CN104276631B - A kind of iron scale basal granule sub-electrode and preparation method thereof - Google Patents
A kind of iron scale basal granule sub-electrode and preparation method thereof Download PDFInfo
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 38
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 11
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- 239000008187 granular material Substances 0.000 title claims 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims abstract description 138
- 239000002245 particle Substances 0.000 claims abstract description 74
- 239000012190 activator Substances 0.000 claims abstract description 12
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 12
- 239000002994 raw material Substances 0.000 claims abstract description 12
- 235000012054 meals Nutrition 0.000 claims description 16
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 10
- 239000007772 electrode material Substances 0.000 claims description 10
- 229920002037 poly(vinyl butyral) polymer Polymers 0.000 claims description 10
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 10
- 239000004570 mortar (masonry) Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 7
- 229920002472 Starch Polymers 0.000 claims description 6
- 235000019698 starch Nutrition 0.000 claims description 6
- 239000008107 starch Substances 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 239000004793 Polystyrene Substances 0.000 claims description 4
- 229920002223 polystyrene Polymers 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 2
- 229920000265 Polyparaphenylene Polymers 0.000 claims 1
- -1 polyphenylene Polymers 0.000 claims 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims 1
- 229920002554 vinyl polymer Polymers 0.000 claims 1
- 239000002440 industrial waste Substances 0.000 abstract description 2
- 239000002910 solid waste Substances 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract 2
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 9
- 239000012535 impurity Substances 0.000 description 8
- 238000002791 soaking Methods 0.000 description 8
- 238000005406 washing Methods 0.000 description 8
- 238000001816 cooling Methods 0.000 description 7
- 238000004043 dyeing Methods 0.000 description 7
- 230000005611 electricity Effects 0.000 description 7
- 230000000630 rising effect Effects 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000005242 forging Methods 0.000 description 2
- 238000005098 hot rolling Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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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
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
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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
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46133—Electrodes characterised by the material
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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
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46152—Electrodes characterised by the shape or form
- C02F2001/46157—Perforated or foraminous electrodes
- C02F2001/46161—Porous electrodes
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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
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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- Processing Of Solid Wastes (AREA)
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Abstract
本发明涉及一种三维电极反应器的氧化铁皮基粒子电极及其制备方法:由氧化铁皮、页岩、成孔剂、活化剂组成,按重量百分比计,干燥细氧化铁皮颗粒为50-60%、干燥细页岩为10-20%、成孔剂为10-20%、活化剂为10-20%。本发明以氧化铁皮为原料制备粒子电极,开辟了氧化铁皮应用的新途径,实现了最大限度地回收利用工业废弃物,提高了氧化铁皮的综合利用水平,有利于我国工业的可持续发展,对于我国实现固体废弃物“无害化,减量化,资源化”具有现实意义。The invention relates to an iron oxide sheet-based particle electrode for a three-dimensional electrode reactor and a preparation method thereof: it is composed of iron oxide sheet, shale, a pore-forming agent and an activator, and the dry fine iron sheet particle is 50-60% by weight percentage 10-20% dry fine shale, 10-20% pore-forming agent, and 10-20% activator. The present invention uses iron oxide scale as a raw material to prepare particle electrodes, opens up a new way for the application of iron oxide scale, realizes the maximum recycling of industrial waste, improves the comprehensive utilization level of iron oxide scale, and is beneficial to the sustainable development of my country's industry. It is of practical significance for our country to realize the "harmless, reduction, and recycling" of solid waste.
Description
技术领域 technical field
本发明属于废水处理技术领域,特别涉及一种用于处理城市污水中难降解有机物的氧化铁皮基粒子电极及其制备方法。 The invention belongs to the technical field of wastewater treatment, and in particular relates to an iron oxide skin-based particle electrode for treating refractory organic matter in urban sewage and a preparation method thereof.
背景技术 Background technique
氧化铁皮是在钢材锻造和热轧热加工时,由于钢铁和空气中氧的反应形成的。如果对这些资源合理利用,可以降低生产成本,同时可以起到环保节能作用。氧化铁皮的主要成分是Fe2O3、Fe3O4和FeO,这些氧化物恰恰也是粒子电极制备的活化促进成分。因此利用氧化铁皮中的这些可利用氧化物来合成高效、环保的粒子电极,用于处理城市污水,可使氧化铁皮得到有效利用,从而达到“以废治废”的目的,获得良好的经济效益。 Iron oxide scale is formed by the reaction of steel and oxygen in the air during forging and hot rolling of steel. If these resources are used rationally, production costs can be reduced, and at the same time, environmental protection and energy saving can be played. The main components of iron oxide scale are Fe 2 O 3 , Fe 3 O 4 and FeO, and these oxides are precisely the activation-promoting components for particle electrode preparation. Therefore, using these available oxides in iron oxide scales to synthesize efficient and environmentally friendly particle electrodes for the treatment of urban sewage can make effective use of iron oxide scales, so as to achieve the purpose of "treating waste with waste" and obtain good economic benefits. .
发明内容 Contents of the invention
本发明的目的是以氧化铁皮为基质,提供一种氧化铁皮基粒子电极及其制备方法。本发明所提供的粒子电极材料作为三维电极反应器的工作电极,可有效降解废水中的有机物,且电流效率高,能耗低。 The object of the present invention is to provide an iron oxide scale-based particle electrode and a preparation method thereof with the iron oxide scale as the substrate. The particle electrode material provided by the invention is used as a working electrode of a three-dimensional electrode reactor, can effectively degrade organic matter in waste water, and has high current efficiency and low energy consumption.
一种氧化铁皮基粒子电极,按照重量百分比计,干燥细氧化铁皮颗粒占50-60%、干燥细页岩占10-20%、成孔剂占10-20%、活化剂占10-20%。 An iron oxide scale-based particle electrode, in terms of weight percentage, dry fine iron oxide scale particles account for 50-60%, dry fine shale accounts for 10-20%, pore-forming agent accounts for 10-20%, and activator accounts for 10-20% .
所述成孔剂可以是炭粉、锯末屑、淀粉、聚乙烯醇(PVA)、聚乙烯醇缩丁醛(PVB)、聚苯乙烯颗粒中的一种。 The pore-forming agent may be one of carbon powder, sawdust, starch, polyvinyl alcohol (PVA), polyvinyl butyral (PVB), and polystyrene particles.
所述活化剂可以是Fe3O4、Fe2O3、MnO2、ZnO中的一种。 The activator may be one of Fe 3 O 4 , Fe 2 O 3 , MnO 2 , and ZnO.
所述氧化铁皮是在钢材锻造和热轧热加工时,由于钢铁和空气中氧的反应形成的,其主要成分是Fe2O3、Fe3O4和FeO,是一种工业废弃物。 The iron oxide scale is formed by the reaction of steel and oxygen in the air during steel forging and hot rolling, and its main components are Fe 2 O 3 , Fe 3 O 4 and FeO, which is a kind of industrial waste.
上述氧化铁皮基粒子电极的制备方法,包括如下步骤: The preparation method of the above-mentioned iron oxide skin-based particle electrode comprises the following steps:
A、氧化铁皮颗粒于球磨机中球磨,取出后洗涤、浸泡(洗涤、浸泡的目的在于解吸杂质),于烘箱内120℃下烘干,然后过60目筛,取干燥细氧化铁皮颗粒备用; A. The iron oxide scale particles are ball milled in a ball mill, washed and soaked after being taken out (the purpose of washing and soaking is to desorb impurities), dried in an oven at 120°C, and then passed through a 60-mesh sieve to take dry fine iron oxide scale particles for later use;
B、页岩放于烘箱内120℃烘干,将烘干的页岩在研钵中粉碎,然后过60目筛,取干燥细页岩备用; B. Put the shale in an oven to dry at 120°C, crush the dried shale in a mortar, pass through a 60-mesh sieve, and take the dried fine shale for later use;
C、将步骤A中的干燥细氧化铁皮颗粒、步骤B中的干燥细页岩、成孔剂和活化剂按照一定的重量百分比,混合并搅拌均匀,挤压成生料球; C. Mix and stir the dry fine iron scale particles in step A, dry fine shale in step B, pore-forming agent and activator according to a certain weight percentage, and extrude them into raw material balls;
D、将步骤C中的生料球在烘箱中120℃下烘24小时; D. Bake the raw meal balls in step C at 120°C in an oven for 24 hours;
E、将步骤D中烘干后的生料球,置于高温炉中从室温以120℃/h升至300℃,加热2h,然后以60℃/h升至550℃,活化10-30min,再以300℃/h升至1050℃焙烧10-30min,自然冷却至室温,得到氧化铁皮基粒子电极材料。 E. Put the raw material balls dried in step D in a high-temperature furnace from room temperature at 120°C/h to 300°C, heat for 2 hours, then rise at 60°C/h to 550°C, activate for 10-30min, Then heat it up to 1050°C at 300°C/h and bake for 10-30min, then cool down to room temperature naturally to obtain the iron oxide skin-based particle electrode material.
按照重量百分比计,干燥细氧化铁皮颗粒占50-60%、干燥细页岩占10-20%、成孔剂占10-20%、活化剂占10-20%。 In terms of weight percentage, dry fine iron oxide scale particles account for 50-60%, dry fine shale accounts for 10-20%, pore forming agent accounts for 10-20%, and activator accounts for 10-20%.
所述成孔剂可以是炭粉、锯末屑、淀粉、聚乙烯醇(PVA)、聚乙烯醇缩丁醛(PVB)、聚苯乙烯颗粒中的一种。 The pore-forming agent may be one of carbon powder, sawdust, starch, polyvinyl alcohol (PVA), polyvinyl butyral (PVB), and polystyrene particles.
所述活化剂可以是Fe3O4、Fe2O3、MnO2、ZnO中的一种。 The activator may be one of Fe 3 O 4 , Fe 2 O 3 , MnO 2 , and ZnO.
通过上述制备方法制备的氧化铁皮基粒子电极,取固体废弃物氧化铁皮为原料。氧化铁皮中含有多种氧化物,其中Fe2O3、Fe3O4和FeO的含量较高,这些氧化物恰恰也是粒子电极制备的活化促进剂成分。氧化铁皮基粒子电极颗粒表面粗燥,对废水中的污染物质具有较好的吸附、去除作用。而且,氧化铁皮的堆放不仅需要资金和大面积堆场,而且污染环境。利用氧化铁皮制作三维电极用的粒子催化电极,可以变废为宝,减少环境的污染、解决土地的占用等问题。 The iron oxide sheet-based particle electrode prepared by the above preparation method takes solid waste iron oxide sheet as a raw material. Iron oxide scale contains many kinds of oxides, among which the content of Fe 2 O 3 , Fe 3 O 4 and FeO is relatively high, and these oxides are precisely the components of activation promoters for the preparation of particle electrodes. Iron oxide skin-based particle electrode particles have a rough surface, which has a good adsorption and removal effect on pollutants in wastewater. Moreover, the stacking of iron oxide scales not only requires capital and a large area of stockpiles, but also pollutes the environment. Utilizing iron oxide sheets to make particle catalytic electrodes for three-dimensional electrodes can turn waste into treasure, reduce environmental pollution, and solve land occupation problems.
本发明提供的氧化铁皮基粒子电极及其制备方法,符合当前国家节能减排的环保政策。制备的粒子电极多孔,且孔径大,具有很大的比表面积、很强的吸附性能、良好的导电性和催化性能是一种新型高效的粒子电极。 The iron oxide skin-based particle electrode and the preparation method thereof provided by the invention comply with the current national environmental protection policy of energy conservation and emission reduction. The prepared particle electrode is porous and has a large pore size, has a large specific surface area, strong adsorption performance, good conductivity and catalytic performance, and is a new type of high-efficiency particle electrode.
以下结合具体实施方式对本发明作进一步说明。 The present invention will be further described below in combination with specific embodiments.
具体实施方式 detailed description
实施例一: Embodiment one:
A、氧化铁皮颗粒于球磨机中球磨,取出后洗涤、浸泡(洗涤、浸泡的目的在于解吸杂质),于烘箱内120℃下烘干,然后过60目筛,取干燥细氧化铁皮颗粒备用; A. The iron oxide scale particles are ball milled in a ball mill, washed and soaked after being taken out (the purpose of washing and soaking is to desorb impurities), dried in an oven at 120°C, and then passed through a 60-mesh sieve to take dry fine iron oxide scale particles for later use;
B、页岩放于烘箱内120℃烘干,将烘干的页岩在研钵中粉碎,然后过60目筛,取干燥细页岩备用; B. Put the shale in an oven to dry at 120°C, crush the dried shale in a mortar, pass through a 60-mesh sieve, and take the dried fine shale for later use;
C、将步骤A中的干燥细氧化铁皮颗粒、步骤B中的干燥细页岩、炭粉和Fe3O4按照50%:20%:20%:10%的重量百分比,混合并搅拌均匀,挤压成生料球; C, the dry fine iron scale particles in step A, the dry fine shale in step B, carbon powder and Fe 3 O 4 are mixed and stirred evenly according to the weight percentage of 50%:20%:20%:10%, Extruded into raw material balls;
D、将步骤C中的生料球在烘箱中120℃下烘24小时; D. Bake the raw meal balls in step C at 120°C in an oven for 24 hours;
E、将步骤D中烘干后的生料球,置于高温炉中从室温以120℃/h升至300℃,加热2h,然后以60℃/h升至550℃,活化20min,再以300℃/h升至1050℃焙烧30min,自然冷却至室温,得到氧化铁皮基粒子电极材料。 E. Put the raw meal balls dried in step D in a high-temperature furnace from room temperature at 120°C/h to 300°C, heat for 2 hours, then rise at 60°C/h to 550°C, activate for 20 minutes, and then 300°C/h rising to 1050°C for 30min, then naturally cooling to room temperature to obtain the iron oxide skin-based particle electrode material.
取上述实施例中制备的氧化铁皮基粒子电极5.0g,填充于反应器中,制得三维电极反应器,在电压为6.0V,电流为0.2A时,通电降解30ml印染废水45min,CODcr去除率达到95%。 Take 5.0 g of the iron oxide sheet-based particle electrode prepared in the above example, fill it in the reactor, and make a three-dimensional electrode reactor. When the voltage is 6.0V and the current is 0.2A, 30ml of printing and dyeing wastewater is degraded by electricity for 45min, and the removal rate of CODcr Reach 95%.
实施例二: Embodiment two:
A、氧化铁皮颗粒于球磨机中球磨,取出后洗涤、浸泡(洗涤、浸泡的目的在于解吸杂质),于烘箱内120℃下烘干,然后过60目筛,取干燥细氧化铁皮颗粒备用; A. The iron oxide scale particles are ball milled in a ball mill, washed and soaked after being taken out (the purpose of washing and soaking is to desorb impurities), dried in an oven at 120°C, and then passed through a 60-mesh sieve to take dry fine iron oxide scale particles for later use;
B、页岩放于烘箱内120℃烘干,将烘干的页岩在研钵中粉碎,然后过60目筛,取干燥细页岩备用; B. Put the shale in an oven to dry at 120°C, crush the dried shale in a mortar, pass through a 60-mesh sieve, and take the dried fine shale for later use;
C、将步骤A中的干燥细氧化铁皮颗粒、步骤B中的干燥细页岩、锯末屑和Fe2O3按照55%:15%:15%:15%的重量百分比,混合并搅拌均匀,挤压成生料球; C, the dry fine iron scale particles in step A, the dry fine shale in step B, sawdust and Fe 2 O 3 are mixed and stirred evenly according to the weight percentage of 55%:15%:15%:15%, Extruded into raw material balls;
D、将步骤C中的生料球在烘箱中120℃下烘24小时; D. Bake the raw meal balls in step C at 120°C in an oven for 24 hours;
E、将步骤D中烘干后的生料球,置于高温炉中从室温以120℃/h升至300℃,加热2h,然后以60℃/h升至550℃,活化20min,再以300℃/h升至1050℃焙烧30min,自然冷却至室温,得到氧化铁皮基粒子电极材料。 E. Put the raw meal balls dried in step D in a high-temperature furnace from room temperature at 120°C/h to 300°C, heat for 2 hours, then rise at 60°C/h to 550°C, activate for 20 minutes, and then 300°C/h rising to 1050°C for 30min, then naturally cooling to room temperature to obtain the iron oxide skin-based particle electrode material.
取上述实施例中制备的氧化铁皮基粒子电极5.0g,填充于反应器中,制得三维电极反应器,在电压为6.0V,电流为0.2A时,通电降解30ml印染废水45min,CODcr去除率达到94%。 Take 5.0 g of the iron oxide sheet-based particle electrode prepared in the above example, fill it in the reactor, and make a three-dimensional electrode reactor. When the voltage is 6.0V and the current is 0.2A, 30ml of printing and dyeing wastewater is degraded by electricity for 45min, and the removal rate of CODcr Reached 94%.
实施例三: Embodiment three:
A、氧化铁皮颗粒于球磨机中球磨,取出后洗涤、浸泡(洗涤、浸泡的目的在于解吸杂质),于烘箱内120℃下烘干,然后过60目筛,取干燥细氧化铁皮颗粒备用; A. The iron oxide scale particles are ball milled in a ball mill, washed and soaked after being taken out (the purpose of washing and soaking is to desorb impurities), dried in an oven at 120°C, and then passed through a 60-mesh sieve to take dry fine iron oxide scale particles for later use;
B、页岩放于烘箱内120℃烘干,将烘干的页岩在研钵中粉碎,然后过60目筛,取干燥细页岩备用; B. Put the shale in an oven to dry at 120°C, crush the dried shale in a mortar, pass through a 60-mesh sieve, and take the dried fine shale for later use;
C、将步骤A中的干燥细氧化铁皮颗粒、步骤B中的干燥细页岩、淀粉和MnO2按照60%:15%:15%:10%的重量百分比,混合并搅拌均匀,挤压成生料球; C, the dry fine iron scale particles in step A, the dry fine shale in step B, starch and MnO According to the percentage by weight of 60%: 15%: 15%: 10%, mix and stir, extrude into raw material ball;
D、将步骤C中的生料球在烘箱中120℃下烘24小时; D. Bake the raw meal balls in step C at 120°C in an oven for 24 hours;
E、将步骤D中烘干后的生料球,置于高温炉中从室温以120℃/h升至300℃,加热2h,然后以60℃/h升至550℃,活化20min,再以300℃/h升至1050℃焙烧30min,自然冷却至室温,得到氧化铁皮基粒子电极材料。 E. Put the raw meal balls dried in step D in a high-temperature furnace from room temperature at 120°C/h to 300°C, heat for 2 hours, then rise at 60°C/h to 550°C, activate for 20 minutes, and then 300°C/h rising to 1050°C for 30min, then naturally cooling to room temperature to obtain the iron oxide skin-based particle electrode material.
取上述实施例中制备的氧化铁皮基粒子电极5.0g,填充于反应器中,制得三维电极反应器,在电压为6.0V,电流为0.2A时,通电降解30ml印染废水45min,CODcr去除率达到94%。 Take 5.0 g of the iron oxide sheet-based particle electrode prepared in the above example, fill it in the reactor, and make a three-dimensional electrode reactor. When the voltage is 6.0V and the current is 0.2A, 30ml of printing and dyeing wastewater is degraded by electricity for 45min, and the removal rate of CODcr Reached 94%.
实施例四: Embodiment four:
A、氧化铁皮颗粒于球磨机中球磨,取出后洗涤、浸泡(洗涤、浸泡的目的在于解吸杂质),于烘箱内120℃下烘干,然后过60目筛,取干燥细氧化铁皮颗粒备用; A. The iron oxide scale particles are ball milled in a ball mill, washed and soaked after being taken out (the purpose of washing and soaking is to desorb impurities), dried in an oven at 120°C, and then passed through a 60-mesh sieve to take dry fine iron oxide scale particles for later use;
B、页岩放于烘箱内120℃烘干,将烘干的页岩在研钵中粉碎,然后过60目筛,取干燥细页岩备用; B. Put the shale in an oven to dry at 120°C, crush the dried shale in a mortar, pass through a 60-mesh sieve, and take the dried fine shale for later use;
C、将步骤A中的干燥细氧化铁皮颗粒、步骤B中的干燥细页岩、淀粉和MnO2按照60%:10%:10%:20%的重量百分比,混合并搅拌均匀,挤压成生料球; C, dry fine iron oxide scale particles in step A, dry fine shale in step B, starch and MnO According to the percentage by weight of 60%: 10%: 10%: 20%, mix and stir, extrude into raw material ball;
D、将步骤C中的生料球在烘箱中120℃下烘24小时; D. Bake the raw meal balls in step C at 120°C in an oven for 24 hours;
E、将步骤D中烘干后的生料球,置于高温炉中从室温以120℃/h升至300℃,加热2h,然后以60℃/h升至550℃,活化20min,再以300℃/h升至1050℃焙烧30min,自然冷却至室温,得到氧化铁皮基粒子电极材料。 E. Put the raw meal balls dried in step D in a high-temperature furnace from room temperature at 120°C/h to 300°C, heat for 2 hours, then rise at 60°C/h to 550°C, activate for 20 minutes, and then 300°C/h rising to 1050°C for 30min, then naturally cooling to room temperature to obtain the iron oxide skin-based particle electrode material.
取上述实施例中制备的氧化铁皮基粒子电极5.0g,填充于反应器中,制得三维电极反应器,在电压为6.0V,电流为0.2A时,通电降解30ml印染废水45min,CODcr去除率达到96%。 Take 5.0 g of the iron oxide sheet-based particle electrode prepared in the above example, fill it in the reactor, and make a three-dimensional electrode reactor. When the voltage is 6.0V and the current is 0.2A, 30ml of printing and dyeing wastewater is degraded by electricity for 45min, and the removal rate of CODcr Reached 96%.
实施例五: Embodiment five:
A、氧化铁皮颗粒于球磨机中球磨,取出后洗涤、浸泡(洗涤、浸泡的目的在于解吸杂质),于烘箱内120℃下烘干,然后过60目筛,取干燥细氧化铁皮颗粒备用; A. The iron oxide scale particles are ball milled in a ball mill, washed and soaked after being taken out (the purpose of washing and soaking is to desorb impurities), dried in an oven at 120°C, and then passed through a 60-mesh sieve to take dry fine iron oxide scale particles for later use;
B、页岩放于烘箱内120℃烘干,将烘干的页岩在研钵中粉碎,然后过60目筛,取干燥细页岩备用; B. Put the shale in an oven to dry at 120°C, crush the dried shale in a mortar, pass through a 60-mesh sieve, and take the dried fine shale for later use;
C、将步骤A中的干燥细氧化铁皮颗粒、步骤B中的干燥细页岩、聚乙烯醇(PVA)和ZnO按照55%:15%:20%:10%的重量百分比,混合并搅拌均匀,挤压成生料球; C. Mix and stir the dry fine iron scale particles in step A, the dry fine shale in step B, polyvinyl alcohol (PVA) and ZnO according to the weight percentage of 55%:15%:20%:10%. , extruded into raw material balls;
D、将步骤C中的生料球在烘箱中120℃下烘24小时; D. Bake the raw meal balls in step C at 120°C in an oven for 24 hours;
E、将步骤D中烘干后的生料球,置于高温炉中从室温以120℃/h升至300℃,加热2h,然后以60℃/h升至550℃,活化20min,再以300℃/h升至1050℃焙烧30min,自然冷却至室温,得到氧化铁皮基粒子电极材料。 E. Put the raw meal balls dried in step D in a high-temperature furnace from room temperature at 120°C/h to 300°C, heat for 2 hours, then rise at 60°C/h to 550°C, activate for 20 minutes, and then 300°C/h rising to 1050°C for 30min, then naturally cooling to room temperature to obtain the iron oxide skin-based particle electrode material.
取上述实施例中制备的氧化铁皮基粒子电极5.0g,填充于反应器中,制得三维电极反应器,在电压为6.0V,电流为0.2A时,通电降解30ml印染废水45min,CODcr去除率达到96%。 Take 5.0 g of the iron oxide sheet-based particle electrode prepared in the above example, fill it in the reactor, and make a three-dimensional electrode reactor. When the voltage is 6.0V and the current is 0.2A, 30ml of printing and dyeing wastewater is degraded by electricity for 45min, and the removal rate of CODcr Reached 96%.
实施例六: Embodiment six:
A、氧化铁皮颗粒于球磨机中球磨,取出后洗涤、浸泡(洗涤、浸泡的目的在于解吸杂质),于烘箱内120℃下烘干,然后过60目筛,取干燥细氧化铁皮颗粒备用; A. The iron oxide scale particles are ball milled in a ball mill, washed and soaked after being taken out (the purpose of washing and soaking is to desorb impurities), dried in an oven at 120°C, and then passed through a 60-mesh sieve to take dry fine iron oxide scale particles for later use;
B、页岩放于烘箱内120℃烘干,将烘干的页岩在研钵中粉碎,然后过60目筛,取干燥细页岩备用; B. Put the shale in an oven to dry at 120°C, crush the dried shale in a mortar, pass through a 60-mesh sieve, and take the dried fine shale for later use;
C、将步骤A中的干燥细氧化铁皮颗粒、步骤B中的干燥细页岩、聚乙烯醇缩丁醛(PVB)和ZnO按照55%:15%:20%:10%的重量百分比,混合并搅拌均匀,挤压成生料球; C, the dry fine iron scale particles in step A, the dry fine shale in step B, polyvinyl butyral (PVB) and ZnO are mixed according to the weight percentage of 55%:15%:20%:10%. And stir evenly, extrude into raw material ball;
D、将步骤C中的生料球在烘箱中120℃下烘24小时; D. Bake the raw meal balls in step C at 120°C in an oven for 24 hours;
E、将步骤D中烘干后的生料球,置于高温炉中从室温以120℃/h升至300℃,加热2h,然后以60℃/h升至550℃,活化20min,再以300℃/h升至1050℃焙烧30min,自然冷却至室温,得到氧化铁皮基粒子电极材料。 E. Put the raw meal balls dried in step D in a high-temperature furnace from room temperature at 120°C/h to 300°C, heat for 2 hours, then rise at 60°C/h to 550°C, activate for 20 minutes, and then 300°C/h rising to 1050°C for 30min, then naturally cooling to room temperature to obtain the iron oxide skin-based particle electrode material.
取上述实施例中制备的氧化铁皮基粒子电极5.0g,填充于反应器中,制得三维电极反应器,在电压为6.0V,电流为0.2A时,通电降解30ml印染废水45min,CODcr去除率达到97%。 Take 5.0 g of the iron oxide sheet-based particle electrode prepared in the above example, fill it in the reactor, and make a three-dimensional electrode reactor. When the voltage is 6.0V and the current is 0.2A, 30ml of printing and dyeing wastewater is degraded by electricity for 45min, and the removal rate of CODcr Reached 97%.
实施例七: Embodiment seven:
A、氧化铁皮颗粒于球磨机中球磨,取出后洗涤、浸泡(洗涤、浸泡的目的在于解吸杂质),于烘箱内120℃下烘干,然后过60目筛,取干燥细氧化铁皮颗粒备用; A. The iron oxide scale particles are ball milled in a ball mill, washed and soaked after being taken out (the purpose of washing and soaking is to desorb impurities), dried in an oven at 120°C, and then passed through a 60-mesh sieve to take dry fine iron oxide scale particles for later use;
B、页岩放于烘箱内120℃烘干,将烘干的页岩在研钵中粉碎,然后过60目筛,取干燥细页岩备用; B. Put the shale in an oven to dry at 120°C, crush the dried shale in a mortar, pass through a 60-mesh sieve, and take the dried fine shale for later use;
C、将步骤A中的干燥细氧化铁皮颗粒、步骤B中的干燥细页岩、聚苯乙烯和ZnO按照55%:10%:15%:20%的重量百分比,混合并搅拌均匀,挤压成生料球; C. Mix and stir the dry fine iron scale particles in step A, the dry fine shale in step B, polystyrene and ZnO according to the weight percentage of 55%:10%:15%:20%, and extrude into raw material balls;
D、将步骤C中的生料球在烘箱中120℃下烘24小时; D. Bake the raw meal balls in step C at 120°C in an oven for 24 hours;
E、将步骤D中烘干后的生料球,置于高温炉中从室温以120℃/h升至300℃,加热2h,然后以60℃/h升至550℃,活化20min,再以300℃/h升至1050℃焙烧30min,自然冷却至室温,得到氧化铁皮基粒子电极材料。 E. Put the raw meal balls dried in step D in a high-temperature furnace from room temperature at 120°C/h to 300°C, heat for 2 hours, then rise at 60°C/h to 550°C, activate for 20 minutes, and then 300°C/h rising to 1050°C for 30min, then naturally cooling to room temperature to obtain the iron oxide skin-based particle electrode material.
取上述实施例中制备的氧化铁皮基粒子电极5.0g,填充于反应器中,制得三维电极反应器,在电压为6.0V,电流为0.2A时,通电降解30ml印染废水45min,CODcr去除率达到94%。 Take 5.0 g of the iron oxide sheet-based particle electrode prepared in the above example, fill it in the reactor, and make a three-dimensional electrode reactor. When the voltage is 6.0V and the current is 0.2A, 30ml of printing and dyeing wastewater is degraded by electricity for 45min, and the removal rate of CODcr Reached 94%.
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CN102001737A (en) * | 2010-10-26 | 2011-04-06 | 中山大学 | Electrocatalysis particle for treating cyanide-containing waste water and method for treating cyanide-containing waste water |
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