[go: up one dir, main page]

CN107398268A - A kind of preparation method of manganese oxide carbon nano-fiber catalytic membrane - Google Patents

A kind of preparation method of manganese oxide carbon nano-fiber catalytic membrane Download PDF

Info

Publication number
CN107398268A
CN107398268A CN201710590436.4A CN201710590436A CN107398268A CN 107398268 A CN107398268 A CN 107398268A CN 201710590436 A CN201710590436 A CN 201710590436A CN 107398268 A CN107398268 A CN 107398268A
Authority
CN
China
Prior art keywords
preparation
membrane
manganese oxide
temperature
carbon nano
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.)
Pending
Application number
CN201710590436.4A
Other languages
Chinese (zh)
Inventor
王军
丁邮
张勇
侯得印
曹爱新
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.)
Research Center for Eco Environmental Sciences of CAS
Original Assignee
Research Center for Eco Environmental Sciences of CAS
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 Research Center for Eco Environmental Sciences of CAS filed Critical Research Center for Eco Environmental Sciences of CAS
Priority to CN201710590436.4A priority Critical patent/CN107398268A/en
Publication of CN107398268A publication Critical patent/CN107398268A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/32Manganese, technetium or rhenium
    • B01J23/34Manganese
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/20Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
    • B01J35/23Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/50Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/58Fabrics or filaments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment
    • B01J37/082Decomposition and pyrolysis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/34Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
    • B01J37/341Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation
    • B01J37/342Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation making use of electric or magnetic fields, wave energy or particle radiation of electric, magnetic or electromagnetic fields, e.g. for magnetic separation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/34Organic compounds containing oxygen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/34Organic compounds containing oxygen
    • C02F2101/345Phenols
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/36Organic compounds containing halogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/38Organic compounds containing nitrogen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Water Supply & Treatment (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Electromagnetism (AREA)
  • Optics & Photonics (AREA)
  • Health & Medical Sciences (AREA)
  • Plasma & Fusion (AREA)
  • Toxicology (AREA)
  • Thermal Sciences (AREA)
  • Catalysts (AREA)

Abstract

一种氧化锰/碳纳米纤维复合催化膜的制备方法,包括以下步骤:A、铸膜液配备:通过8wt%~15wt%聚合物、85wt%~92wt%有机溶剂混合,常温下充分搅拌,得到均匀聚合物铸膜液;连续搅拌的过程中,加入不同质量的四水合醋酸锰,充分搅拌得到暗红均质铸膜液,脱泡备用;B、纤维膜纺制:向静电纺丝推进器注入铸膜液,液滴在高压电场的作用下,喷射成丝,形成Mn(oAc)2/聚合物纳米纤维复合膜;C、复合膜炭化:纤维复合膜在空气中进行预氧化,后进入有惰性气体保护介质中高温炭化,形成氧化锰/碳纳米纤维复合催化膜。

A method for preparing a manganese oxide/carbon nanofiber composite catalytic membrane, comprising the following steps: A, preparation of casting solution: mixing 8wt% to 15wt% polymer and 85wt% to 92wt% organic solvent, fully stirring at normal temperature, to obtain Uniform polymer casting solution; during continuous stirring, add manganese acetate tetrahydrate of different quality, fully stir to obtain dark red homogeneous casting solution, degassing for later use; B, fiber film spinning: to the electrospinning propeller Inject the casting solution, and the droplets are sprayed into filaments under the action of a high-voltage electric field to form a Mn(oAc) 2 /polymer nanofiber composite film; C, carbonization of the composite film: the fiber composite film is pre-oxidized in the air, and then enters High-temperature carbonization in an inert gas-protected medium to form a manganese oxide/carbon nanofiber composite catalytic membrane.

Description

一种氧化锰碳纳米纤维复合催化膜的制备方法A kind of preparation method of manganese oxide carbon nanofiber composite catalytic membrane

技术领域technical field

本发明涉及催化臭氧氧化领域,具体涉及一种氧化锰碳纳米纤维复合催化膜的制备方法。The invention relates to the field of catalytic ozone oxidation, in particular to a method for preparing a manganese oxide carbon nanofiber composite catalytic membrane.

背景技术Background technique

随着环境问题及水资源问题的日益突出,废水排放的严峻性日益凸显,且大部分废水成分复杂,对环境、人体健康和生态都造成了不同程度的危害。一些难降解有机物,存在可生化性差的特点,传统的生物化学处理很难将其完全矿化降解,而高级氧化法(Advanced Oxidation Process,AOPs)可将其直接矿化或通过氧化提高污染物的可生化性。实验研究表明,高级氧化法能够将大部分难降解有机物完全矿化,具有很好的应用前景。With the increasingly prominent environmental problems and water resource problems, the severity of wastewater discharge has become increasingly prominent, and most of the wastewater has complex components, which have caused varying degrees of harm to the environment, human health and ecology. Some refractory organics have the characteristics of poor biodegradability. Traditional biochemical treatment is difficult to completely mineralize and degrade them. Advanced Oxidation Process (AOPs) can directly mineralize them or increase the concentration of pollutants through oxidation. Biodegradability. Experimental studies have shown that the advanced oxidation method can completely mineralize most of the refractory organic matter, and has a good application prospect.

以臭氧为氧化剂的高级氧化法具有氧化能力强,应用范围广,反应速率快等优势,在废水处理中有很好的应用潜力。但是EL-Din等(EL-Din M G,Smith D W.Ozonation ofkraft pulp mill efluents:process dynamics[J].J Environ Eng Sci,2002,1(1):45-57.)研究表明,单独使用臭氧对有机物进行矿化的经济效益很低,存在着利用率低,处理成本高等问题。臭氧催化氧化是近些年来运用较为广泛的一种高级氧化技术,它可以实现在常温常压下对难降解的有机化合物进行矿化,且臭氧利用率高,选择性好等弥补了单独臭氧氧化的短处。催化臭氧化技术是将臭氧与具有吸附和氧化性质的金属氧化物结合起来,在常态条件下将难降解的有机物降解为二氧化碳、水和小分子物质,且无需紫外光、高温和高压的反应条件。The advanced oxidation method using ozone as the oxidant has the advantages of strong oxidation ability, wide application range, fast reaction rate, etc., and has good application potential in wastewater treatment. But EL-Din et al. (EL-Din M G, Smith D W. Ozonation of kraft pulp mill efluents: process dynamics [J]. J Environ Eng Sci, 2002, 1(1): 45-57.) research shows that the use of ozone alone The economic benefits of mineralizing organic matter are very low, and there are problems such as low utilization rate and high processing cost. Ozone catalytic oxidation is an advanced oxidation technology that has been widely used in recent years. It can realize the mineralization of refractory organic compounds at normal temperature and pressure, and has high ozone utilization rate and good selectivity, which makes up for the single ozone oxidation. shortcomings. Catalytic ozonation technology combines ozone with metal oxides with adsorption and oxidation properties to degrade refractory organic substances into carbon dioxide, water and small molecular substances under normal conditions, without the need for ultraviolet light, high temperature and high pressure reaction conditions .

纳米材料由于其独特的结构特点,具有量子尺寸效应、小尺寸效应、界面或表面效应及宏观量子隧道效应,使其在光电器件、传感器、催化剂、功能复合材料等领域发挥重要作用。金属氧化物纳米材料被广泛应用于制作催化剂、半导体材料、磁性材料、荧光材料等等。在实际应用中,将金属氧化物负载在比表面积较大的载体上,能够很好的解决纳米粉体易团聚,难回收的缺点,同时也可以增加其稳定性,催化活性以及达到重复利用的性能。Due to their unique structural characteristics, nanomaterials have quantum size effects, small size effects, interface or surface effects, and macroscopic quantum tunneling effects, making them play an important role in the fields of optoelectronic devices, sensors, catalysts, and functional composite materials. Metal oxide nanomaterials are widely used in the production of catalysts, semiconductor materials, magnetic materials, fluorescent materials and so on. In practical applications, loading metal oxides on a carrier with a large specific surface area can well solve the shortcomings of nano-powders that are easy to agglomerate and difficult to recycle, and can also increase its stability, catalytic activity and achieve reuse. performance.

静电纺丝技术通过高压静电场的作用下使熔融状态的聚合物或聚合物溶液形成纤维的过程。在高压静电场中,带有电荷的熔融状态高分子或高分子溶液经过喷射、拉伸、劈裂、溶剂挥发或固化,最终形成纤维状物质。Electrospinning technology is a process in which molten polymer or polymer solution is formed into fibers under the action of a high-voltage electrostatic field. In the high-voltage electrostatic field, the charged molten polymer or polymer solution undergoes spraying, stretching, splitting, solvent volatilization or solidification, and finally forms a fibrous substance.

氧化锰由于其特殊的物理化学性质,被广泛的运用于催化剂、电化学等各种领域,且其在自然界中存量丰富,价格低廉且无毒。纳米氧化锰的合成方法主要有水热法、液相合成法、前驱体转化法,但合成的纳米材料在实际的催化运用中存在回收困难,重复利用率低等问题,极大的限制了其在废水处理中的应用。Due to its special physical and chemical properties, manganese oxide is widely used in various fields such as catalysts and electrochemistry, and it is abundant in nature, cheap and non-toxic. The synthesis methods of nano-manganese oxide mainly include hydrothermal method, liquid-phase synthesis method, and precursor conversion method, but the synthesis of nano-materials has problems such as difficult recovery and low recycling rate in actual catalytic applications, which greatly limit its use. application in wastewater treatment.

通过静电纺丝的方法,混合了金属氧化物前驱体及聚合物的铸膜液,通过高压静电场的作用制备而成的纳米纤维膜可以很好的解决以上金属氧化物纳米粉体材料的缺陷,并能有较好的催化臭氧氧化效果。且现有的研究中,氧化锰/碳纳米复合纤维膜多用做电化学方向的研究内容,而采用该方法制备复合纤维催化膜却确鲜见报道。Through the method of electrospinning, the nanofibrous membrane prepared by mixing the metal oxide precursor and the polymer casting liquid under the action of a high-voltage electrostatic field can well solve the defects of the above metal oxide nanopowder materials. , and can have a better catalytic effect of ozone oxidation. Moreover, in the existing research, the manganese oxide/carbon nanocomposite fiber membrane is mostly used as the research content of the electrochemical direction, but the preparation of the composite fiber catalytic membrane by this method is rarely reported.

发明内容Contents of the invention

有鉴于此,本发明针对以上的问题,主要的目的是提出一种氧化锰/碳纳米纤维复合催化膜的制备方法,该方法可操作性强,工艺简单,重复利用率高,且易回收。在催化臭氧氧化过程中表现出良好的催化活性及稳定性。In view of this, the present invention aims at the above problems, and the main purpose is to propose a method for preparing a manganese oxide/carbon nanofiber composite catalytic membrane, which has strong operability, simple process, high recycling rate and easy recycling. It shows good catalytic activity and stability in the catalytic ozonation process.

本发明通过以下技术方法来实现以上目的:一种氧化锰/碳纳米纤维复合催化膜的制备方法:The present invention achieves the above object through the following technical methods: a preparation method of manganese oxide/carbon nanofiber composite catalytic membrane:

步骤1:铸膜液的制备Step 1: Preparation of casting solution

将85wt%~92wt%分散有机溶剂,8wt%~15wt%聚合物,加入搅拌罐中充分搅拌,设定常温,得到均匀透明聚合物铸膜液,后在连续搅拌过程中加入不同质量的四水合醋酸锰,充分搅拌得到暗红色均质铸膜液,脱泡备用,所述分散有机溶剂为N,N-二甲基甲酰胺(DMF)、二甲基乙酰胺(DMAC)、二甲基亚砜(DMSO)、二氯甲烷(DCM);Put 85wt%~92wt% dispersed organic solvent, 8wt%~15wt% polymer into the mixing tank and stir well, set the normal temperature to get a uniform transparent polymer casting solution, and then add different quality tetrahydrate during the continuous stirring process Manganese acetate, fully stirred to obtain a dark red homogeneous casting solution, degassing for subsequent use, the dispersed organic solvent is N,N-dimethylformamide (DMF), dimethylacetamide (DMAC), dimethylmethylene Sulfone (DMSO), dichloromethane (DCM);

步骤2:Mn(oAc)2/聚合物纳米纤维复合膜的制备Step 2: Preparation of Mn(oAc) 2 /polymer nanofiber composite membrane

将步骤1制得的铸膜液注入静电纺丝推进器中,液滴在高压电场的作用下,喷射纺丝成膜,干燥后得到Mn(oAc)2/聚合物纳米纤维复合膜;Inject the film casting solution prepared in step 1 into the electrospinning propeller, and the droplets are jet-spun to form a film under the action of a high-voltage electric field, and the Mn(oAc) 2 /polymer nanofiber composite film is obtained after drying;

步骤3:氧化锰/碳纳米纤维复合催化膜的制备Step 3: Preparation of manganese oxide/carbon nanofiber composite catalytic membrane

将上述步骤2中纤维复合膜在空气中进行热稳定处理,后将其在有惰性气体保护的气氛炉中进行炭化,降至室温得到氧化锰/碳纳米复合纤维催化膜。The fiber composite membrane in the above step 2 is thermally stabilized in the air, and then carbonized in an atmosphere furnace protected by an inert gas, and lowered to room temperature to obtain a manganese oxide/carbon nanocomposite fiber catalytic membrane.

进一步,步骤1所述聚合物为聚丙烯腈(PAN)、N-乙烯基-2-吡咯烷酮(PVP)、聚偏氟乙烯(PVDF)或聚甲基丙烯酸甲酯(PMMA)。Further, the polymer described in step 1 is polyacrylonitrile (PAN), N-vinyl-2-pyrrolidone (PVP), polyvinylidene fluoride (PVDF) or polymethyl methacrylate (PMMA).

进一步,步骤1所述四水合醋酸锰添加量为10wt%、20wt%、30wt%、40wt%、50wt%聚合物添加量。Further, the addition amount of manganese acetate tetrahydrate described in step 1 is 10wt%, 20wt%, 30wt%, 40wt%, 50wt% polymer addition.

进一步,步骤2所述静电纺丝条件为:纺丝电压16kv~20kv,喷丝头和负极接收器之前距离15cm,纺丝液推进速率0.6~2.0ml/min,纺丝温度30℃,复合膜的干燥条件50℃条件下干燥12h。Further, the electrospinning conditions in step 2 are as follows: spinning voltage 16kv-20kv, distance between the spinneret and the negative electrode receiver 15cm, spinning solution propulsion rate 0.6-2.0ml/min, spinning temperature 30°C, composite membrane The drying conditions were 12 hours at 50°C.

进一步,步骤3所述热稳定又称预氧化处理,在200~300℃的空气中,保持该温度下退火2h,使其转换为热稳定态,处理过程中采用氧化铝高温夹板使纳米纤维膜定型。Further, the heat stabilization described in step 3 is also called pre-oxidation treatment. In the air at 200-300°C, anneal at this temperature for 2 hours to convert it into a heat-stable state. During the process, aluminum oxide high-temperature splints are used to make the nanofiber film stereotyped.

进一步,步骤3所述炭化过程为复合膜在高纯氮气N2、Ar或He在内的惰性气体气氛条件下加热,于800℃温度下持续加热1h使纳米纤维膜炭化,处理过程中使用氧化铝高温夹板使其定型。Further, the carbonization process described in step 3 is to heat the composite membrane under an inert gas atmosphere including high-purity nitrogen N 2 , Ar or He, and continue heating at 800°C for 1 hour to carbonize the nanofiber membrane. Aluminum high temperature splints give it shape.

进一步,步骤3所述预氧化升温过程为程序升温,程序升温速率为5℃/min。步骤三所述炭化升温为程序升温,升温速率3℃/min。Further, the pre-oxidation heating process described in step 3 is a programmed temperature increase, and the programmed temperature increase rate is 5° C./min. The carbonization temperature increase in step 3 is a programmed temperature increase, and the temperature increase rate is 3°C/min.

如上述方法制备的氧化锰/碳纳米纤维复合催化膜用了催化臭氧氧化降解难降解有机物的用途。The manganese oxide/carbon nanofiber composite catalytic membrane prepared by the above method is used to catalyze the oxidation and degradation of refractory organic matter by ozone.

本发明的有益效果是:The beneficial effects of the present invention are:

本发明采用静电纺丝的方法制备氧化锰/碳纳米复合纤维催化膜的方法,操作简单,可控性强,可根据实际需求控制催化剂的负载量。复合膜微观结构呈现由纳米纤维交织而成的纳米网状结构,烧结而成的纳米氧化锰颗粒分布于碳纳米纤维表面,实现高比表面积,孔径分布均匀等优势。在实际的催化臭氧氧化实验中,该复合膜呈现出卓越的催化臭氧氧化效果,提高了臭氧利用率,且重复性高,稳定性强。The invention adopts the electrospinning method to prepare the manganese oxide/carbon nanometer composite fiber catalytic membrane, which is simple in operation and strong in controllability, and can control the loading capacity of the catalyst according to the actual requirement. The microstructure of the composite membrane presents a nano-network structure interwoven by nanofibers, and the sintered nano-manganese oxide particles are distributed on the surface of carbon nanofibers, achieving high specific surface area and uniform pore size distribution. In the actual catalytic ozone oxidation experiment, the composite membrane showed excellent catalytic ozone oxidation effect, improved ozone utilization rate, high repeatability and strong stability.

附图说明Description of drawings

图1所示为催化臭氧氧化实验流程图。Figure 1 shows the flow chart of the catalytic ozone oxidation experiment.

其中,1氧气罐;2臭氧发生器;3臭氧浓度检测仪;4磁力搅拌系统;5反应玻璃瓶;6尾气吸收装置;7催化剂;8取样口Among them, 1 oxygen tank; 2 ozone generator; 3 ozone concentration detector; 4 magnetic stirring system; 5 reaction glass bottle; 6 tail gas absorption device; 7 catalyst; 8 sampling port

具体实施方式detailed description

下面对本发明作进一步详细说明。The present invention will be described in further detail below.

以下结合附图和实例对本发明的技术方案进行详细描述,所举实例只用于解释本发明,并非用于限定本发明的范围。The technical solutions of the present invention will be described in detail below in conjunction with the accompanying drawings and examples, and the given examples are only used to explain the present invention, and are not intended to limit the scope of the present invention.

实验材料Experimental Materials

实施例1Example 1

一种MnO2/CNF复合催化膜的制备方法:A preparation method of MnO 2 /CNF composite catalytic membrane:

步骤1:铸膜液的配置Step 1: Configuration of casting solution

称取4.8g聚丙烯腈(PAN)分散于55.2g的DMF中,常温下搅拌均匀。后在连续搅拌过程中分别加入10wt%、20wt%、30wt%PAN的四水合醋酸锰,充分搅拌至暗红色均质铸膜液,静置脱泡。Weigh 4.8g of polyacrylonitrile (PAN) and disperse in 55.2g of DMF, and stir evenly at room temperature. Then add 10wt%, 20wt%, 30wt% PAN manganese acetate tetrahydrate respectively in the process of continuous stirring, fully stir until the dark red homogeneous casting solution is left standing for defoaming.

步骤2:Mn(oAc)2/PAN纳米纤维复合膜的制备Step 2: Preparation of Mn(oAc) 2 /PAN nanofiber composite membrane

将步骤1制得的铸膜液注入静电纺丝设备中,纺丝电压16kv,喷丝头和负极接收器之前距离为15cm,纺丝液推挤速率为1.0ml/min,纺丝温度为30℃,通过高压电场的作用,喷射纺丝成膜,50℃干燥后12h得到Mn(oAc)2/PAN-1、Mn(oAc)2/PAN-2、Mn(oAc)2/PAN-3纳米纤维复合膜。Inject the casting solution prepared in step 1 into the electrospinning equipment, the spinning voltage is 16kv, the distance between the spinneret and the negative electrode receiver is 15cm, the spinning solution pushing rate is 1.0ml/min, and the spinning temperature is 30 ℃, through the action of high-voltage electric field, jet spinning to form a film, after drying at 50 ℃ for 12 hours, Mn(oAc) 2 /PAN-1, Mn(oAc) 2 /PAN-2, Mn(oAc) 2 /PAN-3 nano fiber composite membrane.

步骤3:MnO2/CNF复合催化膜的制备Step 3: Preparation of MnO 2 /CNF composite catalytic membrane

将上述步骤2得到的纤维复合膜在空气气氛中进行预氧化,温度按5℃/min速率升温至250℃,保持该温度下退火2h,处理过程中采用氧化铝高温夹板使纳米纤维膜定型。The fiber composite membrane obtained in the above step 2 was pre-oxidized in an air atmosphere, the temperature was raised to 250°C at a rate of 5°C/min, and annealed at this temperature for 2 hours. During the treatment, the nanofiber membrane was shaped by using an alumina high-temperature splint.

进一步在高纯氮气N2、Ar或He保护介质中,以3℃/min升温速率到800℃,并保持该温度1h使纳米纤维膜炭化,处理过程中使用氧化铝高温夹板使其定型。待降至室温后,取出制得MnO2/CNF-1、MnO2/CNF-2、MnO2/CNF-3复合催化膜。Further, in the protective medium of high-purity nitrogen N 2 , Ar or He, the temperature was raised to 800°C at a rate of 3°C/min, and the temperature was maintained for 1 hour to carbonize the nanofibrous membrane. During the treatment, an alumina high-temperature splint was used to shape it. After cooling down to room temperature, take out the prepared MnO 2 /CNF-1, MnO 2 /CNF-2, MnO 2 /CNF-3 composite catalytic membranes.

本实例制得的MnO2/CNF复合催化膜纤维直径为100nm~200nm,MnO2/CNF-1、MnO2/CNF-2、MnO2/CNF-3对草酸臭氧催化氧化降解率分别为49%、53%、57%,相对于直接臭氧氧化的降解率13%有了极大的提升(其中草酸溶液初始浓度为100ppm,臭氧投加量为50mg/L、50ml/min,反应时间为60min,催化剂投加量为0.5g/L)。The diameter of the MnO 2 /CNF composite catalytic membrane fiber prepared in this example is 100nm-200nm, and the catalytic oxidation degradation rates of MnO 2 /CNF-1, MnO 2 /CNF-2, and MnO 2 /CNF-3 to oxalic acid are 49% respectively . Catalyst dosage is 0.5g/L).

实施例2Example 2

铸膜液配制,将4.8g聚丙烯腈(PAN)、55.2g DMF加入搅拌罐中混合充分搅拌,设定温度为20℃,搅拌6h得到均匀聚合物铸膜液。在连续搅拌的聚合物铸膜液中加入30wt%PAN的四水合醋酸锰,设定温度为20℃,搅拌4h得到均质暗红透明铸膜液,静置脱泡。The casting solution was prepared by adding 4.8g of polyacrylonitrile (PAN) and 55.2g of DMF into a stirring tank, mixing and stirring thoroughly, setting the temperature at 20°C, and stirring for 6 hours to obtain a uniform polymer casting solution. Add 30wt% PAN manganese acetate tetrahydrate to the continuously stirred polymer casting solution, set the temperature at 20° C., stir for 4 hours to obtain a homogeneous dark red transparent casting solution, and let stand for defoaming.

纺丝成膜,将步骤1制得的铸膜液注入静电纺丝纺丝推进器中,设定纺丝推进速率0.6ml/min,纺丝电压16kv,喷丝头和负极接收器之前距离为15cm,纺丝温度为30℃,通过高压电场的作用,喷射纺丝成膜,设定烘箱温度50℃,干燥12h得到Mn(oAc)2/PAN纳米纤维复合膜。Spinning to form a film, inject the casting solution prepared in step 1 into the electrospinning spinning propeller, set the spinning propulsion rate to 0.6ml/min, the spinning voltage to 16kv, and the distance between the spinneret and the negative electrode receiver to be 15cm, the spinning temperature is 30°C, through the action of high-voltage electric field, jet spinning to form a film, set the oven temperature to 50°C, and dry for 12h to obtain Mn(oAc) 2 /PAN nanofiber composite film.

膜片炭化,将上述步骤得到的Mn(oAc)2/PAN纤维复合膜在空气气氛中进行预氧化,设定程序升温5℃/min至250℃,250℃温度下退火2h,退火过程采用氧化铝耐高温夹板使纳米纤维膜定型。The membrane is carbonized, and the Mn(oAc) 2 /PAN fiber composite membrane obtained in the above steps is pre-oxidized in an air atmosphere, and the temperature is programmed to rise at 5°C/min to 250°C, and annealed at 250°C for 2 hours. The annealing process uses oxidation The aluminum high temperature resistant splint makes the nanofiber membrane shape.

进一步在高纯氮气N2、Ar或He保护介质中,设定程序升温3℃/min至800℃,800℃保持1h使其炭化,处理过程中使用氧化铝高温夹板使其定型。待降至室温后,取出得到MnO2/CNF复合催化膜。Further, in the protective medium of high-purity nitrogen N2, Ar or He, set the temperature program to rise at 3°C/min to 800°C, and keep at 800°C for 1h to carbonize, and use alumina high-temperature splints to shape it during the treatment. After cooling down to room temperature, the MnO 2 /CNF composite catalytic membrane was obtained.

本实例制得的MnO2/CNF复合催化膜纤维直径为100nm~200nm,将制得的催化膜分别用于催化臭氧氧化草酸、苯酚、硝基苯、氯苯酚四种难降解有机物(其中污染物初始浓度均为100ppm,臭氧投加量为50mg/L、50ml/min,反应时间为60min,催化剂投加量为0.5g/L),各种污染物去除率结果如下表所示:The MnO 2 /CNF composite catalytic membrane fiber diameter that this example makes is 100nm~200nm, and the catalytic membrane that makes is used for catalytic ozone to oxidize oxalic acid, phenol, nitrobenzene, chlorophenol four kinds of refractory organic matter respectively (wherein pollutant The initial concentration is 100ppm, the dosage of ozone is 50mg/L, 50ml/min, the reaction time is 60min, and the dosage of catalyst is 0.5g/L). The results of the removal rates of various pollutants are shown in the following table:

Claims (7)

  1. A kind of 1. preparation method of manganese oxide/carbon nano-fiber catalytic membrane, it is characterised in that:
    Step 1:The preparation of casting solution
    85wt%~92wt% is disperseed into organic solvent, 8wt%~15wt% polymer, adds in agitator tank and is sufficiently stirred, if Permanent temperature, obtain homogeneous transparent polymeric casting film liquid, after during continuously stirring add different quality four hydration manganese acetates, It is sufficiently stirred to obtain kermesinus homogeneous casting solution, deaeration is standby, and the scattered organic solvent is DMF (DMF), dimethyl acetamide (DMAC), dimethyl sulfoxide (DMSO) (DMSO), dichloromethane (DCM);
    Step 2:Mn(oAc)2The preparation of/polymer nanofiber composite membrane
    By made from step 1 casting solution injection electrostatic spinning propeller in, drop in the presence of high voltage electric field, jet spinning into Film, Mn (oAc) is obtained after drying2/ polymer nanofiber composite membrane;
    Step 3:The preparation of manganese oxide/carbon nano-fiber catalytic membrane
    Composite fiber membrane in above-mentioned steps 2 is subjected to heat stabilisation process in atmosphere, after it is being had into the gas of inert gas shielding Carbonized in atmosphere stove, be down to room temperature and obtain manganese oxide/carbon nano-composite fiber catalytic membrane.
  2. 2. the preparation method of manganese oxide according to claim 1/carbon nano-fiber catalytic membrane, it is characterised in that:Step Rapid 1 polymer is polyacrylonitrile (PAN), NVP (PVP), Kynoar (PVDF) or poly- first Base methyl acrylate (PMMA).
  3. 3. the preparation method of manganese oxide according to claim 1/carbon nano-fiber catalytic membrane, it is characterised in that:Step The rapid 1 four hydrations manganese acetate addition is 10wt%, 20wt%, 30wt%, 40wt%, 50wt% polymer addition.
  4. 4. the preparation method of manganese oxide according to claim 1/carbon nano-fiber catalytic membrane, it is characterised in that:Step Rapid 2 electrospinning conditions are:The front distance 15cm of spinning voltage 16kv~20kv, spinning head and negative pole receiver, spinning Liquid promotes 0.6~2.0ml/min of speed, 30 DEG C of spinning temperature, 12h is dried under the conditions of 50 DEG C of the drying condition of composite membrane.
  5. 5. the preparation method of manganese oxide according to claim 1/carbon nano-fiber catalytic membrane, it is characterised in that:Step Rapid 3 thermostabilization is also known as pre-oxidation treatment, in 200~300 DEG C of air, keeps the 2h that anneals at this temperature, makes its conversion For thermostabilization state, nano fibrous membrane is set to shape using alumina high temperature clamping plate in processing procedure.
  6. 6. the preparation method of manganese oxide according to claim 1/carbon nano-fiber catalytic membrane, it is characterised in that:Step Rapid 3 carbonization process is composite membrane in high pure nitrogen N2, heat under the conditions of inert gas atmosphere including Ar or He, in 800 Continuous heating 1h carbonizes nano fibrous membrane at a temperature of DEG C, makes its sizing using alumina high temperature clamping plate in processing procedure.
  7. 7. the preparation method of manganese oxide according to claim 1/carbon nano-fiber catalytic membrane, it is characterised in that:Step The rapid 3 pre-oxidation temperature-rise period is temperature programming, and programmed rate is 5 DEG C/min.Charing heating is journey described in step 3 Sequence heats up, 3 DEG C/min of heating rate.
CN201710590436.4A 2017-07-19 2017-07-19 A kind of preparation method of manganese oxide carbon nano-fiber catalytic membrane Pending CN107398268A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710590436.4A CN107398268A (en) 2017-07-19 2017-07-19 A kind of preparation method of manganese oxide carbon nano-fiber catalytic membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710590436.4A CN107398268A (en) 2017-07-19 2017-07-19 A kind of preparation method of manganese oxide carbon nano-fiber catalytic membrane

Publications (1)

Publication Number Publication Date
CN107398268A true CN107398268A (en) 2017-11-28

Family

ID=60402219

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710590436.4A Pending CN107398268A (en) 2017-07-19 2017-07-19 A kind of preparation method of manganese oxide carbon nano-fiber catalytic membrane

Country Status (1)

Country Link
CN (1) CN107398268A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109004185A (en) * 2018-06-13 2018-12-14 福建翔丰华新能源材料有限公司 Method for preparing independent negative electrode material of flexible lithium ion battery
CN111495213A (en) * 2019-01-30 2020-08-07 宁波方太厨具有限公司 Preparation method of nanofiber filtering membrane
CN111558371A (en) * 2020-04-20 2020-08-21 上海海庭环境工程有限公司 A catalyst preparation method based on a ceramic-based and carbon-based mixture as a carrier and a matching flat plate type ozone oxidation reactor
CN114196979A (en) * 2021-12-13 2022-03-18 中国科学院生态环境研究中心 A method for preparing coated titanium electrode by electrospinning
CN114405546A (en) * 2022-01-27 2022-04-29 郑州大学 Manganese-loaded fiber catalyst for catalytic oxidation of ozone and preparation method and application thereof
CN116332235A (en) * 2022-12-02 2023-06-27 佳木斯大学 MnO (MnO) 2 Preparation method and application of NTs/CNFs

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101385971A (en) * 2007-09-13 2009-03-18 中国科学院生态环境研究中心 Catalyst preparation method for highly efficient catalytic ozonation of organic pollutants in water
EP2204349A1 (en) * 2008-12-26 2010-07-07 Korea Institute of Science and Technology Nano powder, nano ink and micro rod, and the fabrication methods thereof
CN103382623A (en) * 2013-07-19 2013-11-06 浙江理工大学 Electrostatic spinning preparation method of manganese dioxide/polyacrylonitrile (MD/PAN) base oxygenolysis methanal type nanofiber membrane
CN104150881A (en) * 2014-07-30 2014-11-19 东华大学 Flexible manganese oxide nano fibrous membrane and preparation method thereof
CN104882299A (en) * 2015-05-13 2015-09-02 扬州大学 Preparation method of manganic manganous oxide/ carbon matrix composite nanoelectrode material
CN105013504A (en) * 2015-07-20 2015-11-04 华南理工大学 Loaded binary composite metal oxide catalytic ozonation catalyst and preparation method thereof
CN105316798A (en) * 2014-08-05 2016-02-10 无锡华臻新能源科技有限公司 Preparation method of nitrogen-doped mesoporous carbon modified manganese dioxide fibers
CN105926083A (en) * 2016-06-24 2016-09-07 南京国轩电池有限公司 Preparation method for MnO2/C composite fibres
CN106807362A (en) * 2017-02-24 2017-06-09 广州市华绿环保科技有限公司 One kind load manganese dioxide activated-carbon catalyst and preparation method and application

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101385971A (en) * 2007-09-13 2009-03-18 中国科学院生态环境研究中心 Catalyst preparation method for highly efficient catalytic ozonation of organic pollutants in water
EP2204349A1 (en) * 2008-12-26 2010-07-07 Korea Institute of Science and Technology Nano powder, nano ink and micro rod, and the fabrication methods thereof
CN103382623A (en) * 2013-07-19 2013-11-06 浙江理工大学 Electrostatic spinning preparation method of manganese dioxide/polyacrylonitrile (MD/PAN) base oxygenolysis methanal type nanofiber membrane
CN104150881A (en) * 2014-07-30 2014-11-19 东华大学 Flexible manganese oxide nano fibrous membrane and preparation method thereof
CN105316798A (en) * 2014-08-05 2016-02-10 无锡华臻新能源科技有限公司 Preparation method of nitrogen-doped mesoporous carbon modified manganese dioxide fibers
CN104882299A (en) * 2015-05-13 2015-09-02 扬州大学 Preparation method of manganic manganous oxide/ carbon matrix composite nanoelectrode material
CN105013504A (en) * 2015-07-20 2015-11-04 华南理工大学 Loaded binary composite metal oxide catalytic ozonation catalyst and preparation method thereof
CN105926083A (en) * 2016-06-24 2016-09-07 南京国轩电池有限公司 Preparation method for MnO2/C composite fibres
CN106807362A (en) * 2017-02-24 2017-06-09 广州市华绿环保科技有限公司 One kind load manganese dioxide activated-carbon catalyst and preparation method and application

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
潘超等: "静电纺氧化锰复合碳纳米纤维柔性膜的电化学性能", 《高等学校化学学报》 *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109004185A (en) * 2018-06-13 2018-12-14 福建翔丰华新能源材料有限公司 Method for preparing independent negative electrode material of flexible lithium ion battery
CN109004185B (en) * 2018-06-13 2021-12-24 福建翔丰华新能源材料有限公司 Method for preparing independent negative electrode material of flexible lithium ion battery
CN111495213A (en) * 2019-01-30 2020-08-07 宁波方太厨具有限公司 Preparation method of nanofiber filtering membrane
CN111558371A (en) * 2020-04-20 2020-08-21 上海海庭环境工程有限公司 A catalyst preparation method based on a ceramic-based and carbon-based mixture as a carrier and a matching flat plate type ozone oxidation reactor
CN111558371B (en) * 2020-04-20 2023-12-15 上海海庭环境工程有限公司 Preparation method of catalyst based on ceramic base and carbon base mixture as carrier and matched flat-plate ozone oxidation reactor
CN114196979A (en) * 2021-12-13 2022-03-18 中国科学院生态环境研究中心 A method for preparing coated titanium electrode by electrospinning
CN114405546A (en) * 2022-01-27 2022-04-29 郑州大学 Manganese-loaded fiber catalyst for catalytic oxidation of ozone and preparation method and application thereof
CN116332235A (en) * 2022-12-02 2023-06-27 佳木斯大学 MnO (MnO) 2 Preparation method and application of NTs/CNFs

Similar Documents

Publication Publication Date Title
CN107398268A (en) A kind of preparation method of manganese oxide carbon nano-fiber catalytic membrane
CN108842304A (en) A kind of porous support type Static Spinning nano-photo catalytic tunica fibrosa and preparation method thereof
CN108786814B (en) A copper-cobalt bimetal/porous carbon nanofiber composite material and its preparation method and application
WO2016146070A1 (en) Bismuth-titanium oxide nanowire material used for photocatalysis, and preparation method
CN105780198B (en) A kind of preparation method of order mesoporous carbon nano-fiber
CN104772160B (en) A kind of carbonitride photocatalytic activity nano fibrous membrane and preparation method thereof
CN101905121B (en) Preparation method of alumina-based ceramic hollow fiber membrane
CN103451852B (en) A kind of TiO 2the preparation method of nanometer rods/SiC composite fibrofelt
CN103382623A (en) Electrostatic spinning preparation method of manganese dioxide/polyacrylonitrile (MD/PAN) base oxygenolysis methanal type nanofiber membrane
Taha et al. Porous WO 3–carbon nanofibers: high-performance and recyclable visible light photocatalysis
CN105214668A (en) Catalyst based and the blending preparation method of a kind of efficient carbon nanofiber
CN107376888A (en) A kind of flexible titanium oxide/silica/carbon composite nano-fiber film and preparation method thereof
CN106944091A (en) A kind of photochemical catalyst Cu CuO MnO2And its preparation method and application
KR20180028765A (en) Carbon nanofiber composite having three layer structure and method for manufacturing thereof
CN106978652A (en) A kind of preparation method of the sour oxygen titanium precursors colloidal sol spinning solution of poly-vinegar and TiOx nano fiber photocatalyst
CN106964331A (en) A kind of photochemical catalyst/porous carbon fiber composite and its preparation method and application
CN106943890B (en) A kind of attapulgite-graphitic phase carbon nitride composite hollow fiber microfiltration membrane with photocatalytic performance and its preparation method and application
CN114561719B (en) Cerium oxide/silicon oxide composite fiber material with fiber interweaved structure and preparation method and application thereof
CN110327914B (en) A tungsten trioxide/cadmium tungstate nanofiber photocatalytic material and its preparation method and application
CN114950407B (en) Preparation method of a multifunctional flexible photocatalytic film
CN105214738B (en) A kind of nanofiber-based catalyst of efficient carbon and its wet dip preparation method
CN110801809A (en) Preparation method of porous visible light catalytic composite material with high adsorption capacity
CN113289669B (en) Preparation method of beaded carbon nanofiber loaded titanium oxide photocatalyst
CN103320902A (en) Bio-based active carbon fiber filtering material and preparation method thereof
CN106964330B (en) Activated carbon fiber film loads TiO2The preparation method of/ZnO photocatalyst

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20171128