WO2016041380A1 - Supported catalyst suitable for purifying air at normal temperature - Google Patents

Supported catalyst suitable for purifying air at normal temperature Download PDF

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WO2016041380A1
WO2016041380A1 PCT/CN2015/080483 CN2015080483W WO2016041380A1 WO 2016041380 A1 WO2016041380 A1 WO 2016041380A1 CN 2015080483 W CN2015080483 W CN 2015080483W WO 2016041380 A1 WO2016041380 A1 WO 2016041380A1
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nano
supported catalyst
copper
manganese
normal temperature
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PCT/CN2015/080483
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French (fr)
Chinese (zh)
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许钧强
康伦国
姚东生
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合众(佛山)化工有限公司
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/16Clays or other mineral silicates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/10Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/32Manganese, technetium or rhenium
    • B01J23/34Manganese
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/72Copper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/83Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium

Definitions

  • the invention relates to a preparation method of a supported catalyst for purifying air, in particular to a suitable supported catalyst for purifying air at a normal temperature, and belongs to the technical field of catalysts.
  • indoor decoration pollution is mainly chemical pollutants such as formaldehyde, benzene, ammonia, etc.
  • the release period of such pollutants is up to 15 years, and it is not a problem of two months to solve the problem.
  • indoor decoration pollution is mainly chemical pollutants such as formaldehyde, benzene, ammonia, etc.
  • the release period of such pollutants is up to 15 years, and it is not a problem of two months to solve the problem.
  • In the enclosed room of summer air conditioning and cold winter heating Due to the lack of outdoor fresh air, the damage is even more serious!
  • hotel, conference room, furniture mall, building materials market, etc. do you have headaches, dazzling, cough, chest tightness, nausea, vomiting, etc.
  • Indoor invisible killer caused by air pollutants The main pollution of indoor air comes from materials such as construction, decoration and furniture, including formaldehyde, benzene and ammonia. Among them, formaldehyde pollution is the most harmful to human health.
  • formaldehyde scavenger or formaldehyde lyase these are chemical methods to "remove" formaldehyde, the essence of this method is to reduce the target substance to reduce toxicity or conversion to non-toxic substances, formaldehyde can be oxygen The formation of formic acid can also be reduced to methanol. The toxicity of these two substances still exists, which is easy to cause secondary pollution, and it is impossible to "spray forever".
  • photocatalyst method but the photocatalyst should play a role, there must be ultraviolet light to stimulate, no effect at night and no visible light.
  • the particles of the photocatalyst are very small and easily suspended in the air. It is like dust and cannot be seen with the naked eye. Even if it is inhaled, it is not noticeable, and it is easy to cause secondary pollution, which is likely to cause damage to the human lungs.
  • photocatalysts that have the property of decomposing organic substances, which can damage any organism such as leather products, hair grass and high-grade clothing and skin.
  • photocatalyst manufacturers do not mention it, do not inform consumers, and even mislead consumers of photocatalysts as long as they have Light is good, and such behavior should be blamed.
  • photocatalysts have a limited effect on removing polluting gases from the air, so they are rarely used in developed countries as civilian photocatalytic materials.
  • the plasma technology method is to generate a large amount of plasma to oxidize formaldehyde in the air to achieve the purpose of purifying air. This method is easy to generate ozone to cause secondary pollution to the air, and the device is complicated and consumes a large amount of energy; the conventional thermal catalytic oxidation method It is the use of a catalyst to catalyze the oxidation of formaldehyde under the action of thermal energy. However, this method generally requires a higher temperature.
  • room temperature-supported formaldehyde-removing catalysts contain precious metals such as gold, palladium, rhodium, iridium, and platinum. Due to the scarcity of precious metal resources, the price is expensive, which limits The promotion and application of formaldehyde removal by room temperature catalytic oxidation, such as patents CN100360224C, CN102284288B, CN103894194A contain precious metals.
  • Patent CN103599793A, CN103433054A, CN101274281B although excluding precious metals, but only in the air VOC S formaldehyde removal, and in addition to air VOC S-trityl there formaldehyde, ammonia, carbon monoxide, nitric oxide, sulfur dioxide and other pollutants Therefore, it is very important to develop an economical catalyst that can effectively remove harmful substances in the air at normal temperature.
  • An object of the present invention is to provide an economical applicability and a supported composite catalyst capable of removing formaldehyde, triphenyl, CO, NO, and SO 2 in air VOC S under normal temperature conditions.
  • the composite catalyst carrier of the present invention is prepared by purifying nano attapulgite or nano-sorbitite powder and supporting manganese, copper and cerium oxide.
  • Nano attapulgite and nano-sorbitite powder are porous mineral crystal materials, and their microstructure has a unique crystal regular structure. There are a large number of nano-scale pores in the crystal, the pore size is 2.7-9.8 angstroms, and the surface of the micropores is polar. Due to its nanometer pore size, it can selectively adsorb toxic substances such as benzene, xylene, formaldehyde, carbon monoxide, sulfur dioxide and ammonia in the nanometer molecular diameter (formaldehyde, ammonia, benzene, toluene and xylene have molecular diameters of 0.4 to 0.62). Between nanometers, and these compounds are polar molecules, which are nano-scale polar compounds), so nano-attapulgite and nano-sepiolite powder pores have superior adsorption and sustainable functions.
  • Manganese-copper composite oxide can effectively treat harmful gases in the air such as formaldehyde, triphenyl, carbon monoxide, nitrogen monoxide and sulfur dioxide.
  • Rare earth cerium oxide has redox characteristics, oxygen storage and synergistic catalysis, and can effectively increase manganese at normal temperature.
  • the catalytic activity of the copper composite oxide can also improve the stability and anti-poisoning ability of the catalyst;
  • the supported catalyst prepared by loading the manganese attapulgite composite oxide with nano attapulgite or nano sepiolite powder, and having a super-normal temperature at room temperature Strong adsorption capacity, can enrich a small amount of harmful gases in the air, and can effectively remove harmful gases in the air through synergistic catalytic oxidation of manganese-copper bismuth; and high treatment efficiency, low cost, wide economic applicability, no production Secondary pollution.
  • the present invention relates to a suitable load-type catalyst for purifying air at normal temperature, characterized in that copper, cerium and manganese are active components, and the carrier is a nano attapulgite rod. Soil or nano-porphyry powder, wherein the content of copper, barium and manganese is 15% to 40% of the total mass, and the molar ratio is 1:1:1 to 1:2:4.
  • the invention provides a preparation method of a suitable load-type catalyst for purifying air at normal temperature, and the preparation process is as follows: adding nano attapulgite or nano sepiolite powder to ethanol, deionized water, and adding nanometer cerium oxide by stirring under agitation. Ultrasonic dispersion for 1h, the nanosuspension was prepared, and then an aqueous solution of copper nitrate and manganese nitrate was added according to the formula molar ratio, and stirred at 30 to 50 ° C for 2 to 4 hours, the solution was removed, and dried at 110 to 120 ° C for 5 to 10 hours. After calcination at 500 to 800 ° C for 3 to 6 hours in a muffle furnace, the fineness is milled to 20 ⁇ or less.
  • the applicable load-type catalyst for purifying air at normal temperature prepared by the invention has superior adsorption capacity, and can continuously and effectively remove triphenyl, formaldehyde, ketone, ammonia and carbon monoxide which are volatilized from the decoration materials used in the interior decoration process. Nitrogen oxide, sulfur dioxide and other harmful gases, high processing efficiency, low cost, wide economic applicability, no secondary pollution, suitable for home, office, hotel, conference room, furniture shopping mall, building materials market and other space pollutants Removal.
  • nano-boehmite powder into 200ml ethanol-water solution, add 6g nano-cerium oxide under stirring, and disperse ultrasonically for 1h to prepare nano-sepiolite powder/cerium oxide suspension, add 50% copper nitrate aqueous solution 6g and 50% manganese nitrate.
  • 25 g of an aqueous solution was stirred at 40 to 50 ° C for 3 hours to remove the solution.
  • After drying and activating at 120 ° C for 6 h it was calcined in a muffle furnace at 700 for 4 h and then ground to a fineness of 20 ⁇ to prepare a supported catalyst with a loading of 20% and a molar ratio of copper, ruthenium and manganese of 1:2: 3.
  • Catalyst performance test The supported catalyst prepared in the example of the present invention was placed in a fixed bed reactor under the following conditions: gas composition: oxygen 20%, nitrogen 80%, formaldehyde gas, benzene gas respectively from formaldehyde gas generator, benzene
  • gas composition oxygen 20%, nitrogen 80%, formaldehyde gas, benzene gas respectively from formaldehyde gas generator, benzene
  • the gas generator is generated and blown into the reaction system by nitrogen gas to control the concentration of formaldehyde gas to be 0.05% and the concentration of benzene gas to be 0.1%.
  • Example 2 Example 3 Formaldehyde removal rate 95.6% 92.5% 94.6% Formaldehyde removal effect persistence 76.4% 73.8% 75.2% Benzene removal rate 97.5% 96.2% 95.6% Benzene removal effect persistence 77.5% 73.6% 74.8%
  • Catalyst performance test The supported catalyst prepared in the example of the present invention was placed in a fixed bed reactor under the following conditions: a gas sampler was used to take the automobile exhaust gas, a dryer was used to remove the moisture in the exhaust gas, and the CO in the exhaust gas was tested. The content of NO and SO 2 was further injected into the reaction system by nitrogen gas, and after reacting at 25 ° C for 48 hours, the contents of CO, NO and SO 2 were tested according to standard methods. The catalytic performance CO emission rate, NO removal rate, and SO 2 removal rate test results of the three examples are shown in Table 2.
  • Example 1 Example 2
  • Example 3 CO removal rate 82.5% 80.6% 81.2% NO removal rate 78.4% 72.6% 75.3% SO 2 removal rate 87.2% 86.5% 85.4%

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Abstract

The present invention relates to a supported catalyst suitable for purifying air at normal temperature, comprising copper, cerium and manganese as active ingredients with nano-attapulgite or a nano-sepiolite powder as a carrier wherein the content of copper, cerium and manganese accounts for 15%-40% of the total mass and the molar ratio thereof is 1 : 1 : 1 - 1 : 2 : 4; the raw materials are ultrasonically dispersed for 1 h, stirred for 2 h-4 h under the conditions of 30°C-50°C, dried at 110°C-120°C for 5 h-10 h for activation, calcined in a muffle furnace at 500°C-800°C for 3 h-6 h and then ground to a fineness of not more than 20 μ; the supported catalyst prepared in the present invention has strong adsorption capacity, can remove benzene, toluene, xylene, formaldehyde, CO, NO, SO2 and other harmful gases in air continuously and efficiently, has a high processing efficiency, low costs, wide economic applicability and does not produce secondary pollution, and is suitable for removing pollutants in houses, offices, hotels, meeting rooms, furniture stores, building material markets and other spaces.

Description

一种在常温下净化空气的适用性负载型催化剂Applicable supported catalyst for purifying air at normal temperature 技术领域Technical field
本发明涉及一种净化空气的负载型催化剂的制备方法,尤其涉及一种在常温下净化空气的适用性负载型催化剂,属于催化剂技术领域。The invention relates to a preparation method of a supported catalyst for purifying air, in particular to a suitable supported catalyst for purifying air at a normal temperature, and belongs to the technical field of catalysts.
背景技术Background technique
人的一生绝大多数时间生活和工作在室内,室内装修造成的环境污染导致人病、残、死亡的现象已经成为了社会问题,室内环境污染被列入“十大杀手”之一,这些污染气体对人体影响极大,容易导致呼吸道疾病、癌症、白血病、神经疾病,尤其对孕妇、儿童、老人危害严重。Most of the life of a person lives and works indoors. The environmental pollution caused by indoor decoration has caused people's illness, disability, and death. It has become a social problem. Indoor environmental pollution has been listed as one of the "Top Ten Killers". Gas has a great impact on the human body, and it is easy to cause respiratory diseases, cancer, leukemia, and neurological diseases, especially for pregnant women, children, and the elderly.
通常,人们习惯于装修后通风两个月,然后入住。但是,室内装修污染主要是甲醛、苯、氨等化学污染物,这类污染物释放期最长达15年,绝非两个月就可以解决问题,在盛夏空调和寒冬暖气的封闭房间内,由于缺乏室外新风,其危害更加严重!当你较长时间在新装修的新家或新的办公室、宾馆、会议室、家具商场、建材市场等地时,你是否会有头痛、眼花、咳嗽、胸闷、恶心、呕吐等症状,这些都是室内隐形杀手空气污染物所造成的。室内空气的主要污染来自建筑、装饰和家具等材料中,包括甲醛、苯、氨等,其中甲醛污染对人体健康的危害最大。Usually, people are used to ventilating for two months after renovation and then staying. However, indoor decoration pollution is mainly chemical pollutants such as formaldehyde, benzene, ammonia, etc. The release period of such pollutants is up to 15 years, and it is not a problem of two months to solve the problem. In the enclosed room of summer air conditioning and cold winter heating, Due to the lack of outdoor fresh air, the damage is even more serious! When you are in a newly renovated new home or new office, hotel, conference room, furniture mall, building materials market, etc., do you have headaches, dazzling, cough, chest tightness, nausea, vomiting, etc. Indoor invisible killer caused by air pollutants. The main pollution of indoor air comes from materials such as construction, decoration and furniture, including formaldehyde, benzene and ammonia. Among them, formaldehyde pollution is the most harmful to human health.
目前市场上净化空气的方法有:1、竹炭、活性炭吸附法,但竹炭、活性炭的吸附能力非常有限,仅对苯有一些作用,对甲醛的吸附效果并不好,且存在吸收饱和的问题,温度低时吸收量相对较大,温度升高又会释放出来。At present, the methods for purifying air on the market are as follows: 1. Bamboo charcoal and activated carbon adsorption method, but the adsorption capacity of bamboo charcoal and activated carbon is very limited, only has some effects on benzene, the adsorption effect on formaldehyde is not good, and there is a problem of absorption saturation. When the temperature is low, the absorption amount is relatively large, and the temperature rise is released again.
2、甲醛清除剂或甲醛溶解酶,这些是靠化学反应的方法“除掉”甲醛,这种方法的实质是将目标物质降低毒性或转化为无毒物质,甲醛可以被氧 化成甲酸,也可以被还原为甲醇,这两种物质的毒性依然存在,易造成二次污染,而且不可能“一喷永逸”。2, formaldehyde scavenger or formaldehyde lyase, these are chemical methods to "remove" formaldehyde, the essence of this method is to reduce the target substance to reduce toxicity or conversion to non-toxic substances, formaldehyde can be oxygen The formation of formic acid can also be reduced to methanol. The toxicity of these two substances still exists, which is easy to cause secondary pollution, and it is impossible to "spray forever".
3、光触媒法,但光触媒要发挥作用,要有紫外线光来激发,在夜间及无可见光没有任何效果。另外光触媒的粒子非常微小,极易悬浮于空气中,就像灰尘一般无法用肉眼看见,即使吸入亦无法察觉,易造成二次污染,极有可能对人体肺部造成伤害。还有光触媒具有分解有机物质之性能,对任何有机体如真皮制品、毛草及高级衣物、皮肤都有损害作用,而光触媒厂商却绝口不提,也不告知消费者,甚至误导消费者光触媒只要有光就好,如此行为,应受到指责。实际上光触媒对去除空气中的污染气体效果有限,因此发达国家目前极少将它们用作为民用光催化材料。3, photocatalyst method, but the photocatalyst should play a role, there must be ultraviolet light to stimulate, no effect at night and no visible light. In addition, the particles of the photocatalyst are very small and easily suspended in the air. It is like dust and cannot be seen with the naked eye. Even if it is inhaled, it is not noticeable, and it is easy to cause secondary pollution, which is likely to cause damage to the human lungs. There are also photocatalysts that have the property of decomposing organic substances, which can damage any organism such as leather products, hair grass and high-grade clothing and skin. However, photocatalyst manufacturers do not mention it, do not inform consumers, and even mislead consumers of photocatalysts as long as they have Light is good, and such behavior should be blamed. In fact, photocatalysts have a limited effect on removing polluting gases from the air, so they are rarely used in developed countries as civilian photocatalytic materials.
4、另外等离子技术法是通过放电产生大量等离子体氧化空气中的甲醛以达到净化空气的目的,此法易产生臭氧对空气造成二次污染,且装置复杂,能耗大;传统热催化氧化法是利用催化剂在热能的作用下催化氧化甲醛,然而此法一般需要较高温度。4. The plasma technology method is to generate a large amount of plasma to oxidize formaldehyde in the air to achieve the purpose of purifying air. This method is easy to generate ozone to cause secondary pollution to the air, and the device is complicated and consumes a large amount of energy; the conventional thermal catalytic oxidation method It is the use of a catalyst to catalyze the oxidation of formaldehyde under the action of thermal energy. However, this method generally requires a higher temperature.
在常温条件下去除甲醛的负载型催化剂,近年来得到了广泛重视,但是目前室温负载型除甲醛催化剂都含有贵重金属如金、钯、钌、铑、铂,由于贵金属资源稀少,价格昂贵,限制了室温催化氧化法去除甲醛的推广和应用,如专利CN100360224C、CN102284288B、CN103894194A含有贵重金属。如专利CN103599793A、CN103433054A、CN101274281B虽不含贵重金属,但仅对空气VOCS中的甲醛有去除效果,而空气VOCS中除甲醛外还有三苯、氨、一氧化碳、一氧化氮、二氧化硫等污染物,因此开发一种在常温下能有效去除空气中有害物质的经济适用型催化剂非常重要。Supported catalysts for removing formaldehyde under normal temperature conditions have received extensive attention in recent years, but currently, room temperature-supported formaldehyde-removing catalysts contain precious metals such as gold, palladium, rhodium, iridium, and platinum. Due to the scarcity of precious metal resources, the price is expensive, which limits The promotion and application of formaldehyde removal by room temperature catalytic oxidation, such as patents CN100360224C, CN102284288B, CN103894194A contain precious metals. Patent CN103599793A, CN103433054A, CN101274281B although excluding precious metals, but only in the air VOC S formaldehyde removal, and in addition to air VOC S-trityl there formaldehyde, ammonia, carbon monoxide, nitric oxide, sulfur dioxide and other pollutants Therefore, it is very important to develop an economical catalyst that can effectively remove harmful substances in the air at normal temperature.
发明内容 Summary of the invention
本发明的目的是提供一种在常温条件下能去除空气VOCS中的甲醛、三苯、CO、NO、SO2的经济适用性、负载型复合催化剂。SUMMARY OF THE INVENTION An object of the present invention is to provide an economical applicability and a supported composite catalyst capable of removing formaldehyde, triphenyl, CO, NO, and SO 2 in air VOC S under normal temperature conditions.
针对上面存在的技术问题,本发明复合催化剂载体选用提纯后的纳米凹凸棒土或纳米海泡石粉,负载锰、铜、铈氧化物制备而成。In view of the above technical problems, the composite catalyst carrier of the present invention is prepared by purifying nano attapulgite or nano-sorbitite powder and supporting manganese, copper and cerium oxide.
纳米凹凸棒土和纳米海泡石粉是种多孔矿晶物质,其微观结构具有独特的晶体规则结构,晶体内大量纳米级孔隙,孔径大小为2.7~9.8埃米,以及微孔表面带极性。由于其纳米级孔径可选择性地吸附纳米级分子直径的苯、二甲苯、甲醛、一氧化碳、二氧化硫、氨等有毒有害物(甲醛、氨、苯、甲苯、二甲苯的分子直径都在0.4~0.62纳米之间,而且这些化合物都是极性分子,就是纳米级的极性化合物),因此纳米凹凸棒土和纳米海泡石粉孔径具有超强的吸附力和可持续功能。Nano attapulgite and nano-sorbitite powder are porous mineral crystal materials, and their microstructure has a unique crystal regular structure. There are a large number of nano-scale pores in the crystal, the pore size is 2.7-9.8 angstroms, and the surface of the micropores is polar. Due to its nanometer pore size, it can selectively adsorb toxic substances such as benzene, xylene, formaldehyde, carbon monoxide, sulfur dioxide and ammonia in the nanometer molecular diameter (formaldehyde, ammonia, benzene, toluene and xylene have molecular diameters of 0.4 to 0.62). Between nanometers, and these compounds are polar molecules, which are nano-scale polar compounds), so nano-attapulgite and nano-sepiolite powder pores have superior adsorption and sustainable functions.
锰铜复合氧化物能有效处理空气中有害气体如甲醛、三苯、一氧化碳、一氧化氮、二氧化硫;稀土氧化铈具有氧化还原特性、储放氧能力和协同催化作用,在常温下能有效提高锰铜复合氧化物的催化活性,还能提高催化剂的稳定性和抗中毒能力;本发明通过锰铜铈复合氧化物负载纳米凹凸棒土或纳米海泡石粉制得的负载型催化剂,常温下具有超强吸附能力,能把空气中少量的有害气体富集,通过锰铜铈协同催化氧化作用,能有效地去除空气中的有害气体;并且处理效率高,成本低,经济适用性广,不产生二次污染。Manganese-copper composite oxide can effectively treat harmful gases in the air such as formaldehyde, triphenyl, carbon monoxide, nitrogen monoxide and sulfur dioxide. Rare earth cerium oxide has redox characteristics, oxygen storage and synergistic catalysis, and can effectively increase manganese at normal temperature. The catalytic activity of the copper composite oxide can also improve the stability and anti-poisoning ability of the catalyst; the supported catalyst prepared by loading the manganese attapulgite composite oxide with nano attapulgite or nano sepiolite powder, and having a super-normal temperature at room temperature Strong adsorption capacity, can enrich a small amount of harmful gases in the air, and can effectively remove harmful gases in the air through synergistic catalytic oxidation of manganese-copper bismuth; and high treatment efficiency, low cost, wide economic applicability, no production Secondary pollution.
为了解决上面所述的技术问题,本发明采取以下技术方案:本发明涉及一种常温下净化空气的适用性负载型催化剂,其特征为:铜、铈和锰为活性成分,载体为纳米凹凸棒土或纳米海泡石粉,其中铜、铈和锰的含量占总质量的15%~40%,其摩尔比为1∶1∶1~1∶2∶4。 In order to solve the above-mentioned technical problems, the present invention adopts the following technical solutions: The present invention relates to a suitable load-type catalyst for purifying air at normal temperature, characterized in that copper, cerium and manganese are active components, and the carrier is a nano attapulgite rod. Soil or nano-porphyry powder, wherein the content of copper, barium and manganese is 15% to 40% of the total mass, and the molar ratio is 1:1:1 to 1:2:4.
本发明提出一种常温下净化空气的适用性负载型催化剂的制备方法,制备工艺如下:把纳米凹凸棒土或纳米海泡石粉加入乙醇、去离子水中,搅拌下按摩尔比加入纳米氧化铈,超声波分散1h,制得纳米悬浮液,然后按配方摩尔比加入硝酸铜和硝酸锰的水溶液,在30~50℃条件下搅拌2~4h,除去溶液,在110~120℃下干燥活化5~10h,于马弗炉中在500~800℃下焙烧3~6h后研磨细度至20μ以下。The invention provides a preparation method of a suitable load-type catalyst for purifying air at normal temperature, and the preparation process is as follows: adding nano attapulgite or nano sepiolite powder to ethanol, deionized water, and adding nanometer cerium oxide by stirring under agitation. Ultrasonic dispersion for 1h, the nanosuspension was prepared, and then an aqueous solution of copper nitrate and manganese nitrate was added according to the formula molar ratio, and stirred at 30 to 50 ° C for 2 to 4 hours, the solution was removed, and dried at 110 to 120 ° C for 5 to 10 hours. After calcination at 500 to 800 ° C for 3 to 6 hours in a muffle furnace, the fineness is milled to 20 μ or less.
本发明制得的常温下净化空气的适用性负载型催化剂,具有超强的吸附能力,能持续有效地去除室内装修过程中使用的装潢材料挥发出来的三苯、甲醛、酮、氨、一氧化碳、一氧化氮、二氧化硫等各种有害气体,并且处理效率高,成本低,经济适用性广,不产生二次污染,适用于居家、办公室、宾馆、会议室、家具商场、建材市场等空间污染物的去除。The applicable load-type catalyst for purifying air at normal temperature prepared by the invention has superior adsorption capacity, and can continuously and effectively remove triphenyl, formaldehyde, ketone, ammonia and carbon monoxide which are volatilized from the decoration materials used in the interior decoration process. Nitrogen oxide, sulfur dioxide and other harmful gases, high processing efficiency, low cost, wide economic applicability, no secondary pollution, suitable for home, office, hotel, conference room, furniture shopping mall, building materials market and other space pollutants Removal.
具体实施方式detailed description
实施例1:Example 1:
称取70g纳米凹凸棒土加入200ml乙醇-水溶液中,搅拌下加入7g纳米氧化铈,超声波分散1h,制得纳米凹凸棒土/氧化铈悬浮液,加入50%硝酸铜水溶液7.5g和50%硝酸锰水溶液40g,在40~50℃条件下搅拌2h,除去溶液,在110℃下干燥活化6h,于马弗炉中在600下焙烧4h后研磨细度至20μ,即制得负载型催化剂,负载量为30%,铜、铈、锰摩尔比为1∶2∶4。70 g of nano attapulgite was weighed into 200 ml of ethanol-water solution, 7 g of nano-cerium oxide was added under stirring, and ultrasonic dispersion was carried out for 1 h to prepare a nano-attapulgite/cerium oxide suspension, and a 50% copper nitrate aqueous solution of 7.5 g and 50% nitric acid was added. 40 g of manganese aqueous solution was stirred at 40 to 50 ° C for 2 h, the solution was removed, dried at 110 ° C for 6 h, and calcined in a muffle furnace at 600 for 4 h, and then ground to a fineness of 20 μ to prepare a supported catalyst. The amount is 30%, and the molar ratio of copper, bismuth and manganese is 1:2:4.
实施例2:Example 2:
称取85g纳米海泡石粉加入200ml乙醇-水溶液中,搅拌下加入6g纳米氧化铈,超声波分散1h,制得纳米海泡石粉/氧化铈悬浮液,加入50%硝酸铜水溶液6g和50%硝酸锰水溶液25g,在40~50℃条件下搅拌3h,除去溶液, 在120℃下干燥活化6h,于马弗炉中在700下焙烧4h后研磨细度至20μ,即制得负载型催化剂,负载量为20%,铜、铈、锰摩尔比为1∶2∶3。Weigh 85g nano-boehmite powder into 200ml ethanol-water solution, add 6g nano-cerium oxide under stirring, and disperse ultrasonically for 1h to prepare nano-sepiolite powder/cerium oxide suspension, add 50% copper nitrate aqueous solution 6g and 50% manganese nitrate. 25 g of an aqueous solution was stirred at 40 to 50 ° C for 3 hours to remove the solution. After drying and activating at 120 ° C for 6 h, it was calcined in a muffle furnace at 700 for 4 h and then ground to a fineness of 20 μ to prepare a supported catalyst with a loading of 20% and a molar ratio of copper, ruthenium and manganese of 1:2: 3.
实施例3:Example 3:
称取75g纳米凹凸棒土加入200ml乙醇-水溶液中,搅拌下加入6.5g纳米氧化铈,超声波分散1h,制得纳米凹凸棒土/氧化铈悬浮液,加入50%硝酸铜水溶液14g和50%硝酸锰水溶液37.6g,在40~50℃条件下搅拌2h,除去溶液,在110℃下干燥活化6h,于马弗炉中在700下焙烧4h后研磨细度至20μ,即制得负载型催化剂,负载量为30%,铜、铈、锰摩尔比为1∶1∶2。Weigh 75g of nano attapulgite into 200ml ethanol-water solution, add 6.5g nano-cerium oxide under stirring, and disperse ultrasonically for 1h to prepare nano attapulgite/cerium oxide suspension, add 50% copper nitrate aqueous solution 14g and 50% nitric acid. 37.6 g of an aqueous manganese solution was stirred at 40 to 50 ° C for 2 h, the solution was removed, dried at 110 ° C for 6 h, and calcined in a muffle furnace at 700 for 4 h, and then ground to a fineness of 20 μ to prepare a supported catalyst. The loading was 30%, and the molar ratio of copper, bismuth and manganese was 1:1:1.
实施例4:Example 4:
催化剂性能测试:将本发明实例中制得的负载型催化剂置于固定床反应器中,实验条件:气体组成:氧气20%、氮气80%,甲醛气体、苯气体分别由甲醛气体发生器、苯气体发生器产生,由氮气吹入反应体系中,控制甲醛气体浓度为0.05%、苯气体浓度为0.1%,在25℃条件下反应48h后,按GB/T18204.26-2000中第一法:酚试剂分光光度法测试甲醛的含量,按GB/T18883-2002附录B的规定测试苯的含量。三个实施例催化性能甲醛去除率、苯去除率、去除效果持久性测试结果如表1所示。Catalyst performance test: The supported catalyst prepared in the example of the present invention was placed in a fixed bed reactor under the following conditions: gas composition: oxygen 20%, nitrogen 80%, formaldehyde gas, benzene gas respectively from formaldehyde gas generator, benzene The gas generator is generated and blown into the reaction system by nitrogen gas to control the concentration of formaldehyde gas to be 0.05% and the concentration of benzene gas to be 0.1%. After reacting at 25 ° C for 48 hours, according to the first method in GB/T18204.26-2000: The content of formaldehyde was measured by phenol reagent spectrophotometry, and the content of benzene was tested according to the provisions of Appendix B of GB/T18883-2002. The test results of catalytic performance, benzene removal rate, and removal effect durability of the three examples are shown in Table 1.
表1:三个实施例催化性能测试结果Table 1: Three Examples Catalytic Performance Test Results
项目project 实例1Example 1 实例2Example 2 实例3Example 3
甲醛去除率Formaldehyde removal rate 95.6%95.6% 92.5%92.5% 94.6%94.6%
甲醛去除效果持久性Formaldehyde removal effect persistence 76.4%76.4% 73.8%73.8% 75.2%75.2%
苯去除率Benzene removal rate 97.5%97.5% 96.2%96.2% 95.6%95.6%
苯去除效果持久性Benzene removal effect persistence 77.5%77.5% 73.6%73.6% 74.8%74.8%
实施例5: Example 5:
催化剂性能测试:将本发明实例中制得的负载型催化剂置于固定床反应器中,实验条件:用气体采样器采取汽车尾气,用干燥器除去尾气中的水份,并测试尾气中CO、NO、SO2的含量;再由氮气吹入反应体系中,在25℃条件下反应48h后,按照标准方法测试CO、NO、SO2的含量。三个实施例催化性能CO去除率、NO去除率、SO2去除率测试结果如表2所示。Catalyst performance test: The supported catalyst prepared in the example of the present invention was placed in a fixed bed reactor under the following conditions: a gas sampler was used to take the automobile exhaust gas, a dryer was used to remove the moisture in the exhaust gas, and the CO in the exhaust gas was tested. The content of NO and SO 2 was further injected into the reaction system by nitrogen gas, and after reacting at 25 ° C for 48 hours, the contents of CO, NO and SO 2 were tested according to standard methods. The catalytic performance CO emission rate, NO removal rate, and SO 2 removal rate test results of the three examples are shown in Table 2.
表2:三个实施例去除汽车尾气性能测试结果Table 2: Three examples to remove car exhaust performance test results
项目project 实例1Example 1 实例2Example 2 实例3Example 3
CO去除率CO removal rate 82.5%82.5% 80.6%80.6% 81.2%81.2%
NO去除率NO removal rate 78.4%78.4% 72.6%72.6% 75.3%75.3%
SO2去除率SO 2 removal rate 87.2%87.2% 86.5%86.5% 85.4%85.4%
尽管本发明已作了详细说明并引证了实施例,但对于本领域的普通技术人员,显然可以按照上述说明而做出的各种方案、修改和改动,都应该包括在权利要求的范围之内。 While the invention has been described in detail and shown by the embodiments of the claims .

Claims (2)

  1. 一种在常温下净化空气的适用性负载型催化剂,其特征在于:铜、铈和锰为活性成分,载体为纳米凹凸棒土或纳米海泡石粉,其中铜、铈和锰的含量占总质量的15%~40%,其摩尔比为1∶1∶1~1∶2∶4。A suitable supported catalyst for purifying air at normal temperature, characterized in that copper, cerium and manganese are active components, and the carrier is nano attapulgite or nano-sorbitite powder, wherein the content of copper, strontium and manganese accounts for the total mass. 15% to 40%, the molar ratio is 1:1:1 to 1:2:4.
  2. 如权利要求1所述的一种在常温下净化空气的适用性负载型催化剂的制备方法,其特征在于:所述制备方法为:把纳米凹凸棒土或纳米海泡石粉加入乙醇、去离子水中,搅拌下按摩尔比加入纳米氧化铈,超声波分散1h,制得纳米悬浮液,然后按配方摩尔比加入硝酸铜和硝酸锰的水溶液,在30~50℃条件下搅拌2~4h,除去溶液,在110~120℃下干燥活化5~10h,于马弗炉中在500~800℃下焙烧3~6h后研磨细度至20μ以下。 The method for preparing a suitable supported catalyst for purifying air at a normal temperature according to claim 1, wherein the preparation method comprises: adding nano attapulgite or nano-sorbitite powder to ethanol and deionized water. After stirring, the nanometer cerium oxide is added by stirring, and the nano-suspension is prepared by ultrasonic wave dispersion for 1 hour, and then an aqueous solution of copper nitrate and manganese nitrate is added according to the formula molar ratio, and stirred at 30 to 50 ° C for 2 to 4 hours to remove the solution. It is dried and activated at 110 to 120 ° C for 5 to 10 hours, and calcined at 500 to 800 ° C for 3 to 6 hours in a muffle furnace, and then the fineness is 20 μ or less.
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