CN106731234B - A kind of preparation method of binary denitration sulfur resistant catalyst composite filtering material - Google Patents
A kind of preparation method of binary denitration sulfur resistant catalyst composite filtering material Download PDFInfo
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- 238000002360 preparation method Methods 0.000 title claims description 8
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- 238000001914 filtration Methods 0.000 title claims 6
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- FIXLYHHVMHXSCP-UHFFFAOYSA-H azane;dihydroxy(dioxo)molybdenum;trioxomolybdenum;tetrahydrate Chemical compound N.N.N.N.N.N.O.O.O.O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O[Mo](O)(=O)=O.O[Mo](O)(=O)=O.O[Mo](O)(=O)=O FIXLYHHVMHXSCP-UHFFFAOYSA-H 0.000 description 5
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- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 1
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- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 1
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8628—Processes characterised by a specific catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts 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
- B01J23/84—Catalysts 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
- B01J23/889—Manganese, technetium or rhenium
- B01J23/8892—Manganese
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/10—Filtering material manufacturing
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- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
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- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
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Abstract
本发明提供了一种二元脱硝抗硫催化剂复合滤料的制备方法。以经过表面活性剂处理的聚苯硫醚滤料为载体,KMnO4和MnSO4·H2O和(NH4)6Mo7O24·4H2O为催化剂前驱体,以去离子水为溶剂,通过高温高压水热法制得复合型滤料。本发明由于采用二元脱硝抗硫催化剂,比单组分催化剂更好的脱硝抗硫性能,而且采用高温高压水热的方法,有利于催化剂在聚苯硫醚滤料表面的生成和负载,催化剂的负载量大于5mg/cm2时都可获得较好的脱硝性能。本发明反应合成方法快速和操作简单,制得的复合滤料适用于除尘剂和脱硝剂。
The invention provides a method for preparing a composite filter material of a binary denitrification and antisulfur catalyst. The surfactant-treated polyphenylene sulfide filter material is used as the carrier, KMnO 4 and MnSO 4 ·H 2 O and (NH 4 ) 6 Mo 7 O 24 ·4H 2 O are used as catalyst precursors, and deionized water is used as the solvent , the composite filter material is prepared by high temperature and high pressure hydrothermal method. Because the present invention adopts a binary denitrification and antisulfur catalyst, it has better denitrification and antisulfur performance than a single-component catalyst, and adopts a high-temperature, high-pressure hydrothermal method, which is beneficial to the formation and loading of the catalyst on the surface of the polyphenylene sulfide filter material. Good denitrification performance can be obtained when the loading amount is greater than 5mg/cm 2 . The reaction synthesis method of the invention is quick and easy to operate, and the prepared composite filter material is suitable for dust remover and denitrification agent.
Description
技术领域technical field
本发明属于功能性复合滤料技术领域,特别涉及到制备一种二元脱硝抗硫催化剂复合滤料的制备方法。The invention belongs to the technical field of functional composite filter materials, and in particular relates to a method for preparing a composite filter material for binary denitrification and anti-sulfur catalysts.
背景技术Background technique
我国是一个缺油、少气、富煤的国家,煤炭是我国的主要能源,煤炭原料的燃烧会产生大量的污染物,空气污染物中87%的二氧化硫(SO2),71%的一氧化碳(CO),67%的氮氧化物(NOx)和60%的烟尘均来源于煤炭原料的燃烧。一大部分污染物是氮氧化合物,NOx已与SO2、CO齐名,成为造成空气污染的主要污染源之一,主要包括一氧化氮(NO)、二氧化氮(NO2)和一氧化二氮(N2O),其中NO占了90-95%,NO2占5-10%,而N2O仅有1%左右。空气中的NOx对人类健康和生态环境均有严重的危害。NO是无色无味的气体,其与血红蛋白中的氧结合能力很强,会严重影响血液的输氧能力并刺激人的眼睛、呼吸器官等,严重时会诱发细胞癌变。另外,NO还容易在空气中自发的被氧化成NO2,从而造成更严重后果。China is a country short of oil, gas, and rich in coal. Coal is the main energy source in our country. The combustion of coal raw materials will produce a large number of pollutants. Among the air pollutants, 87% are sulfur dioxide (SO 2 ), and 71% are carbon monoxide ( CO), 67% of nitrogen oxides (NO x ) and 60% of soot all come from the combustion of coal raw materials. A large part of the pollutants are nitrogen oxides. NO x has become one of the main sources of air pollution with the same name as SO 2 and CO. It mainly includes nitric oxide (NO), nitrogen dioxide (NO 2 ) and di Nitrogen (N 2 O), of which NO accounts for 90-95%, NO 2 accounts for 5-10%, and N 2 O only accounts for about 1%. NO x in the air is a serious hazard to human health and ecological environment. NO is a colorless and odorless gas. It has a strong ability to combine with oxygen in hemoglobin, which will seriously affect the oxygen transport capacity of the blood and stimulate human eyes and respiratory organs. In severe cases, it will induce cell cancer. In addition, NO is easily oxidized into NO 2 spontaneously in the air, causing more serious consequences.
另一部分污染物是硫化物,最终燃煤烟气中硫元素以SO2形态存在。SO2是一种无色具有强烈刺激性气味的气体,易溶解于人体的血液和其他黏性液。大气中的SO2会导致呼吸道炎症、支气管炎、肺气肿、眼结膜炎症等。同时还会使青少年的免疫力降低,抗病能力变弱。 SO2在氧化剂、光的作用下,能生成硫酸盐气溶胶,硫酸盐气溶胶能使人致病,增加病人死亡率。根据经济合作发展组织(OECD)的研究 ,当硫酸盐年浓度在10μg/m3 左右时,每减少10%的浓度能使死亡率降低0.5%; SO2还能与大气中的飘尘黏附,当人体呼吸时吸入带有SO2的飘尘,会使SO2的毒性增强。研究表明,在高浓度的SO2的影响下,植物产生急性危害,叶片表面产生坏死斑,或直接使植物叶片枯萎脱落;在低浓度SO2的影响下,植物的生长机能受到影响,造成产量下降,品质变坏。Another part of the pollutants is sulfide, and the sulfur element in the final coal-fired flue gas exists in the form of SO 2 . SO 2 is a colorless gas with a strong pungent odor, easily soluble in human blood and other viscous fluids. SO 2 in the atmosphere can cause respiratory inflammation, bronchitis, emphysema, conjunctival inflammation, etc. At the same time, it will reduce the immunity of young people and weaken their disease resistance. Under the action of oxidants and light, SO 2 can generate sulfate aerosols, which can make people sick and increase the mortality of patients. According to the research of the Organization for Economic Co-operation and Development (OECD), when the annual concentration of sulfate is around 10 μg/m 3 , every 10% reduction in the concentration can reduce the mortality rate by 0.5%; SO 2 can also adhere to the floating dust in the atmosphere. When the human body inhales the floating dust with SO 2 , the toxicity of SO 2 will be enhanced. Studies have shown that under the influence of high concentrations of SO 2 , plants are acutely damaged, resulting in necrotic spots on the surface of leaves, or directly causing the leaves of plants to wither and fall off; under the influence of low concentrations of SO 2 , the growth function of plants is affected, resulting in yield loss. decline, the quality deteriorates.
目前用来处理吸收电厂燃煤锅炉和垃圾焚烧所产生的废气主要选用滤料,其中聚苯硫醚(PPS)滤料是目前电厂燃煤锅炉和垃圾焚烧滤袋上的首选材料,因其具有耐高温、抗水解、高阻燃、耐酸碱的优异性能。然而,商用催化剂的温度窗口在300-400℃的高温区域,远高于聚苯硫醚滤料的使用温度(170℃左右);另外,聚苯硫醚惰性的分子结构也使其表面很难固定住催化剂颗粒。因此,研究和开发低温高效的二元脱硝抗硫催化剂及其与滤料的复合技术成为的研究重点。At present, filter materials are mainly used to treat and absorb the waste gas produced by coal-fired boilers and waste incineration in power plants. Among them, polyphenylene sulfide (PPS) filter materials are the preferred materials for coal-fired boilers in power plants and waste incineration filter bags, because of their unique properties. Excellent properties of high temperature resistance, hydrolysis resistance, high flame retardancy, acid and alkali resistance. However, the temperature window of commercial catalysts is in the high-temperature region of 300-400°C, which is much higher than the use temperature of polyphenylene sulfide filter media (about 170°C); in addition, the inert molecular structure of polyphenylene sulfide also makes it difficult to Holds catalyst particles. Therefore, the research and development of low-temperature and high-efficiency binary denitrification and anti-sulfur catalysts and their composite technology with filter materials have become the research focus.
已商业化的钒钛体系催化剂起活温度高(>300℃),难以在烟气处理系统末端应用,且安装运行费用较高。因此,经济性高且适用于末端处理的低温SCR技术成为研究人员关注的热点。无载体Mn-MoOx催化剂在许多文献中记录的其在低温中高效的脱硝效率,其脱硝能力在120℃时NOx可几乎完全转化为N2是脱硝处理的首选,但还没有合适的技术将其成功的应用于滤料上。因此本专利突破性的运用高温高压水热法将其负载在滤料上。The commercialized vanadium-titanium system catalyst has a high activation temperature (>300°C), which is difficult to apply at the end of the flue gas treatment system, and the installation and operation costs are high. Therefore, low-temperature SCR technology that is economical and suitable for end treatment has become a hot spot for researchers. The unsupported Mn- MoOx catalyst has been recorded in many literatures for its high denitrification efficiency at low temperatures, and its denitrification ability can almost completely convert NOx into N2 at 120 °C. It is the first choice for denitrification treatment, but there is no suitable technology to convert It is successfully applied to the filter material. Therefore, this patent breakthrough uses high temperature and high pressure hydrothermal method to load it on the filter material.
发明内容Contents of the invention
本发明的目的是要制备将高效的脱硝抗硫二元催化剂与聚苯硫醚(PPS)相结合的方法,通过水热法的方式,将催化剂一步负载到聚苯硫醚(PPS)表面,由于高温高压的水热的方法,使Mn-MoOx催化剂在PPS表面负载均匀牢固,且具有较高的脱销率和较好的抗硫效果。The purpose of the present invention is to prepare a method of combining an efficient denitrification and anti-sulfur binary catalyst with polyphenylene sulfide (PPS), and load the catalyst on the surface of polyphenylene sulfide (PPS) in one step through the hydrothermal method. Due to the hydrothermal method of high temperature and high pressure, the Mn-MoO x catalyst is evenly and firmly loaded on the surface of PPS, and has a high stock removal rate and a good anti-sulfur effect.
本发明采用的技术方案是:The technical scheme adopted in the present invention is:
一种二元脱硝抗硫催化剂复合滤料的制备方法:以经过表面活性剂处理的聚苯硫醚为载体,KMnO4和MnSO4·H2O和(NH4)6Mo7O24·4H2O为催化剂前驱体,以去离子水为溶剂,通过高温高压水热法制得复合型滤料。A preparation method of a binary denitrification antisulfur catalyst composite filter material: using surfactant-treated polyphenylene sulfide as a carrier, KMnO 4 and MnSO 4 ·H 2 O and (NH 4 ) 6 Mo 7 O 24 ·4H 2 O is used as catalyst precursor, and deionized water is used as solvent to prepare composite filter material by high temperature and high pressure hydrothermal method.
具体步骤如下:Specific steps are as follows:
(1)称0.0273g十二烷基硫酸钠溶于50ml去离子水中,然后放入剪成小圆片的聚苯硫醚滤料,超声处理1h,再取出烘干备用;(1) Dissolve 0.0273g of sodium lauryl sulfate in 50ml of deionized water, then put it into the polyphenylene sulfide filter material cut into small discs, ultrasonically treat it for 1 hour, then take it out and dry it for later use;
(2)将四水合钼酸铵((NH4)6Mo7O24·4H2O)加入到盛有20ml去离子水的烧杯中,并放入搅拌子,室温下搅拌5min,待四水合钼酸铵充分溶解后,加入配置0.2M的KMnO4溶液20~80ml,并在室温中搅拌10min。(2) Add ammonium molybdate tetrahydrate ((NH 4 ) 6 Mo 7 O 24 4H 2 O) into a beaker filled with 20ml of deionized water, put it into a stirring bar, stir at room temperature for 5min, and wait for tetrahydration After the ammonium molybdate is fully dissolved, add 20-80ml of 0.2M KMnO 4 solution and stir at room temperature for 10min.
(3)10min后待溶液搅拌均匀,配置0.006~0.024mol的MnSO4·H2O溶液30ml并在超声环境下溶解,之后加入之前混合均匀的溶液,同时加入之前处理过的PPS滤料,再在室温下搅拌15min。(3) After 10 minutes, when the solution is stirred evenly, prepare 30ml of 0.006~0.024mol MnSO 4 ·H 2 O solution and dissolve it in an ultrasonic environment, then add the previously mixed solution, and add the previously treated PPS filter material at the same time, and then Stir at room temperature for 15 min.
(4)将混合均匀的溶液倒入聚四氟乙烯内胆中,在放入高压釜中,置于180℃的真空干燥箱中反应18h,之后取出高压釜,冷却到室温打开反应釜取出PPS滤料洗净烘干待测。(4) Pour the uniformly mixed solution into a polytetrafluoroethylene liner, put it in an autoclave, and place it in a vacuum oven at 180°C to react for 18 hours, then take out the autoclave, cool to room temperature, open the autoclave and take out the PPS The filter material was washed and dried for testing.
进一步地,按质量比计,聚苯硫醚:高锰酸钾=1:1.5-2.5。Further, in terms of mass ratio, polyphenylene sulfide:potassium permanganate=1:1.5-2.5.
进一步地,溶液中的Mn:Mo的摩尔比例为1~3:1。Further, the molar ratio of Mn:Mo in the solution is 1˜3:1.
所述的滤料为聚苯硫醚针刺滤料,是以聚苯硫醚纤维为原料,经开松、复合混料、梳理、铺网、针刺、热定型和烧毛压光制备而成,平均孔径40μm。The filter material is polyphenylene sulfide needle-punched filter material, which is prepared from polyphenylene sulfide fibers through opening, compound mixing, carding, net laying, acupuncture, heat setting and singeing. into, with an average pore size of 40 μm.
所述的复合滤料可同时作为除尘剂和脱硝剂应用,催化剂的负载量大于5mg/cm2时都可获得较好的脱硝性能。The composite filter material can be used as a dedusting agent and a denitration agent at the same time, and better denitrification performance can be obtained when the loading amount of the catalyst is greater than 5 mg/cm 2 .
本发明利用表面活性剂SDS预先处理聚苯硫醚PPS滤料,使其表面获得较多的活性含氧官能团,例如羟基,羧基等。由于这些含氧官能团的存在使得原本惰性的聚苯硫醚表面得以活化,并可以通过静电效应吸收(NH4)6Mo7O24·4H2O和MnSO4·H2O中的Mo4+和Mn2+,为之后在PPS滤料表面生成催化剂提供基础。The present invention utilizes surfactant SDS to pre-treat polyphenylene sulfide PPS filter material to obtain more active oxygen-containing functional groups on its surface, such as hydroxyl group and carboxyl group. Due to the existence of these oxygen-containing functional groups, the original inert polyphenylene sulfide surface is activated, and can absorb Mo 4+ in (NH 4 ) 6 Mo 7 O 24 ·4H 2 O and MnSO 4 ·H 2 O through electrostatic effect. and Mn 2+ , which provide the basis for the formation of catalysts on the surface of the PPS filter material.
本发明的有益效果:Beneficial effects of the present invention:
1、相比一元Mn基为主的脱销滤料,由于脱硝的过程中,废气中SO2容易与高效脱硝催化剂MnOx反应形成MnSO4,此时催化剂变性失活,导致了滤料的脱销率大大下降,甚至几乎失去脱硝性能,本法由于加了稀土元素Mo,并且Mo是目前主流的抗硫剂,具有很好的抗硫效果,因此使其具有比单组分催化剂更好的脱硝抗硫性能。1. Compared with the out-of-stock filter material based on the monobasic Mn base, during the denitrification process, SO 2 in the exhaust gas is easy to react with the efficient denitration catalyst MnO x to form MnSO 4 . At this time, the catalyst is denatured and deactivated, resulting in the out-of-stock rate of the filter material The denitrification performance is greatly reduced, or even almost lost. This method has a better denitrification resistance than the single-component catalyst due to the addition of rare earth element Mo, and Mo is the current mainstream antisulfur agent, which has a good antisulfur effect. sulfur properties.
2、催化剂是通过高温高压水热法负载在聚苯硫醚(PPS)上的,一是通过高温反应是催化剂在PPS表面生成,二是通过强压使溶液中的其余催化剂负载在PPS上。高效利用,稳定负载。2. The catalyst is loaded on polyphenylene sulfide (PPS) through high temperature and high pressure hydrothermal method. First, the catalyst is generated on the surface of PPS through high temperature reaction, and second, the rest of the catalyst in the solution is loaded on PPS by strong pressure. Efficient utilization and stable load.
3、反应合成方法和操作都很简单,并且其反应快速,反应容器普遍使用简单,并且合成物质对环境没有污染,合成后的滤料表面负载量均匀且牢固,脱销率高。3. The reaction synthesis method and operation are very simple, and the reaction is fast, the reaction vessel is generally easy to use, and the synthetic substance does not pollute the environment, the surface load of the synthetic filter material is uniform and firm, and the out-of-stock rate is high.
4、合成过程中产生的催化剂可以回收使用,环保高效。4. The catalyst produced in the synthesis process can be recycled and used, which is environmentally friendly and efficient.
附图说明Description of drawings
图1 催化剂活性测试中,自制管式SCR反应器装置图。图中,1为气源;2为减压阀;3为质量流量计;4为混合器;5为空气预热器;6为催化床;7为滤料;8为烟气分析仪。;图2 为元素Mn:Mo摩尔比2:1时制备的样品的扫描电镜图。Fig. 1 Diagram of self-made tubular SCR reactor device in catalyst activity test. In the figure, 1 is a gas source; 2 is a pressure reducing valve; 3 is a mass flow meter; 4 is a mixer; 5 is an air preheater; 6 is a catalytic bed; 7 is a filter material; 8 is a flue gas analyzer. ; Fig. 2 is the scanning electron micrograph of the sample prepared when the element Mn:Mo molar ratio is 2:1.
具体实施方式Detailed ways
以下是本发明的几个具体实施例,进一步说明本发明,但是本发明不仅限于此。The following are several specific embodiments of the present invention to further illustrate the present invention, but the present invention is not limited thereto.
下列实施例中的PPS针刺毡滤料按以下方法制备得到:以聚苯硫醚(PPS)纤维为原料,经开松、复合混料、梳理、铺网、针刺、热定型和烧毛压光制备得到针刺毡滤料,平均孔径40μm。The PPS needle-punched felt filter material in the following examples is prepared by the following method: using polyphenylene sulfide (PPS) fibers as raw materials, through opening, compound mixing, carding, web laying, needle punching, heat setting and singeing The needle-punched felt filter material was prepared by calendering, with an average pore size of 40 μm.
实施例 1Example 1
首先称0.0273g十二烷基硫酸钠加入50ml去离子水中,然后放入剪成质量为0:4213g的PPS滤料圆片,超声处理1h,处理完取出烘干备用。再称取20ml去离子水加入250ml的烧杯中。然后准确称量四水合钼酸铵((NH4)6Mo7O24·4H2O)1.7651g,加入磁子搅拌5min,直至溶液混合均匀为止。配置浓度为0.2M的高锰酸钾溶液20ml,将所配的溶液超声或者摇晃至溶质完全溶解,加入之前的烧杯中,一起混合搅拌4min。再配置0.006mol的一水合硫酸锰30ml,加入之前混合均匀的溶液中,此时溶液中的Mn:Mo的比例为1:1,将之前烘干的PPS滤料圆片加入其中,置于室温下搅拌15min,混合均匀后溶液为棕褐色。First weigh 0.0273g of sodium lauryl sulfate and add it to 50ml of deionized water, then put it into a PPS filter disc with a cut mass of 0:4213g, ultrasonically treat it for 1 hour, take it out and dry it for later use. Then weigh 20ml of deionized water and add it to a 250ml beaker. Then accurately weigh 1.7651 g of ammonium molybdate tetrahydrate ((NH 4 ) 6 Mo 7 O 24 ·4H 2 O), add a magnet and stir for 5 minutes until the solution is evenly mixed. Prepare 20ml of potassium permanganate solution with a concentration of 0.2M, sonicate or shake the prepared solution until the solute is completely dissolved, add it to the previous beaker, and mix and stir for 4 minutes. Then configure 30ml of 0.006mol manganese sulfate monohydrate, and add it to the solution that was mixed uniformly before. At this time, the ratio of Mn:Mo in the solution is 1:1, and add the previously dried PPS filter disc into it, and place it at room temperature Stir for 15 minutes, and the solution is brown after mixing evenly.
待混合均匀后,将溶液转移到聚四氟乙烯内胆中,密封好后封装于高压釜中,放置于180℃的真空干燥箱中反应18h,反应结束后置于室温下冷却,冷却至室温后打开高压釜取出PPS滤料,并用去离子水和乙醇洗净,置于105℃中干燥4h,待测试。高锰酸钾的质量计算如下:0.2×0.02×158=0.632g。After mixing evenly, transfer the solution to a polytetrafluoroethylene liner, seal it well, package it in an autoclave, and place it in a vacuum drying oven at 180°C for 18 hours. After the reaction is completed, place it at room temperature and cool it down to room temperature Finally, open the autoclave to take out the PPS filter material, wash it with deionized water and ethanol, and dry it at 105°C for 4 hours before testing. The mass of potassium permanganate is calculated as follows: 0.2×0.02×158=0.632g.
复合滤料的脱硝性能在自制管式SCR反应器中进行评价。NO和NH3体积分数均为0.05 %,O2体积分数为5 %,其余为N2,气体流速为700mL·min-1,温度设置为140℃,用英国KM940烟气分析仪测得脱硝率为69%;温度设置为160℃,脱硝率为80%,温度设置为180℃,脱硝率为99%。并在180℃间隔30min测试抗硫能力,最后脱销率基本稳定在44%。The denitrification performance of the composite filter material was evaluated in a self-made tubular SCR reactor. The volume fractions of NO and NH 3 are both 0.05%, the volume fraction of O 2 is 5%, and the rest is N 2 , the gas flow rate is 700mL·min -1 , the temperature is set at 140°C, and the denitrification rate is measured by the British KM940 flue gas analyzer The temperature is set at 160°C, the denitrification rate is 80%, and the temperature is set at 180°C, the denitrification rate is 99%. The anti-sulfur ability was tested at 180°C at intervals of 30 minutes, and the final out-of-stock rate was basically stable at 44%.
实施例2Example 2
首先称0.0273g十二烷基硫酸钠加入50ml去离子水中,然后放入剪成质量为0.6320g的PPS滤料圆片,超声处理1h,处理完取出烘干备用。再称取20ml去离子水加入250ml的烧杯中。然后准确称量四水合钼酸铵((NH4)6Mo7O24·4H2O)1.7651g,加入磁子搅拌5min,直至溶液混合均匀为止。配置浓度为0.2M的高锰酸钾溶液40ml,将所配的溶液超声或者摇晃至溶质完全溶解,加入之前的烧杯中,一起混合搅拌4min。再配置0.012mol的一水合硫酸锰30ml,加入之前混合均匀的溶液中,此时溶液中的Mn:Mo的比例为2:1,将之前烘干的PPS滤料圆片加入其中,置于室温下搅拌15min,混合均匀后溶液为棕褐色。First weigh 0.0273g of sodium lauryl sulfate and add it to 50ml of deionized water, then put it into a PPS filter disc with a cut mass of 0.6320g, ultrasonically treat it for 1 hour, take it out and dry it for later use. Then weigh 20ml of deionized water and add it to a 250ml beaker. Then accurately weigh 1.7651 g of ammonium molybdate tetrahydrate ((NH 4 ) 6 Mo 7 O 24 ·4H 2 O), add a magnet and stir for 5 minutes until the solution is evenly mixed. Prepare 40ml of potassium permanganate solution with a concentration of 0.2M, sonicate or shake the prepared solution until the solute is completely dissolved, add it to the previous beaker, and mix and stir for 4 minutes. Then configure 30ml of 0.012mol manganese sulfate monohydrate, and add it to the solution that was mixed uniformly before. At this time, the ratio of Mn:Mo in the solution is 2:1. Add the previously dried PPS filter disc into it, and place it at room temperature Stir for 15 minutes, and the solution is brown after mixing evenly.
待混合均匀后,将溶液转移到聚四氟乙烯内胆中,密封好后封装于高压釜中,放置于180℃的真空干燥箱中反应18h,反应结束后置于室温下冷却,冷却至室温后打开高压釜取出PPS滤料,并用去离子水和乙醇洗净,置于105℃中干燥4h,待测试。高锰酸钾的质量计算如下:0.2×0.04×158=1.264g。After mixing evenly, transfer the solution to a polytetrafluoroethylene liner, seal it well, package it in an autoclave, and place it in a vacuum drying oven at 180°C for 18 hours. After the reaction is completed, place it at room temperature and cool it down to room temperature Finally, open the autoclave to take out the PPS filter material, wash it with deionized water and ethanol, and dry it at 105°C for 4 hours before testing. The mass of potassium permanganate is calculated as follows: 0.2×0.04×158=1.264g.
复合滤料的脱硝性能在自制管式SCR反应器中进行评价。NO和NH3体积分数均为0.05 %,O2体积分数为5 %,其余为N2,气体流速为700mL·min-1,温度设置为140℃,用英国KM940烟气分析仪测得脱硝率为77%;温度设置为160℃,脱硝率为100%。并在180℃间隔30min测试抗硫能力,最后脱销率基本稳定在55%。The denitrification performance of the composite filter material was evaluated in a self-made tubular SCR reactor. The volume fractions of NO and NH 3 are both 0.05%, the volume fraction of O 2 is 5%, and the rest is N 2 , the gas flow rate is 700mL·min -1 , the temperature is set at 140°C, and the denitrification rate is measured by the British KM940 flue gas analyzer is 77%; the temperature is set to 160°C, and the denitrification rate is 100%. The anti-sulfur ability was tested at 180°C at intervals of 30 minutes, and the final out-of-stock rate was basically stable at 55%.
实施例3Example 3
首先称0.0273g十二烷基硫酸钠加入50ml去离子水中,然后放入剪成质量为1.011g的PPS滤料圆片,超声处理1h,处理完取出烘干备用。再称取20ml去离子水加入250ml的烧杯中。然后准确称量四水合钼酸铵((NH4)6Mo7O24·4H2O)1.7651g,加入磁子搅拌5min,直至溶液混合均匀为止。配置浓度为0.2M的高锰酸钾溶液80ml,将所配的溶液超声或者摇晃至溶质完全溶解,加入之前的烧杯中,一起混合搅拌4min。再配置0.009mol的一水合硫酸锰30ml,加入之前混合均匀的溶液中,此时溶液中的Mn:Mo的比例为2.5:1,将之前烘干的PPS滤料圆片加入其中,置于室温下搅拌15min,混合均匀后溶液为棕褐色。First weigh 0.0273g of sodium lauryl sulfate and add it to 50ml of deionized water, then put it into a PPS filter disc with a mass of 1.011g, ultrasonicate for 1 hour, take it out and dry it for later use. Then weigh 20ml of deionized water and add it to a 250ml beaker. Then accurately weigh 1.7651 g of ammonium molybdate tetrahydrate ((NH 4 ) 6 Mo 7 O 24 ·4H 2 O), add a magnet and stir for 5 minutes until the solution is evenly mixed. Prepare 80ml of potassium permanganate solution with a concentration of 0.2M, sonicate or shake the prepared solution until the solute is completely dissolved, add it to the previous beaker, and mix and stir for 4 minutes. Then configure 30ml of 0.009mol manganese sulfate monohydrate, and add it to the solution that was mixed uniformly before. At this time, the ratio of Mn:Mo in the solution is 2.5:1. Add the previously dried PPS filter disc into it, and place it at room temperature Stir for 15 minutes, and the solution is brown after mixing evenly.
待混合均匀后,将溶液转移到聚四氟乙烯内胆中,密封好后封装于高压釜中,放置于200℃的真空干燥箱中反应18h,反应结束后置于室温下冷却,冷却至室温后打开高压釜取出PPS滤料,并用去离子水和乙醇洗净,置于105℃中干燥4h,待测试。高锰酸钾的质量计算如下:0.2×0.08×158=2.528g。After mixing evenly, transfer the solution to a polytetrafluoroethylene liner, seal it well, package it in an autoclave, and place it in a vacuum oven at 200°C for 18 hours of reaction. After the reaction, place it at room temperature and cool it down to room temperature Finally, open the autoclave to take out the PPS filter material, wash it with deionized water and ethanol, and dry it at 105°C for 4 hours before testing. The mass of potassium permanganate is calculated as follows: 0.2×0.08×158=2.528g.
复合滤料的脱硝性能在自制管式SCR反应器中进行评价。NO和NH3体积分数均为0.05 %,O2体积分数为5 %,其余为N2,气体流速为700mL·min-1,温度设置为140℃,用英国KM940烟气分析仪测得脱硝率为70%;温度设置为160℃,脱硝率为81%;温度设置为180℃,脱销率为100%。并在180℃间隔30min测试抗硫能力,最后脱销率基本稳定在48%。The denitrification performance of the composite filter material was evaluated in a self-made tubular SCR reactor. The volume fractions of NO and NH 3 are both 0.05%, the volume fraction of O 2 is 5%, and the rest is N 2 , the gas flow rate is 700mL·min -1 , the temperature is set at 140°C, and the denitrification rate is measured by the British KM940 flue gas analyzer is 70%; the temperature is set to 160°C, and the denitrification rate is 81%; the temperature is set to 180°C, and the out-of-stock rate is 100%. The anti-sulfur ability was tested at 180°C at intervals of 30 minutes, and the final out-of-stock rate was basically stable at 48%.
实施例4Example 4
首先称0.0273g十二烷基硫酸钠加入50ml去离子水中,然后放入剪成质量为1.011g的PPS滤料圆片,超声处理1h,处理完取出烘干备用。再称取20ml去离子水加入250ml的烧杯中。然后准确称量四水合钼酸铵((NH4)6Mo7O24·4H2O)1.7651g,加入磁子搅拌5min,直至溶液混合均匀为止。配置浓度为0.2M的高锰酸钾溶液80ml,将所配的溶液超声或者摇晃至溶质完全溶解,加入之前的烧杯中,一起混合搅拌4min。再配置0.014mol的一水合硫酸锰30ml,加入之前混合均匀的溶液中,此时溶液中的Mn:Mo的比例为3:1,将之前烘干的PPS滤料圆片加入其中,置于室温下搅拌15min,混合均匀后溶液为棕褐色。First weigh 0.0273g of sodium lauryl sulfate and add it to 50ml of deionized water, then put it into a PPS filter disc with a mass of 1.011g, ultrasonicate for 1 hour, take it out and dry it for later use. Then weigh 20ml of deionized water and add it to a 250ml beaker. Then accurately weigh 1.7651 g of ammonium molybdate tetrahydrate ((NH 4 ) 6 Mo 7 O 24 ·4H 2 O), add a magnet and stir for 5 minutes until the solution is evenly mixed. Prepare 80ml of potassium permanganate solution with a concentration of 0.2M, sonicate or shake the prepared solution until the solute is completely dissolved, add it to the previous beaker, and mix and stir for 4 minutes. Then configure 30ml of 0.014mol manganese sulfate monohydrate, and add it to the solution that was mixed uniformly before. At this time, the ratio of Mn:Mo in the solution is 3:1. Add the previously dried PPS filter disc into it, and place it at room temperature Stir for 15 minutes, and the solution is brown after mixing evenly.
待混合均匀后,将溶液转移到聚四氟乙烯内胆中,密封好后封装于高压釜中,放置于200℃的真空干燥箱中反应18h,反应结束后置于室温下冷却,冷却至室温后打开高压釜取出PPS滤料,并用去离子水和乙醇洗净,置于105℃中干燥4h,待测试。高锰酸钾的质量计算如下:0.2×0.08×158=2.528g。After mixing evenly, transfer the solution to a polytetrafluoroethylene liner, seal it well, package it in an autoclave, and place it in a vacuum oven at 200°C for 18 hours of reaction. After the reaction, place it at room temperature and cool it down to room temperature Finally, open the autoclave to take out the PPS filter material, wash it with deionized water and ethanol, and dry it at 105°C for 4 hours before testing. The mass of potassium permanganate is calculated as follows: 0.2×0.08×158=2.528g.
复合滤料的脱硝性能在自制管式SCR反应器中进行评价。NO和NH3体积分数均为0.05 %,O2体积分数为5 %,其余为N2,气体流速为700mL·min-1,温度设置为140℃,用英国KM940烟气分析仪测得脱硝率为66%;温度设置为160℃,脱硝率为77%;温度设置为180℃,脱销率为99%。并在180℃间隔30min测试抗硫能力,最后脱销率基本稳定在47%。The denitrification performance of the composite filter material was evaluated in a self-made tubular SCR reactor. The volume fractions of NO and NH 3 are both 0.05%, the volume fraction of O 2 is 5%, and the rest is N 2 , the gas flow rate is 700mL·min -1 , the temperature is set at 140°C, and the denitrification rate is measured by the British KM940 flue gas analyzer The temperature is set at 160°C, and the denitrification rate is 77%; the temperature is set at 180°C, and the out-of-stock rate is 99%. The anti-sulfur ability was tested at 180°C at intervals of 30 minutes, and the final out-of-stock rate was basically stable at 47%.
活性评价:催化剂在自制管式SCR反应器中进行评价。反应器为外部电加热, 反应管催化剂床层旁放置热电偶测量温度,实验装置流程如图1所示。以钢气瓶模拟烟气组成,烟气中包括NO、O2、N2、NH3为还原气体,NO和NH3体积分数均为0.04-0.06%,O2体积分数为4-6%,其余为N2,气体流速为700mL·min-1,温度控制在120~200℃间,气体流量、组成由质量流量计调节和控制。气体分析采用英国KM940烟气分析仪,为了保证数据的稳定性和准确性,每个工况至少稳定30min。Activity evaluation: The catalyst was evaluated in a self-made tubular SCR reactor. The reactor was heated externally, and a thermocouple was placed next to the catalyst bed in the reaction tube to measure the temperature. The flow chart of the experimental device is shown in Figure 1. The composition of flue gas is simulated by steel cylinders. The flue gas includes NO, O 2 , N 2 , and NH 3 as reducing gases. The volume fractions of NO and NH 3 are both 0.04-0.06%, and the volume fraction of O 2 is 4-6%. The rest is N 2 , the gas flow rate is 700mL·min -1 , the temperature is controlled between 120 and 200°C, and the gas flow and composition are regulated and controlled by mass flow meters. The gas analysis adopts the British KM940 flue gas analyzer. In order to ensure the stability and accuracy of the data, each working condition is stable for at least 30 minutes.
表1各种因素对复合滤料脱硝率的影响(反应温度为180℃):Table 1 The influence of various factors on the denitrification rate of the composite filter material (reaction temperature is 180°C):
从表1数据可以看出,在140℃的时候,随着两个金属元素的摩尔比的不断增加,脱硝率随着出现了先增加到一个最大值后减少的趋势,在1:2出出现了最大值。并且到了180℃,基本都达到了100%的脱硝率。并且在180℃时显示了最好的抗硫性能。It can be seen from the data in Table 1 that at 140°C, as the molar ratio of the two metal elements increases, the denitrification rate first increases to a maximum value and then decreases, and appears at 1:2 the maximum value. And when it reaches 180℃, the denitrification rate basically reaches 100%. And it shows the best anti-sulfur performance at 180°C.
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