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 PDFInfo
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- 239000012528 membrane Substances 0.000 title claims abstract description 51
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 40
- 239000002134 carbon nanofiber Substances 0.000 title claims abstract description 22
- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- PQQBWLKXIHCGRL-UHFFFAOYSA-N [O-2].[Mn+2].[C+4].[O-2].[O-2] Chemical compound [O-2].[Mn+2].[C+4].[O-2].[O-2] PQQBWLKXIHCGRL-UHFFFAOYSA-N 0.000 title description 2
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 claims abstract description 40
- 239000002131 composite material Substances 0.000 claims abstract description 36
- 238000000034 method Methods 0.000 claims abstract description 24
- 238000005266 casting Methods 0.000 claims abstract description 21
- 229920000642 polymer Polymers 0.000 claims abstract description 21
- 238000009987 spinning Methods 0.000 claims abstract description 19
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000000835 fiber Substances 0.000 claims abstract description 14
- 239000002121 nanofiber Substances 0.000 claims abstract description 13
- 238000003756 stirring Methods 0.000 claims abstract description 13
- 239000011572 manganese Substances 0.000 claims abstract description 11
- 238000001523 electrospinning Methods 0.000 claims abstract description 9
- 238000003763 carbonization Methods 0.000 claims abstract description 5
- 230000005684 electric field Effects 0.000 claims abstract description 5
- 239000003960 organic solvent Substances 0.000 claims abstract description 5
- 230000003647 oxidation Effects 0.000 claims description 20
- 238000007254 oxidation reaction Methods 0.000 claims description 20
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 13
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000011261 inert gas Substances 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 239000002033 PVDF binder Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical class [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 claims description 3
- 239000002114 nanocomposite Substances 0.000 claims description 3
- 229920003229 poly(methyl methacrylate) Polymers 0.000 claims description 3
- 239000004926 polymethyl methacrylate Substances 0.000 claims description 3
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 2
- 229940071125 manganese acetate Drugs 0.000 claims description 2
- 230000006641 stabilisation Effects 0.000 claims description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims 6
- 239000000243 solution Substances 0.000 claims 3
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 claims 2
- 229940113088 dimethylacetamide Drugs 0.000 claims 2
- 230000036571 hydration Effects 0.000 claims 2
- 238000006703 hydration reaction Methods 0.000 claims 2
- 238000010041 electrostatic spinning Methods 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 238000004513 sizing Methods 0.000 claims 1
- 229940082328 manganese acetate tetrahydrate Drugs 0.000 abstract description 4
- CESXSDZNZGSWSP-UHFFFAOYSA-L manganese(2+);diacetate;tetrahydrate Chemical compound O.O.O.O.[Mn+2].CC([O-])=O.CC([O-])=O CESXSDZNZGSWSP-UHFFFAOYSA-L 0.000 abstract description 4
- 238000002156 mixing Methods 0.000 abstract description 4
- 238000007872 degassing Methods 0.000 abstract description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 17
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical group CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 9
- 239000003054 catalyst Substances 0.000 description 7
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 6
- 239000000463 material Substances 0.000 description 4
- 229910044991 metal oxide Inorganic materials 0.000 description 4
- 150000004706 metal oxides Chemical class 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000005686 electrostatic field Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 239000002086 nanomaterial Substances 0.000 description 3
- 238000006385 ozonation reaction Methods 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 description 2
- 238000009303 advanced oxidation process reaction Methods 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000011858 nanopowder Substances 0.000 description 2
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 2
- 235000006408 oxalic acid Nutrition 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 230000005476 size effect Effects 0.000 description 2
- 238000001308 synthesis method Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- AWZRBUVZMPCWDR-UHFFFAOYSA-N 2-sulfonylpropane Chemical compound CC(C)=S(=O)=O AWZRBUVZMPCWDR-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 101710185016 Proteasome-activating nucleotidase 1 Proteins 0.000 description 1
- 101710185022 Proteasome-activating nucleotidase 2 Proteins 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033558 biomineral tissue development Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- 238000003760 magnetic stirring Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012702 metal oxide precursor Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 230000001089 mineralizing effect Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000005693 optoelectronics Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000004540 process dynamic Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 150000004685 tetrahydrates Chemical class 0.000 description 1
- 230000005641 tunneling Effects 0.000 description 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts 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
- B01J23/32—Manganese, technetium or rhenium
- B01J23/34—Manganese
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/20—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
- B01J35/23—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J35/58—Fabrics or filaments
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
- B01J37/082—Decomposition and pyrolysis
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/34—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
- B01J37/341—Irradiation 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
- B01J37/342—Irradiation 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
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
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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
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)
- 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 solution85wt%~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 membraneBy 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 membraneComposite 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. 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. 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. 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. 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. 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. 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.
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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 |
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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 |
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