CN112546748B - Preparation method of low-temperature denitration filter material based on water quenching method - Google Patents
Preparation method of low-temperature denitration filter material based on water quenching method Download PDFInfo
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 239000000463 material Substances 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims abstract description 21
- 238000002360 preparation method Methods 0.000 title claims abstract description 10
- 238000010791 quenching Methods 0.000 title claims abstract description 9
- 230000000171 quenching effect Effects 0.000 title claims abstract description 9
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000000839 emulsion Substances 0.000 claims abstract description 51
- 239000004744 fabric Substances 0.000 claims abstract description 42
- 238000003756 stirring Methods 0.000 claims abstract description 40
- 239000012018 catalyst precursor Substances 0.000 claims abstract description 30
- 239000000843 powder Substances 0.000 claims abstract description 20
- QQZMWMKOWKGPQY-UHFFFAOYSA-N cerium(3+);trinitrate;hexahydrate Chemical compound O.O.O.O.O.O.[Ce+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O QQZMWMKOWKGPQY-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000008367 deionised water Substances 0.000 claims abstract description 17
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 17
- 239000003607 modifier Substances 0.000 claims abstract description 12
- 238000001354 calcination Methods 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims abstract description 6
- 238000001035 drying Methods 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 238000002844 melting Methods 0.000 claims abstract 3
- 230000008018 melting Effects 0.000 claims abstract 3
- 239000004642 Polyimide Substances 0.000 claims description 18
- 229920001721 polyimide Polymers 0.000 claims description 18
- 239000000835 fiber Substances 0.000 claims description 8
- 229910052720 vanadium Inorganic materials 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 4
- 238000005470 impregnation Methods 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 12
- 239000003546 flue gas Substances 0.000 abstract description 12
- 238000002156 mixing Methods 0.000 abstract description 4
- 238000000746 purification Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 14
- 239000003054 catalyst Substances 0.000 description 7
- 239000000428 dust Substances 0.000 description 3
- 238000011068 loading method Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- -1 polytetrafluoroethylene Polymers 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- SKAXWKNRKROCKK-UHFFFAOYSA-N [V].[Ce] Chemical compound [V].[Ce] SKAXWKNRKROCKK-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- UNTBPXHCXVWYOI-UHFFFAOYSA-O azanium;oxido(dioxo)vanadium Chemical compound [NH4+].[O-][V](=O)=O UNTBPXHCXVWYOI-UHFFFAOYSA-O 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000005185 salting out Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
-
- 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
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J23/16—Catalysts 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
- B01J23/20—Vanadium, niobium or tantalum
- B01J23/22—Vanadium
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Biomedical Technology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
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Abstract
Description
技术领域Technical Field
本发明涉及工业锅炉烟气净化技术领域,具体为一种基于水淬法的低温脱硝滤料的制备方法。The invention relates to the technical field of industrial boiler flue gas purification, and in particular to a method for preparing a low-temperature denitration filter material based on a water quenching method.
背景技术Background Art
近年来,我国的工业化水平迅速提高,同时也加剧了空气污染恶化,PM2.5超标等环境问题。虽然已经开始推行相应的环保政策,但大气环境形势依然十分严峻。其中工业锅炉燃烧产生的烟气中有大量的氮氧化物、二氧化硫及烟尘等,若直接排放至环境中,则严重威胁人类健康。因此,如何进一步降低工业锅炉烟气中的污染物含量,提高工业锅炉的清洁性仍是当前亟待解决的难题。In recent years, my country's industrialization level has increased rapidly, which has also aggravated environmental problems such as worsening air pollution and excessive PM2.5. Although corresponding environmental protection policies have been implemented, the atmospheric environment is still very severe. Among them, the flue gas produced by the combustion of industrial boilers contains a large amount of nitrogen oxides, sulfur dioxide and smoke, which, if directly discharged into the environment, will seriously threaten human health. Therefore, how to further reduce the content of pollutants in the flue gas of industrial boilers and improve the cleanliness of industrial boilers is still a problem that needs to be solved urgently.
由于工业锅炉的排烟温度较低,若直接采用电站锅炉的脱硝除尘工艺,会出现脱硝温度和除尘温度相差较大,造成脱硝效率较低等问题。滤袋脱硝是一种新型的烟气脱硝技术,借助一种具有催化功能的滤袋,利用袋式除尘工艺,在低温下实现烟气脱硝。该技术在国外工业锅炉上获得了广泛应用。由于钒铈基催化剂有良好的低温活性,所以现有的低温脱硝滤料制备工艺通常采用浸渍法,将钒的前驱体(偏钒酸铵)溶解于稀硫酸中,制成脱硝溶液,再将滤布浸渍在溶液中,在500℃左右煅烧。上述方法脱硝活性组分分散性较差,催化剂与滤袋纤维结合力较弱,降低滤布的纤维强度,影响滤布的使用寿命。因此,研制新型的脱硝滤袋制备技术显得尤为必要与重要。Since the exhaust temperature of industrial boilers is relatively low, if the denitration and dust removal process of power station boilers is directly adopted, there will be a large difference between the denitration temperature and the dust removal temperature, resulting in low denitration efficiency and other problems. Filter bag denitration is a new flue gas denitration technology. With the help of a filter bag with catalytic function and a bag dust removal process, flue gas denitration is achieved at low temperature. This technology has been widely used in foreign industrial boilers. Since vanadium cerium-based catalysts have good low-temperature activity, the existing low-temperature denitration filter material preparation process usually adopts an impregnation method to dissolve the vanadium precursor (ammonium metavanadate) in dilute sulfuric acid to prepare a denitration solution, and then immerse the filter cloth in the solution and calcine it at about 500°C. The above method has poor dispersibility of the denitration active components, weak bonding between the catalyst and the filter bag fiber, reduced fiber strength of the filter cloth, and affected the service life of the filter cloth. Therefore, it is particularly necessary and important to develop a new denitration filter bag preparation technology.
发明内容Summary of the invention
针对现有技术中存在的问题,本发明提供一种基于水淬法的脱硝滤袋的制备方法,脱硝活性组分分散性好,有效提高了滤布的纤维强度,保证滤布的使用寿命,而且加强了催化剂与滤布纤维的结合力。In view of the problems existing in the prior art, the present invention provides a method for preparing a denitrification filter bag based on a water quenching method. The denitrification active components have good dispersibility, which effectively improves the fiber strength of the filter cloth, ensures the service life of the filter cloth, and strengthens the bonding force between the catalyst and the filter cloth fiber.
本发明是通过以下技术方案来实现:The present invention is achieved through the following technical solutions:
一种基于水淬法的低温脱硝滤料的制备方法,包括以下步骤:A method for preparing a low-temperature denitration filter material based on a water quenching method comprises the following steps:
步骤1,将五氧化二钒粉末、有机改性剂和六水硝酸铈粉末混合搅拌均匀制备成低温脱硝催化剂前驱体乳液;Step 1, mixing vanadium pentoxide powder, an organic modifier and cerium nitrate hexahydrate powder and stirring them uniformly to prepare a low-temperature denitration catalyst precursor emulsion;
步骤2,将低温脱硝催化剂前驱体乳液加入反应釜中,并将滤布置于反应釜中在真空下浸泡;Step 2, adding a low-temperature denitration catalyst precursor emulsion into a reactor, and placing a filter in the reactor and soaking it under vacuum;
步骤3,将浸泡好的滤布进行干燥,中温煅烧后得到低温脱硝滤料。Step 3, drying the soaked filter cloth, and calcining at medium temperature to obtain a low-temperature denitration filter material.
进一步的,步骤1中,低温脱硝催化剂前驱体乳液的制备方法如下,Furthermore, in step 1, the preparation method of the low-temperature denitration catalyst precursor emulsion is as follows:
步骤1.1,在反应釜中添加去离子水,将五氧化二钒粉末加热融化后,迅速倒入去离子水中,超声搅拌溶解;Step 1.1, add deionized water to a reactor, heat and melt the vanadium pentoxide powder, then quickly pour it into the deionized water and stir and dissolve it by ultrasonic stirring;
步骤1.2,在步骤1.1得到的溶液中加入有机改性剂,充分搅拌混合均匀,得到稳定的五氧化二钒乳液;Step 1.2, adding an organic modifier to the solution obtained in step 1.1, stirring and mixing thoroughly to obtain a stable vanadium pentoxide emulsion;
步骤1.3,在步骤1.2得到的溶液中加入六水硝酸铈粉末,搅拌至完全溶解后得到低温脱硝催化剂前驱体乳液。Step 1.3, adding cerium nitrate hexahydrate powder to the solution obtained in step 1.2, stirring until completely dissolved to obtain a low-temperature denitration catalyst precursor emulsion.
更进一步的,步骤1.1中,加热融化时,温度为800℃~900℃;水钒比为30mL/g~35mL/g;去离子水的温度范围为25℃~30℃。Furthermore, in step 1.1, when heating to melt, the temperature is 800°C to 900°C; the water-vanadium ratio is 30mL/g to 35mL/g; and the temperature range of deionized water is 25°C to 30°C.
更进一步的,步骤1.1中,超声搅拌溶解时,搅拌速度为100r/min。Furthermore, in step 1.1, during ultrasonic stirring for dissolution, the stirring speed is 100 r/min.
更进一步的,步骤1.2中,有机改性剂为聚酰亚胺乳液,其质量浓度为20%,占整个催化剂前驱体乳液质量的3%~8%,加入至溶液后,搅拌速度为60r/min。Furthermore, in step 1.2, the organic modifier is a polyimide emulsion with a mass concentration of 20%, accounting for 3% to 8% of the mass of the entire catalyst precursor emulsion. After being added to the solution, the stirring speed is 60 r/min.
更进一步的,步骤1.3中,六水硝酸铈和五氧化二钒质量比为2:1,加入至溶液后,搅拌速度为10r/min~15r/min。Furthermore, in step 1.3, the mass ratio of cerium nitrate hexahydrate to vanadium pentoxide is 2:1, and after being added into the solution, the stirring speed is 10 r/min to 15 r/min.
进一步的,步骤2中,所述的滤布为聚酰亚胺纤维滤布,其在反应釜内真空浸渍,真空度维持在0.05MPa~0.1MPa,温度控制在58℃~60℃,时间为至少3h。Furthermore, in step 2, the filter cloth is a polyimide fiber filter cloth, which is vacuum impregnated in a reaction kettle, the vacuum degree is maintained at 0.05MPa to 0.1MPa, the temperature is controlled at 58°C to 60°C, and the time is at least 3h.
进一步的,步骤3中,所述的浸泡后的滤布呈透明状,先常温干燥,然后在130℃烘箱中干燥至整块滤布变成黑色,最后将黑色的滤布在240℃马弗炉中煅烧4h后,得到低温脱硝滤料。Furthermore, in step 3, the soaked filter cloth is transparent, first dried at room temperature, then dried in an oven at 130°C until the entire filter cloth turns black, and finally the black filter cloth is calcined in a muffle furnace at 240°C for 4 hours to obtain a low-temperature denitration filter material.
与现有技术相比,本发明具有以下有益的技术效果:Compared with the prior art, the present invention has the following beneficial technical effects:
本发明采用水淬法制取液态五氧化二钒,向其中添加有机改性剂和六水硝酸铈粉末,最终得到低温脱硝催化剂前驱体乳液;然后在负压条件下将滤布浸渍在该乳液中,经过煅烧后将低温脱硝催化剂负载于聚酰亚胺纤维滤布上制成低温脱硝滤料,与传统的低温脱硝催化剂前驱体乳液制备方法不同,本发明技术工程实施需要用加热至800℃~900℃,保温1h后,迅速倒入去离子水中,制成均匀的五氧化二钒水溶液,再向其中添加聚酰亚胺乳液和六水硝酸铈,制备出低温脱硝催化剂前驱体乳液。该催化剂前驱体乳液分具有高度的稳定性,对温度不敏感,能够保持一年以上。其中,聚酰亚胺乳液作为有机改性剂能够显著提高五氧化二钒溶液稳定性,亦可作为粘结剂,提高活性组分在滤布上的负载率,且可以重复利用,大大提高了经济性,便于工业大规模生产及推广应用。The present invention adopts a water quenching method to prepare liquid vanadium pentoxide, adds an organic modifier and hexahydrate cerium nitrate powder thereto, and finally obtains a low-temperature denitration catalyst precursor emulsion; then the filter cloth is immersed in the emulsion under negative pressure conditions, and after calcination, the low-temperature denitration catalyst is loaded on the polyimide fiber filter cloth to prepare a low-temperature denitration filter material. Different from the traditional method for preparing a low-temperature denitration catalyst precursor emulsion, the technical engineering implementation of the present invention requires heating to 800°C to 900°C, keeping warm for 1h, and then quickly pouring into deionized water to prepare a uniform vanadium pentoxide aqueous solution, and then adding polyimide emulsion and hexahydrate cerium nitrate to it to prepare a low-temperature denitration catalyst precursor emulsion. The catalyst precursor emulsion has a high degree of stability, is not sensitive to temperature, and can be maintained for more than one year. Among them, the polyimide emulsion as an organic modifier can significantly improve the stability of the vanadium pentoxide solution, and can also be used as a binder to increase the loading rate of the active component on the filter cloth, and can be reused, which greatly improves the economy and is convenient for industrial large-scale production and promotion and application.
进一步,本发明是在真空条件下,将滤布浸泡在催化剂前驱体乳液中,有利于活性组分进入到滤布的微孔内部,进一步提高催化剂活性组分的负载率和均匀性。Furthermore, the present invention soaks the filter cloth in the catalyst precursor emulsion under vacuum conditions, which is beneficial for the active components to enter the micropores of the filter cloth, further improving the loading rate and uniformity of the active components of the catalyst.
进一步,本发明只需将负载脱硝催化剂前驱体的滤布在240℃左右进行煅烧,无需在500℃高温焙烧,规避了高温焙烧导致滤布自燃,产生大量污染气体,催化剂前驱体乳液中的活性组分在滤布表面盐析的问题,降低了对原料滤布耐高温的要求,可有效降低滤袋的生产成本。Furthermore, the present invention only needs to calcine the filter cloth loaded with the denitration catalyst precursor at about 240°C, and there is no need to roast it at a high temperature of 500°C, thereby avoiding the problem of spontaneous combustion of the filter cloth and generation of a large amount of polluting gas due to high-temperature roasting, and the problem of salting out of the active components in the catalyst precursor emulsion on the surface of the filter cloth, thereby reducing the requirement for high temperature resistance of the raw filter cloth, and effectively reducing the production cost of the filter bag.
具体实施方式DETAILED DESCRIPTION
下面结合具体的实施例对本发明做进一步的详细说明,所述是对本发明的解释而不是限定。The present invention is further described in detail below in conjunction with specific embodiments, which are intended to explain the present invention rather than to limit it.
本发明一种基于水淬法的脱硝滤料的制备方法,采用水淬法制取液态五氧化二钒,并向其中添加有机改性剂和助剂,最终得到低温脱硝催化剂前驱体乳液;然后在负压条件下将滤布浸渍在低温脱硝催化剂前驱体乳液中,240℃煅烧后将低温脱硝催化剂负载于聚酰亚胺纤维滤布上制成低温脱硝滤料,具体步骤如下:The present invention discloses a method for preparing a denitration filter material based on a water quenching method. The method comprises the following steps: preparing liquid vanadium pentoxide by a water quenching method, adding an organic modifier and an auxiliary agent thereto, and finally obtaining a low-temperature denitration catalyst precursor emulsion; then, immersing a filter cloth in the low-temperature denitration catalyst precursor emulsion under negative pressure conditions, calcining at 240° C., and loading the low-temperature denitration catalyst on a polyimide fiber filter cloth to prepare a low-temperature denitration filter material. The specific steps are as follows:
(1)在反应釜中添加去离子水,将五氧化二钒粉末加热融化后,迅速倒入去离子水中,超声搅拌溶解。(1) Add deionized water to a reaction kettle, heat and melt the vanadium pentoxide powder, and then quickly pour it into the deionized water and dissolve it by ultrasonic stirring.
(2)在上述溶液中加入有机改性剂,充分搅拌混合均匀,得到稳定的五氧化二钒乳液。(2) Add an organic modifier to the above solution, stir and mix thoroughly to obtain a stable vanadium pentoxide emulsion.
(3)在上述溶液中加入六水硝酸铈粉末,搅拌至完全溶解后得到低温脱硝催化剂前驱体乳液。(3) Add cerium nitrate hexahydrate powder to the above solution and stir until completely dissolved to obtain a low-temperature denitration catalyst precursor emulsion.
(4)将滤布置于反应釜中,用真空维持泵使反应釜内保持负压。(4) Place the filter in the reactor and use a vacuum pump to maintain negative pressure in the reactor.
(5)将浸泡后的滤布,进行干燥,中温煅烧,得到低温脱硝滤料。(5) Drying the soaked filter cloth and calcining it at medium temperature to obtain a low-temperature denitration filter material.
其中,(1)、(2)、(3)为制备低温脱硝催化剂前驱体乳液的步骤,其由五氧化二钒粉末、六水硝酸铈、有机改性剂制成;Among them, (1), (2) and (3) are steps for preparing a low-temperature denitration catalyst precursor emulsion, which is made of vanadium pentoxide powder, cerium nitrate hexahydrate and an organic modifier;
其中,步骤(1)中,将五氧化二钒粉末加热至800℃~900℃,保温1h后,迅速倒入去离子水中。其中,水钒比为30mL/g~35mL/g,温度保持在25℃~30℃。反应釜搅拌器以100r/min的速度进行搅拌,搅拌时间为1h;Wherein, in step (1), the vanadium pentoxide powder is heated to 800°C to 900°C, kept warm for 1 hour, and then quickly poured into deionized water. Wherein, the water-vanadium ratio is 30mL/g to 35mL/g, and the temperature is maintained at 25°C to 30°C. The reactor agitator is stirred at a speed of 100r/min for 1 hour;
其中,步骤(2)中,有机改性剂为聚酰亚胺乳液,其质量浓度为20%,占低温脱硝催化剂前驱体乳液的3%~8%,加入后搅拌速度为60r/min,搅拌时间为30h;Wherein, in step (2), the organic modifier is a polyimide emulsion, and its mass concentration is 20%, accounting for 3% to 8% of the low-temperature denitration catalyst precursor emulsion. After addition, the stirring speed is 60r/min, and the stirring time is 30h;
其中,步骤(3)中,六水硝酸铈和五氧化二钒质量比为2:1。加入六水硝酸铈后,以10r/min~15r/min的速度充分搅拌,搅拌时间为30min;Wherein, in step (3), the mass ratio of cerium nitrate hexahydrate to vanadium pentoxide is 2:1. After adding cerium nitrate hexahydrate, stir thoroughly at a speed of 10 r/min to 15 r/min for 30 min;
其中,步骤(4)中,反应釜内真空度维持在0.05MPa~0.1MPa,滤布在反应釜中浸泡1h~2h,温度控制在60℃左右;Wherein, in step (4), the vacuum degree in the reactor is maintained at 0.05 MPa to 0.1 MPa, the filter cloth is immersed in the reactor for 1 h to 2 h, and the temperature is controlled at about 60° C.;
其中,步骤(5)中,取出滤布后,先常温干燥12h,然后在130℃烘箱中干燥2h~3h,最后在240℃马弗炉中煅烧4h得到低温脱硝滤料;Wherein, in step (5), after taking out the filter cloth, first dry it at room temperature for 12 hours, then dry it in an oven at 130° C. for 2 hours to 3 hours, and finally calcine it in a muffle furnace at 240° C. for 4 hours to obtain a low-temperature denitration filter material;
在实际应用中,利用本发明提供的方法制备低温脱硝滤料时,包括以下步骤:In practical applications, when preparing low-temperature denitration filter material using the method provided by the present invention, the following steps are included:
首先,称取适量五氧化二钒粉末,放入钳锅中,在马弗炉中加热至800℃~900℃,保温1h,得到熔融状态的五氧化二钒;First, weigh an appropriate amount of vanadium pentoxide powder, put it into a tongs pot, heat it to 800°C to 900°C in a muffle furnace, and keep it warm for 1 hour to obtain vanadium pentoxide in a molten state;
在反应釜加入去离子水,水钒比为30mL/g~35mL/g,将步骤(1)获得的五氧化二钒迅速倒入去离子水中,立即搅拌。反应釜内溶液控制在25℃~30℃,搅拌桨叶转速为100r/min,搅拌时间为1h;Add deionized water to the reactor, with a water-vanadium ratio of 30 mL/g to 35 mL/g, and quickly pour the vanadium pentoxide obtained in step (1) into the deionized water and stir immediately. The solution in the reactor is controlled at 25°C to 30°C, the stirring blade speed is 100 r/min, and the stirring time is 1 hour;
再将质量浓度为20%的聚酰亚胺乳液加入至上述溶液中,充分搅拌均匀,反应釜搅拌速度为60r/min,搅拌时间为30min,得到稳定的五氧化二钒乳液。聚酰亚胺乳液占整个催化剂前驱体乳液质量的3%~8%;Then add 20% polyimide emulsion to the above solution and stir it evenly. The stirring speed of the reactor is 60r/min and the stirring time is 30min to obtain a stable vanadium pentoxide emulsion. The polyimide emulsion accounts for 3% to 8% of the mass of the entire catalyst precursor emulsion.
再将六水硝酸铈加入至上述的五氧化二钒乳液中,搅拌速度为10r/min~15r/min,搅拌时间为30min,最终得到低温脱硝催化剂前驱体乳液。六水硝酸铈与五氧化二钒的质量比为2:1;Then, add cerium nitrate hexahydrate to the above-mentioned vanadium pentoxide emulsion, stir at a speed of 10 r/min to 15 r/min, and stir for 30 min to finally obtain a low-temperature denitration catalyst precursor emulsion. The mass ratio of cerium nitrate hexahydrate to vanadium pentoxide is 2:1;
其次,将聚酰亚胺滤布浸渍在步骤(4)低温脱硝催化及前驱体乳液中,密封反应釜。利用真空维持泵,对反应釜内进行抽真空。将聚四氟乙烯滤布在0.05MPa~0.1MPa真空度,58℃~60℃条件下,浸渍1h~2h。Next, the polyimide filter cloth is immersed in the low-temperature denitration catalyst and precursor emulsion in step (4), and the reactor is sealed. The reactor is evacuated using a vacuum maintenance pump. The polytetrafluoroethylene filter cloth is immersed in a vacuum degree of 0.05 MPa to 0.1 MPa and a temperature of 58° C. to 60° C. for 1 h to 2 h.
最后,将浸泡后呈透明状的滤布平铺于晾网上常温干燥12h,直至滤布表面干燥。然后在130℃烘箱中干燥,至整块滤布变成黑色为止,约2h~3h左右。最后在240℃马弗炉中煅烧4h后,得到低温脱硝滤料。Finally, spread the transparent filter cloth on a drying net and dry it at room temperature for 12 hours until the surface of the filter cloth is dry. Then dry it in a 130℃ oven until the entire filter cloth turns black, which takes about 2 to 3 hours. Finally, calcine it in a muffle furnace at 240℃ for 4 hours to obtain a low-temperature denitrification filter material.
将所得低温脱硝滤料在试验台上利用模拟烟气进行脱硝性能评价。用烟气分析仪测试反应器进出口烟气中NO和NO2浓度,计算NOx脱除效率。The obtained low-temperature denitrification filter material was used to evaluate the denitrification performance using simulated flue gas on a test bench. The concentrations of NO and NO2 in the flue gas at the inlet and outlet of the reactor were tested using a flue gas analyzer to calculate the NOx removal efficiency.
实施例1Example 1
本实施例中采用水钒比为30mL/g,五氧化二钒加热温度为800℃,去离子水温度为25℃,聚酰亚胺乳液含量为3%,真空度为0.05MPa进行具体说明,并将在该条件下所得的低温脱硝滤料在试验台上利用模拟烟气进行脱硝性能评价,即用烟气分析仪测试反应器进出口烟气中NO和NO2浓度,计算NOx脱除效率为82%。In this embodiment, a water-vanadium ratio of 30 mL/g, a vanadium pentoxide heating temperature of 800°C, a deionized water temperature of 25°C, a polyimide emulsion content of 3%, and a vacuum degree of 0.05 MPa are used for specific description, and the low-temperature denitration filter material obtained under these conditions is evaluated for denitration performance using simulated flue gas on a test bench, that is, the NO and NO2 concentrations in the reactor inlet and outlet flue gas are tested with a flue gas analyzer, and the NOx removal efficiency is calculated to be 82%.
在上述参数条件下,具体制备过程如下,Under the above parameter conditions, the specific preparation process is as follows:
(1)称取适量五氧化二钒粉末,放入钳锅中,在马弗炉中加热至800℃,保温1h,得到熔融状态的五氧化二钒。(1) Weigh an appropriate amount of vanadium pentoxide powder, put it into a tongs pot, heat it to 800°C in a muffle furnace, and keep it warm for 1 hour to obtain vanadium pentoxide in a molten state.
(2)在反应釜加入去离子水,水钒比为30mL/g,将步骤(1)获得的五氧化二钒迅速倒入去离子水中,立即搅拌。反应釜内溶液控制在25℃,搅拌桨叶转速为100r/min,搅拌时间为1h。(2) Add deionized water to the reactor, with a water-vanadium ratio of 30 mL/g, and quickly pour the vanadium pentoxide obtained in step (1) into the deionized water, and stir immediately. The solution in the reactor is controlled at 25° C., the stirring blade speed is 100 r/min, and the stirring time is 1 h.
(3)再将质量浓度为20%的聚酰亚胺乳液加入至步骤(2)溶液中,充分搅拌均匀,反应釜搅拌速度为60r/min,搅拌时间为30min,得到稳定的五氧化二钒乳液。聚酰亚胺乳液占整个催化剂前驱体乳液质量的3%。(3) Adding a polyimide emulsion with a mass concentration of 20% to the solution of step (2), stirring the mixture evenly, stirring the mixture at a stirring speed of 60 r/min for 30 min, and obtaining a stable vanadium pentoxide emulsion. The polyimide emulsion accounts for 3% of the mass of the catalyst precursor emulsion.
(4)向步骤(3)中的五氧化二钒乳液加入六水硝酸铈,搅拌速度为10r/min,搅拌时间为30min,最终得到低温脱硝催化剂前驱体乳液。六水硝酸铈与五氧化二钒的质量比为2:1。(4) adding cerium nitrate hexahydrate to the vanadium pentoxide emulsion in step (3), stirring at a speed of 10 r/min for 30 min, and finally obtaining a low-temperature denitration catalyst precursor emulsion. The mass ratio of cerium nitrate hexahydrate to vanadium pentoxide is 2:1.
(5)将聚酰亚胺滤布浸渍在步骤(4)得到的低温脱硝催化剂前驱体乳液中,密封反应釜。利用真空维持泵,对反应釜内进行抽真空。将聚四氟乙烯滤布在0.05MPa真空度,58℃~60℃条件下,浸渍1h~2h。(5) Immerse the polyimide filter cloth in the low-temperature denitration catalyst precursor emulsion obtained in step (4), and seal the reactor. Use a vacuum maintenance pump to evacuate the reactor. Immerse the polytetrafluoroethylene filter cloth at a vacuum degree of 0.05 MPa and a temperature of 58° C. to 60° C. for 1 h to 2 h.
(6)将浸泡后呈透明状的滤布平铺于晾网上常温干燥12h,直至滤布表面干燥。然后在130℃烘箱中干燥,至整块滤布变成黑色为止,约2h~3h左右。最后在240℃马弗炉中煅烧4h后,得到低温脱硝滤料。(6) Spread the transparent filter cloth after soaking on a drying net and dry it at room temperature for 12 hours until the surface of the filter cloth is dry. Then dry it in a 130℃ oven until the entire filter cloth turns black, which takes about 2 to 3 hours. Finally, calcine it in a muffle furnace at 240℃ for 4 hours to obtain a low-temperature denitrification filter material.
实施例1-实施例10的制备参数及NOx脱出效率如下表所示,其制备过程同实施例1,仅制备参数不同。The preparation parameters and NOx removal efficiency of Examples 1 to 10 are shown in the following table. The preparation process is the same as that of Example 1, except for the different preparation parameters.
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