CN106044862A - Method for preparing nano-manganese oxide through low-temperature electrolysis - Google Patents
Method for preparing nano-manganese oxide through low-temperature electrolysis Download PDFInfo
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- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 58
- 238000000034 method Methods 0.000 title claims abstract description 32
- AMWRITDGCCNYAT-UHFFFAOYSA-L manganese oxide Inorganic materials [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 title 1
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims abstract description 87
- 239000003792 electrolyte Substances 0.000 claims abstract description 17
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000010439 graphite Substances 0.000 claims abstract description 12
- 229910002804 graphite Inorganic materials 0.000 claims abstract description 12
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000010949 copper Substances 0.000 claims abstract description 10
- 229910052802 copper Inorganic materials 0.000 claims abstract description 10
- 238000002360 preparation method Methods 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 239000002245 particle Substances 0.000 claims abstract description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 17
- 229940099596 manganese sulfate Drugs 0.000 claims description 15
- 235000007079 manganese sulphate Nutrition 0.000 claims description 15
- 239000011702 manganese sulphate Substances 0.000 claims description 15
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 claims description 15
- 239000000243 solution Substances 0.000 claims description 11
- 239000008151 electrolyte solution Substances 0.000 claims description 9
- 239000002994 raw material Substances 0.000 claims description 9
- 239000002270 dispersing agent Substances 0.000 claims description 7
- 230000008569 process Effects 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 5
- 235000011149 sulphuric acid Nutrition 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 3
- 239000011572 manganese Substances 0.000 claims description 3
- 239000001117 sulphuric acid Substances 0.000 claims 3
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims 2
- 229910052748 manganese Inorganic materials 0.000 claims 2
- 229910000357 manganese(II) sulfate Inorganic materials 0.000 claims 2
- 241000790917 Dioxys <bee> Species 0.000 claims 1
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims 1
- 239000006185 dispersion Substances 0.000 claims 1
- DDXLVDQZPFLQMZ-UHFFFAOYSA-M dodecyl(trimethyl)azanium;chloride Chemical compound [Cl-].CCCCCCCCCCCC[N+](C)(C)C DDXLVDQZPFLQMZ-UHFFFAOYSA-M 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- PAVJEQIFHXNOSM-UHFFFAOYSA-H manganese(3+);trisulfate Chemical compound [Mn+3].[Mn+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O PAVJEQIFHXNOSM-UHFFFAOYSA-H 0.000 claims 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
- 239000004408 titanium dioxide Substances 0.000 claims 1
- 229910006287 γ-MnO2 Inorganic materials 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- 238000009776 industrial production Methods 0.000 abstract description 2
- 239000002105 nanoparticle Substances 0.000 abstract 1
- 239000012798 spherical particle Substances 0.000 abstract 1
- 239000000047 product Substances 0.000 description 16
- 239000000706 filtrate Substances 0.000 description 10
- 239000008367 deionised water Substances 0.000 description 5
- 229910021641 deionized water Inorganic materials 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000004570 mortar (masonry) Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 239000010453 quartz Substances 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000005303 weighing Methods 0.000 description 4
- 230000001276 controlling effect Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000003978 infusion fluid Substances 0.000 description 3
- 238000012824 chemical production Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 239000012456 homogeneous solution Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- 229910001289 Manganese-zinc ferrite Inorganic materials 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- JIYIUPFAJUGHNL-UHFFFAOYSA-N [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[Mn++].[Mn++].[Mn++].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Zn++].[Zn++] Chemical compound [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[Mn++].[Mn++].[Mn++].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Zn++].[Zn++] JIYIUPFAJUGHNL-UHFFFAOYSA-N 0.000 description 1
- FBDMJGHBCPNRGF-UHFFFAOYSA-M [OH-].[Li+].[O-2].[Mn+2] Chemical compound [OH-].[Li+].[O-2].[Mn+2] FBDMJGHBCPNRGF-UHFFFAOYSA-M 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- WJZHMLNIAZSFDO-UHFFFAOYSA-N manganese zinc Chemical compound [Mn].[Zn] WJZHMLNIAZSFDO-UHFFFAOYSA-N 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G45/00—Compounds of manganese
- C01G45/02—Oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y40/00—Manufacture or treatment of nanostructures
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/21—Manganese oxides
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
- H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
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- General Chemical & Material Sciences (AREA)
- Nanotechnology (AREA)
- General Physics & Mathematics (AREA)
- Manufacturing & Machinery (AREA)
- Crystallography & Structural Chemistry (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- Materials Engineering (AREA)
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Abstract
本发明提供一种纳米电解二氧化锰的低温制备方法,属于二氧化锰制备技术领域。该方法是用铜板作阴极,石墨板作阳极进行电解,电解温度为5~30℃,阳极电流密度为100~1000A/m2,电解液中H2SO4浓度为30~60g/L,MnSO4浓度为40~70g/L,制得的电解MnO2再经过静置、抽滤(水洗+醇洗)、真空干燥、研磨,即可制得纳米MnO2成品。制得的纳米MnO2为球型粒子,粒径为50‑200nm。本发明相较于其他高温电解二氧化锰(通常为98℃左右),产品为粒径均匀的纳米γ‑MnO2,且条件温和,生产设备简单、成本更低,电解体系稳定可控,且处理简单、安全,环境污染小,废液可循环电解,有更可观的电流效率和可操作性,能够进行大规模工业化生产。The invention provides a low-temperature preparation method of nanometer electrolytic manganese dioxide, which belongs to the technical field of manganese dioxide preparation. The method uses a copper plate as a cathode and a graphite plate as an anode for electrolysis, the electrolysis temperature is 5-30°C, the anode current density is 100-1000A/m 2 , the concentration of H 2 SO 4 in the electrolyte is 30-60g/L, MnSO 4 The concentration is 40-70g/L, and the electrolytic MnO 2 prepared is then left to stand, suction filtered (washed with water + alcohol), vacuum dried, and ground to obtain a finished nano-MnO 2 product. The prepared nanometer MnO2 is a spherical particle with a particle diameter of 50-200nm. Compared with other high-temperature electrolytic manganese dioxide (usually around 98°C), the product of the present invention is nano-sized γ-MnO 2 with uniform particle size, and the conditions are mild, the production equipment is simple, the cost is lower, the electrolytic system is stable and controllable, and The treatment is simple and safe, the environmental pollution is small, the waste liquid can be recycled and electrolyzed, the current efficiency and operability are more considerable, and large-scale industrial production can be carried out.
Description
技术领域technical field
本发明属于电解二氧化锰制备技术领域,具体是低温电解制备纳米二氧化锰的方法。The invention belongs to the technical field of electrolytic manganese dioxide preparation, in particular to a method for preparing nano manganese dioxide by low-temperature electrolysis.
背景技术Background technique
自1888年发明干电池以来,二氧化锰作为干电池主要的正极材料,其性能对锌锰干电池的性能有着决定性影响。目前,二氧化锰的制备方法主要有化学法、电解法等。化学二氧化锰的产率和纯度都较高,但化学二氧化锰存在平均粒径较大、操作复杂、环境污染严重、不能连续生产、不适于工业化生产等缺点,而具有纯度高、放电容量大、电化学活性强、体积小、寿命长等优点的电解二氧化锰,不仅可用作优良的电池去极化剂,也可用作超级电容器材料、化工生产中的氧化剂、锂离子电池和锰锌铁氧体软磁材料的原料,也是优良的净水滤料,且相比活性炭、沸石,其吸附性能更好。Since the invention of dry batteries in 1888, manganese dioxide has been used as the main positive electrode material of dry batteries, and its performance has a decisive impact on the performance of zinc-manganese dry batteries. At present, the preparation methods of manganese dioxide mainly include chemical methods and electrolytic methods. The yield and purity of chemical manganese dioxide are high, but chemical manganese dioxide has the disadvantages of large average particle size, complicated operation, serious environmental pollution, non-continuous production, and unsuitability for industrial production. Electrolytic manganese dioxide, which has the advantages of large size, strong electrochemical activity, small size, and long life, can not only be used as an excellent battery depolarizer, but also can be used as a supercapacitor material, an oxidant in chemical production, lithium-ion batteries and The raw material of manganese zinc ferrite soft magnetic material is also an excellent water purification filter material, and its adsorption performance is better than activated carbon and zeolite.
该法生产的纳米电解二氧化锰,相比于化学二氧化锰,其化学成分和晶体结构基本一致,且具有粒径小且均匀、体积小、比表面积大、电化学活性好等优点,产率为92%,100目的产品指标为90%,产品纯度为95%。该法生产的纳米电解二氧化锰可用作电池原料,也可广泛用作精细化工生产中的氧化/还原剂、催化剂、净水滤料等。市场上现行的电解二氧化锰方法多为高温制备块状微米级二氧化锰材料,能耗高,不易处理。控制电解条件,可减少二氧化锰在电极板上的沉积。专利201110171479.1中,采用超声电解,同时利用隔膜和添加剂,使二氧化锰尽可能分散在电解液中。本专利在无隔膜的条件下,通过控制低温和分散剂,控制二氧化锰成核和生长机制,使其悬浮于电解液中,产品为粒径均匀的纳米γ-MnO2。此方法条件温和,生产设备简单,产率高,电解体系稳定可控,且废液处理简单、安全,环境污染小,废液可循环电解,生产成本更低。通过研究适当温度、适当电流密度、高电流效率下,低温电解制备纳米二氧化锰的方法,可以明显降低企业的原料和电费成本,提高企业市场竞争力,实现节能环保。Compared with chemical manganese dioxide, the nano-electrolytic manganese dioxide produced by this method has basically the same chemical composition and crystal structure, and has the advantages of small and uniform particle size, small volume, large specific surface area, and good electrochemical activity. The rate is 92%, the 100-mesh product index is 90%, and the product purity is 95%. The nano electrolytic manganese dioxide produced by this method can be used as a battery raw material, and can also be widely used as an oxidation/reduction agent, catalyst, water purification filter material, etc. in fine chemical production. Most of the current electrolytic manganese dioxide methods on the market are high-temperature preparation of massive micron-sized manganese dioxide materials, which require high energy consumption and are difficult to handle. Controlling the electrolysis conditions can reduce the deposition of manganese dioxide on the electrode plate. In patent 201110171479.1, ultrasonic electrolysis is used, and a separator and additives are used at the same time to disperse manganese dioxide in the electrolyte as much as possible. In this patent, under the condition of no diaphragm, by controlling the low temperature and dispersant, the nucleation and growth mechanism of manganese dioxide is controlled, so that it is suspended in the electrolyte, and the product is nanometer γ-MnO 2 with uniform particle size. The method has mild conditions, simple production equipment, high yield, stable and controllable electrolysis system, simple and safe treatment of waste liquid, less environmental pollution, recyclable electrolysis of waste liquid, and lower production cost. By studying the method of preparing nano-manganese dioxide by low-temperature electrolysis under appropriate temperature, appropriate current density, and high current efficiency, the cost of raw materials and electricity charges can be significantly reduced, the market competitiveness of enterprises can be improved, and energy conservation and environmental protection can be realized.
发明内容Contents of the invention
本发明的目的在于:针对上述存在的问题,提供一种低温电解制备纳米二氧化锰的方法,该方法针对以MnSO4+H2SO4水溶液为电解液,铜板作阴极、石墨板作阳极,低温电解制备纳米二氧化锰的方法,可以明显降低企业的生产成本,提高企业市场竞争力,实现节能环保。The object of the present invention is to: in view of the above-mentioned existing problems, provide a kind of method for preparing nano-manganese dioxide by low-temperature electrolysis, this method aims at using MnSO 4 +H 2 SO 4 aqueous solution as electrolyte, copper plate as cathode, graphite plate as anode, The method for preparing nano-manganese dioxide by low-temperature electrolysis can significantly reduce the production cost of the enterprise, improve the market competitiveness of the enterprise, and realize energy saving and environmental protection.
为了实现上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
低温电解制备纳米二氧化锰的方法,该方法包括以下步骤:A method for preparing nano-manganese dioxide by low-temperature electrolysis, the method comprising the following steps:
(1)配制电解液:以工业硫酸锰为原料,溶于去离子水中,按照一定的质量比,加入浓硫酸,及少量分散剂A,搅拌形成均匀溶液,在室温下静止一段时间。(1) Preparation of electrolyte: use industrial manganese sulfate as raw material, dissolve in deionized water, add concentrated sulfuric acid and a small amount of dispersant A according to a certain mass ratio, stir to form a uniform solution, and let it stand at room temperature for a period of time.
(2)预处理:利用水浴加热装置对电解液加热,使溶液温度保持在5 ~ 30℃,对两个电极板进行清洗。(2) Pretreatment: Use a water bath heating device to heat the electrolyte to keep the temperature of the solution at 5-30°C, and clean the two electrode plates.
(3)电解:搭好电解装置及进、出液管,对电解液进行电解,在阳极上析出二氧化锰。(3) Electrolysis: Set up the electrolysis device and the inlet and outlet pipes, electrolyze the electrolyte, and precipitate manganese dioxide on the anode.
(4)后处理:电解后,将石墨板上的二氧化锰处理干净,并将电解液静置,抽滤(用水和乙醇淋洗),收集滤液,继续电解,最后真空干燥、研磨,得到低温电解纳米二氧化锰成品,滤液继续电解。(4) Post-treatment: After electrolysis, clean the manganese dioxide on the graphite plate, let the electrolyte stand still, filter with suction (rinse with water and ethanol), collect the filtrate, continue electrolysis, and finally vacuum dry and grind to obtain Low-temperature electrolysis of nano-manganese dioxide finished products, and the filtrate continues to be electrolyzed.
电解槽中,使用铜板作阴极,石墨板作阳极进行电解,电解温度为5 ~ 30℃,阳极电流密度为100 ~ 1000A/m2,电解液中H2SO4浓度为30 ~ 50g/L,MnSO4浓度为40 ~ 60g/L。In the electrolytic cell, copper plates are used as cathodes and graphite plates are used as anodes for electrolysis. The electrolysis temperature is 5-30°C, the anode current density is 100-1000A/m 2 , and the concentration of H 2 SO 4 in the electrolyte is 30-50g/L. The concentration of MnSO 4 is 40-60g/L.
进一步优选,使用铜板作阴极,石墨板作阳极进行电解,电解温度为5 ~ 30℃,阳极电流密度为300 ~ 800A/m2,电解液中H2SO4浓度为30 ~ 50g/L,MnSO4浓度为40 ~60g/L。More preferably, copper plates are used as cathodes, graphite plates are used as anodes for electrolysis, the electrolysis temperature is 5-30°C, the anode current density is 300-800A / m2 , the concentration of H2SO4 in the electrolyte is 30-50g/L, MnSO 4 The concentration is 40-60g/L.
进一步地,所选用的进、出液管,均在阳极板一侧,通过核算,控制合适的流速。Furthermore, the selected liquid inlet and outlet pipes are all on the side of the anode plate, and the appropriate flow rate is controlled through calculation.
生产电解二氧化锰的主要反应为:The main reactions to produce electrolytic manganese dioxide are:
阳极上主要发生的反应为:Mn2++2H2O→MnO2+4H++2e-(E1=1.23V)The main reaction on the anode is: Mn 2+ +2H 2 O→MnO 2 +4H + +2e - (E 1 =1.23V)
阴极上主要发生的反应为:2H++2e-→H2↑(E2=0V)The main reaction on the cathode is: 2H + +2e - → H 2 ↑ (E 2 =0V)
电解过程中发生的总反应为: MnSO4+2H2O→MnO2+H2SO4+H2↑The total reaction that occurs during electrolysis is: MnSO 4 +2H 2 O→MnO 2 +H 2 SO 4 +H 2 ↑
理论分解电压为: E= E1-E2=1.23VThe theoretical decomposition voltage is: E= E 1 -E 2 =1.23V
综上所述,由于采用了上述技术方案,本发明的有益效果是:本发明通过控制阳极电流密度、电解液浓度、电解温度、电极板类型等技术手段达到低温电解制备纳米二氧化锰的目的。该方法在保证产品品质的同时,低温电解降低电费成本,也减少了阳极板上二氧化锰的沉积,增加阳极寿命,延长电解时间,进一步降低企业生产成本,提升其市场竞争力,实现节能环保。In summary, due to the adoption of the above technical scheme, the beneficial effects of the present invention are: the present invention achieves the purpose of preparing nano-manganese dioxide by low-temperature electrolysis by controlling the anode current density, electrolyte concentration, electrolysis temperature, electrode plate type and other technical means . While ensuring product quality, low-temperature electrolysis reduces the cost of electricity, reduces the deposition of manganese dioxide on the anode plate, increases the life of the anode, prolongs the electrolysis time, further reduces the production cost of the enterprise, improves its market competitiveness, and realizes energy conservation and environmental protection .
附图说明Description of drawings
图1是低温电解制备纳米二氧化锰成品的扫描电镜图;Fig. 1 is the scanning electron micrograph of the nano-manganese dioxide finished product prepared by low-temperature electrolysis;
图2是低温电解制备纳米二氧化锰成品的XRD图;Fig. 2 is the XRD pattern of nano-manganese dioxide finished product prepared by low-temperature electrolysis;
图3是低温电解制备纳米二氧化锰成品的锂-二氧化锰电池的放电曲线。Fig. 3 is the discharge curve of the lithium-manganese dioxide battery in which the nano-manganese dioxide finished product is prepared by low-temperature electrolysis.
具体实施方式detailed description
下面结合附图对本发明做进一步的详细说明,以下实施例是对本发明的解释,本发明并不局限于以下实施例。The present invention will be described in further detail below in conjunction with the accompanying drawings. The following embodiments are explanations of the present invention, and the present invention is not limited to the following embodiments.
实施例1:Example 1:
以工业硫酸锰为原料,烧杯为电解槽,于5L的烧杯中,用去离子水配制40±10g/L硫酸锰,按照质量比1:1缓慢加入浓硫酸,搅拌形成均匀溶液,在室温下静止一段时间,将大烧杯置于水浴锅中,设置温度为5 ~ 10℃,控制电解液温度。以石墨为阳极板,铜板为阴极板,将阴、阳极板浸没于5 ~ 10℃的电解液中。将80±10g/L的硫酸锰补加液装于吊瓶中,当稳压直流电源在100±10A/m2的电流密度下开始电解时,在阳极板一侧进行补加,同时用输液管排出电解过程中产生的硫酸,保证体系酸度稳定,观察二氧化锰析出情况,电解12h。将电解停止后的电解液静置一夜后,用布氏漏斗进行抽滤,收集滤液,并用水和乙醇各淋洗2次,70℃真空干燥,干燥后的固体在石英研钵中研磨,得到电解制备的黑色纳米二氧化锰粉末。称重,产率为30%,产品纯度为90%,100目的产品指标为40%,装于封口袋中。收集的滤液再进行电解。Use industrial manganese sulfate as raw material, and the beaker is the electrolytic cell. In a 5L beaker, prepare 40±10g/L manganese sulfate with deionized water, slowly add concentrated sulfuric acid according to the mass ratio of 1:1, and stir to form a uniform solution. Stand still for a period of time, place the large beaker in a water bath, set the temperature at 5-10°C, and control the temperature of the electrolyte. Use graphite as the anode plate and copper plate as the cathode plate, and immerse the cathode and anode plates in the electrolyte solution at 5-10°C. Put 80±10g/L manganese sulfate replenishing solution in the hanging bottle, when the regulated DC power supply starts electrolysis at the current density of 100±10A/ m2 , replenish it on the side of the anode plate, and use the infusion solution at the same time The sulfuric acid produced in the electrolysis process was discharged through the pipe to ensure the stability of the acidity of the system, and the precipitation of manganese dioxide was observed, and the electrolysis was performed for 12 hours. After the electrolysis was stopped, the electrolyte solution was left to stand overnight, then suction filtered with a Buchner funnel, the filtrate was collected, rinsed twice with water and ethanol, dried in vacuum at 70°C, and the dried solid was ground in a quartz mortar to obtain Black nano manganese dioxide powder prepared by electrolysis. Weighing, productive rate is 30%, and product purity is 90%, and 100 mesh product indexs are 40%, are contained in sealing bag. The collected filtrate is then subjected to electrolysis.
实施例2:Example 2:
以工业硫酸锰为原料,烧杯为电解槽,于5L的烧杯中,用去离子水配制40±10g/L硫酸锰,按照质量比1:1缓慢加入浓硫酸,搅拌形成均匀溶液,在室温下静止一段时间,将大烧杯置于水浴锅中,设置温度为10~ 20℃,控制电解液温度。以石墨为阳极板,铜板为阴极板,将阴、阳极板浸没于10 ~ 20℃的电解液中。将80±10g/L的硫酸锰补加液装于吊瓶中,当稳压直流电源在200±10A/m2的电流密度下开始电解时,在阳极板一侧进行补加,同时用输液管排出电解过程中产生的硫酸,保证体系酸度稳定,观察二氧化锰析出情况,电解12h。将电解停止后的电解液静置一夜后,用布氏漏斗进行抽滤,收集滤液,并用水和乙醇各淋洗2次,70℃真空干燥,干燥后的固体在石英研钵中研磨,得到电解制备的黑色纳米二氧化锰粉末。称重,产率为40%,产品纯度为90%,100目的产品指标为50%,装于封口袋中。收集的滤液再进行电解。Use industrial manganese sulfate as raw material, and the beaker is the electrolytic cell. In a 5L beaker, prepare 40±10g/L manganese sulfate with deionized water, slowly add concentrated sulfuric acid according to the mass ratio of 1:1, and stir to form a uniform solution. Stand still for a period of time, place the large beaker in a water bath, set the temperature at 10-20°C, and control the temperature of the electrolyte. Use graphite as the anode plate and copper plate as the cathode plate, and immerse the cathode and anode plates in the electrolyte solution at 10-20°C. Put 80±10g/L manganese sulfate replenishing solution in the hanging bottle, when the stabilized DC power supply starts electrolysis at the current density of 200 ±10A/m2, replenish it on the side of the anode plate, and use the infusion solution at the same time The sulfuric acid produced in the electrolysis process was discharged through the pipe to ensure the stability of the acidity of the system, and the precipitation of manganese dioxide was observed, and the electrolysis was performed for 12 hours. After the electrolysis was stopped, the electrolyte solution was left to stand overnight, then suction filtered with a Buchner funnel, the filtrate was collected, rinsed twice with water and ethanol, dried in vacuum at 70°C, and the dried solid was ground in a quartz mortar to obtain Black nano manganese dioxide powder prepared by electrolysis. Weighing, productive rate is 40%, and product purity is 90%, and 100 mesh product indexs are 50%, are contained in sealing bag. The collected filtrate is then subjected to electrolysis.
实施例3:Example 3:
以工业硫酸锰为原料,烧杯为电解槽,于5L的烧杯中,用去离子水配制40±10g/L硫酸锰,按照质量比1:1:0.05,缓慢加入浓硫酸,及少量分散剂A,搅拌形成均匀溶液,在室温下静止一段时间,将大烧杯置于水浴锅中,设置温度为10 ~ 20℃,控制电解液温度。以石墨为阳极板,铜板为阴极板,将阴、阳极板浸没于10 ~ 20℃的电解液中。将80±10g/L的硫酸锰补加液装于吊瓶中,当稳压直流电源在200±10A/m2的电流密度下开始电解时,在阳极板一侧进行补加,同时用输液管排出电解过程中产生的硫酸,保证体系酸度稳定,观察二氧化锰析出情况,电解12h。将电解停止后的电解液静置一夜后,用布氏漏斗进行抽滤,收集滤液,并用水和乙醇各淋洗2次,70℃真空干燥,干燥后的固体在石英研钵中研磨,得到低温电解的黑色纳米二氧化锰粉末。称重,产率为70%,产品纯度为90%,100目的产品指标为70%,装于封口袋中。收集的滤液再进行电解。Use industrial manganese sulfate as raw material, and the beaker is the electrolytic cell. In a 5L beaker, prepare 40±10g/L manganese sulfate with deionized water, and slowly add concentrated sulfuric acid and a small amount of dispersant A according to the mass ratio of 1:1:0.05. , stirred to form a homogeneous solution, stood still at room temperature for a period of time, placed the large beaker in a water bath, set the temperature at 10-20°C, and controlled the temperature of the electrolyte. Use graphite as the anode plate and copper plate as the cathode plate, and immerse the cathode and anode plates in the electrolyte solution at 10-20°C. Put 80±10g/L manganese sulfate replenishing solution in the hanging bottle, when the stabilized DC power supply starts electrolysis at the current density of 200 ±10A/m2, replenish it on the side of the anode plate, and use the infusion solution at the same time The sulfuric acid produced in the electrolysis process was discharged through the pipe to ensure the stability of the acidity of the system, and the precipitation of manganese dioxide was observed, and the electrolysis was performed for 12 hours. After the electrolysis was stopped, the electrolyte solution was left to stand overnight, then suction filtered with a Buchner funnel, the filtrate was collected, rinsed twice with water and ethanol, dried in vacuum at 70°C, and the dried solid was ground in a quartz mortar to obtain Low-temperature electrolytic black nano manganese dioxide powder. Weighing, productive rate is 70%, and product purity is 90%, and 100 object product indexes are 70%, are contained in sealing bag. The collected filtrate is then subjected to electrolysis.
实施例4:Example 4:
以工业硫酸锰为原料,烧杯为电解槽,于5L的烧杯中,用去离子水配制40±10g/L硫酸锰,按照质量比1:1:0.1缓慢加入浓硫酸,及少量分散剂A,搅拌形成均匀溶液,在室温下静止一段时间,将大烧杯置于水浴锅中,设置温度为20 ~ 30℃,加热电解液至设定温度。以石墨为阳极板,铜板为阴极板,将阴、阳极板浸没于20 ~ 30℃的电解液中。将80±10g/L的硫酸锰补加液装于吊瓶中,当稳压直流电源在200±10A/m2的电流密度下开始电解时,在阳极板一侧进行补加,同时在阳极板一侧用输液管排出电解过程中产生的硫酸,保证体系酸度稳定,观察二氧化锰析出情况,电解12h。将电解停止后的电解液静置一夜后,用布氏漏斗进行抽滤,收集滤液,并用水和乙醇各淋洗2次,70℃真空干燥,干燥后的固体在石英研钵中研磨,得到电解制备的黑色纳米二氧化锰粉末。称重,产率为90%,产品纯度为95%,100目的产品指标为85%,装于封口袋中。收集的滤液再进行电解。Use industrial manganese sulfate as raw material, and the beaker is the electrolytic cell. In a 5L beaker, prepare 40±10g/L manganese sulfate with deionized water, slowly add concentrated sulfuric acid and a small amount of dispersant A according to the mass ratio of 1:1:0.1, Stir to form a homogeneous solution, let stand at room temperature for a period of time, place the large beaker in a water bath, set the temperature at 20-30°C, and heat the electrolyte to the set temperature. Use graphite as the anode plate and copper plate as the cathode plate, and immerse the cathode and anode plates in the electrolyte solution at 20-30°C. Put 80±10g/L manganese sulfate replenishing solution in the hanging bottle, and when the regulated DC power supply starts electrolysis at the current density of 200 ±10A/m2, add it on the side of the anode plate, and at the same time On one side of the plate, discharge the sulfuric acid produced during the electrolysis process with an infusion tube to ensure that the acidity of the system is stable, observe the precipitation of manganese dioxide, and perform electrolysis for 12 hours. After the electrolysis was stopped, the electrolyte solution was left to stand overnight, then suction filtered with a Buchner funnel, the filtrate was collected, rinsed twice with water and ethanol, dried in vacuum at 70°C, and the dried solid was ground in a quartz mortar to obtain Black nano manganese dioxide powder prepared by electrolysis. Weighing, productive rate is 90%, and product purity is 95%, and 100 order product indexs are 85%, are contained in sealing bag. The collected filtrate is then subjected to electrolysis.
上述说明是针对本发明可行实施例的详细说明,但实施例并非用以限定本发明的专利申请范围,凡本发明所提示的技术精神下所完成的同等变化或修饰变更,均应属于本发明所涵盖的专利范围。The above description is a detailed description of the feasible embodiments of the present invention, but the embodiments are not used to limit the scope of the patent application of the present invention. All equivalent changes or modifications made under the technical spirit suggested by the present invention shall belong to the present invention The scope of patents covered.
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