CN105457627B - A kind of glass fabric Supported Manganese base low temperature SCR denitration catalyst and preparation method thereof - Google Patents
A kind of glass fabric Supported Manganese base low temperature SCR denitration catalyst and preparation method thereof Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 86
- 239000011572 manganese Substances 0.000 title claims abstract description 72
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 229910052748 manganese Inorganic materials 0.000 title claims abstract description 66
- 239000004744 fabric Substances 0.000 title claims abstract description 56
- 238000002360 preparation method Methods 0.000 title claims description 18
- 239000011521 glass Substances 0.000 title 1
- 239000003365 glass fiber Substances 0.000 claims abstract description 55
- 239000003292 glue Substances 0.000 claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 14
- 238000011068 loading method Methods 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 9
- 238000005260 corrosion Methods 0.000 claims abstract description 6
- 230000007797 corrosion Effects 0.000 claims abstract description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 20
- 238000003756 stirring Methods 0.000 claims description 17
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 16
- 239000011259 mixed solution Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 11
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 8
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 claims description 8
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 7
- 238000000576 coating method Methods 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 6
- 239000011248 coating agent Substances 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 5
- 238000005303 weighing Methods 0.000 claims description 5
- 229910010413 TiO 2 Inorganic materials 0.000 claims description 4
- 239000008098 formaldehyde solution Substances 0.000 claims description 4
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- 239000007864 aqueous solution Substances 0.000 claims description 3
- 239000000084 colloidal system Substances 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 2
- 229910017604 nitric acid Inorganic materials 0.000 claims description 2
- 229960000935 dehydrated alcohol Drugs 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 12
- 238000009413 insulation Methods 0.000 abstract description 2
- 239000000499 gel Substances 0.000 description 7
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000003546 flue gas Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 239000000969 carrier Substances 0.000 description 3
- 238000010531 catalytic reduction reaction Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000013618 particulate matter Substances 0.000 description 3
- 238000011056 performance test Methods 0.000 description 3
- 239000010453 quartz Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 description 2
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- 229940071125 manganese acetate Drugs 0.000 description 2
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000012286 potassium permanganate Substances 0.000 description 2
- XKZQKPRCPNGNFR-UHFFFAOYSA-N 2-(3-hydroxyphenyl)phenol Chemical compound OC1=CC=CC(C=2C(=CC=CC=2)O)=C1 XKZQKPRCPNGNFR-UHFFFAOYSA-N 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Substances C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000008262 pumice Substances 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- 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
- B01J23/32—Manganese, technetium or rhenium
- B01J23/34—Manganese
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- 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
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
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- 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
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Abstract
本发明公开了一种玻璃纤维布负载锰基低温SCR脱硝催化剂的制备方法,包括玻璃纤维布的预处理、利用低温脱硝锰系催化剂负载用低温胶将锰基低温SCR脱硝催化剂负载到玻璃纤维布上的工艺、热处理和红外照射处理等。本发明制备的玻璃纤维布负载锰基低温SCR脱硝催化剂既保留了玻璃纤维绝缘性好、耐热性强、抗腐蚀性好和机械强度高等特点,同时制备得到的材料中催化剂在玻璃纤维上负载均匀,牢固度较好,且在低温条件下(80~180℃)具有良好的脱硝性能(最高可达98%),具有广阔的应用前景。The invention discloses a method for preparing a manganese-based low-temperature SCR denitrification catalyst loaded on glass fiber cloth, including pretreatment of glass fiber cloth, and loading the manganese-based low-temperature SCR denitrification catalyst on the glass fiber cloth by using low-temperature glue for loading manganese-based catalysts for low-temperature denitrification The above process, heat treatment and infrared irradiation treatment, etc. The glass fiber cloth loaded manganese-based low-temperature SCR denitrification catalyst prepared by the present invention not only retains the characteristics of good insulation of glass fiber, strong heat resistance, good corrosion resistance and high mechanical strength, but also the catalyst in the prepared material is loaded on glass fiber Uniformity, good firmness, good denitrification performance (up to 98%) under low temperature conditions (80-180° C.), and broad application prospects.
Description
技术领域technical field
本发明属于工业废气处理和环保催化材料领域,具体涉及一种玻璃纤维布负载锰基低温SCR脱硝催化剂及其制备方法。The invention belongs to the field of industrial waste gas treatment and environmental protection catalytic materials, and in particular relates to a manganese-based low-temperature SCR denitrification catalyst supported by glass fiber cloth and a preparation method thereof.
背景技术Background technique
氮氧化物(NOx)不仅能导致酸雨的形成,而且可与臭氧等反应,形成光化学烟雾。目前,光化学烟雾已成为仅次于可吸入颗粒物和二氧化硫的重要大气污染物。值得注意的是,随着NOx排放量逐年增加,区域酸沉降趋势不断恶化,大气中二次颗粒物臭氧(O3)和微细可吸入颗粒物(PM 2.5)居高难下,人体健康和生态环境受到了巨大威胁。氮氧化物的控制与治理势在必行。Nitrogen oxides (NO x ) can not only lead to the formation of acid rain, but also react with ozone to form photochemical smog. At present, photochemical smog has become an important air pollutant after inhalable particulate matter and sulfur dioxide. It is worth noting that with the increase of NOx emissions year by year, the trend of regional acid deposition is deteriorating, secondary particulate matter ozone (O 3 ) and fine inhalable particulate matter (PM 2.5) in the atmosphere are high and difficult, and human health and ecological environment are affected. a huge threat. The control and treatment of nitrogen oxides is imperative.
在众多脱硝技术中,选择性催化还原法(selective catalytic reduction,SCR)是一项比较有前景的脱硝技术。此技术是指在催化剂和氧气存在条件下,利用还原剂(如NH3、H2、CO或碳氢化合物等)有选择性的将NOx催化还原成N2和H2O。SCR脱硝技术的核心就是SCR脱硝催化剂。根据工业上温度的需要可以分为中高温SCR脱硝催化剂和低温SCR脱硝催化剂。其中,适用温度范围在200℃以内的SCR低温脱硝催化剂因其具有良好的经济效益与社会效益得到了广泛研究,目前对SCR低温脱硝催化剂活性组分应用和研究较多的是锰及其氧化物。Among many denitrification technologies, selective catalytic reduction (selective catalytic reduction, SCR) is a more promising denitrification technology. This technology refers to the selective catalytic reduction of NO x to N 2 and H 2 O by using a reducing agent (such as NH 3 , H 2 , CO or hydrocarbons, etc.) in the presence of a catalyst and oxygen. The core of SCR denitration technology is the SCR denitration catalyst. According to the needs of industrial temperature, it can be divided into medium and high temperature SCR denitration catalysts and low temperature SCR denitration catalysts. Among them, the SCR low-temperature denitrification catalyst with an applicable temperature range of less than 200 ° C has been extensively studied because of its good economic and social benefits. At present, manganese and its oxides are widely used and studied for the active components of SCR low-temperature denitrification catalysts. .
载体能使制成的催化剂具有合适的形状、尺寸和机械强度,以符合工业反应器的操作要求;载体可使活性组分分散在载体表面上,获得较高的比表面积,提高单位质量活性组分的催化效率。因此,SCR低温脱硝催化剂常常被负载于特定的载体之上,常见的载体有二氧化钛、氧化铝、硅胶、氧化锆、氧化铈、活性炭及某些天然产物如浮石、硅藻土等。这些常用的载体通常具有较大的比表面积和较好的热稳定性,从而能够促进催化反应的进行和防止催化剂的烧结。此外,有些载体还有一些特殊的性能:CeO2作为载体时具有很好的储氧功能,从而促进了催化反应;分子筛具有离子交换性能、均一的分子大小的孔道、酸催化活性,并有良好的热稳定性和水热稳定性,可制成对许多反应有高活性、高选择性的催化剂。The carrier can make the catalyst have suitable shape, size and mechanical strength to meet the operating requirements of industrial reactors; the carrier can disperse the active components on the surface of the carrier to obtain a higher specific surface area and increase the active mass per unit mass. points of catalytic efficiency. Therefore, SCR low-temperature denitrification catalysts are often supported on specific carriers. Common carriers include titanium dioxide, alumina, silica gel, zirconia, ceria, activated carbon, and some natural products such as pumice, diatomaceous earth, etc. These commonly used supports usually have a large specific surface area and good thermal stability, which can promote the catalytic reaction and prevent the sintering of the catalyst. In addition, some carriers have some special properties: CeO2 has a good oxygen storage function when used as a carrier, thereby promoting the catalytic reaction; molecular sieves have ion exchange properties, uniform molecular size pores, acid catalytic activity, and good Excellent thermal stability and hydrothermal stability can be made into catalysts with high activity and high selectivity for many reactions.
目前,锰基SCR低温脱硝催化剂的负载方法主要包括浸渍法、涂覆法、水热合成法等。浸渍法因其具有操作步骤简单、制备周期短和安全节能等优点,是目前为止采取较多的一种负载方式。但是由于其制备得到的样品中催化剂的负载不均匀,牢固度较差,很难在环境复杂的实际的工业生产中得到运用,因此该种方法目前仅限于实验室制备使用。At present, the loading methods of manganese-based SCR low-temperature denitration catalysts mainly include impregnation method, coating method, hydrothermal synthesis method, etc. The impregnation method is a loading method that has been adopted so far because of its advantages such as simple operation steps, short preparation cycle, safety and energy saving. However, due to the inhomogeneous loading of the catalyst in the prepared sample and the poor firmness, it is difficult to be applied in the actual industrial production with complex environment, so this method is currently limited to laboratory preparation.
发明内容Contents of the invention
本发明的目的是提供一种玻璃纤维布负载锰基低温SCR脱硝催化剂及其制备方法,该方法简单、易操作,可解决锰基低温SCR脱硝催化剂在负载中存在的负载不均匀、牢固度差等问题,适合推广应用。The purpose of the present invention is to provide a manganese-based low-temperature SCR denitration catalyst loaded on glass fiber cloth and its preparation method. The method is simple and easy to operate, and can solve the problem of uneven loading and poor firmness of the manganese-based low-temperature SCR denitrification catalyst in the load. And other issues, suitable for promotion and application.
为实现上述目的,本发明采用的技术方案为:To achieve the above object, the technical solution adopted in the present invention is:
一种玻璃纤维布负载锰基低温SCR脱硝催化剂的制备方法,包括以下步骤:A method for preparing a manganese-based low-temperature SCR denitration catalyst supported by glass fiber cloth, comprising the following steps:
1)根据实际用途将玻璃纤维布剪成一定尺寸与形状,放入肥皂水中浸泡后进行洗涤、晾干;然后置于盐酸溶液中进行腐蚀处理,得预处理后的玻璃纤维布,干燥并称重后,静置备用;1) Cut the glass fiber cloth into a certain size and shape according to the actual use, soak it in soapy water, wash and dry it; then put it in hydrochloric acid solution for corrosion treatment, and obtain the pretreated glass fiber cloth, dry it and weigh it After weighing, let it stand for later use;
2)将低温脱硝锰系催化剂负载用低温胶和锰基低温SCR脱硝催化剂搅拌混合均匀,静置备用;2) Stir and mix the low-temperature denitrification manganese-based catalyst-loaded low-temperature glue and the manganese-based low-temperature SCR denitrification catalyst evenly, and set aside for later use;
3)将步骤1)所得预处理后的玻璃纤维布平铺于不锈钢工作台上,利用喷涂机将步骤2)中混合均匀的低温胶和锰基低温SCR脱硝催化剂均匀涂覆到步骤1)所得预处理后的玻璃纤维布上,并置于烘箱内干燥;3) Spread the pretreated glass fiber cloth obtained in step 1) on the stainless steel workbench, and use a spraying machine to evenly coat the low-temperature glue and manganese-based low-temperature SCR denitration catalyst in step 2) on the obtained product in step 1). Put it on the pretreated glass fiber cloth, and place it in an oven to dry;
4)将步骤3)所得材料置于马弗炉内进行热处理,冷却得负载锰基低温SCR脱硝催化剂的玻璃纤维布;4) placing the material obtained in step 3) in a muffle furnace for heat treatment, and cooling to obtain a glass fiber cloth loaded with a manganese-based low-temperature SCR denitration catalyst;
5)将步骤4)所得负载锰基低温SCR脱硝催化剂的玻璃纤维布进行红外照射处理,即得所述的玻璃纤维布负载锰基低温SCR脱硝催化剂。5) The glass fiber cloth loaded with the manganese-based low-temperature SCR denitration catalyst obtained in step 4) is subjected to infrared irradiation treatment to obtain the glass fiber cloth-loaded manganese-based low-temperature SCR denitration catalyst.
上述方案中,步骤1)中所述肥皂水中浸泡时间为20~60min。In the above scheme, the soaking time in soapy water described in step 1) is 20 to 60 minutes.
上述方案中,步骤1)中所述盐酸溶液浓度为1~3mol/L,腐蚀处理时间为20~60min。In the above solution, the concentration of the hydrochloric acid solution in step 1) is 1-3 mol/L, and the corrosion treatment time is 20-60 min.
上述方案中,步骤2)中所述低温脱硝锰系催化剂负载用低温胶的体积与锰基SCR低温脱硝催化剂的质量之比为(2~10):1。In the above scheme, the ratio of the volume of the low-temperature gel for supporting the low-temperature denitration manganese-based catalyst in step 2) to the mass of the manganese-based SCR low-temperature denitration catalyst is (2-10):1.
上述方案中,步骤3)中所述涂覆厚度为0.2~1.2mm。In the above solution, the coating thickness in step 3) is 0.2-1.2 mm.
上述方案中,步骤4)中所述热处理步骤为:加热至200~400℃保温2~6h。In the above solution, the heat treatment step in step 4) is: heating to 200-400° C. for 2-6 hours.
上述方案中,步骤5)中所述红外照射处理中选取的红外光波段为中红外波段(2.5~25μm),处理时间10~30min。In the above scheme, the infrared light band selected in the infrared irradiation treatment in step 5) is the mid-infrared band (2.5-25 μm), and the treatment time is 10-30 min.
上述方案中,所述低温脱硝锰系催化剂负载用低温胶的制备方法为:1)依次添加无水乙醇、水、异丙醇、正硅酸乙酯、邻苯二酚和甲醛水溶液,进行不断搅拌与超声分散,得均匀的混合液I;2)向所得混合液I中缓慢加入强酸,调节PH值至2~4,得混合液II,同时进行搅拌和超声分散;3)将混合液II加热至70~90℃,并进行恒温搅拌反应2~8h,至得粘性透明胶体,即为所述的低温脱硝锰系催化剂负载用低温胶。In the above scheme, the preparation method of the low-temperature gel for low-temperature denitrification manganese-based catalyst loading is as follows: 1) adding absolute ethanol, water, isopropanol, tetraethyl orthosilicate, catechol and formaldehyde aqueous solution in sequence, and continuously Stir and ultrasonically disperse to obtain a uniform mixed solution I; 2) Slowly add strong acid to the obtained mixed solution I to adjust the pH value to 2-4 to obtain a mixed solution II, which is simultaneously stirred and ultrasonically dispersed; 3) Mixed solution II Heating to 70-90°C, and carrying out constant temperature stirring reaction for 2-8 hours, until a viscous transparent colloid is obtained, which is the low-temperature glue for supporting low-temperature denitrification manganese-based catalysts.
上述方案中,所述无水乙醇、水、正硅酸乙酯和异丙醇的体积比为(3~8):1:(2~4):(0.05~0.1);邻苯二酚和甲醛水溶液的体积比为(1~1.2):1;正硅酸乙酯与甲醛水溶液的体积比为(20~60):1;强酸为盐酸或硝酸,浓度为1~3mol/L。In the above scheme, the volume ratio of the absolute ethanol, water, tetraethyl orthosilicate and Virahol is (3~8):1:(2~4):(0.05~0.1); The volume ratio of formaldehyde solution is (1~1.2):1; the volume ratio of tetraethyl orthosilicate to formaldehyde solution is (20~60):1; the strong acid is hydrochloric acid or nitric acid, the concentration is 1~3mol/L.
上述方案中,步骤2)中所述锰基低温SCR脱硝催化剂为MnOx(非负载型)、MnOx/TiO2(负载型)或Cu-MnOx/TiO2(负载型)型低温SCR脱硝催化剂,其中MnOx的存在形式为MnO2、Mn2O3、Mn3O4中的一种或几种。In the above scheme, the manganese-based low-temperature SCR denitration catalyst in step 2) is MnO x (non-supported), MnO x /TiO 2 (supported) or Cu-MnO x /TiO 2 (supported) type low-temperature SCR denitration The catalyst, wherein the form of MnO x is one or more of MnO 2 , Mn 2 O 3 , and Mn 3 O 4 .
根据上述方案制备的玻璃纤维布负载锰基低温SCR脱硝催化剂,其在温度范围为80-180℃、空速为20000~30000h-1的条件下,其脱硝效率可达98%。The manganese-based low-temperature SCR denitration catalyst supported on glass fiber cloth prepared according to the above scheme has a denitration efficiency of 98% under the conditions of a temperature range of 80-180°C and a space velocity of 20000-30000h -1 .
本发明的有益效果在于:The beneficial effects of the present invention are:
1)玻璃纤维布具有物理化学性能稳定、绝缘性好、耐热性强、抗腐蚀性好和机械强度高等特点,利用玻璃纤维布负载锰基低温SCR脱硝催化剂可以延长催化剂的使用寿命,提高催化剂的机械强度,并有效降低生产成本。同时,玻璃纤维布在做成烟气过滤结构的同时,发挥脱硝的作用。1) Glass fiber cloth has the characteristics of stable physical and chemical properties, good insulation, strong heat resistance, good corrosion resistance and high mechanical strength. Using glass fiber cloth to load manganese-based low-temperature SCR denitrification catalyst can prolong the service life of the catalyst and improve the performance of the catalyst. Mechanical strength, and effectively reduce production costs. At the same time, the glass fiber cloth plays the role of denitrification while making the flue gas filtering structure.
2)本发明通过利用水解合成法制备得到的低温脱硝锰系催化剂负载用低温胶将锰基低温SCR脱硝催化剂负载于玻璃纤维布表面,制备得到的材料中催化剂在玻璃纤维布上负载均匀,牢固度较好,且具有良好的脱硝性能。2) In the present invention, the manganese-based low-temperature SCR denitration catalyst is loaded on the surface of glass fiber cloth by using low-temperature adhesive for low-temperature denitrification manganese-based catalyst prepared by hydrolysis synthesis method, and the catalyst in the prepared material is evenly loaded on the glass fiber cloth, firm It has good denitrification performance and good denitrification performance.
3)通过对制备得到的催化材料进行红外处理,不仅可以提高催化剂和玻璃纤维布之间的牢固度,还能提高催化剂样品的活性及其脱硝效率。3) By infrared treatment of the prepared catalytic material, not only the firmness between the catalyst and the glass fiber cloth can be improved, but also the activity of the catalyst sample and its denitrification efficiency can be improved.
具体实施方式detailed description
为了更好地理解本发明,下面结合实施例进一步阐明本发明的内容,但本发明不仅仅局限于下面的实施例。In order to better understand the present invention, the content of the present invention is further illustrated below in conjunction with the examples, but the present invention is not limited to the following examples.
以下实施例如无具体说明,采用的试剂市售化学试剂或工业产品。The following examples are not specifically described, and the reagents used are commercially available chemical reagents or industrial products.
以下实施例中,所述低温脱硝锰系催化剂负载用低温胶的制备方法为:1)依次将30ml无水乙醇、10ml去离子水、0.5ml异丙醇、20ml正硅酸乙酯、邻苯二酚和甲醛(其中邻苯二酚和甲醛水溶液的体积比为1:1,二者总体积为1ml)加入三口烧瓶中,进行不断搅拌与超声分散,持续30min,得均匀的混合液I;2)向所得混合液I中缓慢加入盐酸溶液(浓度为1mol/L),调节PH值为2,得混合液II,同时进行搅拌和超声分散,时间为10min;3)将混合液II以3℃/min的速率加热至70℃,并进行恒温搅拌反应8h,至得粘性透明胶体(在烧杯中有挂壁现象),即为所述的低温脱硝锰系催化剂负载用低温胶。In the following examples, the preparation method of the low-temperature gel for low-temperature denitrification manganese-based catalyst loading is as follows: 1) sequentially mix 30ml of absolute ethanol, 10ml of deionized water, 0.5ml of isopropanol, 20ml of tetraethyl orthosilicate, o-benzene Add diphenol and formaldehyde (wherein the volume ratio of catechol and formaldehyde aqueous solution is 1:1, and the total volume of the two is 1ml) into a three-necked flask, continuously stir and ultrasonically disperse for 30min to obtain a uniform mixed solution I; 2) Slowly add hydrochloric acid solution (concentration: 1mol/L) to the obtained mixed solution I, adjust the pH value to 2 to obtain the mixed solution II, and simultaneously stir and ultrasonically disperse for 10 minutes; 3) Mix the mixed solution II with 3 Heat to 70°C at a rate of °C/min, and carry out a constant temperature stirring reaction for 8 hours to obtain a viscous transparent colloid (there is wall hanging in the beaker), which is the low-temperature glue for supporting low-temperature denitrification manganese-based catalysts.
以下实施例中采用的锰基低温SCR脱硝催化剂为非负载型的MnOx低温SCR脱硝催化剂,其制备方法包括如下步骤:1)将高锰酸钾和醋酸锰以1:2的摩尔比分别溶解于蒸馏水;2)将所得醋酸锰溶液缓慢加入高锰酸钾溶液中并充分搅拌,反应10min后抽滤并进行超声洗涤,直至滤液呈中性;3)将沉淀物置于烘箱中干燥后,置于马弗炉中加热至400℃焙烧3h,充分研磨后即得非负载型的MnOx低温SCR脱硝催化剂(其主要成分为MnO2,还有少量Mn2O3和Mn3O4)。The manganese-based low-temperature SCR denitration catalyst adopted in the following examples is a non-supported MnO x low-temperature SCR denitration catalyst, and its preparation method comprises the following steps: 1) Potassium permanganate and manganese acetate are dissolved respectively with a molar ratio of 1:2 in distilled water; 2) Slowly add the obtained manganese acetate solution into the potassium permanganate solution and fully stir, after 10 minutes of reaction, suction filtration and ultrasonic washing are performed until the filtrate is neutral; 3) After drying the precipitate in an oven, place Heat it in a muffle furnace to 400°C and roast for 3 hours, and grind it thoroughly to get a non-supported MnO x low-temperature SCR denitration catalyst (its main component is MnO 2 , and there are a small amount of Mn 2 O 3 and Mn 3 O 4 ).
实施例1Example 1
一种玻璃纤维布负载锰基低温SCR脱硝催化剂的制备方法,包括以下步骤:A method for preparing a manganese-based low-temperature SCR denitration catalyst supported by glass fiber cloth, comprising the following steps:
1)根据实际用途将玻璃纤维布剪成一定尺寸与形状,放入肥皂水中浸泡后洗涤、晾干,然后置于1mol/L的盐酸中腐蚀20min,得预处理后的玻璃纤维布,干燥并称重后,静置备用;1) Cut the glass fiber cloth into a certain size and shape according to the actual use, soak it in soapy water, wash and dry it, and then corrode it in 1mol/L hydrochloric acid for 20 minutes to obtain the pretreated glass fiber cloth, dry it and After weighing, put it aside for later use;
2)将低温脱硝锰系催化剂负载用低温胶和锰基低温SCR脱硝催化剂按低温胶的体积与锰基低温SCR脱硝催化剂的质量为2:1的比例加入容器中,并用搅拌棒进行搅拌,混合均匀,静置备用;2) Put the low-temperature glue for low-temperature denitrification manganese-based catalyst loading and the manganese-based low-temperature SCR denitration catalyst into the container at a ratio of 2:1 between the volume of the low-temperature glue and the mass of the manganese-based low-temperature SCR denitration catalyst, and stir with a stirring bar to mix Evenly, stand for later use;
3)将步骤1)所得预处理后的玻璃纤维布平铺于不锈钢工作台上,利用喷涂机将步骤2)中混合均匀的低温胶和锰基低温SCR脱硝催化剂均匀涂覆于预处理后的玻璃纤维布上,涂覆厚度为0.2mm,并置于烘箱内干燥;3) Spread the pretreated glass fiber cloth obtained in step 1) on a stainless steel workbench, and use a sprayer to evenly coat the low-temperature glue and manganese-based low-temperature SCR denitration catalyst mixed uniformly in step 2) on the pretreated On glass fiber cloth, the coating thickness is 0.2mm, and placed in an oven to dry;
4)将步骤3)所得材料置于马弗炉内进行热处理,热处理温度为200℃,时间为2h,冷却后得负载锰基低温SCR脱硝催化剂的玻璃纤维布;4) placing the material obtained in step 3) in a muffle furnace for heat treatment, the heat treatment temperature is 200° C., and the time is 2 hours. After cooling, a glass fiber cloth loaded with a manganese-based low-temperature SCR denitration catalyst is obtained;
5)将步骤4)所得负载锰基低温SCR脱硝催化剂的玻璃纤维布进行红外照射处理,选取的红外光波段为中红外波段(2.5~25μm),处理时间为10min,即得所述的玻璃纤维布负载锰基低温SCR脱硝催化剂。5) The glass fiber cloth loaded with the manganese-based low-temperature SCR denitration catalyst obtained in step 4) is subjected to infrared irradiation treatment, the selected infrared light band is the mid-infrared band (2.5-25 μm), and the treatment time is 10 minutes to obtain the glass fiber Cloth-loaded manganese-based low-temperature SCR denitration catalyst.
将本实施例所得产物置于固定床石英管反应器中进行脱硝性能测试,模拟烟气由N2、O2、NO、NH3组成,其中NO为720ppm,NH3为800ppm,O2为体积分数为3%的,N2作为平衡气;测试温度范围为80-180℃、空速为30000h-1。测试结果表明:随测试温度的升高,脱硝效率逐渐提升,其平均脱硝效率可达到70%。其中在100℃时脱硝率为53%,120℃可达72%,高于120℃时均在80%以上,180℃时最高,可达到86%。The product obtained in this example was placed in a fixed-bed quartz tube reactor for denitration performance test. The simulated flue gas was composed of N 2 , O 2 , NO, and NH 3 , where NO was 720 ppm, NH 3 was 800 ppm, and O 2 was the volume When the fraction is 3%, N 2 is used as the balance gas; the test temperature range is 80-180°C, and the space velocity is 30000h -1 . The test results show that: with the increase of the test temperature, the denitrification efficiency gradually increases, and the average denitrification efficiency can reach 70%. Among them, the denitrification rate is 53% at 100°C, 72% at 120°C, above 80% at 120°C, and the highest at 180°C, reaching 86%.
实施例2Example 2
一种玻璃纤维布负载锰基低温SCR脱硝催化剂的制备方法,包括以下步骤:A method for preparing a manganese-based low-temperature SCR denitration catalyst supported by glass fiber cloth, comprising the following steps:
1)根据实际用途将玻璃纤维布剪成一定尺寸与形状,放入肥皂水中浸泡后洗涤、晾干,然后置于2mol/L的盐酸中腐蚀30min,得预处理后的玻璃纤维布,干燥并称重后,静置备用;1) Cut the glass fiber cloth into a certain size and shape according to the actual use, soak it in soapy water, wash and dry it, and then corrode it in 2mol/L hydrochloric acid for 30 minutes to obtain the pretreated glass fiber cloth, dry it and After weighing, put it aside for later use;
2)将低温脱硝锰系催化剂负载用低温胶和锰基低温SCR脱硝催化剂按低温胶的体积与锰基低温SCR脱硝催化剂的质量为4:1的比例加入容器中,并用搅拌棒进行搅拌,混合均匀,静置备用;2) Put the low-temperature gel for low-temperature denitrification manganese-based catalyst loading and the manganese-based low-temperature SCR denitrification catalyst into the container at a ratio of 4:1 between the volume of the low-temperature gel and the mass of the manganese-based low-temperature SCR denitrification catalyst, and stir with a stirring bar to mix Evenly, stand for later use;
3)将步骤1)所得预处理后的玻璃纤维布平铺于不锈钢工作台上,利用喷涂机将步骤2)中混合均匀的低温胶和锰基低温SCR脱硝催化剂均匀涂覆于预处理后的玻璃纤维布上,涂覆厚度为0.4mm,并置于烘箱内干燥;3) Spread the pretreated glass fiber cloth obtained in step 1) on a stainless steel workbench, and use a sprayer to evenly coat the low-temperature glue and manganese-based low-temperature SCR denitration catalyst mixed uniformly in step 2) on the pretreated On glass fiber cloth, the coating thickness is 0.4mm, and placed in an oven to dry;
4)将步骤3)所得材料置于马弗炉内进行热处理,热处理温度为300℃,时间为3h,冷却后得负载锰基低温SCR脱硝催化剂的玻璃纤维布;4) placing the material obtained in step 3) in a muffle furnace for heat treatment, the heat treatment temperature is 300° C., and the time is 3 hours. After cooling, a glass fiber cloth loaded with a manganese-based low-temperature SCR denitration catalyst is obtained;
5)将步骤4)所得负载锰基低温SCR脱硝催化剂的玻璃纤维布进行红外照射处理,选取的红外光波段为中红外波段(2.5~25μm),处理时间为20min,即得所述的玻璃纤维布负载锰基低温SCR脱硝催化剂。5) The glass fiber cloth loaded with the manganese-based low-temperature SCR denitration catalyst obtained in step 4) is subjected to infrared irradiation treatment, the selected infrared light band is the mid-infrared band (2.5-25 μm), and the treatment time is 20 minutes to obtain the glass fiber cloth Cloth-loaded manganese-based low-temperature SCR denitration catalyst.
将本实施例所得产物置于固定床石英管反应器中进行脱硝性能测试,模拟烟气由N2、O2、NO、NH3组成,其中NO为720ppm,NH3为800ppm,O2为体积分数为3%,N2作为平衡气;测试温度范围为80-180℃、空速为25000h-1。测试结果表明:随测试温度的升高,脱硝效率逐渐提升,其平均脱硝效率可达到90%。其中在100℃时脱硝率为75%,高于100℃时均在90%以上,且在180℃时最高,可达到98%。The product obtained in this example was placed in a fixed-bed quartz tube reactor for denitration performance test. The simulated flue gas was composed of N 2 , O 2 , NO, and NH 3 , where NO was 720 ppm, NH 3 was 800 ppm, and O 2 was the volume The fraction is 3%, and N 2 is used as the balance gas; the test temperature range is 80-180°C, and the space velocity is 25000h -1 . The test results show that: with the increase of the test temperature, the denitrification efficiency gradually increases, and the average denitrification efficiency can reach 90%. Among them, the denitrification rate is 75% at 100°C, above 90% at higher than 100°C, and the highest at 180°C, reaching 98%.
实施例3Example 3
一种玻璃纤维布负载锰基低温SCR脱硝催化剂的制备方法,包括以下步骤:A method for preparing a manganese-based low-temperature SCR denitration catalyst supported by glass fiber cloth, comprising the following steps:
1)根据实际用途将玻璃纤维布剪成一定尺寸与形状,放入肥皂水中浸泡后洗涤、晾干,然后置于3mol/L的盐酸中腐蚀40min,得预处理后的玻璃纤维布,干燥并称重后,静置备用;1) Cut the glass fiber cloth into a certain size and shape according to the actual use, soak it in soapy water, wash and dry it, and then corrode it in 3mol/L hydrochloric acid for 40min to obtain the pretreated glass fiber cloth, dry it and After weighing, put it aside for later use;
2)将低温脱硝锰系催化剂负载用低温胶和锰基低温SCR脱硝催化剂按低温胶的体积与锰基低温SCR脱硝催化剂的质量为8:1的比例加入容器中,并用搅拌棒进行搅拌,混合均匀,静置备用;2) Put the low-temperature gel for low-temperature denitrification manganese-based catalyst loading and the manganese-based low-temperature SCR denitrification catalyst into the container at a ratio of 8:1 between the volume of the low-temperature gel and the mass of the manganese-based low-temperature SCR denitrification catalyst, and stir with a stirring bar to mix Evenly, stand for later use;
3)将步骤1)所得预处理后的玻璃纤维布平铺于不锈钢工作台上,利用喷涂机将步骤2)中混合均匀的低温胶和锰基低温SCR脱硝催化剂均匀涂覆于预处理后的玻璃纤维布上,涂覆厚度为1.0mm,并置于烘箱内干燥;3) Spread the pretreated glass fiber cloth obtained in step 1) on a stainless steel workbench, and use a sprayer to evenly coat the low-temperature glue and manganese-based low-temperature SCR denitration catalyst mixed uniformly in step 2) on the pretreated On glass fiber cloth, the coating thickness is 1.0mm, and placed in an oven to dry;
4)将步骤3)所得材料置于马弗炉内进行热处理,热处理温度为400℃,时间为4h,冷却后得负载锰基低温SCR脱硝催化剂的玻璃纤维布;4) placing the material obtained in step 3) in a muffle furnace for heat treatment, the heat treatment temperature is 400° C., and the time is 4 hours. After cooling, a glass fiber cloth loaded with a manganese-based low-temperature SCR denitration catalyst is obtained;
5)将步骤4)所得负载锰基低温SCR脱硝催化剂的玻璃纤维布进行红外照射处理,选取的红外光波段为中红外波段(2.5~25μm),处理时间为30min,即得所述的玻璃纤维布负载锰基低温SCR脱硝催化剂。5) The glass fiber cloth loaded with the manganese-based low-temperature SCR denitration catalyst obtained in step 4) is subjected to infrared irradiation treatment, the selected infrared light band is the mid-infrared band (2.5-25 μm), and the treatment time is 30 minutes to obtain the glass fiber cloth Cloth-loaded manganese-based low-temperature SCR denitration catalyst.
将本实施例所得产物置于固定床石英管反应器中进行脱硝性能测试,模拟烟气由N2、O2、NO、NH3组成,其中NO为720ppm,NH3为800ppm,O2为体积分数为3%,N2作为平衡气;测试温度范围为80-180℃、空速为20000h-1。测试结果表明:随测试温度的升高,脱硝效率逐渐提升,其平均脱硝效率可达到80%。其中在100℃时脱硝率为69%,120℃为76%,180℃时达到最高,为88%。The product obtained in this example was placed in a fixed-bed quartz tube reactor for denitration performance test. The simulated flue gas was composed of N 2 , O 2 , NO, and NH 3 , where NO was 720 ppm, NH 3 was 800 ppm, and O 2 was the volume The fraction is 3%, N 2 is used as the balance gas; the test temperature range is 80-180°C, and the space velocity is 20000h -1 . The test results show that: with the increase of the test temperature, the denitrification efficiency gradually increases, and the average denitrification efficiency can reach 80%. Among them, the denitrification rate is 69% at 100°C, 76% at 120°C, and reaches the highest at 88% at 180°C.
以上所述仅为本发明的优选实施方式,应当指出,对于本领域的普通技术人员来说,在不脱离本发明创造构思的前提下,做出若干改进和变换,这些都属于本发明的保护范围。The above is only a preferred embodiment of the present invention, it should be pointed out that for those of ordinary skill in the art, without departing from the creative concept of the present invention, some improvements and changes are made, and these all belong to the protection of the present invention. scope.
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