[go: up one dir, main page]

CN1328425C - Active carbon fiber in hollow morphological structure, and preparation method - Google Patents

Active carbon fiber in hollow morphological structure, and preparation method Download PDF

Info

Publication number
CN1328425C
CN1328425C CNB2005100305458A CN200510030545A CN1328425C CN 1328425 C CN1328425 C CN 1328425C CN B2005100305458 A CNB2005100305458 A CN B2005100305458A CN 200510030545 A CN200510030545 A CN 200510030545A CN 1328425 C CN1328425 C CN 1328425C
Authority
CN
China
Prior art keywords
hollow
activated carbon
carbon fiber
fiber
hollow fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CNB2005100305458A
Other languages
Chinese (zh)
Other versions
CN1760414A (en
Inventor
孙俊芬
王庆瑞
陈雪英
朱思君
武利顺
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Donghua University
Original Assignee
Donghua University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Donghua University filed Critical Donghua University
Priority to CNB2005100305458A priority Critical patent/CN1328425C/en
Publication of CN1760414A publication Critical patent/CN1760414A/en
Application granted granted Critical
Publication of CN1328425C publication Critical patent/CN1328425C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

本发明涉及一种采用中空形态结构的活性炭纤维和制备方法,其中,中孔和大孔的孔径分布为2~90nm,中孔的孔径分布主要为2~5nm。采用医用聚丙烯腈中空纤维作为原料,在含磷化物溶液中浸泡预处理,然后经预氧化、炭化、活化而成。用该方法生产的聚丙烯腈基活性炭纤维具有较高的比表面积,且该炭纤维中的中孔含量和中孔的比表面积较高,对小分子物质和中分子物质都具有较高的吸附率。本发明的方法工艺简单,投资少,产品具有高吸附性能,适用范围广,净化效果好,可适用于空气净化、水净化、有机物吸附净化、血液净化等需要吸附净化的领域。The invention relates to an activated carbon fiber with a hollow shape structure and a preparation method, wherein the pore size distribution of the mesopores and macropores is 2-90 nm, and the pore size distribution of the mesopores is mainly 2-5 nm. The medical polyacrylonitrile hollow fiber is used as the raw material, soaked in the phosphide-containing solution for pretreatment, and then pre-oxidized, carbonized and activated. The polyacrylonitrile-based activated carbon fiber produced by this method has a high specific surface area, and the mesopore content and the specific surface area of the mesopore in the carbon fiber are high, and have high adsorption capacity for small molecular substances and medium molecular substances. Rate. The method of the invention has simple process, low investment, high adsorption performance, wide application range and good purification effect, and can be applied to fields requiring adsorption purification such as air purification, water purification, organic matter adsorption purification, blood purification and the like.

Description

具有中空形态结构的活性炭纤维和制备方法Activated carbon fiber with hollow morphology and preparation method

技术领域technical field

本发明涉及一种具有中空形态结构的活性炭纤维和制备方法。The invention relates to an activated carbon fiber with a hollow shape structure and a preparation method.

背景技术Background technique

活性炭纤维(ACF)是在炭纤维基础上发展起来的炭质吸附材料,是以有机纤维为原料,经高温炭化活化而成。ACF与传统的活性炭相比,具有以下特点:比表面积大;孔径分布集中;吸脱附速率快,可具有毡、布、纸等多种加工形态;吸附效应与吸附质浓度无关,对ppb级的痕量物质吸附特别有效,亦即低浓度下吸附效率高。而活性中空炭纤维(ACHF)则起步较晚,是一种新型的吸附材料,与ACF相比,具有中空、多孔、自我支撑、孔径可以通过原纤维和炭化、活化过程的加工条件来控制等特点,很小的体积就可以有很大的比表面积,可以用于液体或气体混合物的吸附、分离和渗析等,拓宽了它在催化、医药、电子及液相吸附等领域的应用。Activated carbon fiber (ACF) is a carbon adsorption material developed on the basis of carbon fiber. It is made of organic fiber as raw material and activated by high-temperature carbonization. Compared with traditional activated carbon, ACF has the following characteristics: large specific surface area; concentrated pore size distribution; fast adsorption and desorption rate, and can have various processing forms such as felt, cloth, and paper; The adsorption of trace substances is particularly effective, that is, the adsorption efficiency is high at low concentrations. Activated hollow carbon fiber (ACHF) started late and is a new type of adsorption material. Compared with ACF, it is hollow, porous, self-supporting, and the pore size can be controlled by fibrils, carbonization, and activation process conditions. Features, small volume can have a large specific surface area, can be used for adsorption, separation and dialysis of liquid or gas mixture, broaden its application in the fields of catalysis, medicine, electronics and liquid phase adsorption.

1999年陈露(专利申请号:97120296.6)报道了采用实心聚丙烯腈纤维为原料生产活性炭纤维的方法,但预氧丝用无机盐NaCO3进行了浸泡,但这种方法使用了含金属离子的预氧丝,使最终ACF中不可避免地含有较多的金属离子,从而限制了其在医药、催化等领域的应用。1997年张引枝(专利申请号:95119030.X)等人报道了采用树脂与炭素材料的混合原料制备中孔活性炭纤维的方法,所制得的中孔活性炭纤维中的中孔率为50-70%。1994年刘智仁(专利申请号:94108414.0)报道了采用木基粘胶纤维无纺布或木基粘胶纤维纸为原料制备高吸附性活性炭纤维的方法。1997年曾汉民报道了(专利申请号:97108889.6)采用天然纤维为原料(如剑麻纤维)制备活性炭纤维的方法。以上所述的各种纤维均为实心纤维,实心结构的纤维内部含有较少的孔,在进行后期的预氧化、炭化和活化工艺时,影响了气体的渗透,容易造成结构和性能不同的“皮芯”结构。In 1999, Chen Lu (patent application number: 97120296.6) reported the method of using solid polyacrylonitrile fiber as raw material to produce activated carbon fiber, but the pre-oxygenated silk was soaked with inorganic salt NaCO3 , but this method used metal ion-containing Pre-oxygenated silk inevitably contains more metal ions in the final ACF, which limits its application in the fields of medicine and catalysis. In 1997, Zhang Yinzhi (patent application number: 95119030.X) and others reported a method for preparing mesoporous activated carbon fibers using a mixed raw material of resin and carbon material, and the mesoporosity in the prepared mesoporous activated carbon fibers was 50-70% . In 1994, Liu Zhiren (patent application number: 94108414.0) reported the method of using wood-based viscose fiber non-woven fabric or wood-based viscose fiber paper as raw material to prepare highly absorbent activated carbon fibers. In 1997 Zeng Hanmin reported (patent application number: 97108889.6) the method that adopts natural fiber to prepare activated carbon fiber as raw material (as sisal fiber). The various fibers mentioned above are all solid fibers, and the fibers with a solid structure contain fewer pores. When the pre-oxidation, carbonization and activation processes are carried out in the later stage, the permeation of gas is affected, and it is easy to cause "different" structures and properties. skin-core" structure.

发明内容Contents of the invention

本发明的目的是提供一种具有中空形态结构的活性炭纤维。The object of the present invention is to provide an activated carbon fiber with a hollow morphology.

本发明的目的还提供一种具有中空形态结构的活性炭纤维的制备方法。The object of the present invention is also to provide a method for preparing activated carbon fibers with a hollow morphology.

本发明的具有中空形态结构的活性炭纤维,其中,中孔和大孔的孔径分布为2~90nm。除微孔外,孔径由2~50nm的中孔和孔径>50nm~90nm的大孔组成,其中,中孔的孔径分布主要集中在2~5nm,占所有中孔的含量比例大于95%。In the activated carbon fiber with a hollow morphology structure of the present invention, the pore size distribution of the mesopores and macropores is 2-90 nm. In addition to micropores, the pore diameter is composed of mesopores with a diameter of 2-50nm and macropores with a diameter of >50nm-90nm. Among them, the pore size distribution of mesopores is mainly concentrated in the range of 2-5nm, accounting for more than 95% of all mesopores.

本发明的具有中空形态结构的活性炭纤维的制备方法,是将聚丙烯腈中空纤维用磷化物的水溶液进行预处理,随后经预氧化、炭化、活化而成。The preparation method of the activated carbon fiber with a hollow shape structure of the present invention is obtained by pretreating the polyacrylonitrile hollow fiber with an aqueous solution of phosphide, followed by preoxidation, carbonization and activation.

具体制备方法为将原料纤维清洗并浸泡在蒸馏水中1~3天,每隔数小时需换水一次,以去除纤维表面的甘油及其它助剂,然后放入离心机中甩干,并在空气中自然晾干,然后放在盛有P2O5的干燥器中干燥至恒重并称量;随后用浓度为2-10%重量(wt)的磷化物水溶液中浸泡中空纤维10-120分钟进行预处理,取出后在空气中自然晾干,然后放在盛有P2O5的干燥器中至恒重并称量;再放入烘箱中以200-300℃,加热0.5-6小时对中空纤维进行预氧化;再进行炭化处理,将预处理和预氧化过的中空纤维放入管式炉内的石英管中,用真空泵抽去石英管中的空气,开始通入氮气,在氮气保护下,以10℃/min的升温速率加热,炭化温度为500-1000℃,炭化时间为10-110分钟;炭化结束,再进行活化处理,炭化后的中空纤维继续在该炉内在600-1000℃条件下通CO2气体进行活化,活化时间为20-100分钟;活化结束,关闭CO2气体,用真空泵抽去石英管中的CO2气体,再通入氮气,当石英管内的氮气压力为1个大气压时,封堵石英管两端,关闭氮气,直至石英管内温度降至室温时,取出中空纤维,即为成品-具有中空形态的活性炭纤维。The specific preparation method is to wash and soak the raw material fibers in distilled water for 1 to 3 days, and change the water every few hours to remove glycerin and other additives on the surface of the fibers, then put them in a centrifuge to dry them, and dry them in the air. Naturally dry in the middle, then dry to constant weight in a desiccator filled with P 2 O 5 and weigh; then soak the hollow fiber in a 2-10% by weight (wt) phosphide aqueous solution for 10-120 minutes Carry out pretreatment, take it out and dry it naturally in the air, then place it in a desiccator filled with P 2 O 5 to constant weight and weigh it; then put it in an oven at 200-300°C and heat it for 0.5-6 hours The hollow fiber is pre-oxidized; then carbonized, the pre-treated and pre-oxidized hollow fiber is placed in the quartz tube in the tube furnace, the air in the quartz tube is pumped out with a vacuum pump, nitrogen gas is introduced, and the nitrogen gas is protected. Heating at a heating rate of 10°C/min, the carbonization temperature is 500-1000°C, and the carbonization time is 10-110 minutes; after the carbonization is completed, the activation treatment is carried out, and the carbonized hollow fiber continues to be heated in the furnace at 600-1000°C Under the condition of CO 2 gas for activation, the activation time is 20-100 minutes; when the activation is finished, turn off the CO 2 gas, use a vacuum pump to remove the CO 2 gas in the quartz tube, and then inject nitrogen gas, when the nitrogen pressure in the quartz tube is 1 At 1 atmospheric pressure, plug both ends of the quartz tube, turn off the nitrogen gas, and when the temperature in the quartz tube drops to room temperature, take out the hollow fiber, which is the finished product—activated carbon fiber with a hollow shape.

在上述方法中所述的磷化物可以是磷酸铵、磷酸二氢铵,磷酸氢二铵、磷酸或偏磷酸等。The phosphide described in the above method can be ammonium phosphate, ammonium dihydrogen phosphate, diammonium hydrogen phosphate, phosphoric acid or metaphosphoric acid and the like.

本发明中的中空纤维具有中空的结构形态,采用干喷湿纺的成形方法,因而所得到的纤维内部存在较多的微孔结构,其截面为双排指状孔结构,而且纤维的表面具有丰富的孔。这一结构特性决定了后期制备的ACHF也具有丰富的孔结构,从而BET比表面积和吸附率都得到很大的提高,尤其是对中相对分子质量物质,如VB12等的吸附率有明显的提高。The hollow fiber in the present invention has a hollow structure and adopts the forming method of dry jet wet spinning, so there are more microporous structures inside the obtained fiber, and its cross section is a double-row finger-like hole structure, and the surface of the fiber has Rich holes. This structural characteristic determines that the ACHF prepared in the later stage also has a rich pore structure, so that the BET specific surface area and adsorption rate have been greatly improved, especially for the adsorption rate of medium relative molecular weight substances, such as VB 12 , etc. improve.

本发明的具有中空形态结构的活性炭纤维,比实心的活性炭纤维具备更多优点,是一种对小分子物质和中分子物质均具有高吸附性能,适用范围广、成型性好、净化效果好的高吸附性中空形态结构的活性炭纤维。而且是一种工艺简单的制备方法。The activated carbon fiber with a hollow shape structure of the present invention has more advantages than the solid activated carbon fiber. It is a kind of high adsorption performance for small molecular substances and medium molecular substances, wide application range, good formability and good purification effect. Activated carbon fibers with highly absorbent hollow morphology. Moreover, it is a preparation method with simple process.

附图说明Description of drawings

图1是一种具有中空形态结构的活性炭纤维的中孔和大孔孔径分布;Fig. 1 is a kind of mesopore and macropore pore size distribution of activated carbon fiber with hollow morphology structure;

图2是具有中空形态结构的活性炭纤维的吸附等温线;Fig. 2 is the adsorption isotherm of the activated carbon fiber with hollow morphology structure;

图3是具有中空形态结构的活性炭纤维的不同样品的中孔和大孔的孔径分布图。Figure 3 is a diagram of the pore size distribution of mesopores and macropores of different samples of activated carbon fibers with hollow morphology.

附图中,图1的横坐标是相对压力,纵坐标是吸附孔容;图2的横坐标是孔径,纵坐标是递增孔容;图3的横坐标是孔径,纵坐标是递增孔容。In the accompanying drawings, the abscissa of Fig. 1 is the relative pressure, and the ordinate is the adsorption pore volume; the abscissa of Fig. 2 is the pore diameter, and the ordinate is the incremental pore volume; the abscissa of Fig. 3 is the pore diameter, and the ordinate is the incremental pore volume.

具体实施方式Detailed ways

通过以下实施例将有助于理解本发明,但并不限制本发明的内容。The following examples will help to understand the present invention, but do not limit the content of the present invention.

实施例1Example 1

取聚丙烯腈中空纤维原料1.5g在室温下放入浓度为4%重量(wt)的(NH4)2HPO4水溶液中浸泡30分钟,待在空气中自然晾干后,放入烘箱中,在空气中,230℃,加热2小时,预氧化结束;然后将预氧化纤维放入管式炉内的石英管中,在氮气保护下加热到900℃,在900℃加热70分钟,炭化结束;接着将炉温自然降至800℃,通入CO2气体,在800℃加热40分钟,活化结束,关闭CO2气体,用真空泵抽去石英管中的CO2气体,再通入氮气,当石英管内的氮气压力为1个大气压时,封堵石英管两端,关闭氮气,直至石英管内温度降至室温时,取出中空纤维,即为成品-具有中空形态的活性炭纤维。Take 1.5 g of polyacrylonitrile hollow fiber raw material, put it into (NH 4 ) 2 HPO 4 aqueous solution with a concentration of 4% by weight (wt) and soak it for 30 minutes at room temperature, and put it into an oven after being dried naturally in the air. In the air, heat at 230°C for 2 hours, and the pre-oxidation is completed; then put the pre-oxidized fiber into the quartz tube in the tube furnace, heat to 900°C under the protection of nitrogen, and heat at 900°C for 70 minutes, and the carbonization is completed; Then lower the furnace temperature naturally to 800°C, introduce CO 2 gas, and heat at 800°C for 40 minutes. After the activation is completed, turn off the CO 2 gas, use a vacuum pump to remove the CO 2 gas in the quartz tube, and then inject nitrogen gas. When the nitrogen pressure in the tube is 1 atmosphere, seal both ends of the quartz tube and turn off the nitrogen until the temperature in the quartz tube drops to room temperature, then take out the hollow fiber, which is the finished product—activated carbon fiber with a hollow shape.

实施例2Example 2

上述活性炭纤维对小分子物质(肌酐)和中分子物质(VB12)的吸附率如下表所示:在37℃,肌酐和VB12的水溶液中静态吸附24小时。The adsorption rate of above-mentioned activated carbon fiber to small molecular substance (creatinine) and medium molecular substance (VB 12 ) is shown in the following table: Static adsorption in aqueous solution of creatinine and VB 12 at 37°C for 24 hours.

    名称 name     肌酐 creatinine     VB12 VB 12     吸附率(%) Adsorption rate(%)     99 99     84 84

实施例3Example 3

上述活性炭纤维的BET比表面积和中孔比表面积分别为The BET specific surface area and mesopore specific surface area of the above activated carbon fiber are respectively

BET比表面积(m2·g-1)BET specific surface area (m 2 ·g -1 ) 中孔比表面积(m2·g-1)Mesopore specific surface area (m 2 ·g -1 )     样品 sample 1422 1422 1234 1234

实施例4Example 4

上述活性炭纤维的吸附等温线如图1所示。中孔和大孔孔径分布如图2所示。The adsorption isotherms of the above-mentioned activated carbon fibers are shown in Fig. 1. The pore size distribution of mesopores and macropores is shown in Fig. 2.

上述数据的测试是使用美国麦克公司自动吸附仪Tristar 3000采用多点法,以氮气为吸附质子液氮温度(77K)下进行吸附,由测得到吸附等温线采用BET法计算总表面积,由t法(B.C.Lippens等人,J.Cat.,4,319,1985)计算中孔比表面积,由BJH法(E.P.Barrett等人,J.Amer.Chem.Soc.,73,373,1951)计算中孔和大孔孔径分布。The test of the above data is to use the automatic adsorption instrument Tristar 3000 of the American Mike Company to adopt the multi-point method, and use nitrogen as the adsorption proton to carry out the adsorption at the liquid nitrogen temperature (77K). The adsorption isotherm obtained from the measurement is calculated by the BET method. (B.C.Lippens et al., J.Cat., 4,319,1985) calculates mesopore specific surface area, calculates mesopore by BJH method (E.P.Barrett et al., J.Amer.Chem.Soc., 73,373,1951) and macropore size distribution.

实施例5Example 5

取聚丙烯腈中空纤维原料1.5g在室温下放入浓度为4wt%的(NH4)2HP04水溶液中浸泡30分钟,待在空气中自然晾干后,放入烘箱中,在空气中,230℃,加热2小时,预氧化结束;然后将预氧化纤维放入管式炉内的石英管中,在氮气保护下加热到900℃,在900℃加热30分钟,炭化结束;接着将炉温自然降至800℃,通入CO2气体,在800℃加热40分钟,活化结束,关闭CO2气体,用真空泵抽去石英管中的CO2气体,再通入氮气,当石英管内的氮气压力为1个大气压时,封堵石英管两端,关闭氮气,直至石英管内温度降至室温时,取出中空纤维,即为成品-具有中空形态的活性炭纤维,为样品A。Take 1.5g of polyacrylonitrile hollow fiber raw material and put it into a 4wt% (NH 4 ) 2 HP0 4 aqueous solution at room temperature and soak for 30 minutes. After drying naturally in the air, put it in an oven. 230°C, heated for 2 hours, the pre-oxidation was completed; then put the pre-oxidized fiber into the quartz tube in the tube furnace, heated to 900°C under the protection of nitrogen, and heated at 900°C for 30 minutes, the carbonization was completed; then the furnace temperature Naturally lower to 800°C, introduce CO2 gas, heat at 800°C for 40 minutes, after the activation is completed, turn off the CO2 gas, use a vacuum pump to remove the CO2 gas in the quartz tube, and then inject nitrogen gas, when the nitrogen pressure in the quartz tube When the pressure is 1 atmosphere, seal both ends of the quartz tube, turn off the nitrogen gas, and when the temperature in the quartz tube drops to room temperature, take out the hollow fiber, which is the finished product—activated carbon fiber with a hollow shape, which is sample A.

实施例6Example 6

将实施例5的原料1.5g在室温下放入浓度为4wt%的(NH4)H2PO4水溶液中浸泡30分钟,待在空气中自然晾干。预氧化、炭化、活化方法同实施例5,得样品B。1.5 g of the raw material of Example 5 was soaked in 4wt% (NH 4 )H 2 PO 4 aqueous solution at room temperature for 30 minutes, and allowed to dry naturally in the air. Preoxidation, carbonization, and activation methods were the same as in Example 5 to obtain sample B.

实施例7:Embodiment 7:

将实施例5的原料1.5g在室温下放入浓度为4wt%的(NH4)3PO4水溶液中浸泡30分钟,待在空气中自然晾干。预氧化、炭化、活化方法同实施例5,得样品C。1.5 g of the raw material of Example 5 was soaked in a 4 wt % (NH 4 ) 3 PO 4 aqueous solution at room temperature for 30 minutes, and allowed to dry naturally in the air. Preoxidation, carbonization, and activation methods were the same as in Example 5 to obtain sample C.

实施例8Example 8

将实施例5的原料1.5g在室温下放入浓度为4wt%的H3PO4水溶液中浸泡30分钟,待在空气中自然晾干。预氧化、炭化、活化方法同实施例5,得样品D。1.5 g of the raw material of Example 5 was soaked in a 4 wt % H 3 PO 4 aqueous solution at room temperature for 30 minutes, and allowed to dry naturally in the air. Preoxidation, carbonization, and activation methods were the same as in Example 5 to obtain sample D.

实施例9Example 9

将实施例5的原料1.5g在室温下放入浓度为4wt%的HPO3水溶液中浸泡30分钟,在空气中自然晾干。预氧化、炭化、活化方法同实施例5,得样品E。1.5 g of the raw material of Example 5 was put into a 4 wt % HPO aqueous solution at room temperature and soaked for 30 minutes, and then dried naturally in the air. Preoxidation, carbonization, and activation methods were the same as in Example 5 to obtain sample E.

图3为A、B、C、D、E样品的中孔和大孔的孔径分布图。Figure 3 is the pore size distribution diagram of the mesopores and macropores of A, B, C, D, E samples.

下面表内列出的是A、B、C、D、E样品的产率、收缩率、BET比表面积、中孔比表面积、对肌酐和VB12的吸附率Listed in the table below is the yield, shrinkage rate, BET specific surface area, mesopore specific surface area, adsorption rate of creatinine and VB 12 of samples A, B, C, D, and E

上述数据的测试是使用美国麦克公司自动吸附仪Tristar 3000采用多点法,以氮气为吸附质子液氮温度(77K)下进行吸附,由测得到吸附等温线采用BET法计算总表面积,由t法(B.C.Lippens等人,J.Cat.,4,319,1985)计算中孔比表面积,由BJH法(E.P.Barrett等人,J.Amer.Chem.Soc.,73,373,1951)计算中孔和大孔孔径分布。The test of the above data is to use the automatic adsorption instrument Tristar 3000 of the American Mike Company to adopt the multi-point method, and use nitrogen as the adsorption proton to carry out the adsorption at the liquid nitrogen temperature (77K). The adsorption isotherm obtained from the measurement is calculated by the BET method. (B.C.Lippens et al., J.Cat., 4,319,1985) calculates mesopore specific surface area, calculates mesopore by BJH method (E.P.Barrett et al., J.Amer.Chem.Soc., 73,373,1951) and macropore size distribution.

样品 sample     A A     B B     C C     D D     E E 产率/% Yield/%     39.6 39.6     40.3 40.3     40 40     45.2 45.2     42.5 42.5 收缩率/% Shrinkage/%     52.0 52.0     49.3 49.3     49.3 49.3     49.3 49.3     49.3 49.3 BET比表面积/m2·g-1 BET specific surface area/m 2 ·g -1     766 766     659 659     705 705     451 451     428 428 中孔比表面积/m2·g-1 Mesopore specific surface area/m 2 ·g -1     174 174     104 104     93 93     71 71     75 75 对肌酐的吸附率/% Adsorption rate to creatinine/%     93.8 93.8     97.3 97.3     89.5 89.5     89.5 89.5     97.6 97.6 对VB12的吸附率/%Adsorption rate to VB 12 /%     97.7 97.7     93.4 93.4     94.3 94.3     94.7 94.7     97.2 97.2

Claims (5)

1.一种具有中空形态结构的活性炭纤维,其特征是主要由孔径分布主要为2~5nm的中空形态结构的活性炭纤维。1. An activated carbon fiber with a hollow morphological structure, characterized in that it is mainly an activated carbon fiber with a hollow morphological structure of 2 to 5 nm in pore size distribution. 2.如权利要求1所述的一种具有中空形态结构的活性炭纤维的制备方法,其特征是将清洗和干燥过的医用级聚丙烯腈中空纤维用浓度为2-10%重量的磷化物水溶液浸泡10-120分钟进行预处理、晾干;再在200-300℃下保持0.5-6小时对中空纤维进行预氧化;将预处理和预氧化过的中空纤维在氮气保护下进行炭化处理,以10℃/分的升温速率加热,炭化温度为500-1000℃时炭化10-110分钟;炭化后的中空纤维继续在600-1000℃条件下通CO2气体进行活化处理20-100分钟。2. a kind of preparation method with the activated carbon fiber of hollow form structure as claimed in claim 1, it is characterized in that the phosphide aqueous solution of 2-10% weight with the medical grade polyacrylonitrile hollow fiber that cleans and dries Soak for 10-120 minutes to pre-treat and dry; then keep at 200-300°C for 0.5-6 hours to pre-oxidize the hollow fiber; carbonize the pre-treated and pre-oxidized hollow fiber under nitrogen protection to Heating at a heating rate of 10°C/min, and carbonization for 10-110 minutes at a carbonization temperature of 500-1000°C; the carbonized hollow fiber continues to be activated with CO 2 gas at 600-1000°C for 20-100 minutes. 3.如权利要求2所述的方法,其特征是所述的磷化物是磷酸铵、磷酸二氢铵,磷酸氢二铵、磷酸或偏磷酸。3. The method according to claim 2, characterized in that said phosphide is ammonium phosphate, ammonium dihydrogen phosphate, diammonium hydrogen phosphate, phosphoric acid or metaphosphoric acid. 4.如权利要求2所述的方法,其特征是所述的进行活化处理后的中空形态的活性炭纤维在氮气保护下使反应器降至室温和常压。4. The method according to claim 2, characterized in that the activated carbon fibers in the hollow form after the activation treatment make the reactor down to room temperature and normal pressure under nitrogen protection. 5.如权利要2所述的方法,其特征是所述的清洗过聚丙烯腈中空纤维是指在蒸馏水中浸泡1~3天,不断换水,然后干燥过的聚丙烯腈中空纤维。5. The method according to claim 2, characterized in that the cleaned polyacrylonitrile hollow fiber refers to the polyacrylonitrile hollow fiber soaked in distilled water for 1 to 3 days, changing the water continuously, and then dried.
CNB2005100305458A 2005-10-14 2005-10-14 Active carbon fiber in hollow morphological structure, and preparation method Expired - Fee Related CN1328425C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2005100305458A CN1328425C (en) 2005-10-14 2005-10-14 Active carbon fiber in hollow morphological structure, and preparation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2005100305458A CN1328425C (en) 2005-10-14 2005-10-14 Active carbon fiber in hollow morphological structure, and preparation method

Publications (2)

Publication Number Publication Date
CN1760414A CN1760414A (en) 2006-04-19
CN1328425C true CN1328425C (en) 2007-07-25

Family

ID=36706631

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2005100305458A Expired - Fee Related CN1328425C (en) 2005-10-14 2005-10-14 Active carbon fiber in hollow morphological structure, and preparation method

Country Status (1)

Country Link
CN (1) CN1328425C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7934284B2 (en) 2003-02-11 2011-05-03 Braun Gmbh Toothbrushes
US7941886B2 (en) 2003-09-19 2011-05-17 Braun Gmbh Toothbrushes

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8313723B2 (en) 2005-08-25 2012-11-20 Nanocarbons Llc Activated carbon fibers, methods of their preparation, and devices comprising activated carbon fibers
US20070178310A1 (en) 2006-01-31 2007-08-02 Rudyard Istvan Non-woven fibrous materials and electrodes therefrom
US8709972B2 (en) 2007-02-14 2014-04-29 Nanocarbons Llc Methods of forming activated carbons
CA2820810C (en) * 2009-06-10 2014-01-28 Mitsubishi Rayon Co., Ltd. Acrylonitrile swollen fiber for carbon fiber, precursor fiber bundle, stabilized fiber bundle, carbon fiber bundle and production methods thereof
CN102162154B (en) * 2011-03-10 2012-08-15 江苏国正新材料科技有限公司 Method for preparing super-energy battery active electrical carbon hollow fibers
US9096955B2 (en) * 2011-09-30 2015-08-04 Ut-Battelle, Llc Method for the preparation of carbon fiber from polyolefin fiber precursor, and carbon fibers made thereby
CN103093973B (en) * 2013-02-07 2015-08-12 北京化工大学 The preparation method of super capacitor material
CN104549167B (en) * 2014-12-01 2016-09-28 浙江理工大学 A kind of titanium dioxide/cellulosic fibrous substrates absorbent charcoal composite material and preparation method thereof
CN107385559A (en) * 2017-08-11 2017-11-24 南通金康弘纺织品有限公司 A kind of preparation method of NACF
CN109537106B (en) * 2018-11-09 2021-05-18 中国科学院山西煤炭化学研究所 Method for preparing precursor fiber, pre-oxidized fiber or carbon fiber of carbon fiber with special-shaped section by high-speed dry jet spinning
CN109887760A (en) * 2019-02-27 2019-06-14 清华大学 A kind of high conductivity activated carbon and its preparation and use
CN111172627B (en) * 2020-01-14 2022-09-27 安徽工程大学 A kind of hollow structure biomass activated carbon fiber and preparation method thereof
CN112553711A (en) * 2020-12-15 2021-03-26 中南大学 Rapid preoxidation method for polyacrylonitrile fiber precursor

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6426723A (en) * 1987-07-17 1989-01-30 Mitsubishi Rayon Co Finely porous hollow carbon membrane fiber and production thereof
JPH0398624A (en) * 1989-09-11 1991-04-24 Mitsubishi Rayon Co Ltd Carbon fiber-based porous hollow fiber membrane and its preparation
US5089135A (en) * 1988-01-20 1992-02-18 Mitsubishi Rayon Co., Ltd. Carbon based porous hollow fiber membrane and method for producing same
JP3098624B2 (en) * 1992-08-27 2000-10-16 株式会社日立製作所 Liquid crystal display

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6426723A (en) * 1987-07-17 1989-01-30 Mitsubishi Rayon Co Finely porous hollow carbon membrane fiber and production thereof
US5089135A (en) * 1988-01-20 1992-02-18 Mitsubishi Rayon Co., Ltd. Carbon based porous hollow fiber membrane and method for producing same
JPH0398624A (en) * 1989-09-11 1991-04-24 Mitsubishi Rayon Co Ltd Carbon fiber-based porous hollow fiber membrane and its preparation
JP3098624B2 (en) * 1992-08-27 2000-10-16 株式会社日立製作所 Liquid crystal display

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7934284B2 (en) 2003-02-11 2011-05-03 Braun Gmbh Toothbrushes
US8695149B2 (en) 2003-02-11 2014-04-15 Braun Gmbh Toothbrushes
US7941886B2 (en) 2003-09-19 2011-05-17 Braun Gmbh Toothbrushes

Also Published As

Publication number Publication date
CN1760414A (en) 2006-04-19

Similar Documents

Publication Publication Date Title
CN1328425C (en) Active carbon fiber in hollow morphological structure, and preparation method
Zhang et al. Activated carbon adsorbents with micro-mesoporous structure derived from waste biomass by stepwise activation for toluene removal from air
CN104016343B (en) Preparation method of microporous bamboo fiber-based activated carbon fiber with high specific surface area
Pan et al. Facile fabrication of porous carbon nanofibers by electrospun PAN/dimethyl sulfone for capacitive deionization
CN100387762C (en) A kind of polyacrylonitrile-based mesoporous-macroporous ultrafine carbon fiber and preparation method thereof
CN105603584B (en) Mesoporous activated carbon fiber of electrode of super capacitor polyacrylonitrile and preparation method thereof
CN102505187B (en) Hierarchical porosity carbon fiber material, preparation method and application thereof
KR100485603B1 (en) Preparation of activated carbon fibers using nano fibers
KR101756223B1 (en) Method of preparing porous carbon
CN104071770B (en) A kind of method utilizing waste and old cotton textiles to prepare porous Functional Carbon Fiber bunch
Bai et al. Surface oxidation of activated electrospun carbon nanofibers and their adsorption performance for benzene, butanone and ethanol
CN103252214B (en) Activated carbon fibers, hierarchical porous Ni-Ni3P/activated carbon fiber composites and their preparation and application
CN109576824A (en) A kind of preparation method of polyacrylonitrile-radical hollow mesoporous carbon fiber
CN108385209A (en) The preparation method of porous filamentous nanocarbon
JP2014034500A (en) Activated carbon imparted with basic functional group, and method for producing the same
CN1282778C (en) Process for preparing big aperture active carbon fibers
JPH03501509A (en) Improvement of fibrous activated carbon
CN112973625A (en) Lignin-based carbon nanotube and preparation method and application thereof
Bai et al. Ultrafine hierarchically porous carbon fibers and their adsorption performance for ethanol and acetone
CN107055503B (en) A kind of production method of Mesoporous Carbon Materials
JP7229788B2 (en) activated carbon fiber material
Bhati et al. Study on effect of chemical impregnation on the surface and porous characteristics of activated carbon fabric prepared from viscose rayon
CN100382887C (en) A kind of preparation method of activated carbon fiber adsorption material
CN109659152A (en) A kind of three-dimensional micro charcoal-aero gel/ruthenium-oxide combination electrode material and preparation method for supercapacitor
US20240002234A1 (en) Method for preparing porous carbon structure having increased surface area and total pore volume, and porous carbon structure prepared using same

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070725

Termination date: 20101014