离。 Further, after the graphene sponge absorbs the organic solvent or the grease, the decontamination treatment is performed: the decontamination treatment is a method of low-pressure distillation, extraction, or high-temperature distillation, and the organic solvent or grease is removed or recycled from the graphene sponge. . The method of low-pressure distillation is to reduce the boiling point of the adsorbed substance by reducing the gas pressure of the closed container in which the graphene sponge is located, so that the adsorbed substance can be desorbed from the graphene sponge by evaporation. For example, the boiling point of octane is 125. 8 ° C at a pressure of 101. 325 kPa. The octane-absorbing graphene sponge was placed in a flask, and the gas was evacuated by a mechanical pump to reduce the gas pressure in the flask, until the gas pressure was 10.13 kPa, at which point the boiling point of the octane was lowered. The octane is evaporated in a low pressure environment of 10.13 kPa to obtain a clean octane. Low pressure distillation includes vacuum distillation, vacuum distillation, high vacuum distillation, excimer distillation or molecular distillation. The vacuum distillation uses the boiling point of the liquid to change with the external pressure. If the pressure in the system is lowered by means of a vacuum pump, the boiling point of the liquid can be lowered, which is the theoretical basis for the vacuum distillation operation, so it is particularly suitable for Those substances which have been decomposed, oxidized or polymerized by thermal decomposition at atmospheric boiling. Vacuum distillation is carried out under reduced pressure, and is generally used to separate substances which are easily decomposed when heated to a boiling point under normal pressure, or in combination with other distillation methods such as steam distillation to lower the distillation temperature and improve the separation efficiency. High vacuum distillation is for compounds with high boiling points or is easily oxidized by atmospheric distillation. Generally, the vacuum is first applied, and the vacuum is stabilized and then heated. When the temperature approaches the boiling point at this vacuum, the heating rate is slowed down. Excimer or molecular distillation is a distillation process that operates under high vacuum, where the mean free path of the vapor molecules is greater than the distance between the evaporation surface and the condensation surface, thereby allowing the difference in evaporation rates of the components in the feed liquid to be utilized. The liquid mixture is separated.
萃取主要是针对不容易挥发的物质, 比如泵油, 具体过程是将吸有不易挥发物质的石 墨烯海绵置于另一种具有较低沸点的有机溶剂中,而且该不易挥发的物质要易溶于较低 沸点的有机溶剂中, 然后用该有机溶剂置换出不易挥发的物质, 最后在对石墨烯海绵进 行低压或高温蒸馏。例如,将吸有十二烷的石墨烯海绵放入盛有 250毫升乙醇的烧杯中, 待石墨烯海绵中的十二烷充分溶入乙醇中, 即等效于用乙醇替代了石墨烯海绵中的十二 烷, 此时再对石墨烯海绵加热到 80°C, 就可将乙醇全部蒸发出来, 从而得到干净的石墨 烯海绵, 使其可重复使用。  The extraction is mainly for substances that are not easily volatilized, such as pump oil. The specific process is to place the graphene sponge with non-volatile substances in another organic solvent with a lower boiling point, and the non-volatile substance is easy to dissolve. In a lower boiling organic solvent, the organic solvent is then used to displace the non-volatile material, and finally the graphene sponge is subjected to low pressure or high temperature distillation. For example, a graphene sponge with dodecane is placed in a beaker containing 250 ml of ethanol, and the dodecane in the graphene sponge is fully dissolved in ethanol, which is equivalent to replacing the graphene sponge with ethanol. The dodecane, at this time, the graphene sponge is heated to 80 ° C, the ethanol can be completely evaporated, thereby obtaining a clean graphene sponge, which can be reused.
高温蒸馏的方法是通过高温使有机溶剂或油脂蒸发,再通过冷凝对有机溶剂或油脂 进行回收。 例如, 将吸有十二烷的石墨烯海绵放入三角烧瓶中, 三角烧瓶和冷凝装置相 连通, 接着将三角烧瓶加热升温至 220°C, 产生的十二烷蒸汽进入冷凝装置, 又变为液 态的十二烷。  The high-temperature distillation method is to evaporate an organic solvent or fat by a high temperature, and then recover the organic solvent or fat by condensation. For example, a graphene sponge with dodecane is placed in an Erlenmeyer flask, the Erlenmeyer flask is connected to a condensing device, and then the Erlenmeyer flask is heated to 220 ° C, and the generated dodecane vapor enters the condensing device and becomes Liquid dodecane.
如图 2 所示, 横坐标表示温度, 单位。 C, 纵坐标表示石墨烯海绵的重量百分比。 从图 3中可以看出: 当温度升到 70CTC时, 石墨烯海绵并没有发生明显的化学和物理破 坏, 并且石墨烯海绵的重量只减少了 17%左右, 石墨烯海绵具有非常好的热稳定性。 该 特点也让高温分离石墨烯海绵所吸附油脂或有机污染物成为了可能(一般有机物的沸点 都不高)。 也就是说, 通过高温可以将石墨烯海绵所吸附的物质从石墨烯海绵中脱附出 来, 同时又不会影响石墨烯海绵的结构。因为石墨烯海绵耐高温, 即具有高的热稳定性, 所以才可以用高温蒸馏的方法。 实施例 1 As shown in Figure 2, the abscissa represents temperature, in units. C, the ordinate represents the weight percentage of the graphene sponge. As can be seen from Figure 3: When the temperature rises to 70 CTC, the graphene sponge does not undergo significant chemical and physical damage, and the weight of the graphene sponge is only reduced by about 17%. The graphene sponge has very good thermal stability. Sex. The The characteristics also make it possible to adsorb grease or organic contaminants from high temperature separation graphene sponges (generally the boiling point of organic matter is not high). That is to say, the material adsorbed by the graphene sponge can be desorbed from the graphene sponge by high temperature without affecting the structure of the graphene sponge. Since graphene sponges are resistant to high temperatures, that is, have high thermal stability, high temperature distillation can be used. Example 1
利用低压蒸馏的方法, 对吸附了甲苯的石墨烯海绵, 进行吸附、 脱附循环实验。 即对 同一块石墨烯海绵进行实验。 具体过程即是: 将吸附了甲苯的石墨烯海绵置于密闭容器 中, 然后用机械泵将容器里的气体抽出, 降低容器内的气压, 这时甲苯就会通过蒸发的 方式, 从石墨烯海绵中逃逸出来, 待蒸馏完成, 再将该石墨烯海绵置于甲苯中, 重新进 行吸收, 如此循环下去。 如图 3所示, 实验共进行十次。 图 3显示了每次实验中石墨烯 海绵的吸附量和脱附量。 图 3中, 横坐标表示实验的循环次数, 共十次; 纵坐标表示石 墨烯海绵所吸附的甲苯的重量, 单位 mg ; 位于上方的曲线表示所吸附甲苯的重量, 位于 下方的曲线表示石墨烯海绵中残留的甲苯重量。 The graphene sponge to which toluene was adsorbed was subjected to an adsorption and desorption cycle experiment by a method of low-pressure distillation. That is, the same piece of graphene sponge was tested. The specific process is as follows: The graphene sponge to which toluene is adsorbed is placed in a closed container, and then the gas in the container is withdrawn by a mechanical pump to reduce the gas pressure inside the container, and then the toluene is evaporated by means of a graphene sponge. The escape escapes, and after the distillation is completed, the graphene sponge is placed in toluene, reabsorbed, and thus circulated. As shown in Figure 3, the experiment was performed ten times in total. Figure 3 shows the amount of adsorption and desorption of graphene sponge in each experiment. In Fig. 3, the abscissa indicates the number of cycles of the experiment, a total of ten times; the ordinate indicates the weight of toluene adsorbed by the graphene sponge, the unit is m g ; the curve at the top indicates the weight of the adsorbed toluene, and the curve at the lower indicates the graphite The weight of toluene remaining in the olefin sponge.
从图 3中可以看出: 被石墨烯海绵所吸附的甲苯脱附率可以达到 99%以上, 脱附完的 石墨烯海绵所具有的吸附能力基本上没变化, 还可以重复利用。 实施例 2  It can be seen from Fig. 3 that the desorption rate of toluene adsorbed by the graphene sponge can reach 99% or more, and the adsorption capacity of the desorbed graphene sponge is basically unchanged, and can be reused. Example 2
利用乙醇作为萃取剂, 对吸附了十二烷的石墨烯海绵进行吸附、 脱附循环实验。 即 对同一块石墨烯海绵进行实验。 具体过程是: 将吸附了十二烷的石墨烯海绵浸于足够多 的乙醇中, 待十二烷基本上都溶于乙醇中后, 取出石墨烯海绵, 并置于 60°C的温箱中 2 小时, 然后取出再吸附十二烷, 如此循环十次。 图 4显示了每次实验中石墨烯海绵的吸 附量和残留量。 图 4中, 横坐标表示实验的循环次数, 共十次; 纵坐标表示石墨烯海绵 所吸附十二烷的重量, 单位 mg。 位于上方的曲线表示吸附十二烷的重量, 位于下方的曲 线表示石墨烯海绵中的十二烷被低压蒸馏后的石墨烯海绵重量。  The adsorption and desorption cycle experiments of the graphene sponge adsorbed with dodecane were carried out using ethanol as an extractant. That is, the same piece of graphene sponge was tested. The specific process is as follows: The graphene sponge adsorbed with dodecane is immersed in enough ethanol. After the dodecane is substantially dissolved in ethanol, the graphene sponge is taken out and placed in a thermostat at 60 ° C. After 2 hours, then take out and adsorb dodecane, and cycle 10 times. Figure 4 shows the amount of adsorption and residual amount of graphene sponge in each experiment. In Fig. 4, the abscissa indicates the number of cycles of the experiment, ten times in total; the ordinate indicates the weight of dodecane adsorbed by the graphene sponge in units of mg. The upper curve shows the weight of the adsorbed dodecane, and the lower curve shows the weight of the graphene sponge after the low pressure distillation of dodecane in the graphene sponge.
从图 4中可以看出: 被石墨烯海绵所吸附的十二烷脱附率可以达到 99%以上, 脱附完 的石墨烯海绵所具有的吸附能力基本上没变化, 还可以重复利用。  It can be seen from Fig. 4 that the desorption rate of dodecane adsorbed by the graphene sponge can reach 99% or more, and the adsorption capacity of the desorbed graphene sponge is basically unchanged, and can be reused.

Claims

权利要求书 Claim
1.一种石墨烯海绵的应用方法, 其特征在于, 所述的石墨烯海绵用于吸收有机溶剂 或者油脂。 A method of applying a graphene sponge, characterized in that the graphene sponge is used for absorbing an organic solvent or a grease.
2.根据权利要求 1 所述的石墨烯海绵的应用方法, 其特征在于: 所述有机溶剂或者 油脂包括植物油、 原油、 泵油、 十二烷、 正十烷、 辛烷、 己烷、 苯酚、 硝基苯、 三氯甲 烷、 二氯苯、 乙基苯、 甲苯、 苯、 二甲基亚砜、 四氢呋喃、 二甲基甲酰胺、 丙酮、 乙 醇、 甲醇、 煤油、 蓖麻油、 庚烷、 柴油、 汽油、 四氯化碳。  The method for applying a graphene sponge according to claim 1, wherein the organic solvent or fat comprises vegetable oil, crude oil, pump oil, dodecane, n-decane, octane, hexane, phenol, Nitrobenzene, chloroform, dichlorobenzene, ethylbenzene, toluene, benzene, dimethyl sulfoxide, tetrahydrofuran, dimethylformamide, acetone, ethanol, methanol, kerosene, castor oil, heptane, diesel, Gasoline, carbon tetrachloride.
3.根据权利要求 1 所述的石墨烯海绵的应用方法, 其特征在于: 所述的石墨烯海绵 吸收有机溶剂或者油脂以后, 进行除污处理: 除污处理是采用低压蒸馏、 萃取、 或者高 温蒸馏的方法, 将有机溶剂或者油脂从石墨烯海绵中清除或者回收利用。  The method for applying a graphene sponge according to claim 1, wherein: the graphene sponge absorbs an organic solvent or a grease, and then performs a decontamination treatment: the decontamination treatment is a low pressure distillation, extraction, or high temperature. The method of distillation removes or recycles the organic solvent or grease from the graphene sponge.
4.根据权利要求 3 所述的石墨烯海绵的应用方法, 其特征在于, 所述的低压蒸馏包 括减压蒸馏、 真空蒸馏、 高真空蒸馏、 准分子蒸馏或者分子蒸馏。  The method for applying a graphene sponge according to claim 3, wherein the low pressure distillation comprises vacuum distillation, vacuum distillation, high vacuum distillation, excimer distillation or molecular distillation.
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