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CN104353355A - Ceramic purifier for purifying ozone in air and preparation method of ceramic purifier - Google Patents

Ceramic purifier for purifying ozone in air and preparation method of ceramic purifier Download PDF

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CN104353355A
CN104353355A CN201410642022.8A CN201410642022A CN104353355A CN 104353355 A CN104353355 A CN 104353355A CN 201410642022 A CN201410642022 A CN 201410642022A CN 104353355 A CN104353355 A CN 104353355A
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composite catalyst
air
catalyst
purifier
cuo
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房永征
于圣洁
孙玉见
张娜
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Shanghai Institute of Technology
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Abstract

本发明公开一种空气中的臭氧净化用的陶瓷净化器及制备方法,所述空气中的臭氧净化用的陶瓷净化器,即在多孔陶瓷载体上负载有按重量比计算为7-8%的Mn3O4/CuO或Mn3O4/Fe2O3复合催化剂。其制备方法按复合催化剂、水性聚丙烯酸树脂和水混合后放入砂磨机中研磨,然后过325目标准筛,得到催化剂悬浊液;然后将羟基氧化铝溶胶与所得催化剂悬浊液进行混合,利用压缩空气喷枪将得到的催化剂浆料控制压力为5-10MPa喷射到多孔陶瓷载体上,然后放入100-180℃烘箱中进行烘干10-20min;重复喷涂、烘干的过程直至多孔陶瓷载体增重7-8%时停止,即得空气中的臭氧净化用的陶瓷净化器。The invention discloses a ceramic purifier for ozone purification in the air and a preparation method thereof. The ceramic purifier for ozone purification in the air is loaded with 7-8% by weight on a porous ceramic carrier. Mn 3 O 4 /CuO or Mn 3 O 4 /Fe 2 O 3 composite catalyst. The preparation method is as follows: the composite catalyst, water-based polyacrylic acid resin and water are mixed and put into a sand mill for grinding, and then passed through a 325-mesh standard sieve to obtain a catalyst suspension; then the aluminum oxyhydroxide sol is mixed with the obtained catalyst suspension , use a compressed air spray gun to spray the obtained catalyst slurry on the porous ceramic carrier at a controlled pressure of 5-10MPa, and then put it in an oven at 100-180°C for drying for 10-20min; repeat the process of spraying and drying until the porous ceramic When the weight of the carrier increases by 7-8%, it stops, and the ceramic purifier for ozone purification in the air is obtained.

Description

一种空气中的臭氧净化用的陶瓷净化器及其制备方法Ceramic purifier for ozone purification in air and preparation method thereof

技术领域 technical field

    本发明涉及一种空气中的臭氧净化用的陶瓷净化器及其制备方法。 The present invention relates to a ceramic purifier for ozone purification in the air and a preparation method thereof.

背景技术 Background technique

随着人们生活质量的不断提高,大家越来越关注自己生活环境的好坏,空气质量的问题走进了老百姓的视野当中。臭氧、甲醛等污染已经成为不可忽视的问题。近几年的研究表明,目前市场上使用的催化剂主要为金属氧化物以及相应的金属。然而催化活性组份的选择上金属活性比相应的金属氧化物要低,同时金属对于臭氧的分解能力不足,且目前的原料成本相对较高,这对于其应用造成了阻碍。催化剂须附着在一定的载体上才能完成空气净化功能,对于催化剂的载体人们也选用了多种材料。四川成都市疾病预防控制中心的翟莉和章文陆(翟莉,章文陆.甲醛净化纸的研究[J].中国环境卫生,2003,6(1~3):113)研制了捕捉甲醛的净化纸,将净化纸贴在家具上从而达到净化空气的目的。清华大学的张彭义、李昭(张彭义,李昭,田地.二氧化钛涂覆材料对甲苯的光催化降解作用[J].上海环境科学,2002,21(12):709~71l)等人在玻璃、瓷砖和目光灯这3种常见材料表面涂覆了TiO2,期望开发出具有自洁净功能的装修材料。这两种载体存在着易起粉、催化剂与载体粘结不良,光利用率低等缺点。 With the continuous improvement of people's quality of life, people pay more and more attention to the quality of their living environment, and the problem of air quality has entered the field of vision of ordinary people. Pollution such as ozone and formaldehyde has become a problem that cannot be ignored. Studies in recent years have shown that the catalysts currently used in the market are mainly metal oxides and corresponding metals. However, in the selection of catalytically active components, the metal activity is lower than that of the corresponding metal oxides, and the metal's ability to decompose ozone is insufficient, and the current raw material cost is relatively high, which hinders its application. The catalyst must be attached to a certain carrier to complete the air purification function, and people have also selected a variety of materials for the carrier of the catalyst. Zhai Li and Zhang Wenlu from the Chengdu Center for Disease Control and Prevention (Zhai Li, Zhang Wenlu. Research on formaldehyde purification paper [J]. China Environmental Health, 2003, 6(1~3): 113) developed a purification paper that captures formaldehyde, Paste the purification paper on the furniture to achieve the purpose of purifying the air. Zhang Pengyi and Li Zhao from Tsinghua University (Zhang Pengyi, Li Zhao, Tian Di. Photocatalytic degradation of toluene by titanium dioxide coating materials [J]. Shanghai Environmental Science, 2002, 21(12): 709~71l) et al. TiO 2 is coated on the surface of three common materials, ceramic tiles and gaze lamps, and it is expected to develop a decoration material with self-cleaning function. These two carriers have the disadvantages of easy powdering, poor bonding between the catalyst and the carrier, and low light utilization efficiency.

利用多孔陶瓷作为催化剂载体是一个较好的方法,高气孔率多孔陶瓷用于空气净化时不仅其本身可以过滤气体中的尘粒,还可以在担载催化剂后对有害气体进行净化。 Using porous ceramics as a catalyst carrier is a better method. When high-porosity porous ceramics are used for air purification, they can not only filter the dust particles in the gas, but also purify harmful gases after loading the catalyst.

目前国内多孔陶瓷作为一种具有优良特性的环保材料常常用在室外污染气体的过滤,如电厂烟气脱硝、汽车尾气过滤等。催化剂与多孔陶瓷基体组装方式中应用最普遍的是浸涂法和旋转涂覆法,其中浸涂法简便易行不需要复杂的仪器设备而倍受青睐。但是该方法得到的产品比表面积小,使得其催化效率减弱;谢敏在学位论文(谢敏.空气净化用多孔陶瓷的制备及其性能研究. [D].[硕士学位论文].河北: 石家庄铁道学院,2007.)中介绍的,将催化剂溶胶涂覆在多孔陶瓷载体上研究其对甲醛的净化效果,但该方法中受涂膜的厚度和均匀度影响,涂覆干燥后涂膜易开裂,造成与陶瓷体黏结不牢固。综上所述,目前用于空气净化用的陶瓷净化器备受关注,仍存在催化剂与载体的组装的技术问题,而该问题正是本发明下面要解决的技术问题。 At present, domestic porous ceramics, as an environmentally friendly material with excellent characteristics, are often used in the filtration of outdoor polluted gases, such as denitrification of flue gas from power plants, and filtration of automobile exhaust. The most common methods of assembling catalysts and porous ceramic substrates are dip-coating and spin-coating, among which dip-coating is popular because it is simple and does not require complicated equipment. However, the specific surface area of the product obtained by this method is small, which weakens its catalytic efficiency; Xie Min’s dissertation (Xie Min. Preparation and Performance Research of Porous Ceramics for Air Purification. [D].[Master’s Dissertation]. Hebei: Shijiazhuang Introduced in Railway Academy, 2007.), the catalyst sol is coated on a porous ceramic carrier to study its purification effect on formaldehyde, but this method is affected by the thickness and uniformity of the coating film, and the coating film is easy to crack after drying , resulting in weak bonding with the ceramic body. To sum up, ceramic purifiers used for air purification have attracted much attention at present, and there is still a technical problem of assembling the catalyst and the carrier, and this problem is exactly the technical problem to be solved in the present invention.

发明内容 Contents of the invention

本发明目的在于为了解决上述的催化剂与载体的组装等技术问题而提供一种操作简单,实际应用可行性强,成本低且催化降解效率高的空气中的臭氧净化用的陶瓷净化器及其制备方法。 The purpose of the present invention is to provide a ceramic purifier for ozone purification in air with simple operation, strong practical application feasibility, low cost and high catalytic degradation efficiency in order to solve the technical problems of the above-mentioned assembly of catalyst and carrier and its preparation method.

本发明的技术方案 Technical scheme of the present invention

一种空气中的臭氧净化用的陶瓷净化器,即在多孔陶瓷载体上负载有Mn3O4/CuO复合催化剂或Mn3O4/ Fe2O3复合催化剂,优选负载Mn3O4/CuO复合催化剂; A ceramic purifier for ozone purification in air, that is, a porous ceramic carrier is loaded with a Mn 3 O 4 /CuO composite catalyst or a Mn 3 O 4 /Fe 2 O 3 composite catalyst, preferably loaded with Mn 3 O 4 /CuO Composite catalyst;

Mn3O4/CuO复合催化剂或Mn3O4/ Fe2O3复合催化剂的负载量,按重量比计算,即Mn3O4/CuO复合催化剂或Mn3O4/ Fe2O3复合催化剂:多孔陶瓷载体为7-8:100。 The loading capacity of Mn 3 O 4 /CuO composite catalyst or Mn 3 O 4 /Fe 2 O 3 composite catalyst, calculated by weight ratio, that is, Mn 3 O 4 /CuO composite catalyst or Mn 3 O 4 /Fe 2 O 3 composite catalyst : The porous ceramic support is 7-8:100.

上述的一种空气中的臭氧净化用的陶瓷净化器的制备方法,具体包括如下步骤: The above-mentioned preparation method of a ceramic purifier for ozone purification in air specifically comprises the following steps:

(1)、按Mn3O4/CuO或Mn3O4/ Fe2O3复合催化剂:水性聚丙烯酸树脂:水的质量比为1:0.5:2.0-2.7的比例进行混合后放入砂磨机中,控制转速为1200r/min进行研磨30-60min,然后过325目标准筛,得到催化剂悬浊液; (1) Mix according to the ratio of Mn 3 O 4 /CuO or Mn 3 O 4 /Fe 2 O 3 composite catalyst: water-based polyacrylic resin: water in the ratio of 1:0.5:2.0-2.7 and put it into the sand mill In the machine, the control speed is 1200r/min to grind for 30-60min, and then pass through a 325-mesh standard sieve to obtain a catalyst suspension;

(2)、为了进一步增大陶瓷空气过滤器的吸附面积,将固含量为44.2%的羟基氧化铝溶胶与步骤(1)所得催化剂悬浊液按体积比为1:1-1.5的比例进行混合均匀,得催化剂浆料; (2) In order to further increase the adsorption area of the ceramic air filter, mix the alumina oxyhydroxide sol with a solid content of 44.2% and the catalyst suspension obtained in step (1) at a volume ratio of 1:1-1.5 Evenly, the catalyst slurry is obtained;

(3)将步骤(2)所得催化剂浆料利用压缩空气喷枪,控制压力为6-9Mpa喷射到多孔陶瓷载体上,然后将喷涂后的多孔陶瓷载体放入100-180℃,优选为120℃烘箱中进行烘干10-20min; (3) Use a compressed air spray gun to spray the catalyst slurry obtained in step (2) onto the porous ceramic carrier at a controlled pressure of 6-9Mpa, and then put the sprayed porous ceramic carrier into an oven at 100-180°C, preferably 120°C Dry in 10-20min;

重复上述的喷涂、烘干的过程,直至多孔陶瓷载体增重7-8%停止,得负载有Mn3O4/CuO复合催化剂或Mn3O4/ Fe2O3复合催化剂的多孔陶瓷载体,即空气中的臭氧净化用的陶瓷净化器。 Repeat the above-mentioned spraying and drying process until the porous ceramic carrier increases in weight by 7-8% to obtain a porous ceramic carrier loaded with Mn 3 O 4 /CuO composite catalyst or Mn 3 O 4 /Fe 2 O 3 composite catalyst, That is, a ceramic purifier for ozone purification in the air.

上述所得的空气中的臭氧净化用的陶瓷净化器用于对空气中臭氧进行降解。  The above obtained ceramic purifier for ozone purification in air is used for degrading ozone in air. the

本发明的有益效果 Beneficial effects of the present invention

本发明的一种空气中的臭氧净化用的陶瓷净化器,由于选用Mn3O4/CuO或Mn3O4/ Fe2O3复合催化剂,该复合催化剂中的Mn3O4对于O3分解活性很好,第二金属氧化物CuO或Fe2O3,使复合催化剂的性能有了更进一步的提高。考虑到研究和生产成本的因素,优选CuO作为第二金属氧化物,最终所得的空气中的臭氧净化用的陶瓷净化器对空气中的臭氧进行净化,臭氧的降解率可达97%.  A ceramic purifier for ozone purification in air according to the present invention, because Mn 3 O 4 /CuO or Mn 3 O 4 /Fe 2 O 3 composite catalysts are selected for use, Mn 3 O 4 in the composite catalyst is decomposed for O 3 The activity is very good, and the second metal oxide CuO or Fe 2 O 3 further improves the performance of the composite catalyst. Considering the factors of research and production cost, CuO is preferred as the second metal oxide, and the final ceramic purifier used for ozone purification in the air can purify the ozone in the air, and the ozone degradation rate can reach 97%.

进一步,本发明的一种空气中的臭氧净化用的陶瓷净化器的制备方法,由于制备过程中,Mn3O4/CuO或Mn3O4/ Fe2O3复合催化剂比较容易获得,同时采用了球磨技术,获得了颗粒细小,尺寸均匀的催化剂中心浆料,然后采用多次喷涂技术,将催化剂中心浆料均匀的负载到多孔陶瓷载体上。因此所得的陶瓷空气过滤器,其性能一致性好,并且提高了使用寿命。 Further, a kind of preparation method of the ceramic purifier that the ozone in the air of the present invention purifies is useful, because in the preparation process, Mn 3 O 4 /CuO or Mn 3 O 4 /Fe 2 O 3 composite catalysts are relatively easy to obtain, adopt simultaneously The ball milling technology is used to obtain the catalyst center slurry with fine particles and uniform size, and then the catalyst center slurry is uniformly loaded on the porous ceramic carrier by using multiple spraying techniques. Therefore, the obtained ceramic air filter has good performance consistency and a long service life.

具体实施例 specific embodiment

下面通过具体实施例对本发明进一步阐述,但并不限制本发明。 The present invention is further illustrated below by specific examples, but the present invention is not limited.

试剂名称Reagent name 分子式molecular formula 纯度purity 生产厂家Manufacturer 硝酸铜溶液Copper nitrate solution Cu(NO3)2 Cu(NO 3 ) 2 分析纯Analytical pure 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd. 氢氧化钠sodium hydroxide NaOHNaOH 分析纯Analytical pure 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd. 50%硝酸锰溶液50% manganese nitrate solution Mn(NO3)2 Mn( NO3)2 50%水溶液50% aqueous solution 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd. 丙烯酸正丁酯n-butyl acrylate C7H12O2 C 7 H 12 O 2 分析纯Analytical pure 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd. 甲基丙烯酸甲酯Methyl methacrylate C5H8O2 C 5 H 8 O 2 分析纯Analytical pure 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd. 丙烯酸acrylic acid C3H4O2 C 3 H 4 O 2 分析纯Analytical pure 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd. 硫代硫酸钠Sodium thiosulfate Na2S2O3 Na 2 S 2 O 3 分析纯Analytical pure 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd. 98%浓硫酸98% concentrated sulfuric acid H2SO4 H2SO4 _ 分析纯Analytical pure 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd. 碘化钾potassium iodide KIKI 分析纯Analytical pure 国药集团化学试剂有限公司Sinopharm Chemical Reagent Co., Ltd.

根据中华人民共和国城镇建设行业标准中臭氧发生器臭氧浓度、产量、电耗的测量CJ/T3028.2-94标准,测试臭氧浓度进而求出臭氧分解率。 According to the CJ/T3028.2-94 standard for the measurement of ozone concentration, output and power consumption of ozone generators in the urban construction industry standard of the People's Republic of China, the ozone concentration is tested to obtain the ozone decomposition rate.

实施例1Example 1

一种空气中的臭氧净化用的陶瓷净化器,即在多孔陶瓷载体上负载有Mn3O4/CuO复合催化剂; A ceramic purifier for ozone purification in air, that is, a Mn 3 O 4 /CuO composite catalyst is loaded on a porous ceramic carrier;

Mn3O4/CuO复合催化剂的负载量,按重量比计算,即Mn3O4/CuO复合催化剂:多孔陶瓷载体为7:100。 The loading capacity of Mn 3 O 4 /CuO composite catalyst is calculated by weight ratio, that is, Mn 3 O 4 /CuO composite catalyst: porous ceramic carrier is 7:100.

上述的一种空气中的臭氧净化用的陶瓷净化器的制备方法,具体包括如下步骤: The above-mentioned preparation method of a ceramic purifier for ozone purification in air specifically comprises the following steps:

(1)、取10gCu/Mn催化剂、7.27g(固含量68.77%)聚丙烯酸乳脂,与20g水混合后放入砂磨机中,转速为1200r/min,时间为0.5h,保证原料能够充分混合后,过325目标准筛,得到催化剂悬浊液;  (1) Take 10g Cu/Mn catalyst, 7.27g (solid content 68.77%) polyacrylic acid cream, mix it with 20g water and put it into a sand mill with a rotation speed of 1200r/min and a time of 0.5h to ensure that the raw materials can be fully mixed Afterwards, cross 325 mesh standard sieves, obtain catalyst suspension;

(2)、为了进一步增大陶瓷空气过滤器的吸附面积,将30g固含量为44.2%的羟基氧化铝溶胶与45g步骤(1)所得催化剂悬浊液进行混合均匀,得催化剂浆料; (2) In order to further increase the adsorption area of the ceramic air filter, 30g of aluminum oxyhydroxide sol with a solid content of 44.2% was mixed evenly with 45g of the catalyst suspension obtained in step (1) to obtain a catalyst slurry;

(3)将(2)所得催化剂浆料利用压缩空气喷枪,控制压力为10Mpa喷射到多孔陶瓷载体上,然后将喷涂后的多孔陶瓷载体放入120℃烘箱中进行烘干20min; (3) Spray the catalyst slurry obtained in (2) onto the porous ceramic carrier with a compressed air spray gun at a controlled pressure of 10Mpa, and then put the sprayed porous ceramic carrier in an oven at 120°C for 20 minutes;

重复上述的喷涂、烘干的过程,直至多孔陶瓷载体增重7%停止,得负载有Mn3O4/CuO复合催化剂的多孔陶瓷载体,即空气中的臭氧净化用的陶瓷净化器。 Repeat the above process of spraying and drying until the weight of the porous ceramic carrier increases by 7%, and the porous ceramic carrier loaded with the Mn 3 O 4 /CuO composite catalyst is obtained, that is, the ceramic purifier for ozone purification in the air.

实施例2Example 2

一种空气中的臭氧净化用的陶瓷净化器,即在多孔陶瓷载体上负载有Mn3O4/CuO复合催化剂; A ceramic purifier for ozone purification in air, that is, a Mn 3 O 4 /CuO composite catalyst is loaded on a porous ceramic carrier;

Mn3O4/CuO复合催化剂的负载量,按重量比计算,即Mn3O4/CuO复合催化剂:多孔陶瓷载体为7.5:100。 The loading capacity of Mn 3 O 4 /CuO composite catalyst is calculated by weight ratio, that is, Mn 3 O 4 /CuO composite catalyst: porous ceramic support is 7.5:100.

上述的一种空气中的臭氧净化用的陶瓷净化器的制备方法,具体包括如下步骤: The above-mentioned preparation method of a ceramic purifier for ozone purification in air specifically comprises the following steps:

(1)、取10gCu/Mn催化剂、7.27g(固含量68.77%)聚丙烯酸乳脂,与23g水混合后放入砂磨机中,转速为1200r/min,时间为1h,保证原料能够充分混合后,过325目标准筛,得到催化剂悬浊液;  (1) Take 10g Cu/Mn catalyst, 7.27g (solid content 68.77%) polyacrylic acid cream, mix it with 23g water and put it into a sand mill at a speed of 1200r/min for 1h to ensure that the raw materials can be fully mixed , cross 325 mesh standard sieves to obtain catalyst suspension;

(2)、为了进一步增大陶瓷空气过滤器的吸附面积,将30g固含量为44.2%的羟基氧化铝溶胶与40g步骤(1)所得催化剂悬浊液进行混合均匀,得催化剂浆料; (2) In order to further increase the adsorption area of the ceramic air filter, 30g of aluminum oxyhydroxide sol with a solid content of 44.2% was mixed evenly with 40g of the catalyst suspension obtained in step (1) to obtain a catalyst slurry;

(3)将(2)所得催化剂浆料利用压缩空气喷枪,控制压力为9Mpa喷射到多孔陶瓷载体上,然后将喷涂后的多孔陶瓷载体放入120℃烘箱中进行烘干20min; (3) Spray the catalyst slurry obtained in (2) onto the porous ceramic carrier with a compressed air spray gun at a controlled pressure of 9Mpa, and then put the sprayed porous ceramic carrier in an oven at 120°C for 20 minutes;

重复上述的喷涂、烘干的过程,直至多孔陶瓷载体增重7.5%停止,得负载有Mn3O4/CuO复合催化剂的多孔陶瓷载体,即空气中的臭氧净化用的陶瓷净化器。 Repeat the above process of spraying and drying until the weight of the porous ceramic carrier is 7.5%, and the porous ceramic carrier loaded with Mn 3 O 4 /CuO composite catalyst is obtained, that is, the ceramic purifier for ozone purification in the air.

实施例3Example 3

一种空气中的臭氧净化用的陶瓷净化器,即在多孔陶瓷载体上负载有Mn3O4/CuO复合催化剂; A ceramic purifier for ozone purification in air, that is, a Mn 3 O 4 /CuO composite catalyst is loaded on a porous ceramic carrier;

Mn3O4/CuO复合催化剂的负载量,按重量比计算,即Mn3O4/CuO复合催化剂:多孔陶瓷载体为8:100。 The loading capacity of Mn 3 O 4 /CuO composite catalyst is calculated by weight ratio, that is, Mn 3 O 4 /CuO composite catalyst: porous ceramic support is 8:100.

上述的一种空气中的臭氧净化用的陶瓷净化器的制备方法,具体包括如下步骤: The above-mentioned preparation method of a ceramic purifier for ozone purification in air specifically comprises the following steps:

(1)、取10gCu/Mn催化剂、7.27g(固含量68.77%)聚丙烯酸乳脂,与25g水混合后放入砂磨机中,转速为1200r/min,时间为1h,保证原料能够充分混合后,过325目标准筛,得到催化剂悬浊液;  (1) Take 10g Cu/Mn catalyst, 7.27g (solid content 68.77%) polyacrylic acid cream, mix it with 25g water and put it into a sand mill at a speed of 1200r/min for 1h to ensure that the raw materials can be fully mixed , cross 325 mesh standard sieves to obtain catalyst suspension;

(2)、为了进一步增大陶瓷空气过滤器的吸附面积,将30g固含量为44.2%的羟基氧化铝溶胶与40g步骤(1)所得催化剂悬浊液进行混合均匀,得催化剂浆料; (2) In order to further increase the adsorption area of the ceramic air filter, 30g of aluminum oxyhydroxide sol with a solid content of 44.2% was mixed evenly with 40g of the catalyst suspension obtained in step (1) to obtain a catalyst slurry;

(3)将(2)所得催化剂浆料利用压缩空气喷枪,控制压力为7Mpa喷射到多孔陶瓷载体上,然后将喷涂后的多孔陶瓷载体放入120℃烘箱中进行烘干20min; (3) Spray the catalyst slurry obtained in (2) onto the porous ceramic carrier with a compressed air spray gun at a controlled pressure of 7Mpa, and then put the sprayed porous ceramic carrier in an oven at 120°C for 20 minutes;

重复上述的喷涂、烘干的过程,直至多孔陶瓷载体增重8.0%停止,得负载有Mn3O4/CuO复合催化剂的多孔陶瓷载体,即空气中的臭氧净化用的陶瓷净化器。 Repeat the above process of spraying and drying until the weight of the porous ceramic carrier increases by 8.0%, and the porous ceramic carrier loaded with the Mn 3 O 4 /CuO composite catalyst is obtained, that is, the ceramic purifier for ozone purification in the air.

实施例4Example 4

一种空气中的臭氧净化用的陶瓷净化器,即在多孔陶瓷载体上负载有Mn3O4/CuO复合催化剂; A ceramic purifier for ozone purification in air, that is, a Mn 3 O 4 /CuO composite catalyst is loaded on a porous ceramic carrier;

Mn3O4/CuO复合催化剂的负载量,按重量比计算,即Mn3O4/CuO复合催化剂:多孔陶瓷载体为7:100。 The loading capacity of Mn 3 O 4 /CuO composite catalyst is calculated by weight ratio, that is, Mn 3 O 4 /CuO composite catalyst: porous ceramic carrier is 7:100.

上述的一种空气中的臭氧净化用的陶瓷净化器的制备方法,具体包括如下步骤: The above-mentioned preparation method of a ceramic purifier for ozone purification in air specifically comprises the following steps:

(1)、取10gCu/Mn催化剂、7.27g(固含量68.77%)聚丙烯酸乳脂,与27g水混合后放入砂磨机中,转速为1200r/min,时间为1h,保证原料能够充分混合后,过325目标准筛,得到催化剂悬浊液;  (1) Take 10g Cu/Mn catalyst, 7.27g (solid content 68.77%) polyacrylic acid cream, mix it with 27g water and put it into a sand mill at a speed of 1200r/min for 1h to ensure that the raw materials can be fully mixed , cross 325 mesh standard sieves to obtain catalyst suspension;

(2)、为了进一步增大陶瓷空气过滤器的吸附面积,将30g固含量为44.2%的羟基氧化铝溶胶与40g步骤(1)所得催化剂悬浊液进行混合均匀,得催化剂浆料; (2) In order to further increase the adsorption area of the ceramic air filter, 30g of aluminum oxyhydroxide sol with a solid content of 44.2% was mixed evenly with 40g of the catalyst suspension obtained in step (1) to obtain a catalyst slurry;

(3)将(2)所得催化剂浆料利用压缩空气喷枪,控制压力为5Mpa喷射到多孔陶瓷载体上,然后将喷涂后的多孔陶瓷载体放入120℃烘箱中进行烘干10min; (3) Spray the catalyst slurry obtained in (2) onto the porous ceramic carrier with a compressed air spray gun at a controlled pressure of 5Mpa, and then put the sprayed porous ceramic carrier in an oven at 120°C for 10 minutes;

重复上述的喷涂、烘干的过程,直至多孔陶瓷载体增重7%停止,得负载有Mn3O4/CuO复合催化剂的多孔陶瓷载体,即空气中的臭氧净化用的陶瓷净化器。 Repeat the above process of spraying and drying until the weight of the porous ceramic carrier increases by 7%, and the porous ceramic carrier loaded with the Mn 3 O 4 /CuO composite catalyst is obtained, that is, the ceramic purifier for ozone purification in the air.

实施例5Example 5

一种空气中的臭氧净化用的陶瓷净化器,即在多孔陶瓷载体上负载有Mn3O4/CuO复合催化剂; A ceramic purifier for ozone purification in air, that is, a Mn 3 O 4 /CuO composite catalyst is loaded on a porous ceramic carrier;

Mn3O4/CuO复合催化剂的负载量,按重量比计算,即Mn3O4/CuO复合催化剂:多孔陶瓷载体为7.5:100。 The loading capacity of Mn 3 O 4 /CuO composite catalyst is calculated by weight ratio, that is, Mn 3 O 4 /CuO composite catalyst: porous ceramic support is 7.5:100.

上述的一种空气中的臭氧净化用的陶瓷净化器的制备方法,具体包括如下步骤: The above-mentioned preparation method of a ceramic purifier for ozone purification in air specifically comprises the following steps:

一种用于空气净化的陶瓷过滤器的组装方法,具体包括如下步骤: A method for assembling a ceramic filter for air purification, specifically comprising the steps of:

(1)、取10gCu/Mn催化剂、7.27g(固含量68.77%)聚丙烯酸乳脂,与23g水混合后放入砂磨机中,转速为1200r/min,时间为1h,保证原料能够充分混合后,过325目标准筛,得到催化剂悬浊液;  (1) Take 10g Cu/Mn catalyst, 7.27g (solid content 68.77%) polyacrylic acid cream, mix it with 23g water and put it into a sand mill at a speed of 1200r/min for 1h to ensure that the raw materials can be fully mixed , cross 325 mesh standard sieves to obtain catalyst suspension;

(2)、为了进一步增大陶瓷空气过滤器的吸附面积,将30g固含量为44.2%的羟基氧化铝溶胶与30g步骤(1)所得催化剂悬浊液进行混合均匀,得催化剂浆料; (2) In order to further increase the adsorption area of the ceramic air filter, 30 g of aluminum oxyhydroxide sol with a solid content of 44.2% was mixed evenly with 30 g of the catalyst suspension obtained in step (1) to obtain a catalyst slurry;

(3)将(2)所得催化剂浆料利用压缩空气喷枪,控制压力为9Mpa喷射到多孔陶瓷载体上,然后将喷涂后的多孔陶瓷载体放入120℃烘箱中进行烘干20min; (3) Spray the catalyst slurry obtained in (2) onto the porous ceramic carrier with a compressed air spray gun at a controlled pressure of 9Mpa, and then put the sprayed porous ceramic carrier in an oven at 120°C for 20 minutes;

重复上述的喷涂、烘干的过程,直至多孔陶瓷载体增重7.5%停止,得负载有Mn3O4/CuO复合催化剂的多孔陶瓷载体,即空气中的臭氧净化用的陶瓷净化器。 Repeat the above process of spraying and drying until the weight of the porous ceramic carrier is 7.5%, and the porous ceramic carrier loaded with Mn 3 O 4 /CuO composite catalyst is obtained, that is, the ceramic purifier for ozone purification in the air.

应用实施例Application example

利用上述实施例1-5所得的空气净化的陶瓷过滤器分别对含有臭氧的空气进行净化,含有臭氧的空气中O3浓度为2500ppm; Utilize the air-cleaning ceramic filter of above-mentioned embodiment 1-5 gained to purify the air containing ozone respectively, O in the air containing ozone Concentration is 2500ppm ;

控制反应时间30min,空气流速为60ml/min、KI水溶液的浓度为0.1g/ml,Na2S2O3浓度0.05mol/L,根据中华人民共和国城镇建设行业标准中臭氧发生器臭氧浓度、产量、电耗的测量CJ/T3028.2-94标准进行测定,空气中臭氧分解效率结果如下表所示: Control the reaction time for 30 minutes, the air flow rate is 60ml/min, the concentration of KI aqueous solution is 0.1g/ml, the concentration of Na 2 S 2 O 3 is 0.05mol/L, according to the ozone concentration and output of the ozone generator in the urban construction industry standard of the People's Republic of China , Measurement of power consumption CJ/T3028.2-94 standard to measure, the results of ozone decomposition efficiency in the air are shown in the table below:

空气中的臭氧净化用的陶瓷净化器Ceramic purifier for ozone purification in air 降解效率Degradation efficiency 实施例1Example 1 90%90% 实施例2Example 2 92.5%92.5% 实施例3Example 3 97%97% 实施例4Example 4 90%90% 实施例5Example 5 96%96%

从上表可以看出该空气中的臭氧净化用的陶瓷净化器对臭氧的分解率较高可达97%,由此表明了该空气中的臭氧净化用的陶瓷净化器适用于空气净化且净化效果良好。 It can be seen from the above table that the ceramic purifier for ozone purification in the air can decompose ozone up to 97%, which shows that the ceramic purifier for ozone purification in the air is suitable for air purification and purification. works well.

以上所述仅是本发明的实施方式的举例,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明技术原理的前提下,还可以做出若干改进和变型,这些改进和变型也应视为本发明的保护范围。 The foregoing is only an example of the embodiment of the present invention. It should be pointed out that for those of ordinary skill in the art, some improvements and modifications can be made without departing from the technical principles of the present invention. These improvements and Modifications should also be regarded as the scope of protection of the present invention.

Claims (5)

1. a ceramic purifier for the ozone purification in air, it is characterized in that the ceramic purifier of the ozone purification in described air, namely on cellular ceramic substrate, load has Mn 3o 4/ CuO composite catalyst or Mn 3o 4/ Fe 2o 3composite catalyst;
Mn 3o 4/ CuO composite catalyst or Mn 3o 4/ Fe 2o 3the load capacity of composite catalyst, by weight calculating, i.e. Mn 3o 4/ CuO composite catalyst or Mn 3o 4/ Fe 2o 3composite catalyst: cellular ceramic substrate is 7-8:100.
2. as right to remove as described in 1 a kind of air in the ceramic purifier of ozone purification, it is characterized in that load has Mn on cellular ceramic substrate 3o 4/ CuO composite catalyst;
Mn 3o 4the load capacity of/CuO composite catalyst, by weight calculating, i.e. Mn 3o 4/ CuO composite catalyst: cellular ceramic substrate is 7:100.
3. as right to remove as described in 1 a kind of air in the ceramic purifier of ozone purification, it is characterized in that load has Mn on cellular ceramic substrate 3o 4/ CuO composite catalyst;
Mn 3o 4the load capacity of/CuO composite catalyst, by weight calculating, i.e. Mn 3o 4/ CuO composite catalyst: cellular ceramic substrate is 7.5:100.
4. as right to remove as described in 1 a kind of air in the ceramic purifier of ozone purification, it is characterized in that load has Mn on cellular ceramic substrate 3o 4/ CuO composite catalyst;
Mn 3o 4the load capacity of/CuO composite catalyst, by weight calculating, i.e. Mn 3o 4/ CuO composite catalyst: cellular ceramic substrate is 8:100.
5. the preparation method of the ceramic purifier of the ozone purification in a kind of air as claimed in claim 1, is characterized in that specifically comprising the steps:
(1), by Mn 3o 4/ CuO or Mn 3o 4/ Fe 2o 3composite catalyst: aqueous polyacrylamide acid resin: the mass ratio of water is put into sand mill after the ratio of 1:0.5:2.0-2.7 mixes, and controlling rotating speed is that 1200r/min carries out grinding 30-60min, and then mistake 325 mesh standard sieves, obtain catalyst suspension;
(2), by solid content be hydroxyl oxidize Alumina gel and step (1) the gained catalyst suspension of 44.2% by volume for the ratio of 1:1-1.5 mixes, obtain catalyst pulp;
(3) step (2) gained catalyst pulp is utilized compressed ir spray gun, controlled pressure is that 5-10Mpa is ejected on cellular ceramic substrate, then the cellular ceramic substrate after spraying is put into 100-180 DEG C of baking oven and carries out oven dry 10-20min;
Repeat above-mentioned spraying, the process of oven dry, until stop during cellular ceramic substrate weightening finish 7-8%, obtain the ceramic purifier of the ozone purification in air.
CN201410642022.8A 2014-11-14 2014-11-14 Ceramic purifier for purifying ozone in air and preparation method of ceramic purifier Pending CN104353355A (en)

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