CN110124683A - Mesoporous NiMn2O4The preparation method of catalyst, the catalyst thus prepared and application thereof - Google Patents
Mesoporous NiMn2O4The preparation method of catalyst, the catalyst thus prepared and application thereof Download PDFInfo
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- CN110124683A CN110124683A CN201910530910.3A CN201910530910A CN110124683A CN 110124683 A CN110124683 A CN 110124683A CN 201910530910 A CN201910530910 A CN 201910530910A CN 110124683 A CN110124683 A CN 110124683A
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- 239000003054 catalyst Substances 0.000 title claims abstract description 30
- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- MYSWGUAQZAJSOK-UHFFFAOYSA-N ciprofloxacin Chemical compound C12=CC(N3CCNCC3)=C(F)C=C2C(=O)C(C(=O)O)=CN1C1CC1 MYSWGUAQZAJSOK-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000000243 solution Substances 0.000 claims abstract description 33
- 229910003289 NiMn Inorganic materials 0.000 claims abstract description 32
- 239000007787 solid Substances 0.000 claims abstract description 28
- 229960003405 ciprofloxacin Drugs 0.000 claims abstract description 25
- 238000003756 stirring Methods 0.000 claims abstract description 16
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 14
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000011259 mixed solution Substances 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 10
- 239000011943 nanocatalyst Substances 0.000 claims abstract description 8
- 239000012153 distilled water Substances 0.000 claims abstract description 6
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000002904 solvent Substances 0.000 claims abstract description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 11
- 230000003115 biocidal effect Effects 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 239000011572 manganese Substances 0.000 claims description 7
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 6
- 230000000593 degrading effect Effects 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 6
- 229910052748 manganese Inorganic materials 0.000 claims description 6
- 239000010406 cathode material Substances 0.000 claims description 5
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 230000004048 modification Effects 0.000 claims description 4
- 238000012986 modification Methods 0.000 claims description 4
- 229960000935 dehydrated alcohol Drugs 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 238000004090 dissolution Methods 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 2
- 235000012239 silicon dioxide Nutrition 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- SPIFDSWFDKNERT-UHFFFAOYSA-N nickel;hydrate Chemical compound O.[Ni] SPIFDSWFDKNERT-UHFFFAOYSA-N 0.000 claims 3
- 229910005802 NiMn2O4 Inorganic materials 0.000 claims 2
- RCEAADKTGXTDOA-UHFFFAOYSA-N OS(O)(=O)=O.CCCCCCCCCCCC[Na] Chemical compound OS(O)(=O)=O.CCCCCCCCCCCC[Na] RCEAADKTGXTDOA-UHFFFAOYSA-N 0.000 claims 2
- 239000000654 additive Substances 0.000 claims 2
- 230000000996 additive effect Effects 0.000 claims 2
- BZDIAFGKSAYYFC-UHFFFAOYSA-N manganese;hydrate Chemical compound O.[Mn] BZDIAFGKSAYYFC-UHFFFAOYSA-N 0.000 claims 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims 1
- 240000007594 Oryza sativa Species 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 claims 1
- 210000003850 cellular structure Anatomy 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000005297 material degradation process Methods 0.000 claims 1
- 229910017604 nitric acid Inorganic materials 0.000 claims 1
- 235000009566 rice Nutrition 0.000 claims 1
- 241000894007 species Species 0.000 claims 1
- 230000015556 catabolic process Effects 0.000 abstract description 17
- 238000006731 degradation reaction Methods 0.000 abstract description 17
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 abstract description 5
- 235000019333 sodium laurylsulphate Nutrition 0.000 abstract description 5
- 238000001354 calcination Methods 0.000 abstract description 3
- 230000003197 catalytic effect Effects 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 3
- 238000009776 industrial production Methods 0.000 abstract description 2
- 238000001704 evaporation Methods 0.000 abstract 1
- 238000010335 hydrothermal treatment Methods 0.000 abstract 1
- MIVBAHRSNUNMPP-UHFFFAOYSA-N manganese(2+);dinitrate Chemical compound [Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MIVBAHRSNUNMPP-UHFFFAOYSA-N 0.000 abstract 1
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 abstract 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 10
- ALIMWUQMDCBYFM-UHFFFAOYSA-N manganese(2+);dinitrate;tetrahydrate Chemical compound O.O.O.O.[Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ALIMWUQMDCBYFM-UHFFFAOYSA-N 0.000 description 7
- AOPCKOPZYFFEDA-UHFFFAOYSA-N nickel(2+);dinitrate;hexahydrate Chemical compound O.O.O.O.O.O.[Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O AOPCKOPZYFFEDA-UHFFFAOYSA-N 0.000 description 7
- 230000003647 oxidation Effects 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 239000011148 porous material Substances 0.000 description 3
- 238000000026 X-ray photoelectron spectrum Methods 0.000 description 2
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- 150000001721 carbon Chemical class 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 229960004756 ethanol Drugs 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- -1 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 238000004088 simulation Methods 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000004438 BET method Methods 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 206010059866 Drug resistance Diseases 0.000 description 1
- 206010064571 Gene mutation Diseases 0.000 description 1
- 238000001994 activation Methods 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 229940088710 antibiotic agent Drugs 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
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- 238000001816 cooling Methods 0.000 description 1
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- 239000006181 electrochemical material Substances 0.000 description 1
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- 150000002148 esters Chemical class 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
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- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
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- 238000000746 purification Methods 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
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- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000000870 ultraviolet spectroscopy Methods 0.000 description 1
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- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/889—Manganese, technetium or rhenium
- B01J23/8892—Manganese
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- B01J35/20—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
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- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
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- B01J35/633—Pore volume less than 0.5 ml/g
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
- B01J37/0018—Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
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- C—CHEMISTRY; METALLURGY
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
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- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/722—Oxidation by peroxides
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- C—CHEMISTRY; METALLURGY
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- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/343—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the pharmaceutical industry, e.g. containing antibiotics
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/02—Specific form of oxidant
- C02F2305/023—Reactive oxygen species, singlet oxygen, OH radical
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- C—CHEMISTRY; METALLURGY
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- C02F2305/02—Specific form of oxidant
- C02F2305/026—Fenton's reagent
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Abstract
本发明公开了一种具有介孔结构的NiMn2O4纳米催化剂的制备方法,和由其制备的催化剂及其用途。所述制备方法包括步骤:(1)将P123、十二烷基硫酸钠、盐酸溶液加入蒸馏水,然后加入硅酸四乙酯,水热处理得到模板KIT‑6;(2)将硝酸镍和硝酸锰加入无水乙醇中得到混合溶液A;(3)将模板KIT‑6加入溶液A中,形成混合溶液B;(4)将混合溶液B水浴搅拌条件下蒸干溶剂,得到固体C;(5)煅烧固体C得到黑色固体D;(6)将黑色固体D用NaOH溶液洗涤,再离心过滤洗涤后烘干,得到介孔NiMn2O4催化剂。根据本发明的制备方法工艺简单,成本低廉,适合大规模工业化生产。制备得到的介孔NiMn2O4纳米催化剂具有良好的催化性能,对环丙沙星的降解具有明显的提升效果。
The invention discloses a preparation method of a NiMn 2 O 4 nanometer catalyst with a mesoporous structure, the catalyst prepared therefrom and its application. The preparation method comprises steps: (1) adding P123, sodium lauryl sulfate, and hydrochloric acid solution to distilled water, then adding tetraethyl silicate, and performing hydrothermal treatment to obtain template KIT-6; (2) adding nickel nitrate and manganese nitrate Adding absolute ethanol to obtain a mixed solution A; (3) adding the template KIT‑6 to the solution A to form a mixed solution B; (4) evaporating the mixed solution B to dryness of the solvent under stirring in a water bath to obtain a solid C; (5) The black solid D was obtained by calcining the solid C; (6) The black solid D was washed with NaOH solution, then centrifugally filtered and dried to obtain a mesoporous NiMn 2 O 4 catalyst. According to the preparation method of the invention, the process is simple, the cost is low, and it is suitable for large-scale industrial production. The prepared mesoporous NiMn 2 O 4 nano-catalyst has good catalytic performance and can significantly improve the degradation of ciprofloxacin.
Description
技术领域technical field
本发明属于环境电化学材料领域,制备和高级氧化技术处理废水技术领域,具体涉及一种具有介孔结构的NiMn2O4纳米催化剂的制备方法,和由该制备方法得到的NiMn2O4纳米催化剂及其在电芬顿高级氧化技术降解抗生素废水的应用。The invention belongs to the field of environmental electrochemical materials, the technical field of preparation and advanced oxidation technology for treating wastewater, and specifically relates to a method for preparing a NiMn 2 O 4 nanometer catalyst with a mesoporous structure, and the NiMn 2 O 4 nanometer catalyst obtained by the preparation method. Catalyst and its application in the degradation of antibiotic wastewater by Electro-Fenton Advanced Oxidation Technology.
背景技术Background technique
随着医药工业的快速发展,药物成为了一类新兴的环境污染物,对水环境和人类的健康造成了巨大的威胁。其中抗生素污染及其所引起的危害已经引起国内外的广泛关注。而环丙沙星正是抗生素中较为典型的污染源,该废水抗菌能力强,具有生物难降解性,在未经净化处理的情况下直接排入环境中会产生毒副作用,诱导细菌产生耐药性和导致对其他生物基因突变等危害,同时也对水体环境和生态造成潜在的威胁平衡。因此实现高效降解环境中残留的环丙沙星迫在眉睫。With the rapid development of the pharmaceutical industry, drugs have become a new class of environmental pollutants, posing a huge threat to the water environment and human health. Among them, antibiotic pollution and the harm caused by it have aroused widespread concern at home and abroad. Ciprofloxacin is a typical pollution source among antibiotics. The wastewater has strong antibacterial ability and is biodegradable. If it is directly discharged into the environment without purification treatment, it will cause toxic and side effects and induce bacteria to develop drug resistance. and cause harm to other biological gene mutations, and also pose a potential threat balance to the water environment and ecology. Therefore, it is imminent to realize efficient degradation of residual ciprofloxacin in the environment.
高级氧化技术在降解环丙沙星废水方面具有较大潜力。电芬顿高级氧化技术作为一种极具代表性的高级氧化技术,具有条件温和、氧化能力强、反应速度快等优势,在降解环丙沙星废水方面表现出极佳的效果,获得了广泛关注。电芬顿反应机制总的来说是由电化学反应产生的H2O2和Fe2+作为芬顿试剂的持续来源,生成羟基自由基·OH,由羟基自由基的强氧化性引发一系列的链式反应,从而降解有机污染物。Advanced oxidation technology has great potential in degrading ciprofloxacin wastewater. Electro-Fenton advanced oxidation technology, as a representative advanced oxidation technology, has the advantages of mild conditions, strong oxidation ability, and fast reaction speed. It has shown excellent results in degrading ciprofloxacin wastewater and has been widely focus on. The electro-Fenton reaction mechanism generally consists of H 2 O 2 and Fe 2+ produced by electrochemical reactions as a continuous source of Fenton reagents to generate hydroxyl radicals OH, which trigger a series of chain reaction to degrade organic pollutants.
过氧化氢的产量是电芬顿体系降解环丙沙星的关键因素。为了提高过氧化氢的产量,通常以价格低廉的碳毡作为阴极材料,以芬顿催化剂修饰阴极材料,这样提高更多的氧空位,从而大大增加氧吸附量,生成更多的H2O2。但目前研究较热的芬顿催化剂存在产生过氧化氢浓度不高、降解速率慢、产生铁泥等二次污染的问题。因此,仍然需要开发更为有效的阴极催化剂材料。The yield of hydrogen peroxide is the key factor for the degradation of ciprofloxacin by the electro-Fenton system. In order to increase the production of hydrogen peroxide, usually low-cost carbon felt is used as the cathode material, and the cathode material is modified with Fenton catalyst, so as to increase more oxygen vacancies, thereby greatly increasing the amount of oxygen adsorption and generating more H 2 O 2 . However, the Fenton catalysts that are currently being studied have the problems of low concentration of hydrogen peroxide, slow degradation rate, and secondary pollution such as iron sludge. Therefore, there is still a need to develop more efficient cathode catalyst materials.
发明内容Contents of the invention
本发明提供了一种能够提高过氧化氢产量、大幅度提高降解速率且环境友好的催化剂的制备方法,该催化剂可以作为修饰碳毡阴极的催化剂材料。该催化剂为具有较高比表面积的介孔结构的NiMn2O4纳米催化剂,较大的比表面积能够提供更多产生过氧化氢的活性位点,同时金属物种(锰和镍)能够促进活化过氧化氢产生羟基自由基,进一步提高了降解抗生素环丙沙星的效率。The invention provides a preparation method of an environment-friendly catalyst capable of increasing hydrogen peroxide output, greatly increasing degradation rate, and the catalyst can be used as a catalyst material for modifying carbon felt cathodes. The catalyst is a mesoporous NiMn 2 O 4 nanocatalyst with a higher specific surface area. The larger specific surface area can provide more active sites for hydrogen peroxide generation, and metal species (manganese and nickel) can promote the activation process. Hydrogen oxidation produces hydroxyl radicals, which further increase the efficiency of degrading the antibiotic ciprofloxacin.
本发明的一个目的在于提供一种介孔NiMn2O4纳米催化剂的制备方法,所述制备方法包括以下步骤:An object of the present invention is to provide a kind of mesoporous NiMn 2 O The preparation method of nano-catalyst, described preparation method comprises the following steps:
(1)将P123、十二烷基硫酸钠、盐酸溶液加入蒸馏水,搅拌至完全溶解,溶解后加入硅酸四乙酯,继续搅拌,将溶液转移至聚四氟乙烯反应釜中,在80-120℃下加热20-25h,然后将溶液冷却至室温后离心过滤洗涤,将所获得的固体干燥8-10h,得到白色粉末,即为模板KIT-6;(1) Add P123, sodium lauryl sulfate, and hydrochloric acid solution into distilled water, stir until completely dissolved, add tetraethyl silicate after dissolving, continue stirring, transfer the solution to a polytetrafluoroethylene reactor, Heating at 120°C for 20-25h, then cooling the solution to room temperature and washing with centrifugal filtration, drying the obtained solid for 8-10h to obtain a white powder, which is the template KIT-6;
(2)将六水硝酸镍和四水硝酸锰加入无水乙醇中,搅拌至完全溶解,形成混合溶液A;(2) Nickel nitrate hexahydrate and manganese nitrate tetrahydrate are added in absolute ethanol, stirred until fully dissolved, forming mixed solution A;
(3)将步骤1)中得到的模板KIT-6加入溶液A中,剧烈搅拌20-25h,形成混合溶液B;(3) Add the template KIT-6 obtained in step 1) into solution A, and stir vigorously for 20-25 hours to form mixed solution B;
(4)将混合溶液B在50-60℃的水浴搅拌条件下蒸干无水乙醇溶剂,得到固体C;(4) Evaporate the mixed solution B to dry ethanol solvent under the condition of stirring in a water bath at 50-60° C. to obtain solid C;
(5)将固体C在350-400℃的马弗炉中煅烧4-5h,得到黑色固体D;(5) Calcining solid C in a muffle furnace at 350-400°C for 4-5 hours to obtain black solid D;
(6)将黑色固体D用NaOH溶液洗涤三次,再经过离心过滤洗涤至呈中性,将最后离心得到的固体在40-50℃下烘干,得到黑色固体,即为介孔NiMn2O4催化剂。(6) Wash the black solid D with NaOH solution three times, and then wash it through centrifugal filtration until it becomes neutral, and dry the solid obtained by centrifugation at 40-50°C to obtain a black solid, which is mesoporous NiMn 2 O 4 catalyst.
优选地,步骤(1)中,每1000重量份蒸馏水中加入38.5重量份P123、4.4重量份十二烷基硫酸钠、461.5重量份浓度为2mol·L-1的盐酸溶液和82.7重量份硅酸四乙酯。Preferably, in step ( 1 ), 38.5 parts by weight of P123, 4.4 parts by weight of sodium lauryl sulfate, 461.5 parts by weight of hydrochloric acid solution and 82.7 parts by weight of silicic acid are added per 1000 parts by weight of distilled water tetraethyl ester.
优选地,步骤(2)中,每1000重量份无水乙醇中六水硝酸镍和四水硝酸锰的添加量共为70重量份,并且镍和锰的摩尔比为1:2。Preferably, in step (2), the added amount of nickel nitrate hexahydrate and manganese nitrate tetrahydrate is 70 parts by weight per 1000 parts by weight of absolute ethanol, and the molar ratio of nickel and manganese is 1:2.
优选地,步骤(3)中,基于100重量份四水硝酸锰和六水硝酸镍的总和,步骤(1)中制备的模板KIT-6的添加量30-50重量份。所述模板KIT6具有有序介孔结构以及特有的孔道结构,有利于活性物种的负载,且在孔道内负载均匀。负载盐类的总量要满足能充分浸渍并填充到孔道中。Preferably, in step (3), based on 100 parts by weight of the sum of manganese nitrate tetrahydrate and nickel nitrate hexahydrate, the amount of template KIT-6 prepared in step (1) is added in an amount of 30-50 parts by weight. The template KIT6 has an ordered mesoporous structure and a unique pore structure, which is conducive to the loading of active species and is evenly loaded in the pore. The total amount of loaded salts should be sufficient to be fully impregnated and filled into the pores.
优选地,步骤(5)中,马弗炉的升温速率设置为1℃·min-1。Preferably, in step (5), the heating rate of the muffle furnace is set to 1°C·min -1 .
本发明的另一目的在于提供由上述方法制得的介孔NiMn2O4纳米催化剂,该催化剂具有较高的比表面积及很好的催化降解活性。Another object of the present invention is to provide a mesoporous NiMn 2 O 4 nano-catalyst prepared by the above method, which has a relatively high specific surface area and good catalytic degradation activity.
本发明的再一目的在于提供上述介孔NiMn2O4纳米催化剂修饰的碳毡作为阴极材料在降解抗生素环丙沙星的应用。Another object of the present invention is to provide the application of the carbon felt modified by the above-mentioned mesoporous NiMn 2 O 4 nanocatalyst as a cathode material in degrading the antibiotic ciprofloxacin.
本发明的再一目的在于提供一种降解抗生素环丙沙星的方法,该方法采用电芬顿体系,其中作为阴极材料的碳毡用根据本发明的制备方法制备的介孔NiMn2O4纳米催化剂修饰。Another object of the present invention is to provide a method for degrading the antibiotic ciprofloxacin, the method adopts an electric Fenton system, wherein the carbon felt as the cathode material is made of mesoporous NiMn 2 O 4 nanometers prepared according to the preparation method of the present invention catalyst modification.
有益效果Beneficial effect
根据本发明的制备方法工艺简单,成本低廉,适合大规模工业化生产。制备得到的介孔NiMn2O4纳米催化剂具有良好的催化性能,对环丙沙星的降解具有明显的提升效果。According to the preparation method of the invention, the process is simple, the cost is low, and it is suitable for large-scale industrial production. The prepared mesoporous NiMn 2 O 4 nano-catalyst has good catalytic performance and can significantly improve the degradation of ciprofloxacin.
附图说明Description of drawings
图1为实施例1中制备的介孔NiMn2O4和对比实施例1中制备的非介孔NiMn2O4催化剂对抗生素环丙沙星的降解率曲线。Fig. 1 is the degradation rate curve of the antibiotic ciprofloxacin by the mesoporous NiMn 2 O 4 prepared in Example 1 and the non-mesoporous NiMn 2 O 4 catalyst prepared in Comparative Example 1.
图2为实施例1中制备的介孔NiMn2O4和对比实施例1中制备的非介孔NiMn2O4催化剂对TOC的去除率曲线。Fig. 2 is the TOC removal rate curves of the mesoporous NiMn 2 O 4 prepared in Example 1 and the non-mesoporous NiMn 2 O 4 catalyst prepared in Comparative Example 1.
图3为实施例1中制备的介孔NiMn2O4的XPS谱图。FIG. 3 is the XPS spectrum of the mesoporous NiMn 2 O 4 prepared in Example 1.
具体实施方式Detailed ways
以下,将详细地描述本发明。在进行描述之前,应当理解的是,在本说明书和所附的权利要求书中使用的术语不应解释为限制于一般含义和字典含义,而应当在允许发明人适当定义术语以进行最佳解释的原则的基础上,根据与本发明的技术方面相应的含义和概念进行解释。因此,这里提出的描述仅仅是出于举例说明目的的优选实例,并非意图限制本发明的范围,从而应当理解的是,在不偏离本发明的精神和范围的情况下,可以由其获得其他等价方式或改进方式。Hereinafter, the present invention will be described in detail. Before proceeding with the description, it should be understood that the terms used in this specification and appended claims should not be construed as limited to ordinary and dictionary meanings, but should be best interpreted while allowing the inventor to properly define the terms On the basis of the principles of the present invention, explanations are made based on meanings and concepts corresponding to the technical aspects of the present invention. Accordingly, the descriptions set forth herein are preferred examples for illustrative purposes only and are not intended to limit the scope of the invention, so that it should be understood that other, etc. price or improvement.
以下实施例仅是作为本发明的实施方案的例子列举,并不对本发明构成任何限制,本领域技术人员可以理解在不偏离本发明的实质和构思的范围内的修改均落入本发明的保护范围。除非特别说明,以下实施例中使用的试剂和仪器均为市售可得产品。The following examples are only listed as examples of embodiments of the present invention, and do not constitute any limitation to the present invention. Those skilled in the art can understand that modifications within the scope of not departing from the essence and design of the present invention all fall into the protection of the present invention. scope. Unless otherwise specified, the reagents and instruments used in the following examples are all commercially available products.
实施例Example
实施例1Example 1
(1)将P123、十二烷基硫酸钠、盐酸溶液加入蒸馏水,在30℃下搅拌至完全溶解,溶解后加入硅酸四乙酯,保持30℃搅拌24h,将溶液转移至聚四氟乙烯反应釜中,在100℃下加热24h。然后将溶液冷却至室温后离心过滤洗涤,将所获得的固体在40℃干燥12h,得到白色粉末,即为模板KIT-6;该步骤中,每1.0L蒸馏水中加入38.5g的P123、4.4g的十二烷基硫酸钠、461.5g的盐酸溶液(2mol·L-1)和82.7g的硅酸四乙酯;(1) Add P123, sodium lauryl sulfate, and hydrochloric acid solution into distilled water, stir at 30°C until completely dissolved, add tetraethyl silicate after dissolution, keep stirring at 30°C for 24 hours, and transfer the solution to polytetrafluoroethylene Reactor, heated at 100 ° C for 24h. Then the solution was cooled to room temperature, washed by centrifugal filtration, and the obtained solid was dried at 40°C for 12 hours to obtain a white powder, which was template KIT-6; in this step, 38.5 g of P123, 4.4 g of sodium lauryl sulfate, 461.5g of hydrochloric acid solution (2mol L -1 ) and 82.7g of tetraethyl silicate;
(2)将六水硝酸镍和四水硝酸锰加入无水乙醇中,搅拌至完全溶解,形成混合溶液A;该步骤中,每1.0L无水乙醇中六水硝酸镍和四水硝酸锰的添加量共为70g,并且镍和锰的摩尔比为1:2;(2) Nickel nitrate hexahydrate and manganese nitrate tetrahydrate are added in dehydrated alcohol, stir until dissolving completely, form mixed solution A; The amount added is 70g in total, and the molar ratio of nickel and manganese is 1:2;
(3)将步骤1)中得到的模板KIT-6加入溶液A中,剧烈搅拌24h,形成混合溶液B;该步骤中,模板KIT-6的添加重量为四水硝酸锰和六水硝酸镍总重量之和的40%;(3) Add the template KIT-6 obtained in step 1) into solution A, stir vigorously for 24 hours to form a mixed solution B; in this step, the added weight of template KIT-6 is the total amount of manganese nitrate tetrahydrate and nickel nitrate hexahydrate. 40% of the sum of the weights;
(4)将混合溶液B在60℃的水浴搅拌条件下蒸干无水乙醇溶剂,得到固体A;(4) The mixed solution B was evaporated to dry ethanol solvent under the condition of stirring in a water bath at 60° C. to obtain solid A;
(5)将固体A在350℃的马弗炉中煅烧5h,得到黑色固体B;该步骤中,马弗炉的升温速率设置为1℃·min-1;(5) Calcining solid A in a muffle furnace at 350°C for 5h to obtain a black solid B; in this step, the heating rate of the muffle furnace was set to 1°C·min −1 ;
(6)将黑色固体B用NaOH溶液(2mol·L-1)洗涤三次,再经过离心过滤洗涤至呈中性,将最后离心得到的固体在40℃下烘干,得到黑色固体,即为介孔NiMn2O4催化剂。(6) Wash the black solid B with NaOH solution (2mol·L -1 ) three times, then wash it by centrifugal filtration until it becomes neutral, and dry the solid obtained by centrifugation at 40°C to obtain a black solid, which is medium Porous NiMn 2 O 4 catalyst.
本实施例中制得的介孔NiMn2O4催化剂的比表面积经过BET法测定为262m2·g-1,另外通过XPS检测证明其中的Ni主要表现为+2价和+3价,Mn主要表现为+3价和+4价。图3为实施例1中制备的介孔NiMn2O4的XPS谱图。The specific surface area of the mesoporous NiMn 2 O 4 catalyst prepared in this example was determined to be 262m 2 ·g -1 by the BET method. In addition, it was proved by XPS that the Ni in it mainly exhibits +2 and +3 valences, and the Mn mainly Shown as +3 valence and +4 valence. FIG. 3 is the XPS spectrum of the mesoporous NiMn 2 O 4 prepared in Example 1.
对比实施例1Comparative Example 1
为了进行对照,制备了非介孔NiMn2O4催化剂,其制备方法与实施例1中类似,只是在制备过程中未加入KIT-6模板。For comparison, a non-mesoporous NiMn 2 O 4 catalyst was prepared, and its preparation method was similar to that in Example 1, except that no KIT-6 template was added during the preparation process.
非介孔NiMn2O4催化剂合成的具体过程如下:The specific process of the synthesis of non-mesoporous NiMn 2 O 4 catalyst is as follows:
(1)将六水硝酸镍和四水硝酸锰加入无水乙醇中,剧烈搅拌24h,形成混合溶液C;(1) Add nickel nitrate hexahydrate and manganese nitrate tetrahydrate into absolute ethanol, stir vigorously for 24 hours to form mixed solution C;
该步骤中,每1.0L无水乙醇中六水硝酸镍和四水硝酸锰的添加量共为70g,并且镍和锰的摩尔比为1:2;In this step, the addition of nickel nitrate hexahydrate and manganese nitrate tetrahydrate in every 1.0L dehydrated alcohol is 70g altogether, and the mol ratio of nickel and manganese is 1:2;
(2)将混合溶液C在60℃的水浴搅拌条件下蒸干无水乙醇溶剂,得到固体C;(2) Evaporate the mixed solution C to dryness of absolute ethanol solvent under the condition of stirring in a water bath at 60° C. to obtain solid C;
(3)将固体C在350℃的马弗炉中煅烧5h,得到黑色固体B,即为非介孔NiMn2O4催化剂。(3) The solid C was calcined in a muffle furnace at 350° C. for 5 h to obtain a black solid B, which was a non-mesoporous NiMn 2 O 4 catalyst.
表1中列出实施例1和对比实施例1中制备的介孔NiMn2O4催化剂和非介孔NiMn2O4催化剂的性质数据。Table 1 lists the property data of the mesoporous NiMn 2 O 4 catalyst and the non-mesoporous NiMn 2 O 4 catalyst prepared in Example 1 and Comparative Example 1.
表1Table 1
测试实施例1:对环丙沙星的降解的测试Test Example 1: Test on the Degradation of Ciprofloxacin
(1)量取100mL配制的环丙沙星模拟溶液于圆柱形玻璃电池中,采用Pt片(1.0cm×2.0cm)为阳极和以催化剂修饰的碳毡(2.0cm×3.0cm)为阴极,且两个电极之间的距离为1.0cm。在电解开始前30min至实验结束,以50ml·min-1的流速将氧气(O2)注入溶液中。(1) Take 100 mL of the prepared ciprofloxacin simulation solution in a cylindrical glass cell, use a Pt sheet (1.0 cm × 2.0 cm) as the anode and a catalyst-modified carbon felt (2.0 cm × 3.0 cm) as the cathode, And the distance between the two electrodes is 1.0 cm. From 30 min before the start of electrolysis to the end of the experiment, oxygen (O 2 ) was injected into the solution at a flow rate of 50 ml·min -1 .
该步骤中,环丙沙星模拟溶液中的环丙沙星、Fe2+和电解质Na2SO4的浓度分别为0.1mmol·L-1、0.1mmol·L-1和0.05mol·L-1,并通过0.1mol·L-1的H2SO4调节其初始pH值为3.0。In this step, the concentrations of ciprofloxacin, Fe 2+ and electrolyte Na 2 SO 4 in the ciprofloxacin simulated solution are 0.1mmol·L -1 , 0.1mmol·L -1 and 0.05mol·L -1 respectively , and its initial pH value was adjusted to 3.0 by 0.1mol·L -1 H 2 SO 4 .
(2)分别在电解0min、10min、20min、30min、40min、50min、60min、75min、90min、105min、120min时,取一定量的降解溶液过膜,通过紫外可见分光光度计在λ=278nm处测定相应溶液中环丙沙星的浓度C。(2) At 0min, 10min, 20min, 30min, 40min, 50min, 60min, 75min, 90min, 105min, and 120min of electrolysis, take a certain amount of degradation solution to pass through the membrane, and measure it at λ=278nm by an ultraviolet-visible spectrophotometer The concentration C of ciprofloxacin in the corresponding solution.
(3)环丙沙星的降解效率计算公式如下:(3) The degradation efficiency calculation formula of ciprofloxacin is as follows:
降解效率(%)=(C0-C)/C0×100%(1)Degradation efficiency (%) = (C 0 -C)/C 0 ×100% (1)
C0:环丙沙星的初始浓度;C 0 : initial concentration of ciprofloxacin;
C:不同降解时间下的反应溶液中环丙沙星的浓度。C: The concentration of ciprofloxacin in the reaction solution under different degradation times.
图1为实施例1中制备的介孔NiMn2O4和对比实施例1中制备的非介孔NiMn2O4催化剂对抗生素环丙沙星的降解率曲线。Fig. 1 is the degradation rate curve of the antibiotic ciprofloxacin by the mesoporous NiMn 2 O 4 prepared in Example 1 and the non-mesoporous NiMn 2 O 4 catalyst prepared in Comparative Example 1.
测试实施例2:对TOC去除的测试Test Example 2: Test on TOC removal
(1)量取100mL配制的环丙沙星模拟溶液于圆柱形玻璃电池中,采用Pt片(1.0cm×2.0cm)为阳极和以催化剂修饰的碳毡(2.0cm×3.0cm)为阴极,且两个电极之间的距离为1.0cm。在电解开始前30min至实验结束,以50ml·min-1的流速将氧气(O2)注入溶液中。(1) Take 100 mL of the prepared ciprofloxacin simulation solution in a cylindrical glass cell, use a Pt sheet (1.0 cm × 2.0 cm) as the anode and a catalyst-modified carbon felt (2.0 cm × 3.0 cm) as the cathode, And the distance between the two electrodes is 1.0 cm. From 30 min before the start of electrolysis to the end of the experiment, oxygen (O 2 ) was injected into the solution at a flow rate of 50 ml·min -1 .
该步骤中,环丙沙星模拟溶液中的环丙沙星、Fe2+和电解质Na2SO4的浓度分别为0.1mmol·L-1、0.1mmol·L-1和0.05mol·L-1,并通过0.1mol·L-1的H2SO4调节其初始pH值为3.0。In this step, the concentrations of ciprofloxacin, Fe 2+ and electrolyte Na 2 SO 4 in the ciprofloxacin simulated solution are 0.1mmol·L -1 , 0.1mmol·L -1 and 0.05mol·L -1 respectively , and its initial pH value was adjusted to 3.0 by 0.1mol·L -1 H 2 SO 4 .
(2)分别在电解0min、30min、60min、120min、180min、240min、300min时,取一定量的降解溶液过膜,通过总有机碳分析仪测定相应溶液中TOC的值c。(2) At 0 min, 30 min, 60 min, 120 min, 180 min, 240 min, and 300 min of electrolysis, take a certain amount of degradation solution to pass through the membrane, and measure the value c of TOC in the corresponding solution by a total organic carbon analyzer.
(3)TOC去除效率计算公式如下:(3) The calculation formula of TOC removal efficiency is as follows:
TOC去除效率(%)=(c0-c)/c0×100%……………(2)TOC removal efficiency (%)=(c 0 -c)/c 0 ×100%……………(2)
c0:初始TOC;c 0 : initial TOC;
c:不同降解时间下的反应溶液中的TOC。c: TOC in the reaction solution under different degradation times.
图2为实施例1中制备的介孔NiMn2O4和对比实施例1中制备的非介孔NiMn2O4催化剂对TOC的去除率曲线。Fig. 2 is the TOC removal rate curves of the mesoporous NiMn 2 O 4 prepared in Example 1 and the non-mesoporous NiMn 2 O 4 catalyst prepared in Comparative Example 1.
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