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CN105013249B - Nitre and dioxin-removal PPS composite felt functional filtering material and preparation method thereof - Google Patents

Nitre and dioxin-removal PPS composite felt functional filtering material and preparation method thereof Download PDF

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CN105013249B
CN105013249B CN201510381907.1A CN201510381907A CN105013249B CN 105013249 B CN105013249 B CN 105013249B CN 201510381907 A CN201510381907 A CN 201510381907A CN 105013249 B CN105013249 B CN 105013249B
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李刚
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Zhejiang Hongsheng New Material Technology Group Co ltd
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Liaoning Hongsheng Environmental Technology Group Co ltd
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Abstract

本发明提供了一种脱硝和二噁英的PPS复合毡功能滤料的制备方法,包括以下步骤:(1)将活性金属催化剂粉末与PTFE树脂粉末混合后制成含有催化剂的PTFE纤维和含有催化剂的PTFE微孔薄膜;(2)将含有催化剂的PTFE纤维与高强PTFE纤维采用1‑10:1‑10交替布置的方式制成经轴,采用机织的方式制成PTFE基布层;(3)将PPS纤维与含有催化剂的PTFE短纤维混合后与PTFE基布层一起放入针刺机,制成PPS复合针刺毡;(4)将活性金属催化剂乳液与PTFE乳液混合制成催化剂混合处理液,对PPS复合针刺毡进行整体浸渍处理后在280‑350℃下烧结;(5)将烧结后的PPS复合针刺毡与含有催化剂的PTFE微孔薄膜同时引入热覆膜机中,表面进行热压覆膜加工。本发明能够显著提高过滤精度和脱硝和二噁英效率。

The invention provides a method for preparing a PPS composite felt functional filter material for denitrification and dioxin, comprising the following steps: (1) mixing active metal catalyst powder with PTFE resin powder to prepare PTFE fibers containing catalyst and catalyst-containing (2) the PTFE fibers containing the catalyst and the high-strength PTFE fibers are alternately arranged in 1-10:1-10 to make warp beams, and the PTFE base cloth layer is made by weaving; (3 ) Mix PPS fiber with PTFE short fiber containing catalyst and put it into needle punching machine together with PTFE base cloth layer to make PPS composite needle felt; (4) Mix active metal catalyst emulsion and PTFE emulsion to make catalyst mixed treatment (5) The sintered PPS composite needle felt and the PTFE microporous film containing the catalyst are introduced into the thermal laminating machine at the same time, and the surface Carry out hot press lamination processing. The invention can remarkably improve the filtration precision and the denitrification and dioxin efficiency.

Description

一种脱硝和二噁英的PPS复合毡功能滤料及其制备方法A PPS composite felt functional filter material for denitrification and dioxin and preparation method thereof

技术领域technical field

本发明涉及环保除尘烟气净化领域,特别是涉及一种脱硝和二噁英的PPS复合毡功能滤料及其制备方法。The invention relates to the field of environmental protection dust removal flue gas purification, in particular to a PPS composite felt functional filter material for denitrification and dioxin removal and a preparation method thereof.

背景技术Background technique

目前,随着经济的快速发展,工业废气的排放急剧增加。我国大气环境的污染日趋严重,并且逐步由煤烟型污染向混合型污染转变,烟尘、SOx、NOx、Hg排放总量已居世界第一。其中氮氧化物、二噁英是大气中主要污染物之一,排放量超过环境自净能力,危害巨大,环境状况形势十分严峻。氮氧化物、二噁英是影响大气质量的最主要的气态污染物,是衡量大气是否遭到污染的重要标志。At present, with the rapid development of the economy, the emission of industrial waste gas has increased dramatically. The pollution of my country's atmospheric environment is becoming more and more serious, and it is gradually changing from soot pollution to mixed pollution. The total emissions of smoke, SOx, NOx, and Hg rank first in the world. Among them, nitrogen oxides and dioxins are one of the main pollutants in the atmosphere. The emission exceeds the self-purification capacity of the environment, causing great harm and the environmental situation is very severe. Nitrogen oxides and dioxins are the most important gaseous pollutants that affect air quality, and are important indicators to measure whether the atmosphere is polluted.

燃煤电厂和垃圾焚烧厂是SOx和NOx排放的大户,烟气中产生的污染物包括硫氧化物、氮氧化物、粉尘、可吸入颗粒物(IP)、二噁英类(PCDD/Fs)、重金属等有害物质。目前,氮氧化物已逐渐成为第一大酸性污染气体,氮氧化物与空气中的水结合最终会转化成硝酸和硝酸盐,硝酸是酸雨的成因之一,它与其他污染物在一定条件下能产生光化学烟雾污染,严重污染环境并危及人体健康。二噁英是一类来源广、毒性强,稳定性高的有机污染物。它是多氯二苯并二噁英和多氯二苯并呋喃的统称,前者75种,后者135种,共210个同族体。这些化合物大部分具有强烈致癌、致畸、致突变的特点。由于二噁英的稳定性及易溶于油脂的特性,一旦进入人体便难以排出,长期积累,将会永久破坏人体的免疫系统及扰乱人体的激素分泌,对人体构成重大伤害。Coal-fired power plants and waste incineration plants are major emitters of SOx and NOx. The pollutants produced in the flue gas include sulfur oxides, nitrogen oxides, dust, inhalable particulate matter (IP), dioxins (PCDD/Fs), Hazardous substances such as heavy metals. At present, nitrogen oxides have gradually become the largest acid polluting gas. Nitrogen oxides combined with water in the air will eventually be converted into nitric acid and nitrates. Nitric acid is one of the causes of acid rain. It is combined with other pollutants under certain conditions. It can produce photochemical smog pollution, seriously pollute the environment and endanger human health. Dioxins are a class of organic pollutants with wide sources, strong toxicity and high stability. It is a general term for polychlorinated dibenzodioxins and polychlorinated dibenzofurans. There are 75 types of the former and 135 types of the latter, with a total of 210 homologues. Most of these compounds are strongly carcinogenic, teratogenic and mutagenic. Due to the stability and oil-soluble properties of dioxin, it is difficult to discharge once it enters the human body. If it accumulates for a long time, it will permanently damage the human body's immune system and disrupt the body's hormone secretion, causing serious harm to the human body.

氮氧化物、二噁英等有害物质引起的环境问题以及对人体健康的危害巨大。虽然,国内外已研究开发了各种各样的烟气脱硝、脱除二噁英等工艺,各有特色,并取得了一定成果,但共同存在一个有害物质的脱除效率问题,烟气中的氮氧化物、二噁英等有害物质有一定的逃逸现象。The environmental problems caused by harmful substances such as nitrogen oxides and dioxins and the harm to human health are huge. Although various flue gas denitrification and dioxin removal processes have been researched and developed at home and abroad, each has its own characteristics and achieved certain results, but there is a problem of removal efficiency of harmful substances in common. Harmful substances such as nitrogen oxides and dioxins have a certain escape phenomenon.

环境效益和经济效益综合考虑将成为今后氮氧化物、二噁英等有害物质防治技术的发展主流。为了进一步提高有害物质的脱除效率,通过研发设计新型功能性环保除尘过滤材料,在滤料中植入活性催化剂,实现在高温烟气进行除尘同时,对高温烟气中含有的氮氧化物、二噁英等有毒有害物质进行催化分解的目的。因此,在原有的环保除尘系统中,无需改变现有的工艺设备和工况条件,即可完成残余氮氧化物、二噁英等有害物质的催化分解。Comprehensive consideration of environmental benefits and economic benefits will become the mainstream in the development of technologies for the prevention and control of harmful substances such as nitrogen oxides and dioxins in the future. In order to further improve the removal efficiency of harmful substances, through the research and development of new functional and environmentally friendly dust removal filter materials, active catalysts are implanted in the filter materials to achieve dust removal in high-temperature flue gas while removing nitrogen oxides and nitrogen oxides contained in high-temperature flue gas. The purpose of catalytic decomposition of toxic and harmful substances such as dioxins. Therefore, in the original environmental protection dust removal system, the catalytic decomposition of residual nitrogen oxides, dioxins and other harmful substances can be completed without changing the existing process equipment and working conditions.

发明内容Contents of the invention

本发明的目的是解决现有脱硝和二噁英滤料技术中存在的部分问题,提供一种脱硝和二噁英的PPS复合毡功能滤料及其制备方法。The purpose of the present invention is to solve some problems existing in the existing denitrification and dioxin filter material technology, and provide a PPS composite felt functional filter material for denitrification and dioxin and a preparation method thereof.

本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:

一种脱硝和二噁英的PPS复合毡功能滤料的制备方法,包括以下步骤:A preparation method of a PPS composite felt functional filter material for denitrification and dioxin, comprising the following steps:

(1)将活性金属催化剂粉末混合与PTFE树脂混合后,分别制成含有催化剂的PTFE纤维和含有催化剂的PTFE微孔薄膜;(1) After the active metal catalyst powder is mixed with the PTFE resin, the PTFE fiber containing the catalyst and the PTFE microporous film containing the catalyst are made respectively;

(2)将含有催化剂的PTFE纤维与高强PTFE纤维采用1-10:1-10交替布置的方式制成经轴,采用机织的方式织造制成PTFE基布层;(2) the PTFE fiber containing catalyst and the high-strength PTFE fiber adopt the mode of 1-10:1-10 to be arranged alternately to make warp beam, adopt the mode of weaving to weave and make PTFE base cloth layer;

(3)将PPS纤维与含有催化剂的PTFE短纤维混合后与PTFE基布层一起放入针刺机,在PTFE基布层的两侧形成PPS+催化PTFE纤维强度层,制成PPS复合针刺毡;(3) PPS fibers are mixed with short PTFE fibers containing catalysts and put into the needle punching machine together with the PTFE base cloth layer to form PPS+catalyzed PTFE fiber strength layers on both sides of the PTFE base cloth layer to make PPS composite needle felt ;

(4)将活性金属催化剂乳液与PTFE乳液混合制成催化剂混合处理液,对PPS复合针刺毡进行整体浸渍处理,之后在280-350℃进行烧结;(4) Mix the active metal catalyst emulsion with the PTFE emulsion to make a catalyst mixed treatment solution, and perform overall impregnation treatment on the PPS composite needle felt, and then sinter at 280-350°C;

(5)将烧结后的PPS复合针刺毡与含有催化剂的PTFE微孔薄膜同时引入热覆膜机中,表面进行热压覆膜加工。(5) The sintered PPS composite needle-punched felt and the PTFE microporous film containing the catalyst are simultaneously introduced into the hot-coating machine, and the surface is subjected to hot-press coating.

优选地,所述步骤(1)中的活性金属催化剂选自V2O5、WO3、MoO3/TiO2中的一种或几种。Preferably, the active metal catalyst in the step (1) is selected from one or more of V 2 O 5 , WO 3 , MoO 3 /TiO 2 .

优选地,所述步骤(1)中活性金属催化剂粉末、PTFE树脂粉末的质量比为1-10:99-90。Preferably, the mass ratio of the active metal catalyst powder to the PTFE resin powder in the step (1) is 1-10:99-90.

优选地,所述步骤(3)中PPS纤维与含有催化剂的PTFE短纤维的比例为1-99:99-1。Preferably, the ratio of PPS fibers to catalyst-containing short PTFE fibers in the step (3) is 1-99:99-1.

优选地,所述步骤(4)中活性金属催化剂乳液与PTFE乳液的有效成分的质量比为1-99:99-1。Preferably, the mass ratio of the active metal catalyst emulsion to the active ingredient of the PTFE emulsion in the step (4) is 1-99:99-1.

优选地,所述PTFE乳液的固含量为30~50%。Preferably, the solid content of the PTFE emulsion is 30-50%.

优选地,所述活性金属催化剂乳液的有效成分为V2O5、WO3、MoO3/TiO2中的一种或几种。Preferably, the active ingredient of the active metal catalyst emulsion is one or more of V 2 O 5 , WO 3 , MoO 3 /TiO 2 .

优选地,所述活性金属催化剂乳液的固含量为40~60%。Preferably, the solid content of the active metal catalyst emulsion is 40-60%.

根据上述方法制备的脱硝和二噁英的PPS复合毡功能滤料,依次包括含有催化剂的PTFE微孔薄膜层、第一催化剂混合处理液浸渍层、PPS复合针刺毡、第二催化剂混合处理液浸渍层;所述PPS复合针刺毡包括依次连接的第一PPS+催化PTFE纤维强度层、PTFE基布层、第二PPS+催化PTFE纤维强度层;所述含有催化剂的PTFE微孔薄膜层之间第一催化剂混合处理液浸渍层通过热压覆合。The PPS composite felt functional filter material for denitrification and dioxin prepared according to the above method, sequentially includes a PTFE microporous film layer containing a catalyst, a first catalyst mixed treatment liquid impregnation layer, a PPS composite needle felt, and a second catalyst mixed treatment liquid Impregnation layer; the PPS composite needle felt includes the first PPS+catalyzed PTFE fiber strength layer, the PTFE base cloth layer, the second PPS+catalyzed PTFE fiber strength layer connected in sequence; the second PTFE microporous film layer containing the catalyst A catalyst mixed treatment liquid impregnated layer is laminated by hot pressing.

本发明的有益效果:Beneficial effects of the present invention:

(1)本发明的脱硝和二噁英的PPS复合毡功能滤料具有适用工况范围广,无需改变原有的工艺设备和工况条件,即可完成残余氮氧化物、二噁英等有害物质的催化分解;系统运行安全平稳,低阻高效长寿命等显著特征,能源消耗和运行维护费用减低30%;(1) The PPS composite felt functional filter material for denitrification and dioxins of the present invention has a wide range of applicable working conditions, and can complete the removal of harmful substances such as residual nitrogen oxides and dioxins without changing the original process equipment and working conditions. Catalytic decomposition of substances; safe and stable system operation, low resistance, high efficiency and long life, etc., energy consumption and operation and maintenance costs are reduced by 30%;

(2)本发明的脱硝和二噁英的PPS复合毡功能滤料同时具有表面过滤的功效,将粉尘截留在滤料的表面,可以实现粉尘量小于5mg/Nm3的近零排放;(2) The PPS composite felt functional filter material for denitrification and dioxins of the present invention has the effect of surface filtration at the same time, and the dust is trapped on the surface of the filter material, and the near - zero emission of dust amount less than 5mg/Nm can be realized;

(3)本发明的脱硝和二噁英的PPS复合毡功能滤料在烟尘过滤的同时,由于多层次的催化剂分布层的引入,成倍提升废气与催化剂的接触面积,大幅提高对氮氧化物、二噁英等有害物质的催化分解效率;充分发挥滤料脱除有害物质的功能;(3) The PPS composite felt functional filter material for denitrification and dioxins of the present invention filters smoke and dust at the same time, due to the introduction of a multi-layered catalyst distribution layer, the contact area between the exhaust gas and the catalyst is doubled, and the nitrogen oxides are greatly improved. Catalytic decomposition efficiency of harmful substances such as dioxin and dioxin; give full play to the function of filter material to remove harmful substances;

(4)采用超细玻纤与催化PTFE纤维制作基材,保证滤料整体具有较高的拉伸强度,同时具有氮氧化物、二噁英等有害物质的催化分解功能;(4) The base material is made of ultra-fine glass fiber and catalytic PTFE fiber to ensure that the filter material has a high tensile strength as a whole, and at the same time it has the function of catalytic decomposition of harmful substances such as nitrogen oxides and dioxins;

(5)本发明的高精度PPS复合毡功能滤料耐温性能优秀。连续工作温度200℃,瞬间耐温可达220℃,满足催化剂分解氮氧化物、二噁英等有害物质的温度条件和滤袋使用寿命的双重要求。(5) The high-precision PPS composite felt functional filter material of the present invention has excellent temperature resistance. The continuous working temperature is 200°C, and the instantaneous temperature resistance can reach 220°C, which meets the dual requirements of the temperature conditions for the catalyst to decompose harmful substances such as nitrogen oxides and dioxins and the service life of the filter bag.

附图说明Description of drawings

图1是本发明滤料的结构示意图。Fig. 1 is a structural schematic diagram of the filter material of the present invention.

具体实施方式detailed description

为了更好地说明本发明,下面结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述。In order to better illustrate the present invention, the technical solutions in the embodiments of the present invention are clearly and completely described below in conjunction with the drawings in the embodiments of the present invention.

一种脱硝和二噁英的PPS复合毡功能滤料的制备方法,包括以下步骤:(1)将活性金属催化剂粉末混合与PTFE树脂混合后,分别制成含有催化剂的PTFE纤维和含有催化剂的PTFE微孔薄膜;(2)将含有催化剂的PTFE纤维与高强PTFE纤维采用1-10:1-10交替布置的方式制成经轴,采用机织的方式织造制成PTFE基布层;(3)将PPS纤维与含有催化剂的PTFE短纤维混合后与PTFE基布层一起放入针刺机,在PTFE基布层的两侧形成PPS+催化PTFE纤维强度层,制成PPS复合针刺毡;(4)将活性金属催化剂乳液与PTFE乳液混合制成催化剂混合处理液,对PPS复合针刺毡进行整体浸渍处理,之后在280-350℃进行烧结;(5)将烧结后的PPS复合针刺毡与含有催化剂的PTFE微孔薄膜同时引入热覆膜机中,表面进行热压覆膜加工。所述步骤(1)中的活性金属催化剂选自V2O5、WO3、MoO3/TiO2中的一种或几种。所述步骤(1)中活性金属催化剂粉末、PTFE树脂粉末的质量比为1-10:99-90。所述步骤(3)中PPS纤维与含有催化剂的PTFE短纤维的比例为1-99:99-1。所述步骤(4)中活性金属催化剂乳液与PTFE乳液的有效成分的质量比为1-99:99-1。所述PTFE乳液的固含量为30~50%。所述活性金属催化剂乳液的有效成分为V2O5、WO3、MoO3/TiO2中的一种或几种。所述活性金属催化剂乳液的固含量为40~60%。A preparation method of a PPS composite felt functional filter material for denitrification and dioxin, comprising the following steps: (1) After mixing active metal catalyst powder with PTFE resin, respectively make PTFE fiber containing catalyst and PTFE containing catalyst Microporous film; (2) PTFE fibers containing catalysts and high-strength PTFE fibers are alternately arranged in a manner of 1-10:1-10 to make warp beams, and woven into PTFE base cloth layers by weaving; (3) PPS fibers are mixed with short PTFE fibers containing a catalyst and put into a needle punching machine together with the PTFE base cloth layer to form a PPS+catalyzed PTFE fiber strength layer on both sides of the PTFE base cloth layer to make a PPS composite needle felt; (4 ) mixing the active metal catalyst emulsion with the PTFE emulsion to make a catalyst mixed treatment solution, and then impregnating the PPS composite needle felt as a whole, and then sintering at 280-350°C; (5) combining the sintered PPS composite needle felt with The PTFE microporous film containing the catalyst is introduced into the hot coating machine at the same time, and the surface is subjected to hot pressing coating processing. The active metal catalyst in the step (1) is selected from one or more of V 2 O 5 , WO 3 , MoO 3 /TiO 2 . In the step (1), the mass ratio of the active metal catalyst powder to the PTFE resin powder is 1-10:99-90. In the step (3), the ratio of the PPS fiber to the short PTFE fiber containing the catalyst is 1-99:99-1. In the step (4), the active metal catalyst emulsion and the active ingredient of the PTFE emulsion have a mass ratio of 1-99:99-1. The solid content of the PTFE emulsion is 30-50%. The effective components of the active metal catalyst emulsion are one or more of V 2 O 5 , WO 3 , MoO 3 /TiO 2 . The solid content of the active metal catalyst emulsion is 40-60%.

根据上述方法制备的脱硝和二噁英的PPS复合毡功能滤料,依次包括含有催化剂的PTFE微孔薄膜层、第一催化剂混合处理液浸渍层、PPS复合针刺毡、第二催化剂混合处理液浸渍层;所述PPS复合针刺毡包括依次连接的第一PPS+催化PTFE纤维强度层、PTFE基布层、第二PPS+催化PTFE纤维强度层;所述含有催化剂的PTFE微孔薄膜层之间第一催化剂混合处理液浸渍层通过热压覆合。The PPS composite felt functional filter material for denitrification and dioxin prepared according to the above method, sequentially includes a PTFE microporous film layer containing a catalyst, a first catalyst mixed treatment liquid impregnation layer, a PPS composite needle felt, and a second catalyst mixed treatment liquid Impregnation layer; the PPS composite needle felt includes the first PPS+catalyzed PTFE fiber strength layer, the PTFE base cloth layer, the second PPS+catalyzed PTFE fiber strength layer connected in sequence; the second PTFE microporous film layer containing the catalyst A catalyst mixed treatment liquid impregnated layer is laminated by hot pressing.

实施例1Example 1

将活性催化剂V2O5/TiO2微粉与PTFE树脂按2:98的比例均匀的混合在一起,分别制成含有催化剂的PTFE纤维和含有催化剂的PTFE微孔薄膜;其中,助剂的种类及质量可以根据需要任意选择。含有催化剂的PTFE纤维主要用于制作机织过滤布,含有催化剂的PTFE微孔薄膜最终覆合在滤料的表面。通过在滤料中植入活性催化剂的方式,达到在过滤烟尘的同时脱除烟气中氮氧化物和二噁英等有害物质的功效。具体步骤如下:The active catalyst V 2 O 5 /TiO 2 micropowder and PTFE resin are uniformly mixed together at a ratio of 2:98 to make PTFE fiber containing catalyst and PTFE microporous film containing catalyst; among them, the types of additives and The quality can be selected arbitrarily according to the needs. The PTFE fiber containing the catalyst is mainly used to make woven filter cloth, and the PTFE microporous film containing the catalyst is finally coated on the surface of the filter material. By implanting an active catalyst in the filter material, it can achieve the effect of removing harmful substances such as nitrogen oxides and dioxins in the flue gas while filtering the flue dust. Specific steps are as follows:

一是将含有催化剂的PTFE纤维与高强PTFE纤维在织布前的整经工序,采用1:1交替布置的方式制成经轴,采用机织的方式织造成PTFE基布,得到PTFE基布层4;One is the warping process of PTFE fibers containing catalysts and high-strength PTFE fibers before weaving, using a 1:1 alternate arrangement to make warp beams, and weaving them into PTFE base fabrics by weaving to obtain PTFE base fabric layers 4;

二是将PPS纤维与含有催化剂的PTFE短纤维按50:50的比例混合后,与PTFE基布层一同进入针刺机,在PTFE基布层的两侧形成第一PPS+催化PTFE纤维强度层3和第二PPS+催化PTFE纤维强度层5,制成PPS复合针刺毡。The second is to mix the PPS fiber with the PTFE short fiber containing the catalyst in a ratio of 50:50, and then enter the needle punching machine together with the PTFE base cloth layer, and form the first PPS+catalyzed PTFE fiber strength layer on both sides of the PTFE base cloth layer3 And the second PPS+catalyzed PTFE fiber strength layer 5 to make PPS composite needle felt.

三是将固含量为50%的活性金属催化剂乳液与固含量为40%的PTFE乳液按有效成分的质量比为40:60制成催化剂混合处理液,对PPS复合针刺毡进行整体浸渍处理,经过280℃高温烧结后,在PPS复合针刺毡的上下表面形成第一催化剂混合处理液浸渍层2和第二催化剂混合处理液浸渍层6。The third is to make a catalyst mixed treatment solution by making the active metal catalyst emulsion with a solid content of 50% and the PTFE emulsion with a solid content of 40% according to the mass ratio of active ingredients of 40:60, and carry out overall impregnation treatment on the PPS composite needle felt, After sintering at a high temperature of 280°C, the first catalyst mixed treatment liquid impregnated layer 2 and the second catalyst mixed treatment liquid impregnated layer 6 are formed on the upper and lower surfaces of the PPS composite needle felt.

四是滤料整体浸渍处理后与含有催化剂的PTFE微孔薄膜同时引入热覆膜机中,表面进行热压覆膜加工,使含有催化剂的PTFE微孔薄膜1与基材牢固的结合在一起,最终制成PPS复合毡功能滤料。Fourth, after the overall impregnation treatment of the filter material, the PTFE microporous film containing the catalyst is simultaneously introduced into the hot-coating machine, and the surface is subjected to hot-press coating processing, so that the PTFE microporous film 1 containing the catalyst is firmly combined with the substrate, Finally, the PPS composite felt functional filter material is made.

脱硝和二噁英的PPS复合毡功能滤料整体分为六个层次:由迎尘面到净气面依次为含有催化剂的PTFE微孔薄膜层1,第一催化剂混合乳液浸渍处理层2,第一PPS+催化PTFE纤维强度层3,PTFE基布层4,第二PPS+催化PTFE纤维强度层5,第二催化剂混合乳液浸渍处理层6。The PPS composite felt functional filter material for denitrification and dioxin is divided into six layers as a whole: from the dust face to the clean air face, there are PTFE microporous film layer 1 containing catalyst, the first catalyst mixed emulsion impregnated layer 2, and the second A PPS+catalyzed PTFE fiber strength layer 3, a PTFE base cloth layer 4, a second PPS+catalyzed PTFE fiber strength layer 5, and a second catalyst mixed emulsion impregnated treatment layer 6.

脱硝和二噁英的PPS复合毡功能滤料,显著提高滤料的过滤精度,滤料由外到内(迎尘面到净气面)形成多层次的活性催化剂分布层,当高温烟气经过时,粉尘被阻隔在滤料的表面;含有有害物质的气体通过时,氮氧化物和二噁英等有害物质与活性催化剂发生反应,有害成份被分解为无害的物质与粉尘一并进行收集,从而实现烟气除尘和脱除有害物质的双重功效。The PPS composite felt functional filter material for denitrification and dioxin significantly improves the filtration accuracy of the filter material. The filter material forms a multi-layered active catalyst distribution layer from the outside to the inside (the dust-facing surface to the clean gas surface). When the high-temperature flue gas passes through When the dust is blocked on the surface of the filter material; when the gas containing harmful substances passes through, harmful substances such as nitrogen oxides and dioxins react with the active catalyst, and the harmful components are decomposed into harmless substances and collected together with the dust , so as to achieve the double effect of flue gas dust removal and removal of harmful substances.

脱硝和二噁英的PPS复合毡功能滤料的参数Parameters of PPS composite felt functional filter material for denitrification and dioxin

实施例2Example 2

将活性催化剂V2O5-WO3/TiO2微粉与PTFE树脂按10:90的比例均匀的混合在一起,分别制成含有催化剂的PTFE纤维和含有催化剂的PTFE微孔薄膜;其中,助剂的种类及质量可以根据需要任意选择。含有催化剂的PTFE纤维主要用于制作机织过滤布,含有催化剂的PTFE微孔薄膜最终覆合在滤料的表面。通过在滤料中植入活性催化剂的方式,达到在过滤烟尘的同时脱除烟气中氮氧化物和二噁英等有害物质的功效。具体步骤如下:The active catalyst V 2 O 5 -WO 3 /TiO 2 micropowder and PTFE resin are uniformly mixed together in a ratio of 10:90 to make PTFE fiber containing catalyst and PTFE microporous film containing catalyst; among them, the auxiliary agent The type and quality can be arbitrarily selected according to needs. The PTFE fiber containing the catalyst is mainly used to make woven filter cloth, and the PTFE microporous film containing the catalyst is finally coated on the surface of the filter material. By implanting an active catalyst in the filter material, it can achieve the effect of removing harmful substances such as nitrogen oxides and dioxins in the flue gas while filtering the flue dust. Specific steps are as follows:

一是将含有催化剂的PTFE纤维与高强PTFE纤维在织布前的整经工序,采用1:2交替布置的方式制成经轴,采用机织的方式织造成PTFE基布,得到PTFE基布层4;One is the warping process of PTFE fibers containing catalysts and high-strength PTFE fibers before weaving, using a 1:2 alternate arrangement to make warp beams, and weaving them into PTFE base fabrics by weaving to obtain PTFE base fabric layers 4;

二是将PPS纤维与含有催化剂的PTFE短纤维按30:70的比例混合后,与PTFE基布层一同进入针刺机,在PTFE基布层的两侧形成第一PPS+催化PTFE纤维强度层3和第二PPS+催化PTFE纤维强度层5,制成PPS复合针刺毡。The second is to mix the PPS fiber with the PTFE short fiber containing the catalyst in a ratio of 30:70, and then enter the needle punching machine together with the PTFE base cloth layer, and form the first PPS+catalyzed PTFE fiber strength layer on both sides of the PTFE base cloth layer3 And the second PPS+catalyzed PTFE fiber strength layer 5 to make PPS composite needle felt.

三是将固含量为45%的活性金属催化剂乳液与固含量为45%的PTFE乳液按有效成分的质量比为50:50制成催化剂混合处理液,对PPS复合针刺毡进行整体浸渍处理,经过310℃高温烧结后,在PPS复合针刺毡的上下表面形成第一催化剂混合处理液浸渍层2和第二催化剂混合处理液浸渍层6。The third is to make a catalyst mixed treatment solution with an active metal catalyst emulsion with a solid content of 45% and a PTFE emulsion with a solid content of 45% according to the mass ratio of active ingredients of 50:50, and perform overall impregnation treatment on the PPS composite needle felt, After sintering at a high temperature of 310°C, the first catalyst mixed treatment liquid impregnated layer 2 and the second catalyst mixed treatment liquid impregnated layer 6 are formed on the upper and lower surfaces of the PPS composite needle felt.

四是滤料整体浸渍处理后与含有催化剂的PTFE微孔薄膜同时引入热覆膜机中,表面进行热压覆膜加工,使含有催化剂的PTFE微孔薄膜1与基材牢固的结合在一起,最终制成PPS复合毡功能滤料。Fourth, after the overall impregnation treatment of the filter material, the PTFE microporous film containing the catalyst is simultaneously introduced into the hot-coating machine, and the surface is subjected to hot-press coating processing, so that the PTFE microporous film 1 containing the catalyst is firmly combined with the substrate, Finally, the PPS composite felt functional filter material is made.

脱硝和二噁英的PPS复合毡功能滤料整体分为六个层次:由迎尘面到净气面依次为含有催化剂的PTFE微孔薄膜层1,第一催化剂混合乳液浸渍处理层2,第一PPS+催化PTFE纤维强度层3,PTFE基布层4,第二PPS+催化PTFE纤维强度层5,第二催化剂混合乳液浸渍处理层6。The PPS composite felt functional filter material for denitrification and dioxin is divided into six layers as a whole: from the dust face to the clean air face, there are PTFE microporous film layer 1 containing catalyst, the first catalyst mixed emulsion impregnated layer 2, and the second A PPS+catalyzed PTFE fiber strength layer 3, a PTFE base cloth layer 4, a second PPS+catalyzed PTFE fiber strength layer 5, and a second catalyst mixed emulsion impregnated treatment layer 6.

脱硝和二噁英的PPS复合毡功能滤料,显著提高滤料的过滤精度,滤料由外到内(迎尘面到净气面)形成多层次的活性催化剂分布层,当高温烟气经过时,粉尘被阻隔在滤料的表面;含有有害物质的气体通过时,氮氧化物和二噁英等有害物质与活性催化剂发生反应,有害成份被分解为无害的物质与粉尘一并进行收集,从而实现烟气除尘和脱除有害物质的双重功效。The PPS composite felt functional filter material for denitrification and dioxin significantly improves the filtration accuracy of the filter material. The filter material forms a multi-layered active catalyst distribution layer from the outside to the inside (the dust-facing surface to the clean gas surface). When the high-temperature flue gas passes through When the dust is blocked on the surface of the filter material; when the gas containing harmful substances passes through, harmful substances such as nitrogen oxides and dioxins react with the active catalyst, and the harmful components are decomposed into harmless substances and collected together with the dust , so as to achieve the double effect of flue gas dust removal and removal of harmful substances.

脱硝和二噁英的PPS复合毡功能滤料PPS composite felt functional filter material for denitrification and dioxin

以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明披露的技术范围内,可轻易想到的变化或替换,都应该涵盖在本发明的保护范围之内。因此,本发明的保护范围应该以权利要求书的保护范围为准。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any person familiar with the technical field can easily conceive of changes or changes within the technical scope disclosed in the present invention. Replacement should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.

Claims (2)

1.一种脱硝和二噁英的PPS复合毡功能滤料的制备方法,其特征在于,包括以下步骤:1. a preparation method of the PPS composite felt functional filter material of denitrification and dioxin, is characterized in that, comprises the following steps: (1)将活性金属催化剂粉末混合与PTFE树脂混合后,分别制成含有催化剂的PTFE纤维和含有催化剂的PTFE微孔薄膜;(1) After the active metal catalyst powder is mixed with the PTFE resin, the PTFE fiber containing the catalyst and the PTFE microporous film containing the catalyst are made respectively; (2)将含有催化剂的PTFE纤维与高强PTFE纤维采用1-10:1-10交替布置的方式制成经轴,采用机织的方式织造制成PTFE基布层;(2) the PTFE fiber containing catalyst and the high-strength PTFE fiber adopt the mode of 1-10:1-10 to be arranged alternately to make warp beam, adopt the mode of weaving to weave and make PTFE base cloth layer; (3)将PPS纤维与含有催化剂的PTFE短纤维混合后与PTFE基布层一起放入针刺机,在PTFE基布层的两侧形成PPS+催化PTFE纤维强度层,制成PPS复合针刺毡;(3) PPS fibers are mixed with short PTFE fibers containing catalysts and put into the needle punching machine together with the PTFE base cloth layer to form PPS+catalyzed PTFE fiber strength layers on both sides of the PTFE base cloth layer to make PPS composite needle felt ; (4)将活性金属催化剂乳液与PTFE乳液混合制成催化剂混合处理液,对PPS复合针刺毡进行整体浸渍处理,之后在280-350℃进行烧结;(4) Mix the active metal catalyst emulsion with the PTFE emulsion to make a catalyst mixed treatment solution, and perform overall impregnation treatment on the PPS composite needle felt, and then sinter at 280-350°C; (5)将烧结后的PPS复合针刺毡与含有催化剂的PTFE微孔薄膜同时引入热覆膜机中,表面进行热压覆膜加工;所述步骤(1)中的活性金属催化剂选自V2O5、WO3、MoO3/TiO2中的一种或几种;所述步骤(1)中活性金属催化剂粉末、PTFE树脂粉末的质量比为1-10:99-90;所述步骤(3)中PPS纤维与含有催化剂的PTFE短纤维的比例为1-99:99-1;所述步骤(4)中活性金属催化剂乳液与PTFE乳液的有效成分的质量比为1-99:99-1;所述PTFE乳液的固含量为30~50%;所述活性金属催化剂乳液的有效成分为V2O5、WO3、MoO3/TiO2中的一种或几种;所述活性金属催化剂乳液的固含量为40~60%。(5) PPS composite needle-punched felt after sintering and the PTFE microporous film containing catalyst are simultaneously introduced in the hot coating machine, and the surface is subjected to hot pressing coating processing; the active metal catalyst in the step (1) is selected from V One or more of 2 O 5 , WO 3 , MoO 3 /TiO 2 ; the mass ratio of active metal catalyst powder and PTFE resin powder in the step (1) is 1-10:99-90; the step (3) the ratio of PPS fiber and the short PTFE fiber that contains catalyst is 1-99:99-1; The mass ratio of active metal catalyst emulsion and the active ingredient of PTFE emulsion is 1-99:99 in described step (4) -1; the solid content of the PTFE emulsion is 30-50%; the active ingredient of the active metal catalyst emulsion is one or more of V 2 O 5 , WO 3 , MoO 3 /TiO 2 ; the active The solid content of the metal catalyst emulsion is 40-60%. 2.根据权利要求1所述的方法制备的脱硝和二噁英的PPS复合毡功能滤料,其特征在于,依次包括含有催化剂的PTFE微孔薄膜层、第一催化剂混合处理液浸渍层、PPS复合针刺毡、第二催化剂混合处理液浸渍层;所述PPS复合针刺毡包括依次连接的第一PPS+催化PTFE纤维强度层、PTFE基布层、第二PPS+催化PTFE纤维强度层;所述含有催化剂的PTFE微孔薄膜层与第一催化剂混合处理液浸渍层之间通过热压覆合。2. the PPS composite felt functional filter material of the denitrification prepared by the method according to claim 1 and dioxin, is characterized in that, comprises successively the PTFE microporous film layer that contains catalyzer, the first catalyzer mixed treatment liquid impregnated layer, PPS Composite needle felt, the second catalyst mixed treatment liquid impregnation layer; the PPS composite needle felt includes the first PPS+catalyzed PTFE fiber strength layer, PTFE base cloth layer, the second PPS+catalyzed PTFE fiber strength layer connected in sequence; the The PTFE microporous film layer containing the catalyst and the impregnated layer of the first catalyst mixed treatment liquid are laminated by hot pressing.
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CN107261667A (en) * 2017-07-28 2017-10-20 江苏金由新材料有限公司 PTFE with high-temperature catalytic decomposition function is combined filter bag and preparation method thereof
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CN110465288A (en) * 2019-07-24 2019-11-19 南京工业大学 A kind of cooperation-removal nitrogen oxides and the composite filtering material of dioxin function and preparation method thereof
CN113041862A (en) * 2021-04-02 2021-06-29 上海洁晟环保科技有限公司 Composite membrane material, preparation method thereof, filtering membrane and storage device
CN113476959B (en) * 2021-06-28 2023-04-07 南京玻璃纤维研究设计院有限公司 A high temperature catalytic filter material
CN114130119B (en) * 2021-10-19 2023-10-03 安徽元琛环保科技股份有限公司 Preparation method and application of filter material with dust removal, denitration and dioxin removal functions
CN114432796A (en) * 2022-03-22 2022-05-06 安徽元琛环保科技股份有限公司 Silver phosphate carbon nitride composite photocatalytic filter material and preparation method thereof
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5620669A (en) * 1995-08-15 1997-04-15 W. L. Gore & Associates, Inc. Catalytic filter material and method of making same
CN1978717A (en) * 2006-11-30 2007-06-13 浙江理工大学 Method for preparing expanded polytetrafluoroethylene fiber for exhaust decomposition
CN101357279A (en) * 2008-06-26 2009-02-04 南京际华三五二一特种装备有限公司 Dust removal and dioxin decomposition integration filter material and preparation method thereof
CN102120116A (en) * 2011-02-24 2011-07-13 福州大学 Denitration catalyst-supported compound filter material and preparation method thereof
CN203874574U (en) * 2014-02-14 2014-10-15 营口市洪源玻纤科技有限公司 Glass fiber and PTFE fiber blended filter material

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10230119A (en) * 1996-11-25 1998-09-02 Abb Kk Bag filter and manufacturing method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5620669A (en) * 1995-08-15 1997-04-15 W. L. Gore & Associates, Inc. Catalytic filter material and method of making same
CN1978717A (en) * 2006-11-30 2007-06-13 浙江理工大学 Method for preparing expanded polytetrafluoroethylene fiber for exhaust decomposition
CN101357279A (en) * 2008-06-26 2009-02-04 南京际华三五二一特种装备有限公司 Dust removal and dioxin decomposition integration filter material and preparation method thereof
CN102120116A (en) * 2011-02-24 2011-07-13 福州大学 Denitration catalyst-supported compound filter material and preparation method thereof
CN203874574U (en) * 2014-02-14 2014-10-15 营口市洪源玻纤科技有限公司 Glass fiber and PTFE fiber blended filter material

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