[go: up one dir, main page]

CN107626303A - Preparation method of high-efficient purification formaldehyde materials and products thereof and application - Google Patents

Preparation method of high-efficient purification formaldehyde materials and products thereof and application Download PDF

Info

Publication number
CN107626303A
CN107626303A CN201711065016.0A CN201711065016A CN107626303A CN 107626303 A CN107626303 A CN 107626303A CN 201711065016 A CN201711065016 A CN 201711065016A CN 107626303 A CN107626303 A CN 107626303A
Authority
CN
China
Prior art keywords
formaldehyde
activated alumina
purification
preparation
formic acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201711065016.0A
Other languages
Chinese (zh)
Inventor
何丹农
袁静
蔡婷
赵昆峰
杨玲
金彩虹
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai National Engineering Research Center for Nanotechnology Co Ltd
Original Assignee
Shanghai National Engineering Research Center for Nanotechnology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shanghai National Engineering Research Center for Nanotechnology Co Ltd filed Critical Shanghai National Engineering Research Center for Nanotechnology Co Ltd
Priority to CN201711065016.0A priority Critical patent/CN107626303A/en
Publication of CN107626303A publication Critical patent/CN107626303A/en
Pending legal-status Critical Current

Links

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

本发明公布了一种高效甲醛净化材料的制备方法及其产品和应用,该制备方法可制备出两种甲醛净化材料,粉末MnOx和改性活性氧化铝。该方法是通过摩尔比为2:3的高锰酸钾溶液和甲酸溶液经过简单搅拌、抽滤及后处理后得到。粉末MnOx是高锰酸钾和甲酸溶液反应的滤饼直接置于40~60oC鼓风干燥箱中得到,改性活性氧化铝是将获得的滤液等体积浸渍活性氧化铝得到。高锰酸钾溶液的摩尔浓度控制在0.10~0.20 mol/L,甲酸溶液的浓度控制在0.30~0.60 mol/L。所得净化材料可在低浓度、高空速、流动条件下实现甲醛的高效稳定净化。本发明所公布的方法不仅零废液排放,而且将废液合理利用,变废为宝。The invention discloses a preparation method of a high-efficiency formaldehyde purification material and its product and application. The preparation method can prepare two kinds of formaldehyde purification materials, powdered MnOx and modified activated alumina. The method is obtained by simple stirring, suction filtration and post-treatment of potassium permanganate solution and formic acid solution with a molar ratio of 2:3. The powdered MnOx is obtained by directly placing the filter cake of the reaction of potassium permanganate and formic acid solution in a blast drying oven at 40-60 o C, and the modified activated alumina is obtained by impregnating the obtained filtrate with equal volume of activated alumina. The molar concentration of potassium permanganate solution is controlled at 0.10~0.20 mol/L, and the concentration of formic acid solution is controlled at 0.30~0.60 mol/L. The obtained purification material can realize efficient and stable purification of formaldehyde under low concentration, high space velocity and flow conditions. The method disclosed by the invention not only has zero waste liquid discharge, but also rationally utilizes the waste liquid to turn waste into treasure.

Description

高效净化甲醛材料的制备方法及其产品和应用Preparation method, product and application of high-efficiency purification formaldehyde material

技术领域technical field

本发明属于材料制备领域,具体地涉及一种高效净化甲醛材料的制备方法及其产品和应用。The invention belongs to the field of material preparation, and in particular relates to a preparation method of a high-efficiency formaldehyde purification material and its product and application.

背景技术Background technique

装修的普及使得室内污染物成为影响人们身体健康的重要因素。甲醛是室内污染物中含量较高且最有毒的一类有机物。甲醛超标,主要有三大危害:致敏作用,刺激作用,致突变作用。如皮肤直接接触甲醛可引起过敏性皮炎、色斑、坏死,吸入高浓度甲醛时可诱发支气管哮喘。对皮肤粘膜的刺激作用,能与蛋白质结合、高浓度吸入时出现呼吸道严重的刺激和水肿、眼刺激、头痛。在一定条件下,居室环境内空气中甲醛浓度可聚集到标准允许水平以上,而且释放期比较长,一般情况下,是3-15年。The popularity of decoration makes indoor pollutants an important factor affecting people's health. Formaldehyde is one of the most toxic and relatively high content of indoor pollutants. Excessive formaldehyde has three major hazards: sensitization, stimulation, and mutagenesis. For example, direct skin contact with formaldehyde can cause allergic dermatitis, stains, and necrosis, and inhalation of high concentrations of formaldehyde can induce bronchial asthma. Stimulating effect on skin and mucous membranes, can be combined with protein, severe respiratory tract irritation and edema, eye irritation, headache when inhaled at high concentrations. Under certain conditions, the concentration of formaldehyde in the air of the indoor environment can accumulate above the standard allowable level, and the release period is relatively long, generally 3-15 years.

目前室温甲醛净化的方法主要有吸附法和光催化降解。吸附法中吸附剂容易达到饱和,需要再生且固定时间更换材料等;光催化降解技术中需要引入光源,而且在使用过程中易产生O3等造成对人体的再次伤害。常温下将甲醛彻底净化的且能保持高稳定性的材料是市场需求最高的,也是净化器中优先选用的。目前文献中针对室温催化降解甲醛的材料主要有贵金属Pt、Au、Ag基材料等,资源较少且价格昂贵。过渡金属氧化物由于其具有多价态、快速电子转移及抗S、抗Cl等在碳氢化合物的去除中等表现出极好的性能,是最有潜力的材料。At present, the purification methods of formaldehyde at room temperature mainly include adsorption method and photocatalytic degradation. In the adsorption method, the adsorbent is easy to reach saturation, and needs to be regenerated and the material needs to be replaced at a fixed time; in the photocatalytic degradation technology, a light source needs to be introduced, and it is easy to generate O 3 during use, which will cause further damage to the human body. Materials that can completely purify formaldehyde at room temperature and maintain high stability are the most demanded in the market, and are also preferred in purifiers. At present, materials for catalytic degradation of formaldehyde at room temperature mainly include noble metals such as Pt, Au, and Ag-based materials in the literature, and the resources are few and expensive. Transition metal oxides are the most promising materials because of their multivalent states, fast electron transfer, and anti-S and anti-Cl performances in the removal of hydrocarbons.

值得说明的是,尽管市面上涌现出较多的针对甲醛的净化材料,但实际上能将甲醛彻底净化的高效净化材料较少,尤其针对室内低浓度甲醛的彻底治理。通常情况下,即使制备出较高效的净化甲醛材料,但其制备过程往往比较复杂,同时在大规模生产时,易产生较多的废液,而这些废液比较难治理,所需成本较高。因此,本发明拟针对以上两个问题,提供一种可同时制备出高效甲醛净化材料,并能将废液合理利用的简单制备方法。It is worth noting that although there are many purification materials for formaldehyde on the market, there are actually few efficient purification materials that can completely purify formaldehyde, especially for the thorough treatment of indoor low-concentration formaldehyde. Usually, even if a more efficient formaldehyde purification material is prepared, its preparation process is often more complicated, and at the same time, it is easy to generate more waste liquid during large-scale production, and these waste liquids are difficult to treat and require high costs. . Therefore, the present invention intends to address the above two problems and provide a simple preparation method that can simultaneously prepare high-efficiency formaldehyde purification materials and rationally utilize waste liquid.

发明内容Contents of the invention

为克服现有技术的不足,本发明的目的是:提供一种高效净化甲醛材料的制备方法。In order to overcome the deficiencies of the prior art, the object of the present invention is to provide a preparation method for highly efficient formaldehyde purification material.

本发明的再一目的是:提供上述方法制备的产品。Another object of the present invention is to provide the product prepared by the above method.

本发明的又一目的是:提供上述产品的应用。Another object of the present invention is to provide the application of the above product.

一种高效净化甲醛材料的制备方法,其特征在于具体操作如下:高锰酸钾溶液和甲酸溶液在室温下搅拌2~2.5 h后抽滤后得到滤饼和滤液,滤饼置于40-60 oC鼓风干燥箱中干燥10-14 h得MnOx;滤液等体积浸渍球状活性氧化铝后得到改性活性氧化铝。A preparation method for efficient purification of formaldehyde materials, characterized in that the specific operations are as follows: stirring potassium permanganate solution and formic acid solution at room temperature for 2 to 2.5 hours, then suction filtration to obtain filter cake and filtrate, the filter cake is placed in 40-60 o Dry in a blower drying oven at C for 10-14 h to obtain MnOx; impregnate spherical activated alumina with an equal volume of the filtrate to obtain modified activated alumina.

本发明方法所得净化材料可在低浓度、高空速、流动条件下实现甲醛的高效稳定净化,采用该方法可获得两种净化甲醛材料,一种是方法直接产生的目标产物,一种是废液合理利用后获得的甲醛净化材料。与文献中报道的发明方法不同,本发明提供的方法不仅无废液产生,而且将废液合理利用,变废为宝。The purification material obtained by the method of the present invention can realize high-efficiency and stable purification of formaldehyde under low concentration, high space velocity, and flow conditions, and two kinds of purification formaldehyde materials can be obtained by using the method, one is the target product directly produced by the method, and the other is waste liquid The formaldehyde purification material obtained after reasonable utilization. Different from the inventive method reported in the literature, the method provided by the present invention not only produces no waste liquid, but also makes rational use of the waste liquid, turning waste into treasure.

所述高效净化甲醛材料是MnOx和改性活性氧化铝中的一种或者二者的组合。The high-efficiency purifying formaldehyde material is one or a combination of MnOx and modified activated alumina.

高锰酸钾溶液的摩尔浓度为0.10~0.20 mol/L;所述甲酸溶液的摩尔浓度为0.30~0.60 mol/L。其中,高锰酸钾和甲酸的摩尔比为2:3。The molar concentration of the potassium permanganate solution is 0.10-0.20 mol/L; the molar concentration of the formic acid solution is 0.30-0.60 mol/L. Wherein, the molar ratio of potassium permanganate and formic acid is 2:3.

本发明提供一种高效净化甲醛材料,其特征在于根据上述 任一所述方法制备得到。The present invention provides a kind of high-efficiency purifying formaldehyde material, it is characterized in that it is prepared according to any one of the above-mentioned methods.

本发明提供一种高效净化甲醛材料的应用。The invention provides an application of a formaldehyde purifying material with high efficiency.

具体操作过程如下:高锰酸钾溶液(摩尔浓度为0.10~0.20 mol/L)和甲酸(摩尔浓度为0.30~0.60 mol/L)溶液在室温下搅拌2~2.5 h后抽滤后得到滤饼和滤液。其中,高锰酸钾和甲酸的摩尔比为2:3。滤饼层置于40-60 oC鼓风干燥箱中干燥10-14 h得MnOx;滤液等体积浸渍球状活性氧化铝后得到改性活性氧化铝。所得MnOx和改性活性氧化铝可应用于室内低浓度甲醛气体的净化过程中,MnOx可通过固载技术负载到活性氧化铝上应用于空气净化器的净化模块中,改性状活性氧化铝可直接应用于空气净化器的净化模块中。The specific operation process is as follows: Potassium permanganate solution (molar concentration is 0.10~0.20 mol/L) and formic acid (molar concentration is 0.30~0.60 mol/L) solution is stirred at room temperature for 2~2.5 hours, and the filter cake is obtained after suction filtration and filtrate. Wherein, the molar ratio of potassium permanganate and formic acid is 2:3. The filter cake layer was dried in a blast drying oven at 40-60 o C for 10-14 h to obtain MnOx; the filtrate was impregnated with spherical activated alumina in equal volume to obtain modified activated alumina. The obtained MnOx and modified activated alumina can be used in the purification process of indoor low-concentration formaldehyde gas. MnOx can be loaded onto activated alumina through solid-loading technology and used in the purification module of air purifiers. Modified activated alumina can be directly Applied in the purification module of the air purifier.

本发明提供的方法将产物分为两个部分,滤饼部分即MnOx和滤液部分。高锰酸钾和甲酸反应的时间限制为2-2.5h,通过对比实际产生的产物量和理论值对比,在限定的时间内,二者并未完全反应,结合XRD结果,显示产物是多种价态锰组成的锰氧化物,即不完全反应的产物MnOx。所对应的新鲜滤液的pH在8~9之间,呈现弱碱性。性能测试发现,在低浓度、高空速、流动条件下,MnOx可彻底净化甲醛,对甲醛的去除率可达100%,并且具有非常好的稳定性,6.5h后仍可保持100%转化;改性活性氧化铝球对于甲醛的净化率可达70~80%,且具有非常好的稳定性。The method provided by the invention divides the product into two parts, the filter cake part is MnOx and the filtrate part. The time limit for the reaction of potassium permanganate and formic acid is 2-2.5h. By comparing the actual amount of product produced with the theoretical value, the two did not completely react within the limited time. Combined with the XRD results, it shows that the product is a variety of Manganese oxide composed of valence manganese, that is, the incomplete reaction product MnOx. The pH of the corresponding fresh filtrate is between 8 and 9, which is slightly alkaline. Performance tests found that under low concentration, high space velocity, and flow conditions, MnOx can completely purify formaldehyde, the removal rate of formaldehyde can reach 100%, and it has very good stability, and can still maintain 100% conversion after 6.5 hours; Active alumina balls have a purification rate of 70-80% for formaldehyde and have very good stability.

本发明方法主要具有以下特点:The inventive method mainly has the following characteristics:

(1)以零废液为出发点,在制备高效甲醛净化材料的同时,将废液合理利用,即变废为宝,实现零废液生产。(1) Taking zero waste liquid as the starting point, while preparing high-efficiency formaldehyde purification materials, the waste liquid is rationally utilized, that is, turning waste into treasure and realizing zero waste liquid production.

(2)方法简单,无废液产生,这对于大规模生产极为重要,避免了生产过程中的对环境的危害。(2) The method is simple, and no waste liquid is produced, which is extremely important for large-scale production, and the harm to the environment in the production process is avoided.

(3)对甲醛的净化率高。可完全转化甲醛,且具有非常好的稳定性。达到对室内甲醛的完全净化。(3) The purification rate of formaldehyde is high. It can completely convert formaldehyde and has very good stability. To achieve complete purification of indoor formaldehyde.

附图说明Description of drawings

图1为实施例1中MnOx对甲醛的净化曲线;Fig. 1 is the purifying curve of MnO in embodiment 1 to formaldehyde;

图2为实施例2中改性活性氧化铝对甲醛的净化曲线。Fig. 2 is the purification curve of modified activated alumina to formaldehyde in Example 2.

具体实施方式detailed description

实施例1Example 1

称取3.16 g高锰酸钾(KMnO4)溶于100 mL水中,室温下搅拌至溶解;量取1.33 mL 85%(质量分数)的甲酸溶液溶于50 mL去离子水中。混合均匀后搅拌下将甲酸溶液逐滴加入高锰酸钾溶液中,室温下继续搅拌2 h。真空抽滤得滤饼和滤液部分。滤饼直接置于50 oC鼓风干燥箱中干燥12 h后得到MnOx-1。滤液等体积浸渍活性氧化铝得到改性的活性氧化铝,记为改性活性氧化铝-1。Weigh 3.16 g of potassium permanganate (KMnO 4 ) and dissolve it in 100 mL of water, stir at room temperature until dissolved; measure 1.33 mL of 85% (mass fraction) formic acid solution and dissolve it in 50 mL of deionized water. After mixing evenly, add the formic acid solution dropwise to the potassium permanganate solution under stirring, and continue stirring at room temperature for 2 h. The filter cake and the filtrate part were obtained by vacuum filtration. The filter cake was directly dried in a blast oven at 50 o C for 12 h to obtain MnOx-1. The filtrate is impregnated with activated alumina in equal volume to obtain modified activated alumina, which is denoted as modified activated alumina-1.

图1为本实施例中MnOx对甲醛的净化曲线。Fig. 1 is the purification curve of MnOx to formaldehyde in the present embodiment.

实施例2Example 2

将实施例1中的高锰酸钾的质量3.16 g改为1.58 g,85%甲酸的体积1.33 mL变为0.67mL,其他制备条件与实施例1相同,得MnOx-2和改性活性氧化铝-2。Change the quality 3.16 g of potassium permanganate in Example 1 to 1.58 g, and the volume 1.33 mL of 85% formic acid becomes 0.67 mL, and other preparation conditions are the same as in Example 1 to obtain MnOx-2 and modified activated alumina -2.

图2为本实施例中改性活性氧化铝对甲醛的净化曲线。Fig. 2 is the purification curve of modified activated alumina to formaldehyde in this example.

实施例3Example 3

将实施例1中的高锰酸钾的质量3.16 g改为2.37 g,85%甲酸的体积1.33 mL变为1.0mL,其他制备条件与实施例1相同,得MnOx-3和改性活性氧化铝-3。Change the quality 3.16 g of potassium permanganate in Example 1 to 2.37 g, and the volume 1.33 mL of 85% formic acid becomes 1.0 mL, and other preparation conditions are the same as in Example 1 to obtain MnOx-3 and modified activated alumina -3.

实施例4Example 4

将实施例1中的高锰酸钾的质量3.16 g改为2.84 g,85%甲酸的体积1.33 mL变为1.9mL,其他制备条件与实施例1相同,得MnOx-4和改性活性氧化铝-4。Change the quality 3.16 g of potassium permanganate in Example 1 to 2.84 g, and the volume 1.33 mL of 85% formic acid becomes 1.9 mL, and other preparation conditions are the same as in Example 1 to obtain MnOx-4 and modified activated alumina -4.

应用实施例application example

将实施例1中所得样品MnOx-1和改性活性氧化铝-1应用于室内低浓度甲醛净化反应中,首先在连续流动固定床装置中测试其性能。气体总流量为500 mL/min,反应压力为常压~1atm,甲醛的初始浓度为4.8~5.4 mg/m3,样品用量:0.2 g。结果显示,可将该浓度的甲醛完全净化,即初始净化率为100%,且连续反应6.5 h后初始效率无变化。改性活性氧化铝对甲醛的初始净化率为70%,在该转化率下可维持2.5 h。The sample MnOx-1 and modified activated alumina-1 obtained in Example 1 were applied to indoor low-concentration formaldehyde purification reaction, and their performance was first tested in a continuous flow fixed bed device. The total gas flow rate is 500 mL/min, the reaction pressure is normal pressure~1atm, the initial concentration of formaldehyde is 4.8~5.4 mg/m 3 , and the sample dosage is 0.2 g. The results showed that the concentration of formaldehyde could be completely purified, that is, the initial purification rate was 100%, and the initial efficiency did not change after continuous reaction for 6.5 h. The initial purification rate of formaldehyde by modified activated alumina is 70%, and the conversion rate can be maintained for 2.5 h.

进一步将该材料采用发明人之前已授权专利ZL201510403899.6中的方法涂覆至氧化铝小球上,装填后测试其在30 m3净化仓内对于甲醛的净化性能。净化仓内甲醛的初始浓度为1 mg/m3,结果显示,可实现甲醛的彻底净化。Further, the material was coated on alumina pellets using the method in the inventor's previously authorized patent ZL201510403899.6, and its purification performance for formaldehyde in a 30 m 3 purification chamber was tested after filling. The initial concentration of formaldehyde in the purification chamber is 1 mg/m 3 , and the results show that the complete purification of formaldehyde can be achieved.

Claims (5)

1.一种高效净化甲醛材料的制备方法,其特征在于具体操作如下:高锰酸钾溶液和甲酸溶液在室温下搅拌2~2.5 h后抽滤后得到滤饼和滤液,滤饼置于40-60 oC鼓风干燥箱中干燥10-14 h得MnOx;滤液等体积浸渍球状活性氧化铝后得到改性活性氧化铝。1. A preparation method for efficiently purifying formaldehyde material is characterized in that concrete operations are as follows: potassium permanganate solution and formic acid solution are stirred at room temperature for 2 to 2.5 h and then suction filtered to obtain filter cake and filtrate, and the filter cake is placed in 40 Dry in a blast oven at -60 o C for 10-14 h to obtain MnOx; impregnate spherical activated alumina with an equal volume of the filtrate to obtain modified activated alumina. 2.根据权利要求1所述高效净化甲醛材料的制备方法,其特征在于,所述高效净化甲醛材料是MnOx和改性活性氧化铝中的一种或者二者的组合。2. The preparation method of the high-efficiency purification formaldehyde material according to claim 1, characterized in that, the high-efficiency purification formaldehyde material is one or a combination of MnOx and modified activated alumina. 3.权利要求1所述高效净化甲醛材料的制备方法,其特征在于,高锰酸钾溶液的摩尔浓度为0.10~0.20 mol/L;所述甲酸溶液的摩尔浓度为0.30~0.60 mol/L。其中,高锰酸钾和甲酸的摩尔比为2:3。3. the preparation method of the described efficient purification formaldehyde material of claim 1, is characterized in that, the molar concentration of potassium permanganate solution is 0.10~0.20 mol/L; The molar concentration of described formic acid solution is 0.30~0.60 mol/L. Wherein, the molar ratio of potassium permanganate and formic acid is 2:3. 4.一种高效净化甲醛材料,其特征在于根据权利要求1-3 任一所述方法制备得到。4. A high-efficiency purifying formaldehyde material, characterized in that it is prepared according to any one of claims 1-3. 5.根据权利要求4所述高效净化甲醛材料的应用。5. according to the application of the efficient purifying formaldehyde material described in claim 4.
CN201711065016.0A 2017-11-02 2017-11-02 Preparation method of high-efficient purification formaldehyde materials and products thereof and application Pending CN107626303A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711065016.0A CN107626303A (en) 2017-11-02 2017-11-02 Preparation method of high-efficient purification formaldehyde materials and products thereof and application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711065016.0A CN107626303A (en) 2017-11-02 2017-11-02 Preparation method of high-efficient purification formaldehyde materials and products thereof and application

Publications (1)

Publication Number Publication Date
CN107626303A true CN107626303A (en) 2018-01-26

Family

ID=61107824

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711065016.0A Pending CN107626303A (en) 2017-11-02 2017-11-02 Preparation method of high-efficient purification formaldehyde materials and products thereof and application

Country Status (1)

Country Link
CN (1) CN107626303A (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102742054A (en) * 2010-01-29 2012-10-17 永备电池有限公司 Method of making an electrochemical cell with a catalytic electrode including manganese dioxide
CN103041767A (en) * 2013-01-05 2013-04-17 苏州工业园区安泽汶环保技术有限公司 Preparation method of indicating formaldehyde adsorbent
CN104190251A (en) * 2014-09-09 2014-12-10 清华大学 Air purification material and preparation method and application thereof
CN104258898A (en) * 2014-10-29 2015-01-07 滨州学院 Manganese-loaded oxide zeolite and application of manganese-loaded oxide zeolite in treatment of formaldehyde wastewater
CN104324686A (en) * 2014-10-17 2015-02-04 中科润蓝环保技术(北京)有限公司 Indoor air purifying agent, preparation method thereof, and indoor air purifier filter screen
CN104396054A (en) * 2012-05-23 2015-03-04 巴斯夫欧洲公司 Process for producing a carbon-supported manganese oxide catalyst and its use in rechargeable lithium-air batteries
CN106587246A (en) * 2016-11-29 2017-04-26 洛阳建龙微纳新材料股份有限公司 Application of modified activated alumina in wastewater defluorination
CN106745285A (en) * 2017-03-01 2017-05-31 哈尔滨工业大学 A kind of α MnO2The preparation method of nano wire
CN106824174A (en) * 2017-03-22 2017-06-13 无锡威孚环保催化剂有限公司 A kind of coccoid catalyst of high-efficient purification nitrogen oxides and preparation method thereof

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102742054A (en) * 2010-01-29 2012-10-17 永备电池有限公司 Method of making an electrochemical cell with a catalytic electrode including manganese dioxide
CN104396054A (en) * 2012-05-23 2015-03-04 巴斯夫欧洲公司 Process for producing a carbon-supported manganese oxide catalyst and its use in rechargeable lithium-air batteries
CN103041767A (en) * 2013-01-05 2013-04-17 苏州工业园区安泽汶环保技术有限公司 Preparation method of indicating formaldehyde adsorbent
CN104190251A (en) * 2014-09-09 2014-12-10 清华大学 Air purification material and preparation method and application thereof
CN104324686A (en) * 2014-10-17 2015-02-04 中科润蓝环保技术(北京)有限公司 Indoor air purifying agent, preparation method thereof, and indoor air purifier filter screen
CN104258898A (en) * 2014-10-29 2015-01-07 滨州学院 Manganese-loaded oxide zeolite and application of manganese-loaded oxide zeolite in treatment of formaldehyde wastewater
CN106587246A (en) * 2016-11-29 2017-04-26 洛阳建龙微纳新材料股份有限公司 Application of modified activated alumina in wastewater defluorination
CN106745285A (en) * 2017-03-01 2017-05-31 哈尔滨工业大学 A kind of α MnO2The preparation method of nano wire
CN106824174A (en) * 2017-03-22 2017-06-13 无锡威孚环保催化剂有限公司 A kind of coccoid catalyst of high-efficient purification nitrogen oxides and preparation method thereof

Similar Documents

Publication Publication Date Title
CN101204654A (en) A kind of supported precious metal catalyst and preparation method thereof for catalytic oxidation of benzene series at low temperature
CN101695651B (en) Copper and iron-loaded modified activated carbon absorbent and method for preparing same
CN101279236A (en) Purificant for adsorbing ammonia gas and method of preparing the same
CN110115935B (en) A kind of preparation method of low-concentration formaldehyde purification material
CN103357409A (en) Room-temperature catalytic oxidizing agent of formaldehyde employing composite noble metal alloy, and preparation method thereof
CN107583608A (en) In-situ preparation method of bifunctional material and products thereof and application
CN108499556A (en) A kind of low-temperature denitration catalyst and preparation method thereof
CN108479721A (en) A kind of methyl aldehyde adsorption material and its application
CN110773224A (en) A kind of preparation method of alkali-resistant denitration catalyst
CN116212853B (en) δ-MnO2 catalytic material and its preparation method and its application in the preparation of formaldehyde-degradable filters
CN104841428B (en) Preparation method that is a kind of while removing nitric oxide sulfur dioxide mercury catalyst
CN101693193A (en) Rare earth-Cu-Fe active carbon adsorbent, preparation method and application thereof
CN102614858B (en) Reproducible selective adsorption-photocatalysis composite material and preparation method and application thereof
CN108311147A (en) Preparation method for the perovskite supported noble metal catalyst for purifying benzene
CN107754788A (en) Catalyst of formaldehyde catalytic degradation and its preparation method and application under normal temperature
CN107243321A (en) A kind of air cleaning material of long-acting removal organic polluter
CN103752278A (en) Modified active carbon for mercury removing, and preparation method thereof
CN102580731B (en) Gamma-aluminum oxide globular catalyst for purifying waste gas of volatile compounds and preparation method for catalyst
CN107626303A (en) Preparation method of high-efficient purification formaldehyde materials and products thereof and application
CN112755953B (en) Adsorbent for removing nitrogen oxides in fluid, preparation method and application
CN104353355A (en) Ceramic purifier for purifying ozone in air and preparation method of ceramic purifier
CN108176349B (en) Al (aluminum)2O3@TiO2Preparation method of core-shell structure simultaneous desulfurization and denitrification adsorbent
CN118162096A (en) Activated alumina-based chemical adsorption material and preparation method thereof
CN100431689C (en) Preparation method of composite adsorbent for removing nitrogen oxides
CN110170306B (en) Process for preparing adsorbent for efficiently removing low-concentration formaldehyde in air at normal temperature by two-step modification method, product and application thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20180126