CN118878022A - A highly robust self-supporting three-dimensional porous anode and its preparation method and application - Google Patents
A highly robust self-supporting three-dimensional porous anode and its preparation method and application Download PDFInfo
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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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- 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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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
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- 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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- C02F2101/345—Phenols
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- C02F2101/36—Organic compounds containing halogen
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- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F2101/38—Organic compounds containing nitrogen
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F2101/40—Organic compounds containing sulfur
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Abstract
本发明涉及一种高鲁棒性自支撑三维多孔阳极及其制备方法和应用。以电催化活性物质为基础,以工程纤维为造孔剂,通过压制成形和热处理工艺制备而得。以简单的工艺获得高鲁棒性自支撑三维多孔阳极,可高效、快速、稳定地电催化氧化去除有机污染物,利于产业上大规模生产和应用。The present invention relates to a highly robust self-supporting three-dimensional porous anode and a preparation method and application thereof. The anode is prepared by pressing and heat treatment processes based on electrocatalytic active substances and using engineering fibers as pore-forming agents. The highly robust self-supporting three-dimensional porous anode is obtained by a simple process, and can efficiently, quickly and stably electrocatalytically oxidize and remove organic pollutants, which is conducive to large-scale production and application in the industry.
Description
技术领域Technical Field
本发明涉及阳极及其制备方法和应用,属于电催化氧化领域。The invention relates to an anode and a preparation method and application thereof, and belongs to the field of electrocatalytic oxidation.
背景技术Background Art
在电催化氧化去除持久性有机污染物的过程中,阳极催化电极的性能决定了污染物的氧化去除效果。目前基于电催化活性物质粉体阳极有两种制备方法:以平板基底涂覆粉体催化剂的平面结构阳极和将粉体压片烧制成自支撑的三维结构阳极。与平面结构阳极相比,自支撑三维阳极具有成分简单、结构均一、富含多孔等优势,更有利于电化学氧化反应的快速、稳定进行。在自支撑三维阳极的制备过程中使用造孔剂可在其内部和表面造孔,提高自支撑三维阳极的比表面积和暴露的活性位点数量,从而加快污染物在孔道内的迁移和氧化降解。热解温度不仅影响造孔剂和粘结剂在最终材料中的存在,还影响电催化活性物质颗粒之间的烧结效果。因此,造孔剂和热解温度的选择对最终形成的自支撑三维阳极的结构和性能具有重要的影响。In the process of electrocatalytic oxidation to remove persistent organic pollutants, the performance of the anode catalytic electrode determines the oxidation removal effect of pollutants. At present, there are two preparation methods based on electrocatalytic active material powder anode: a planar structure anode coated with a flat substrate powder catalyst and a self-supporting three-dimensional structure anode sintered by pressing the powder into a tablet. Compared with the planar structure anode, the self-supporting three-dimensional anode has the advantages of simple composition, uniform structure, and rich porosity, which is more conducive to the rapid and stable electrochemical oxidation reaction. In the preparation process of the self-supporting three-dimensional anode, the use of pore-forming agents can form pores inside and on the surface of the self-supporting three-dimensional anode, increase the specific surface area of the self-supporting three-dimensional anode and the number of exposed active sites, thereby accelerating the migration and oxidative degradation of pollutants in the pores. The pyrolysis temperature not only affects the presence of pore-forming agents and binders in the final material, but also affects the sintering effect between the particles of the electrocatalytic active material. Therefore, the selection of pore-forming agents and pyrolysis temperature has an important influence on the structure and performance of the self-supporting three-dimensional anode finally formed.
目前常用的造孔剂有碳酸铵、碳酸氢铵、碳纤维、淀粉等。然而碳酸铵和碳酸氢铵成分较复杂;碳纤维分解温度高,难以在较低温热解过程里完全去除;此类造孔剂容易残留元素形成杂质影响电极性能。而淀粉易发生溶胀,导致压制成型效果差,热解得到的电极片残缺甚至断裂,不利于规模化推广应用。Currently, commonly used pore-forming agents include ammonium carbonate, ammonium bicarbonate, carbon fiber, starch, etc. However, the composition of ammonium carbonate and ammonium bicarbonate is relatively complex; the decomposition temperature of carbon fiber is high, and it is difficult to completely remove it in the low-temperature pyrolysis process; such pore-forming agents are prone to residual elements to form impurities that affect electrode performance. Starch is prone to swelling, resulting in poor pressing and molding effects, and the electrode sheets obtained by pyrolysis are incomplete or even broken, which is not conducive to large-scale promotion and application.
工程纤维是以聚丙烯为主要成分的微米级合成纤维,常用在建筑工程中,成本低廉、来源广、易获得。且仅含有碳和氢元素,热分解温度低,且不与水反应,尚未有在精细合成领域中的应用报道。Engineering fiber is a micron-sized synthetic fiber with polypropylene as the main component. It is often used in construction projects. It is low-cost, widely available, and easy to obtain. It only contains carbon and hydrogen elements, has a low thermal decomposition temperature, and does not react with water. There are no reports on its application in the field of fine synthesis.
发明内容Summary of the invention
本发明的目的在于提供一种具有高机械强度和降解性能的高鲁棒性自支撑三维多孔阳极及其制备方法和应用。选用成本低、易获得的工程纤维作为新造孔剂,通过简易的合成工艺,获得高机械强度高鲁棒性能多孔阳极,解决现有三维多孔阳极机械强度低、降解效率低、稳定性差的问题,更利于实际生产上的广泛应用。The purpose of the present invention is to provide a highly robust self-supporting three-dimensional porous anode with high mechanical strength and degradation performance, and a preparation method and application thereof. Low-cost and easily available engineering fibers are selected as new pore-forming agents, and a porous anode with high mechanical strength and high robustness is obtained through a simple synthesis process, which solves the problems of low mechanical strength, low degradation efficiency and poor stability of existing three-dimensional porous anodes, and is more conducive to wide application in actual production.
根据本发明的第一个方面,本发明提供一种高鲁棒性自支撑三维多孔阳极,其特征在于,包括以下步骤:According to a first aspect of the present invention, the present invention provides a highly robust self-supporting three-dimensional porous anode, characterized in that it comprises the following steps:
步骤一:将电催化活性物质与造孔剂和粘结剂混合均匀,获得混合粉末;Step 1: uniformly mixing the electrocatalytic active material, the pore-forming agent and the binder to obtain a mixed powder;
步骤二:将步骤一中所得的混合粉末挤压成型为所需的形状,得到三维阳极前驱体;Step 2: Extruding the mixed powder obtained in step 1 into a desired shape to obtain a three-dimensional anode precursor;
步骤三:将步骤二中所得的阳极前驱体进行热解获得高鲁棒性自支撑三维多孔阳极。Step 3: Pyrolyze the anode precursor obtained in step 2 to obtain a highly robust self-supporting three-dimensional porous anode.
其中,所述步骤一中的造孔剂为工程纤维或工程纤维与其他造孔剂的组合。Wherein, the pore-forming agent in step 1 is engineering fiber or a combination of engineering fiber and other pore-forming agents.
优选地,所述的电催化活性物质为钛氧化物、锡氧化物、铅氧化物及其C、N、B、F、Ni、Fe、La、Cu、Ce、Nb掺杂物中的一种或几种的组合。Preferably, the electrocatalytically active material is one or a combination of titanium oxide, tin oxide, lead oxide and C, N, B, F, Ni, Fe, La, Cu, Ce, Nb dopants thereof.
优选地,所述粘结剂为石蜡、环糊精、壳聚糖、聚偏氟乙烯、甲基纤维素、海藻酸钠中的一种或几种的组合。Preferably, the binder is one or a combination of paraffin, cyclodextrin, chitosan, polyvinylidene fluoride, methyl cellulose, and sodium alginate.
优选地,所述步骤一中电催化活性物质与造孔剂的质量比为1:0.01~1:0.1。Preferably, in step 1, the mass ratio of the electrocatalytic active material to the pore-forming agent is 1:0.01 to 1:0.1.
优选地,所述步骤二中压制成形所需的压力为10~25bar,作用时间为5~30min。Preferably, the pressure required for the pressing and forming in step 2 is 10 to 25 bar, and the action time is 5 to 30 minutes.
优选地,所述步骤三中的热解气氛为空气,热解温度为400~1800℃,热解时间为1~12小时。Preferably, the pyrolysis atmosphere in step three is air, the pyrolysis temperature is 400 to 1800° C., and the pyrolysis time is 1 to 12 hours.
根据本发明的第二个方面,本发明提供一种高鲁棒性自支撑三维多孔阳极,其特征在于,其具有高机械强度,典型值为硬度和韧性高于150N,弹性大于0.7,内聚性大于0.9。According to a second aspect of the invention, the invention provides a highly robust self-supporting three-dimensional porous anode, characterized in that it has high mechanical strength, with typical values of hardness and toughness greater than 150N, elasticity greater than 0.7, and cohesion greater than 0.9.
根据本发明的第三个方面,本发明提供一种高鲁棒性自支撑三维多孔阳极在电催化氧化降解污染物方面的应用。According to a third aspect of the present invention, the present invention provides a highly robust self-supporting three-dimensional porous anode for use in electrocatalytic oxidation degradation of pollutants.
本发明的有益效果体现在:The beneficial effects of the present invention are embodied in:
(1)造孔剂成本低、易获得,同时合成工艺简单,利于规模化生产。相比碳纤维、果糖、淀粉等造孔剂,工程纤维的用量少,仅需电催化活性物质所用重量的1%~10%即可;且工程纤维的价格低,仅是相同重量的碳纤维造孔剂价格的十分之一,果糖的二分之一,因而更有利于推广应用。(1) Pore-forming agents are low-cost and easy to obtain, and the synthesis process is simple, which is conducive to large-scale production. Compared with pore-forming agents such as carbon fiber, fructose, and starch, the amount of engineering fiber used is small, only 1% to 10% of the weight of the electrocatalytic active material used; and the price of engineering fiber is low, only one-tenth of the price of the same weight of carbon fiber pore-forming agent and one-half of fructose, so it is more conducive to promotion and application.
(2)利用工程纤维特性,替代已有的造孔剂,可获得具有高机械强度和降解性能的高鲁棒性自支撑三维多孔阳极。其在常温常压下不发生吸湿,并可在三维阳极前驱体中形成乱向支撑体系,有效促进了热解所得电极的完整性。与之相比,果糖和淀粉容易发生吸湿,在普通空气中制备难以避免得到断裂破损的电极,不利于推广应用。而且,工程纤维热解温度较低(典型值不高于200℃),即使在较低温度热解(典型值为500~1000℃)也不会残留;而高热解温度(1100~1350oC)的碳纤维在同样低温度热解后,残留较多碳杂质,导致该法所得阳极材料在电催化氧化应用的能耗增加,不利于推广应用。此外,碳酸铵和碳酸氢铵含有的N元素,在热解过程中不仅导致含氮气体污染大气,还可能在电催化活性物质颗粒的浅表面形成掺杂,又在后续电催化氧化应用中容易溶出脱离,因此该法所得阳极材料在电催化氧化应用中的稳定性不足,不利于推广应用。(2) By utilizing the characteristics of engineering fibers to replace existing pore-forming agents, a highly robust self-supporting three-dimensional porous anode with high mechanical strength and degradation performance can be obtained. It does not absorb moisture at room temperature and pressure, and can form a random support system in the three-dimensional anode precursor, which effectively promotes the integrity of the electrode obtained by pyrolysis. In contrast, fructose and starch are prone to hygroscopicity, and it is difficult to avoid broken electrodes when prepared in ordinary air, which is not conducive to promotion and application. In addition, the pyrolysis temperature of engineering fibers is relatively low (typical value is not higher than 200°C), and no residue will remain even when pyrolyzed at a relatively low temperature (typical value is 500-1000°C); while carbon fibers with a high pyrolysis temperature (1100-1350oC) will leave more carbon impurities after pyrolysis at the same low temperature, resulting in an increase in the energy consumption of the anode material obtained by this method in electrocatalytic oxidation applications, which is not conducive to promotion and application. In addition, the N element contained in ammonium carbonate and ammonium bicarbonate not only causes nitrogen-containing gas to pollute the atmosphere during the pyrolysis process, but may also form doping on the shallow surface of the electrocatalytic active material particles, and is easily dissolved and detached in subsequent electrocatalytic oxidation applications. Therefore, the anode material obtained by this method is insufficiently stable in electrocatalytic oxidation applications, which is not conducive to its promotion and application.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为实施例1中制备的高鲁棒性自支撑三维多孔阳极的实物图Figure 1 is a physical picture of the highly robust self-supporting three-dimensional porous anode prepared in Example 1
图2为实施例1中制备的高鲁棒性自支撑三维多孔阳极的扫描电镜照片Figure 2 is a scanning electron microscope photo of the highly robust self-supporting three-dimensional porous anode prepared in Example 1
图3为实施例1中制备的自支撑三维多孔阳极的孔径分布图Figure 3 is a pore size distribution diagram of the self-supporting three-dimensional porous anode prepared in Example 1
图4为实施例1中制备的高鲁棒性三维多孔阳极的机械强度指标图FIG. 4 is a graph showing the mechanical strength index of the highly robust three-dimensional porous anode prepared in Example 1
图5为实施例1中制备的高鲁棒性三维多孔阳极的循环稳定性测试结果FIG5 is a cycle stability test result of the highly robust three-dimensional porous anode prepared in Example 1
图6为对比例2中制备的三维多孔阳极的扫描电镜照片Figure 6 is a scanning electron microscope photo of the three-dimensional porous anode prepared in Comparative Example 2
具体实施方式DETAILED DESCRIPTION
为使本发明的上述目的、特征和优点能够更加明显易懂,下面结合附图对本发明的具体实施方式做详细说明。以下内容仅是对本发明构思所做的举例和说明,所述本领域的技术人员对所描述的具体实施案例做各种修改或补充,或采用类似的方式代替,只要不偏离发明的构思或超越本权利要求书所定义的范围,均应属本发明的保护范围。In order to make the above-mentioned purposes, features and advantages of the present invention more obvious and easy to understand, the specific implementation methods of the present invention are described in detail below in conjunction with the accompanying drawings. The following content is only an example and explanation of the concept of the present invention. The technicians in the field may make various modifications or supplements to the specific implementation cases described, or replace them with similar methods, as long as they do not deviate from the concept of the invention or exceed the scope defined by the claims, they should all fall within the scope of protection of the present invention.
实施例1Example 1
三维多孔电催化阳极的制备过程,包括以下步骤:The preparation process of the three-dimensional porous electrocatalytic anode includes the following steps:
步骤一:在常温常压、空气条件下,采用涡旋混合器将1.2g SnO2-Sb纳米粉末与0.01g工程纤维和0.06g壳聚糖粉末使用涡旋混合器混合均匀,得到混合粉末;Step 1: Under normal temperature, pressure and air conditions, 1.2 g SnO 2 -Sb nanopowder, 0.01 g engineering fiber and 0.06 g chitosan powder were mixed evenly using a vortex mixer to obtain a mixed powder;
步骤二:将步骤一中所得的混合粉末均匀分布在模具内,将模具放置在压片机内,施加20bar的垂直压力,持续10min,得到成形的三维阳极前驱体;Step 2: evenly distribute the mixed powder obtained in step 1 in the mold, place the mold in a tablet press, apply a vertical pressure of 20 bar for 10 minutes, and obtain a formed three-dimensional anode precursor;
步骤三:将步骤二中所得的阳极前驱体在空气中经过1000℃热解12小时去除工程纤维和壳聚糖,获到高鲁棒性自支撑三维多孔阳极,其实物图如图1所示。Step 3: The anode precursor obtained in step 2 is pyrolyzed at 1000°C in air for 12 hours to remove the engineering fiber and chitosan, thereby obtaining a highly robust self-supporting three-dimensional porous anode, as shown in FIG1 .
本实施例中获得的高鲁棒性自支撑三维多孔阳极的扫描电镜照片如图2所示,其孔径分布如图3所示,机械强度指标如图4所示。该电催化阳极呈现深蓝色,为完整的圆盘形貌,直径2.5cm,厚度约1mm。该电极具有较丰富的中孔和大孔,平均孔径约为57nm。此外,该电极还具有高硬度、韧性、弹性和内聚性,各指标对应的数据分别为172.82、162.97、0.82和0.95,适合规模化生产。The scanning electron microscope photo of the highly robust self-supporting three-dimensional porous anode obtained in this embodiment is shown in Figure 2, its pore size distribution is shown in Figure 3, and the mechanical strength index is shown in Figure 4. The electrocatalytic anode is dark blue, with a complete disc morphology, a diameter of 2.5 cm, and a thickness of about 1 mm. The electrode has abundant mesopores and macropores, with an average pore size of about 57 nm. In addition, the electrode also has high hardness, toughness, elasticity and cohesion, and the data corresponding to each index are 172.82, 162.97, 0.82 and 0.95, respectively, which is suitable for large-scale production.
该三维多孔电催化阳极在降解污染物中的应用:Application of the three-dimensional porous electrocatalytic anode in pollutant degradation:
以本实施例中的自支撑三维多孔电极为阳极、铂片为阴极、银/氯化银电极为参比电极、0.1mol L-1Na2SO4为电解液,在单室电解槽中降解阿特拉津。图5为阿特拉津降解的循环稳定性测试结果。从图中可以看出,该高鲁棒性自支撑三维多孔阳极能够高效快速地降解阿特拉津,且具有较高的长期稳定性,有利于实际推广应用。The self-supporting three-dimensional porous electrode in this embodiment is used as the anode, the platinum sheet is used as the cathode, the silver/silver chloride electrode is used as the reference electrode, and 0.1 mol L -1 Na2SO4 is used as the electrolyte to degrade atrazine in a single-chamber electrolytic cell. FIG5 is the test result of the cyclic stability of atrazine degradation. It can be seen from the figure that the highly robust self-supporting three-dimensional porous anode can efficiently and quickly degrade atrazine, and has high long-term stability, which is conducive to practical promotion and application.
对比例1Comparative Example 1
与实施例1相比,使用碳酸氢铵作造孔剂,其他条件相同。在热解过程中碳酸氢铵造孔剂生成氨气逸出,容易造成大气污染。而且,碳酸氢铵中的氮元素在热解过程中极易在电催化活性物质颗粒的浅表面形成掺杂,又在后续电催化氧化应用中容易溶出脱离,因此所得阳极材料在电催化氧化应用中的稳定性不足。Compared with Example 1, ammonium bicarbonate is used as a pore-forming agent, and other conditions are the same. During the pyrolysis process, the ammonium bicarbonate pore-forming agent generates ammonia gas that escapes and easily causes air pollution. In addition, the nitrogen element in the ammonium bicarbonate is very easy to form doping on the shallow surface of the electrocatalytic active material particles during the pyrolysis process, and is easily dissolved and separated in subsequent electrocatalytic oxidation applications. Therefore, the stability of the obtained anode material in electrocatalytic oxidation applications is insufficient.
对比例2Comparative Example 2
与实施例1相比,使用碳纤维作造孔剂,其他条件相同。制备电极所需的热解温度需要高于1200℃才能完全去除碳纤维。图6为使用碳纤维造孔剂在800oC热解温度下所得电极的SEM图片。而且,该法制得电极的机械强度较低,其脆性差到无法用质构仪测得,且硬度、弹性和内聚性等指标分别为140.36,0.74和0.95,远远低于以工程纤维为造孔剂制备的电催化阳极。此外,其价格为同重量的工程纤维的十倍以上。因而使用工程纤维比用碳纤维作为造孔剂具有成本和机械强度优势。Compared with Example 1, carbon fiber is used as a pore former, and other conditions are the same. The pyrolysis temperature required for preparing the electrode needs to be higher than 1200°C to completely remove the carbon fiber. Figure 6 is a SEM image of the electrode obtained at a pyrolysis temperature of 800oC using a carbon fiber pore former. Moreover, the mechanical strength of the electrode prepared by this method is relatively low, and its brittleness is so poor that it cannot be measured by a texture analyzer, and the hardness, elasticity and cohesion indicators are 140.36, 0.74 and 0.95, respectively, which are much lower than the electrocatalytic anode prepared with engineering fiber as a pore former. In addition, its price is more than ten times that of engineering fiber of the same weight. Therefore, the use of engineering fiber has cost and mechanical strength advantages over using carbon fiber as a pore former.
对比例3Comparative Example 3
与实施例1相比,使用淀粉作造孔剂,其他条件相同。在步骤一混合过程中,淀粉在空气中直接制备易发生吸湿团聚现象,不利于造孔剂与电催化活性粉体材料和粘结剂的均匀分散,也不利于电极前驱体的稳定成型。因此使用工程纤维比用淀粉作为造孔剂具有制造条件要求较低的优势。Compared with Example 1, starch is used as a pore former, and other conditions are the same. In the mixing process of step 1, starch prepared directly in the air is prone to moisture absorption and agglomeration, which is not conducive to the uniform dispersion of the pore former and the electrocatalytic active powder material and the binder, and is not conducive to the stable molding of the electrode precursor. Therefore, the use of engineered fiber has the advantage of lower manufacturing conditions than using starch as a pore former.
实施例2Example 2
三维多孔电催化阳极的制备过程,包括以下步骤:The preparation process of the three-dimensional porous electrocatalytic anode includes the following steps:
步骤一:将1.2g PbO2纳米粉末与0.1g工程纤维和0.08g石蜡混合均匀,得到混合粉末;Step 1: Mix 1.2 g of PbO2 nanopowder, 0.1 g of engineering fiber and 0.08 g of paraffin wax to obtain a mixed powder;
步骤二:将步骤一中所得的混合粉末均匀分布在模具内,将模具放置在压片机内,施加10bar的垂直压力,持续30min,得到成形的三维阳极前驱体;Step 2: evenly distribute the mixed powder obtained in step 1 in the mold, place the mold in a tablet press, apply a vertical pressure of 10 bar for 30 minutes, and obtain a formed three-dimensional anode precursor;
步骤三:将步骤二中所得的阳极前驱体在空气中经过800℃高温热解12小时,获到高鲁棒性自支撑三维多孔阳极。Step 3: The anode precursor obtained in step 2 is pyrolyzed at 800° C. in air for 12 hours to obtain a highly robust self-supporting three-dimensional porous anode.
实施例3Example 3
三维多孔电催化阳极的制备过程,包括以下步骤:The preparation process of the three-dimensional porous electrocatalytic anode includes the following steps:
步骤一:将1.2g TiO2粉末与0.08g工程纤维和0.08g甲基纤维素混合均匀,得到混合粉末;Step 1: Mix 1.2 g TiO2 powder, 0.08 g engineering fiber and 0.08 g methyl cellulose to obtain a mixed powder;
步骤二:将步骤一中所得的混合粉末均匀分布在模具内,将模具放置在压片机内,施加25bar的垂直压力,持续5min,得到成形的三维阳极前驱体;Step 2: evenly distribute the mixed powder obtained in step 1 in the mold, place the mold in a tablet press, apply a vertical pressure of 25 bar for 5 minutes, and obtain a formed three-dimensional anode precursor;
步骤三:将步骤二中所得的阳极前驱体在空气中经过1800℃高温热解3小时,获到高鲁棒性自支撑三维多孔阳极。Step 3: The anode precursor obtained in step 2 is pyrolyzed at 1800° C. in air for 3 hours to obtain a highly robust self-supporting three-dimensional porous anode.
实施例4Example 4
三维多孔电催化阳极的制备过程,包括以下步骤:The preparation process of the three-dimensional porous electrocatalytic anode includes the following steps:
步骤一:在常温常压、空气条件下,将1.2g SnO2-F纳米粉末与0.12g工程纤维和0.03g环糊精混合均匀,得到混合粉末;Step 1: Under normal temperature, pressure and air conditions, 1.2 g SnO 2 -F nanopowder, 0.12 g engineering fiber and 0.03 g cyclodextrin were mixed evenly to obtain a mixed powder;
步骤二:将步骤一中所得的混合粉末均匀分布在模具内,将模具放置在压片机内,施加25bar的垂直压力,持续5min,得到成形的三维阳极前驱体;Step 2: evenly distribute the mixed powder obtained in step 1 in the mold, place the mold in a tablet press, apply a vertical pressure of 25 bar for 5 minutes, and obtain a formed three-dimensional anode precursor;
步骤三:将步骤二中所得的阳极前驱体在空气中经过400℃热解6小时,获到高鲁棒性自支撑三维多孔阳极。Step 3: Pyrolyze the anode precursor obtained in step 2 at 400°C in air for 6 hours to obtain a highly robust self-supporting three-dimensional porous anode.
实施例5Example 5
与实施例1相比,活性材料为B、N掺杂的TiO2纳米粉末,热解温度为1600oC。该三维多孔电催化阳极在单室电解槽中可在60分钟快速降解电解液中99.95%的左氧氟沙星。Compared with Example 1, the active material is B and N doped TiO2 nanopowder, and the pyrolysis temperature is 1600°C. The three-dimensional porous electrocatalytic anode can rapidly degrade 99.95% of levofloxacin in the electrolyte within 60 minutes in a single-chamber electrolytic cell.
实施例6Example 6
与实施例1相比,活性材料为La掺杂的TiO2纳米粉末,粘结剂为0.12g环糊精,热解温度为1300℃。该三维多孔电催化阳极在单室电解槽中可在60分钟内快速降解电解液中99.95%的双酚A。Compared with Example 1, the active material is La-doped TiO2 nanopowder, the binder is 0.12 g cyclodextrin, and the pyrolysis temperature is 1300° C. The three-dimensional porous electrocatalytic anode can rapidly degrade 99.95% of bisphenol A in the electrolyte within 60 minutes in a single-chamber electrolytic cell.
以上仅为本发明的示例性实施例,并不用于限制本发明,凡在本发明的精神和原则之内所做的任何修改,等同替换和改进等,均应包含在本发明的保护范围之内。The above are only exemplary embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent substitutions and improvements made within the spirit and principles of the present invention should be included in the protection scope of the present invention.
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CN104157885A (en) * | 2014-08-19 | 2014-11-19 | 大连理工大学 | Preparation method of solid oxide fuel cell electrode with high porosity amount and long tunnel |
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CN110205636A (en) * | 2019-04-22 | 2019-09-06 | 清华大学 | A kind of preparation method of self-cradling type three-dimensional porous structure double-function catalyzing electrode |
CN113293312A (en) * | 2021-05-21 | 2021-08-24 | 中南大学 | Preparation method of composite porous electrode material for lithium extraction |
CN117303512A (en) * | 2023-10-07 | 2023-12-29 | 中国科学院城市环境研究所 | A self-supporting three-dimensional porous electrocatalytic anode and its preparation method and application |
CN117626308A (en) * | 2023-10-26 | 2024-03-01 | 华南理工大学 | Copper-based three-dimensional self-supporting electrode material and preparation method and application thereof |
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JP2016012474A (en) * | 2014-06-30 | 2016-01-21 | 三菱レイヨン株式会社 | Manufacturing method of porous electrode base material |
CN104157885A (en) * | 2014-08-19 | 2014-11-19 | 大连理工大学 | Preparation method of solid oxide fuel cell electrode with high porosity amount and long tunnel |
CN105112936A (en) * | 2015-10-09 | 2015-12-02 | 河北工业大学 | A preparation method of a three-dimensional macroporous structure PbO2 electrode with high catalytic activity |
CN110205636A (en) * | 2019-04-22 | 2019-09-06 | 清华大学 | A kind of preparation method of self-cradling type three-dimensional porous structure double-function catalyzing electrode |
CN113293312A (en) * | 2021-05-21 | 2021-08-24 | 中南大学 | Preparation method of composite porous electrode material for lithium extraction |
CN117303512A (en) * | 2023-10-07 | 2023-12-29 | 中国科学院城市环境研究所 | A self-supporting three-dimensional porous electrocatalytic anode and its preparation method and application |
CN117626308A (en) * | 2023-10-26 | 2024-03-01 | 华南理工大学 | Copper-based three-dimensional self-supporting electrode material and preparation method and application thereof |
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