CN112546854B - Selective thermal sintering molding 3D printing dioxin removal bag cage and preparation method thereof - Google Patents
Selective thermal sintering molding 3D printing dioxin removal bag cage and preparation method thereof Download PDFInfo
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- 238000010146 3D printing Methods 0.000 title claims abstract description 40
- 238000005245 sintering Methods 0.000 title claims abstract description 19
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 title claims abstract 13
- 238000000465 moulding Methods 0.000 title abstract description 6
- 239000000843 powder Substances 0.000 claims abstract description 67
- 239000000463 material Substances 0.000 claims abstract description 48
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims abstract description 24
- 239000004810 polytetrafluoroethylene Substances 0.000 claims abstract description 24
- 238000000498 ball milling Methods 0.000 claims abstract description 18
- 230000003197 catalytic effect Effects 0.000 claims abstract description 16
- -1 polytetrafluoroethylene Polymers 0.000 claims abstract description 16
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 14
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 claims abstract description 11
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000005543 nano-size silicon particle Substances 0.000 claims abstract description 9
- 238000002844 melting Methods 0.000 claims abstract description 6
- 230000008018 melting Effects 0.000 claims abstract description 6
- 238000001125 extrusion Methods 0.000 claims abstract 2
- 238000005469 granulation Methods 0.000 claims abstract 2
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- 235000012239 silicon dioxide Nutrition 0.000 claims abstract 2
- 238000007639 printing Methods 0.000 claims description 33
- 239000002245 particle Substances 0.000 claims description 22
- 239000003054 catalyst Substances 0.000 claims description 19
- 238000000034 method Methods 0.000 claims description 18
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 11
- 238000000227 grinding Methods 0.000 claims description 8
- 238000010128 melt processing Methods 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 7
- 239000002243 precursor Substances 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 3
- 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 description 3
- MEYVLGVRTYSQHI-UHFFFAOYSA-L cobalt(2+) sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Co+2].[O-]S([O-])(=O)=O MEYVLGVRTYSQHI-UHFFFAOYSA-L 0.000 claims description 3
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 3
- MIVBAHRSNUNMPP-UHFFFAOYSA-N manganese(2+);dinitrate Chemical compound [Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MIVBAHRSNUNMPP-UHFFFAOYSA-N 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims description 3
- 238000007142 ring opening reaction Methods 0.000 claims description 2
- 238000007493 shaping process Methods 0.000 claims 2
- 238000007873 sieving Methods 0.000 claims 1
- 238000012360 testing method Methods 0.000 abstract description 23
- 238000005516 engineering process Methods 0.000 abstract description 12
- 239000002994 raw material Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract 1
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 42
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 21
- 239000003546 flue gas Substances 0.000 description 21
- 230000035699 permeability Effects 0.000 description 16
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- 238000007254 oxidation reaction Methods 0.000 description 7
- 239000000758 substrate Substances 0.000 description 7
- 150000002013 dioxins Chemical class 0.000 description 5
- 238000004056 waste incineration Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
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- 239000011148 porous material Substances 0.000 description 2
- 238000003892 spreading Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000007943 implant Substances 0.000 description 1
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- 238000010248 power generation Methods 0.000 description 1
- MCJGNVYPOGVAJF-UHFFFAOYSA-N quinolin-8-ol Chemical compound C1=CN=C2C(O)=CC=CC2=C1 MCJGNVYPOGVAJF-UHFFFAOYSA-N 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
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- 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
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- B01D53/8659—Removing halogens or halogen compounds
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- 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
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Abstract
Description
技术领域technical field
本发明属于垃圾焚烧烟气净化技术领域,具体涉及一种选择性热烧结成型3D打印脱二噁英袋笼及其制备方法。The invention belongs to the technical field of waste incineration flue gas purification, and in particular relates to a selective thermal sintering forming 3D printing dioxin-free bag cage and a preparation method thereof.
背景技术Background technique
垃圾焚烧发电是解决垃圾围城的一种重要方式,其中垃圾焚烧烟气的净化是近年来研究的重点,而烟气脱二噁英又是垃圾焚烧烟气净化的重中之重。滤袋脱二噁英是一种新型的烟气脱二噁英技术,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二噁英。目前只有美国戈尔公司具有成熟应用的催化滤袋产品(US005620669),该技术在国外垃圾焚烧烟气治理上获得了成功应用,但其价格昂贵,研制难度颇大。目前,国内脱二噁英滤袋的制备方法主要是浸渍法(CN110465288A,CN110898829A)。上述方法虽然可以制备脱二噁英滤料,但通常存在脱二噁英活性组分分散性较差,催化剂与滤袋纤维结合强度较弱,导致滤袋脱二噁英效率较低,使用寿命较短,这极大限制了其工程应用。Waste incineration power generation is an important way to solve the siege of waste. Among them, the purification of waste incineration flue gas is the focus of research in recent years, and the removal of dioxins from flue gas is the top priority of waste incineration flue gas purification. Filter bag dioxin removal is a new flue gas dioxin removal technology. With the help of a filter bag with catalytic function, the bag type dust removal process is used to achieve flue gas dioxin removal at low temperature. At present, only U.S. Gore Company has a mature and applied catalytic filter bag product (US005620669). This technology has been successfully applied in foreign waste incineration flue gas treatment, but it is expensive and difficult to develop. At present, the preparation method of the domestic de-dioxin filter bag is mainly the dipping method (CN110465288A, CN110898829A). Although the above method can prepare the dioxin-removing filter material, there are usually poor dispersibility of the dioxin-removing active components, and the combination strength of the catalyst and the filter bag fiber is weak, resulting in a low efficiency of the filter bag to remove dioxins and a long service life. Short, which greatly limits its engineering applications.
发明内容Contents of the invention
本发明的目的在于克服上述现有技术的缺点,提供了一种脱二噁英袋笼的制备方法,跳出滤袋脱除二噁英的框架,转变思路,采用3D打印技术将催化剂负载于滤袋袋笼上,制备出具有脱二噁英功能的脱二噁英除尘一体化袋笼。The purpose of the present invention is to overcome the above-mentioned shortcomings of the prior art, and provide a method for preparing a dioxin-removing bag cage, jumping out of the framework of filter bag removal of dioxins, changing the thinking, and using 3D printing technology to load the catalyst on the filter. On the bag cage, a dioxin-removing and dust-removing integrated bag cage with a dioxin-removing function was prepared.
为实现上述目的,本发明采取如下技术方案:一种选择性热烧结成型3D打印脱二噁英袋笼的制备方法,包括以下步骤:In order to achieve the above purpose, the present invention adopts the following technical scheme: a method for preparing a selective thermal sintering molding 3D printing de-dioxin bag cage, comprising the following steps:
(1)按重量计,将55~80份脱二噁英催化剂粉末、15~35份聚四氟乙烯粉末、1~8份单烷氧基型钛酸酯以及4~12份纳米二氧化硅混合后,进行球磨,然后经过熔融处理得到物料A,然后在该物料A中加入0.2~4份邻苯二甲酸二辛酯,搅拌后挤出造粒,得到用于3D打印的打印材料;(1) By weight, 55-80 parts of dioxin-removing catalyst powder, 15-35 parts of polytetrafluoroethylene powder, 1-8 parts of monoalkoxy titanate and 4-12 parts of nano-silica After mixing, carry out ball milling, and then undergo melting treatment to obtain material A, then add 0.2 to 4 parts of dioctyl phthalate to the material A, and then extrude and granulate after stirring to obtain printing materials for 3D printing;
(2)创建脱二噁英袋笼三维模型,脱二噁英袋笼主体为一个设置有微孔的直筒,直筒底部也设置微孔,设置微孔直径和微孔间距;(2) Create a three-dimensional model of the dioxin-removing bag cage. The main body of the dioxin-removing bag cage is a straight cylinder with micropores, and the bottom of the straight cylinder is also provided with micropores, and the diameter of the micropores and the distance between the micropores are set;
(3)对步骤(2)创建的脱二噁英袋笼三维模型进行切片处理,设置层高和壁厚,得到可执行打印的二噁英袋笼三维模型;(3) slice the dioxin-free cage three-dimensional model created in step (2), set the layer height and wall thickness, and obtain a three-dimensional model of the dioxin cage that can be printed;
(4)3D打印采用选择性热烧结方法,首先将制备好的粉体通过铺粉辊均匀铺设操作台,同时操作台进行预热,然后设置打印头移动速度和功率,基于步骤(3)所得可执行打印的二噁英袋笼三维模型进行3D打印;(4) 3D printing adopts the selective thermal sintering method. Firstly, the prepared powder is evenly spread on the operating table by the powder spreading roller, and the operating table is preheated at the same time, and then the moving speed and power of the printing head are set. The 3D model of the dioxin bag cage that can be printed is 3D printed;
(5)打印结束后进行冷却定型,冷却定型后将未烧结的粉体剔除,最终得到脱二噁英袋笼。(5) After the printing is finished, it is cooled and shaped, and the unsintered powder is removed after cooling and shaped, and finally the dioxin-free bag cage is obtained.
所述步骤(1)将硝酸锰、六水合硝酸铈和七水合硫酸钴按质量比1.5:2.1:1加入去离子水中,搅拌形成溶液,向溶液中滴加氨水控制pH值为8.2直至沉淀完成,依次过滤和烘干后得到前驱体粉末,然后将前驱体粉末在400℃的空气中焙烧4小时,再研磨后过筛制成1200目的颗粒,得到脱二噁英粉催化粉体。In the step (1), add manganese nitrate, cerium nitrate hexahydrate and cobalt sulfate heptahydrate into deionized water in a mass ratio of 1.5:2.1:1, stir to form a solution, add ammonia water dropwise to the solution to control the pH value to 8.2 until the precipitation is completed , followed by filtration and drying to obtain the precursor powder, and then the precursor powder was roasted in the air at 400°C for 4 hours, and then ground and sieved to make 1200 mesh particles to obtain the dedioxin powder catalytic powder.
所述步骤(1)中聚四氟乙烯粉末粒径为500nm~50μm。The particle size of the polytetrafluoroethylene powder in the step (1) is 500nm-50μm.
所述步骤(1)中3D打印材料粒径为25~100μm。The particle size of the 3D printing material in the step (1) is 25-100 μm.
所述步骤(1)中熔融温度为380~400℃。The melting temperature in the step (1) is 380-400°C.
所述步骤(2)脱二噁英袋笼三维模型中的微孔直径为2~10mm,微孔间距为4~15mm。The diameter of micropores in the three-dimensional model of the dioxin-removing bag cage in the step (2) is 2-10 mm, and the distance between micropores is 4-15 mm.
所述步骤(3)中层高0.2~1mm、壁厚0.1~0.3mm,微孔直径为2~10mm,微孔间距为4~15mm。In the step (3), the height of the middle layer is 0.2-1 mm, the wall thickness is 0.1-0.3 mm, the diameter of the pores is 2-10 mm, and the distance between the pores is 4-15 mm.
所述步骤(4)中打印头移动速度为1000-4000mm/min,功率为5~30W。In the step (4), the moving speed of the printing head is 1000-4000mm/min, and the power is 5-30W.
一种脱二噁英袋笼,基于本发明所述方法制备,主体为一个设置有微孔的直筒,直筒底部为笼底,笼底上设置有微孔,微孔直径为2~10mm,微孔间距为4~15mm。A dioxin-removing bag cage, prepared based on the method of the present invention, the main body is a straight cylinder with micropores, the bottom of the straight cylinder is the bottom of the cage, and micropores are arranged on the bottom of the cage, the diameter of the micropores is 2-10mm, The hole spacing is 4-15mm.
直筒的顶端设有翻边式上圈口。The top of the straight cylinder is provided with a flanging type upper ring opening.
与现有技术相比,本发明具有如下有益的技术效果:Compared with the prior art, the present invention has the following beneficial technical effects:
(1)本发明使脱二噁英滤袋和袋笼的功能巧妙地共存为一个主体中,催化剂能够很好的附着在袋笼中,并充分发挥催化效能,本发明所制备的袋笼对滤袋的支撑更加充分且均匀,进一步降低了滤袋表面的受力,能有效延长滤袋的寿命;同时袋笼上布满数量可观的微孔,经测试,常规滤袋加本申请脱二噁英袋笼组合与脱二噁英滤袋加常规袋笼组合相比阻力更小;(1) The present invention makes the functions of the dioxin-removing filter bag and the bag cage cleverly coexist in one main body, the catalyst can be well attached in the bag cage, and fully exerts the catalytic performance. The support of the filter bag is more sufficient and uniform, which further reduces the force on the surface of the filter bag and can effectively prolong the life of the filter bag; at the same time, the bag cage is covered with a considerable number of micropores. Compared with the combination of dioxin removal filter bag and conventional bag cage, the resistance of the oxin bag cage combination is smaller;
(2)本发明所述袋笼是将脱二噁英催化剂通过原料共混植入脱二噁英袋笼中,使得催化剂在袋笼上的负载量大,催化剂在袋笼中分布更加均匀,极大地提高脱二噁英的效率。(2) The bag cage of the present invention is to implant the catalyst for removing dioxin into the bag cage for removing dioxin through raw material blending, so that the loading capacity of the catalyst on the bag cage is large, and the catalyst is more evenly distributed in the bag cage. Greatly improve the efficiency of removing dioxins.
(3)本发明所述原料中,聚四氟乙烯对具有很好的粘连作用,而且在成型后能够对袋笼能起到很好的主体支撑作用,同时利用聚四氟乙烯的良好的疏水性避免催化剂粉末过多接触水而催化性能降低;单烷氧基型钛酸酯能提高袋笼的抗氧化性能,有助于延长催化剂的寿命,另外,也能提高脱二噁英催化剂粉末、聚四氟乙烯粉末以及纳米二氧化硅之间的结合强度,而纳米二氧化硅对袋笼具有很好的增强作用;(3) Among the raw materials of the present invention, polytetrafluoroethylene has good adhesion to the pair, and can play a good main body support effect on the bag cage after molding, while utilizing the good hydrophobicity of polytetrafluoroethylene It can prevent the catalytic performance of the catalyst powder from excessive contact with water and reduce the catalytic performance; the monoalkoxy titanate can improve the oxidation resistance of the bag cage and help to prolong the life of the catalyst. In addition, it can also improve the catalyst powder, The bonding strength between PTFE powder and nano-silica, and nano-silica has a good reinforcing effect on the bag cage;
(4)本发明采用选择性热烧结3D打印方法制备出脱二噁英袋笼,袋笼中具有至关重要作用的微孔尺寸可以根据需求进行设定,而且几乎不存在制备难度,能够充分发挥结构优化设计的极限,兼顾气体阻力与脱除效率。(4) The present invention adopts the selective thermal sintering 3D printing method to prepare the dioxin-free bag cage. The size of micropores in the bag cage can be set according to the requirements, and there is almost no difficulty in preparation, which can fully Play the limit of structural optimization design, taking into account gas resistance and removal efficiency.
本发明所制备的袋笼将功能和结构有机结合在一个主体中,即采用本发明所述袋笼结合普通滤袋就能进行二噁英脱除,本发明所制备的袋笼对滤袋的支撑更加充分且均匀,进一步降低了滤袋表面的受力,能有效延长滤袋的寿命;袋笼上布满数量可观的微孔,经测试,常规滤袋加本申请脱二噁英袋笼组合与脱二噁英滤袋加常规袋笼组合相比阻力更小。The bag cage prepared by the present invention organically combines functions and structures in one main body, that is, the dioxin can be removed by using the bag cage according to the present invention in combination with a common filter bag, and the bag cage prepared by the present invention has a significant effect on the filter bag. The support is more sufficient and uniform, which further reduces the force on the surface of the filter bag and can effectively prolong the life of the filter bag; the bag cage is covered with a considerable number of micropores. After testing, the conventional filter bag plus the application of the dioxin removal bag cage Compared with the combination of de-dioxin filter bag and conventional bag cage, the combination has lower resistance.
附图说明Description of drawings
图1为一种可实施的脱二噁英袋笼模型示意图。Fig. 1 is a schematic diagram of an implementable dioxin removal bag cage model.
图2为一种脱二噁英袋笼俯视示意图。Fig. 2 is a top view schematic diagram of a dioxin-removing bag cage.
图3为一种脱二噁英袋笼侧视示意图。Fig. 3 is a schematic side view of a bag cage for removing dioxins.
图中:1上圈口,2微孔,3微孔间距,4笼底。In the figure: 1 upper ring mouth, 2 microholes, 3 microhole spacing, 4 cage bottom.
具体实施方式Detailed ways
下面结合实施例对本发明进行详细阐述。The present invention will be described in detail below in conjunction with the examples.
参考图1、图2和图3,一种选择性热烧结成型3D打印脱二噁英袋笼及其制备方法,包括以下步骤:Referring to Figure 1, Figure 2 and Figure 3, a selective thermal sintering molding 3D printing de-dioxin bag cage and its preparation method include the following steps:
(1)按重量计,将55~80份脱二噁英催化剂粉末、15~35份聚四氟乙烯粉末、1~8份单烷氧基型钛酸酯以及4~12份纳米二氧化硅混合后,进行球磨,然后经过熔融处理得到物料A,然后在该物料A中加入0.2~4份邻苯二甲酸二辛酯,搅拌后挤出造粒,得到用于3D打印的打印材料;(1) By weight, 55-80 parts of dioxin-removing catalyst powder, 15-35 parts of polytetrafluoroethylene powder, 1-8 parts of monoalkoxy titanate and 4-12 parts of nano-silica After mixing, carry out ball milling, and then undergo melting treatment to obtain material A, then add 0.2 to 4 parts of dioctyl phthalate to the material A, and then extrude and granulate after stirring to obtain printing materials for 3D printing;
(2)创建脱二噁英袋笼三维模型,脱二噁英袋笼主体为一个设置有微孔2的直筒,设置微孔直径和微孔间距;(2) Create a three-dimensional model of the dioxin-removing bag cage. The main body of the dioxin-removing bag cage is a straight tube provided with
(3)对步骤(2)创建的脱二噁英袋笼三维模型进行切片处理,设置层高和壁厚,得到可执行打印的二噁英袋笼三维模型;(3) slice the dioxin-free cage three-dimensional model created in step (2), set the layer height and wall thickness, and obtain a three-dimensional model of the dioxin cage that can be printed;
(4)3D打印采用选择性热烧结方法,首先将制备好的粉体通过铺粉辊均匀铺设操作台,同时操作台进行预热,然后设置打印头移动速度和功率,基于步骤(3)所得可执行打印的二噁英袋笼三维模型进行3D打印;(4) 3D printing adopts the selective thermal sintering method. Firstly, the prepared powder is evenly spread on the operating table by the powder spreading roller, and the operating table is preheated at the same time, and then the moving speed and power of the printing head are set. The 3D model of the dioxin bag cage that can be printed is 3D printed;
(5)打印结束后进行冷却定型,冷却定型后将未烧结的粉体剔除,最终得到脱二噁英袋笼。(5) After the printing is finished, it is cooled and shaped, and the unsintered powder is removed after cooling and shaped, and finally the dioxin-free bag cage is obtained.
所述步骤(1)将硝酸锰、六水合硝酸铈和七水合硫酸钴按质量比1.5:2.1:1加入去离子水中,搅拌形成溶液,向溶液中滴加氨水控制pH值为8.2直至沉淀完成,依次过滤和烘干后得到前驱体粉末,然后将前驱体粉末在400℃的空气中焙烧4小时,再研磨后过筛制成1200目的颗粒,得到脱二噁英粉催化粉体。In the step (1), add manganese nitrate, cerium nitrate hexahydrate and cobalt sulfate heptahydrate into deionized water in a mass ratio of 1.5:2.1:1, stir to form a solution, add ammonia water dropwise to the solution to control the pH value to 8.2 until the precipitation is completed , followed by filtration and drying to obtain the precursor powder, and then the precursor powder was roasted in the air at 400°C for 4 hours, and then ground and sieved to make 1200 mesh particles to obtain the dedioxin powder catalytic powder.
步骤(1)中聚四氟乙烯粉末粒径为500nm~50μm;步骤(1)中3D打印材料粒径为25~100μm;所述步骤(1)中熔融温度为380~400℃;The particle size of the polytetrafluoroethylene powder in the step (1) is 500nm-50 μm; the particle size of the 3D printing material in the step (1) is 25-100 μm; the melting temperature in the step (1) is 380-400°C;
步骤(2)脱二噁英袋笼三维模型中的微孔直径为2~10mm,微孔间距为4~15mm;Step (2) The micropore diameter in the dioxin-removing bag cage three-dimensional model is 2-10mm, and the micropore spacing is 4-15mm;
步骤(3)中层高0.2~1mm、壁厚0.1~0.3mm,微孔直径为2~10mm,微孔间距为4~15mm。In step (3), the height of the middle layer is 0.2-1mm, the wall thickness is 0.1-0.3mm, the diameter of the micropores is 2-10mm, and the distance between the micropores is 4-15mm.
步骤(4)中打印头移动速度为1000-4000mm/min,功率为5~30W。In step (4), the moving speed of the printing head is 1000-4000mm/min, and the power is 5-30W.
一种脱二噁英袋笼,基于本发明所述方法制备,主体为一个设置有微孔2的直筒,直筒底部为笼底4,笼底4上设置有微孔2,微孔直径为2~10mm,微孔间距3为4~15mm;直筒的顶部设有翻边式上圈口1。A dioxin-removing bag cage, prepared based on the method of the present invention, the main body is a straight cylinder provided with
需要说明的是,本发明所述微孔不一定是规则的圆形,微孔直径为该微孔的所有径向距离的平均值。It should be noted that the micropores in the present invention are not necessarily regular circles, and the diameter of the micropores is the average value of all radial distances of the micropores.
遵从所述总体方案,进行如下几种实施:Comply with described general plan, carry out following several implementations:
实施例1Example 1
将7.2kg脱二噁英催化剂粉末、3.1kg聚四氟乙烯粉末、0.4kg单烷氧基型钛酸酯、0.6kg纳米二氧化硅混合后,置于行星式球磨机上进行球磨,球磨机转速220r/min,每20min为一个回合,研磨5个回合,即球磨时间为100min。然后在380℃下熔融处理得到物料A,然后在该物料A中加入0.058kg邻苯二甲酸二辛酯,搅拌后获得物料B,然后通过造粒机挤出平均粒径为5μm的粉粒,得到可供3D打印设备使用的打印材料;使用Solidworks软件创建上创建袋笼3维模型,基体尺寸为:上圈口直径145mm、厚度5mm,底部直径110mm,袋笼长度970mm,微孔直径3mm,微孔间距5mm。使用Simplify 3D软件对创建后的脱二噁英袋笼三维模型进行切片处理,设置层高0.2mm、壁厚0.1mm;3D打印采用选择性热烧结技术,首先将制备好的粉体通过铺粉辊均匀铺设操作台,同时操作台预热至260℃,然后设置打印头移动速度为2000mm/min和功率为30W后,按照建模来进行3D打印;打印结束后在100℃下进行定型,冷却后将未烧结的多余粉体剔除,最终得到脱二噁英袋笼。After mixing 7.2kg of dioxin-removing catalyst powder, 3.1kg of polytetrafluoroethylene powder, 0.4kg of monoalkoxy titanate, and 0.6kg of nano-silicon dioxide, they are placed on a planetary ball mill for ball milling at a speed of 220r /min, every 20min is a round, and there are 5 rounds of grinding, that is, the ball milling time is 100min. Then melt processing at 380° C. to obtain material A, then add 0.058 kg of dioctyl phthalate to the material A, stir to obtain material B, and then extrude powder particles with an average particle size of 5 μm through a granulator, Obtain printing materials that can be used by 3D printing equipment; use Solidworks software to create a 3D model of the bag cage. The size of the substrate is: the diameter of the upper ring is 145mm, the thickness is 5mm, the diameter of the bottom is 110mm, the length of the bag cage is 970mm, and the diameter of the micropore is 3mm. Microhole spacing 5mm. Use Simplify 3D software to slice the created dioxin-free bag cage 3D model, set the layer height to 0.2mm, and the wall thickness to 0.1mm; 3D printing adopts selective thermal sintering technology, firstly, the prepared powder is passed through powder coating The rollers are evenly laid on the operation table, and the operation table is preheated to 260°C at the same time, and then the printing head moving speed is set to 2000mm/min and the power is 30W, and the 3D printing is carried out according to the modeling; after the printing is completed, it is shaped at 100°C and cooled Finally, the unsintered excess powder is removed, and finally the de-dioxin bag cage is obtained.
将所得脱二噁英袋笼在SCR脱二噁英试验台上利用模拟烟气进行脱二噁英性能评价。收集反应器进出口烟气并进行二噁英浓度分析,计算二噁英脱除效率为90.5%。The obtained dioxin removal bag cage was evaluated on the SCR dioxin removal test bench using simulated flue gas to evaluate the dioxin removal performance. The flue gas at the inlet and outlet of the reactor was collected and analyzed for dioxin concentration, and the calculated dioxin removal efficiency was 90.5%.
按照GB/T 5453-1997测试标准,对常规PTFE滤袋+脱二噁英袋笼组合在压差200Pa下进行透气率测试,透气率为7.7m3/m2/min。According to the GB/T 5453-1997 test standard, the air permeability test was performed on the combination of conventional PTFE filter bag + dioxin-free bag cage under a pressure difference of 200Pa, and the air permeability was 7.7m 3 /m 2 /min.
实施例2Example 2
将9.9kg脱二噁英催化剂粉末、3.2kg聚四氟乙烯粉末、0.5kg单烷氧基型钛酸酯、0.75kg纳米二氧化硅混合后,置于行星式球磨机上进行球磨,球磨机转速220r/min,每20min为一个回合,研磨5个回合,即球磨时间为100min。然后在380℃下熔融处理得到物料A,然后在该物料A中加入0.075kg邻苯二甲酸二辛酯,搅拌后获得物料B,然后通过造粒机挤出平均粒径为25μm的粉粒,得到可供3D打印设备使用的打印材料;使用Solidworks软件创建上创建袋笼3维模型,基体尺寸为:上圈口直径145mm、厚度5mm,底部直径110mm,袋笼长度970mm,微孔直径2mm,微孔间距5mm。使用Simplify 3D软件对创建后的脱二噁英袋笼三维模型进行切片处理,设置层高0.2mm、壁厚0.1mm;3D打印采用选择性热烧结技术,首先将制备好的粉体通过铺粉辊均匀铺设操作台,同时操作台预热至260℃,然后设置打印头移动速度为2500mm/min和功率为30W后,按照建模来进行3D打印;打印结束后在100℃下进行定型,冷却后将未烧结的多余粉体剔除,最终得到脱二噁英袋笼。After mixing 9.9kg of dioxin-removing catalyst powder, 3.2kg of polytetrafluoroethylene powder, 0.5kg of monoalkoxy titanate, and 0.75kg of nano-silicon dioxide, they are placed on a planetary ball mill for ball milling at a speed of 220r /min, every 20min is a round, and there are 5 rounds of grinding, that is, the ball milling time is 100min. Then melt processing at 380°C to obtain material A, then add 0.075kg dioctyl phthalate to material A, obtain material B after stirring, and then extrude powder particles with an average particle size of 25 μm through a granulator, Obtain printing materials that can be used by 3D printing equipment; use Solidworks software to create a 3D model of the bag cage. The size of the substrate is: the diameter of the upper ring is 145mm, the thickness is 5mm, the diameter of the bottom is 110mm, the length of the bag cage is 970mm, and the diameter of the micropore is 2mm. Microhole spacing 5mm. Use Simplify 3D software to slice the created dioxin-free bag cage 3D model, set the layer height to 0.2mm, and the wall thickness to 0.1mm; 3D printing adopts selective thermal sintering technology, firstly, the prepared powder is passed through powder coating The rollers are evenly laid on the operation table, and the operation table is preheated to 260°C at the same time, and then the printing head moving speed is set to 2500mm/min and the power is 30W, and the 3D printing is carried out according to the modeling; after the printing is completed, it is shaped at 100°C and cooled Finally, the unsintered excess powder is removed, and finally the de-dioxin bag cage is obtained.
将所得催化氧化滤料在SCR脱二噁英试验台上利用模拟烟气进行脱二噁英性能评价。。收集反应器进出口烟气并进行二噁英浓度分析,计算二噁英脱除效率为95%。The obtained catalytic oxidation filter material was used to evaluate the performance of dioxin removal on the SCR dioxin removal test bench using simulated flue gas. . The flue gas at the inlet and outlet of the reactor was collected and analyzed for dioxin concentration, and the removal efficiency of dioxin was calculated to be 95%.
按照GB/T 5453-1997测试标准,对常规PTFE滤袋+脱二噁英袋笼组合在压差200Pa下进行透气率测试,透气率为8.2m3/m2/min。According to the GB/T 5453-1997 test standard, the air permeability test was carried out on the combination of conventional PTFE filter bag + dioxin-free bag cage under a pressure difference of 200Pa, and the air permeability was 8.2m 3 /m 2 /min.
实施例3Example 3
将9.9kg脱二噁英催化剂粉末、3.2kg聚四氟乙烯粉末、0.5kg单烷氧基型钛酸酯、0.75kg纳米二氧化硅混合后置于行星式球磨机上进行球磨,球磨机转速250r/min,每20min为一个回合,研磨6个回合,即球磨时间为120min。然后在400℃下熔融处理得到物料A,然后在该物料A中加入0.075kg邻苯二甲酸二辛酯,搅拌后获得物料B,然后通过造粒机挤出平均粒径为30μm的粉粒,得到可供3D打印设备使用的打印材料;使用Solidworks软件创建上创建袋笼3维模型,基体尺寸为:上圈口直径145mm、厚度5mm,底部直径110mm,袋笼长度970mm,微孔直径5mm,微孔间距5mm。使用Simplify 3D软件对创建后的脱二噁英袋笼三维模型进行切片处理,设置层高0.2mm、壁厚0.3mm;3D打印采用选择性热烧结技术,首先将制备好的粉体通过铺粉辊均匀铺设操作台,同时操作台预热至260℃,然后设置打印头移动速度为1800mm/min和功率为25W后,按照建模来进行3D打印;打印结束后在100℃下进行定型,冷却后将未烧结的多余粉体剔除,最终得到脱二噁英袋笼。Mix 9.9kg of dioxin-removing catalyst powder, 3.2kg of polytetrafluoroethylene powder, 0.5kg of monoalkoxy titanate, and 0.75kg of nano-silicon dioxide and place them on a planetary ball mill for ball milling. The speed of the ball mill is 250r/ min, every 20min is a round, and there are 6 rounds of grinding, that is, the ball milling time is 120min. Then melt processing at 400°C to obtain material A, then add 0.075kg of dioctyl phthalate to the material A, stir to obtain material B, and then extrude powder particles with an average particle size of 30 μm through a granulator, Obtain printing materials that can be used by 3D printing equipment; use Solidworks software to create a 3D model of the bag cage. The size of the substrate is: the diameter of the upper ring is 145mm, the thickness is 5mm, the diameter of the bottom is 110mm, the length of the bag cage is 970mm, and the diameter of the micropore is 5mm. Microhole spacing 5mm. Use Simplify 3D software to slice the created dioxin-free bag cage 3D model, set the layer height to 0.2mm, and the wall thickness to 0.3mm; 3D printing adopts selective thermal sintering technology. The rollers are evenly laid on the operation table, and the operation table is preheated to 260°C at the same time, and then the printing head moving speed is set to 1800mm/min and the power is 25W, and the 3D printing is carried out according to the modeling; after the printing is completed, it is shaped at 100°C and cooled Finally, the unsintered excess powder is removed, and finally the de-dioxin bag cage is obtained.
将所得催化氧化滤料在SCR脱二噁英试验台上利用模拟烟气进行脱二噁英性能评价。。收集反应器进出口烟气并进行二噁英浓度分析,计算二噁英脱除效率为97%。The obtained catalytic oxidation filter material was used to evaluate the performance of dioxin removal on the SCR dioxin removal test bench using simulated flue gas. . The flue gas at the inlet and outlet of the reactor was collected and analyzed for dioxin concentration, and the calculated dioxin removal efficiency was 97%.
按照GB/T 5453-1997测试标准,对常规PTFE滤袋+脱二噁英袋笼组合在压差200Pa下进行透气率测试,透气率为8.3m3/m2/min。According to the GB/T 5453-1997 test standard, the air permeability test was carried out on the combination of conventional PTFE filter bag + dioxin-free bag cage under a pressure difference of 200Pa, and the air permeability was 8.3m 3 /m 2 /min.
实施例4Example 4
将9.9kg脱二噁英催化剂粉末、3.2kg聚四氟乙烯粉末、0.5kg单烷氧基型钛酸酯、0.75kg纳米二氧化硅混合后置于行星式球磨机上进行球磨,球磨机转速250r/min,每20min为一个回合,研磨6个回合,即球磨时间为120min。然后在400℃下熔融处理得到物料A,然后在该物料A中加入0.075kg邻苯二甲酸二辛酯,搅拌后获得物料B,然后通过造粒机挤出平均粒径为40μm的粉粒,得到可供3D打印设备使用的打印材料;使用Solidworks软件创建上创建袋笼3维模型,基体尺寸为:上圈口直径145mm、厚度5mm,底部直径110mm,袋笼长度970mm,微孔直径10mm,微孔间距15mm。使用Simplify 3D软件对创建后的脱二噁英袋笼三维模型进行切片处理,设置层高0.6mm、壁厚0.3mm;3D打印采用选择性热烧结技术,首先将制备好的粉体通过铺粉辊均匀铺设操作台,同时操作台预热至260℃,然后设置打印头移动速度为1800mm/min和功率为20W后,按照建模来进行3D打印;打印结束后在100℃下进行定型,冷却后将未烧结的多余粉体剔除,最终得到脱二噁英袋笼。Mix 9.9kg of dioxin-removing catalyst powder, 3.2kg of polytetrafluoroethylene powder, 0.5kg of monoalkoxy titanate, and 0.75kg of nano-silicon dioxide and place them on a planetary ball mill for ball milling. The speed of the ball mill is 250r/ min, every 20min is a round, and there are 6 rounds of grinding, that is, the ball milling time is 120min. Then melt processing at 400°C to obtain material A, then add 0.075kg dioctyl phthalate to material A, obtain material B after stirring, and then extrude powder particles with an average particle size of 40 μm through a granulator, Obtain printing materials that can be used by 3D printing equipment; use Solidworks software to create a 3D model of the bag cage. The size of the substrate is: the diameter of the upper ring is 145mm, the thickness is 5mm, the diameter of the bottom is 110mm, the length of the bag cage is 970mm, and the diameter of the micropore is 10mm. Microhole spacing 15mm. Use Simplify 3D software to slice the created dioxin-free bag cage 3D model, set the layer height to 0.6mm, and the wall thickness to 0.3mm; 3D printing adopts selective thermal sintering technology. The rollers are evenly laid on the operation table, and the operation table is preheated to 260°C at the same time, and then the printing head moving speed is set to 1800mm/min and the power is 20W, and the 3D printing is carried out according to the modeling; after the printing is completed, it is shaped at 100°C and cooled Finally, the unsintered excess powder is removed, and finally the de-dioxin bag cage is obtained.
将所得催化氧化滤料在SCR脱二噁英试验台上利用模拟烟气进行脱二噁英性能评价。。收集反应器进出口烟气并进行二噁英浓度分析,计算二噁英脱除效率为92%。The obtained catalytic oxidation filter material was used to evaluate the performance of dioxin removal on the SCR dioxin removal test bench using simulated flue gas. . The flue gas at the inlet and outlet of the reactor was collected and analyzed for dioxin concentration, and the calculated dioxin removal efficiency was 92%.
按照GB/T 5453-1997测试标准,对常规PTFE滤袋+脱二噁英袋笼组合在压差200Pa下进行透气率测试,透气率为10.1m3/m2/min。According to the GB/T 5453-1997 test standard, the air permeability test was carried out on the combination of conventional PTFE filter bag + dioxin-free bag cage under a pressure difference of 200Pa, and the air permeability was 10.1m 3 /m 2 /min.
实施例5Example 5
将9.2kg脱二噁英催化剂粉末、3.8kg聚四氟乙烯粉末、0.45kg单烷氧基型钛酸酯、0.65kg纳米二氧化硅混合后置于行星式球磨机上进行球磨,球磨机转速250r/min,每20min为一个回合,研磨6个回合,即球磨时间为120min。然后在380℃下熔融处理得到物料A,然后在该物料A中加入0.055kg邻苯二甲酸二辛酯,搅拌后获得物料B,然后通过造粒机挤出平均粒径为60μm的粉粒,得到可供3D打印设备使用的打印材料;使用Solidworks软件创建上创建袋笼3维模型,基体尺寸为:上圈口直径145mm、厚度5mm,底部直径110mm,袋笼长度970mm,微孔直径10mm,微孔间距15mm。使用Simplify 3D软件对创建后的脱二噁英袋笼三维模型进行切片处理,设置层高0.8mm、壁厚0.3mm;3D打印采用选择性热烧结技术,首先将制备好的粉体通过铺粉辊均匀铺设操作台,时操作台预热至260℃,然后设置打印头移动速度为1500mm/min和功率为10W后,按照建模来进行3D打印;打印结束后在100℃下进行定型,冷却后将未烧结的多余粉体剔除,最终得到脱二噁英袋笼。Mix 9.2kg of dioxin-removing catalyst powder, 3.8kg of polytetrafluoroethylene powder, 0.45kg of monoalkoxy titanate, and 0.65kg of nano-silicon dioxide and place them on a planetary ball mill for ball milling. The speed of the ball mill is 250r/ min, every 20min is a round, and there are 6 rounds of grinding, that is, the ball milling time is 120min. Then melt processing at 380°C to obtain material A, then add 0.055 kg of dioctyl phthalate to the material A, stir to obtain material B, and then extrude powder particles with an average particle size of 60 μm through a granulator, Obtain printing materials that can be used by 3D printing equipment; use Solidworks software to create a 3D model of the bag cage. The size of the substrate is: the diameter of the upper ring is 145mm, the thickness is 5mm, the diameter of the bottom is 110mm, the length of the bag cage is 970mm, and the diameter of the micropore is 10mm. Microhole spacing 15mm. Use Simplify 3D software to slice the created dioxin-free bag cage 3D model, set the layer height to 0.8mm, and the wall thickness to 0.3mm; 3D printing adopts selective thermal sintering technology. Spread the rollers evenly on the operating table, preheat the operating table to 260°C, then set the printing head moving speed to 1500mm/min and the power to 10W, and then carry out 3D printing according to the modeling; after printing, set the shape at 100°C and cool down Finally, the unsintered excess powder is removed, and finally the de-dioxin bag cage is obtained.
将所得催化氧化滤料在SCR脱二噁英试验台上利用模拟烟气进行脱二噁英性能评价。。收集反应器进出口烟气并进行二噁英浓度分析,计算二噁英脱除效率为94%。The obtained catalytic oxidation filter material was used to evaluate the performance of dioxin removal on the SCR dioxin removal test bench using simulated flue gas. . The flue gas at the inlet and outlet of the reactor was collected and analyzed for dioxin concentration. The calculated dioxin removal efficiency was 94%.
按照GB/T 5453-1997测试标准,对常规PTFE滤袋+脱二噁英袋笼组合在压差200Pa下进行透气率测试,透气率为10m3/m2/min。According to the GB/T 5453-1997 test standard, the air permeability test was carried out on the combination of conventional PTFE filter bag + dioxin-free bag cage under a pressure difference of 200Pa, and the air permeability was 10m 3 /m 2 /min.
实施例6Example 6
将10.5kg脱二噁英催化剂粉末、4.6kg聚四氟乙烯粉末、1.05kg单烷氧基型钛酸酯、1.6kg纳米二氧化硅混合后置于行星式球磨机上进行球磨,球磨机转速250r/min,每20min为一个回合,研磨6个回合,即球磨时间为120min。然后在400℃下熔融处理得到物料A,然后在该物料A中加入0.53kg邻苯二甲酸二辛酯,搅拌后获得物料B,然后通过造粒机挤出平均粒径为40μm的粉粒,得到可供3D打印设备使用的打印材料;使用Solidworks软件创建上创建袋笼3维模型,基体尺寸为:上圈口直径145mm、厚度5mm,底部直径110mm,袋笼长度970mm,微孔直径8mm,微孔间距4mm。使用Simplify 3D软件对创建后的脱二噁英袋笼三维模型进行切片处理,设置层高0.6mm、壁厚0.3mm;3D打印采用选择性热烧结技术,首先将制备好的粉体通过铺粉辊均匀铺设操作台,同时操作台预热至260℃,然后设置打印头移动速度为1000mm/min和功率为5W后,按照建模来进行3D打印;打印结束后在100℃下进行定型,冷却后将未烧结的多余粉体剔除,最终得到脱二噁英袋笼。After mixing 10.5kg of dioxin-removing catalyst powder, 4.6kg of polytetrafluoroethylene powder, 1.05kg of monoalkoxy titanate, and 1.6kg of nano-silicon dioxide, they are placed on a planetary ball mill for ball milling, and the ball mill speed is 250r/ min, every 20min is a round, and there are 6 rounds of grinding, that is, the ball milling time is 120min. Then melt processing at 400°C to obtain material A, then add 0.53kg of dioctyl phthalate to the material A, stir to obtain material B, and then extrude powder particles with an average particle size of 40 μm through a granulator, Obtain printing materials that can be used by 3D printing equipment; use Solidworks software to create a 3D model of the bag cage. The size of the substrate is: the diameter of the upper ring is 145mm, the thickness is 5mm, the diameter of the bottom is 110mm, the length of the bag cage is 970mm, and the diameter of the micropore is 8mm. Microhole spacing 4mm. Use Simplify 3D software to slice the created dioxin-free bag cage 3D model, set the layer height to 0.6mm, and the wall thickness to 0.3mm; 3D printing adopts selective thermal sintering technology. The rollers are evenly laid on the operation table, and the operation table is preheated to 260°C at the same time, and then the printing head moving speed is set to 1000mm/min and the power is 5W, and the 3D printing is carried out according to the modeling; after the printing is completed, it is shaped at 100°C and cooled Finally, the unsintered excess powder is removed, and finally the de-dioxin bag cage is obtained.
将所得催化氧化滤料在SCR脱二噁英试验台上利用模拟烟气进行脱二噁英性能评价。。收集反应器进出口烟气并进行二噁英浓度分析,计算二噁英脱除效率为90%。The obtained catalytic oxidation filter material was used to evaluate the performance of dioxin removal on the SCR dioxin removal test bench using simulated flue gas. . The flue gas at the inlet and outlet of the reactor was collected and analyzed for dioxin concentration, and the removal efficiency of dioxin was calculated to be 90%.
按照GB/T 5453-1997测试标准,对常规PTFE滤袋+脱二噁英袋笼组合在压差200Pa下进行透气率测试,透气率为9.6m3/m2/min。According to the GB/T 5453-1997 test standard, the air permeability test was carried out on the combination of conventional PTFE filter bag + dioxin-free bag cage under a pressure difference of 200Pa, and the air permeability was 9.6m 3 /m 2 /min.
实施例7Example 7
将8.1kg脱二噁英催化剂粉末、2.0kg聚四氟乙烯粉末、0.13kg单烷氧基型钛酸酯、0.53kg纳米二氧化硅混合后置于行星式球磨机上进行球磨,球磨机转速250r/min,每20min为一个回合,研磨6个回合,即球磨时间为120min。然后在400℃下熔融处理得到物料A,然后在该物料A中加入0.026kg邻苯二甲酸二辛酯,搅拌后获得物料B,然后通过造粒机挤出平均粒径为20μm的粉粒,得到可供3D打印设备使用的打印材料;使用Solidworks软件创建上创建袋笼3维模型,基体尺寸为:上圈口直径145mm、厚度5mm,底部直径110mm,袋笼长度970mm,微孔直径4mm,微孔间距8mm。使用Simplify 3D软件对创建后的脱二噁英袋笼三维模型进行切片处理,设置层高0.2mm、壁厚0.3mm;3D打印采用选择性热烧结技术,首先将制备好的粉体通过铺粉辊均匀铺设操作台,同时操作台预热至260℃,然后设置打印头移动速度为4000mm/min和功率为25W后,按照建模来进行3D打印;打印结束后在100℃下进行定型,冷却后将未烧结的多余粉体剔除,最终得到脱二噁英袋笼。Mix 8.1kg of dioxin-removing catalyst powder, 2.0kg of polytetrafluoroethylene powder, 0.13kg of monoalkoxy titanate, and 0.53kg of nano-silicon dioxide and place them on a planetary ball mill for ball milling. The speed of the ball mill is 250r/ min, every 20min is a round, and there are 6 rounds of grinding, that is, the ball milling time is 120min. Then melt processing at 400°C to obtain material A, then add 0.026kg dioctyl phthalate to material A, obtain material B after stirring, and then extrude powder particles with an average particle size of 20 μm through a granulator, Obtain printing materials that can be used by 3D printing equipment; use Solidworks software to create a 3D model of the bag cage. The size of the substrate is: the diameter of the upper ring is 145mm, the thickness is 5mm, the diameter of the bottom is 110mm, the length of the bag cage is 970mm, and the diameter of the micropore is 4mm. Microhole spacing 8mm. Use Simplify 3D software to slice the created dioxin-free bag cage 3D model, set the layer height to 0.2mm, and the wall thickness to 0.3mm; 3D printing adopts selective thermal sintering technology. The rollers are evenly laid on the operation table, and the operation table is preheated to 260°C at the same time, and then the printing head moving speed is set to 4000mm/min and the power is 25W, and the 3D printing is carried out according to the modeling; after the printing is completed, it is shaped at 100°C and cooled Finally, the unsintered excess powder is removed, and finally the de-dioxin bag cage is obtained.
将所得催化氧化滤料在SCR脱二噁英试验台上利用模拟烟气进行脱二噁英性能评价。。收集反应器进出口烟气并进行二噁英浓度分析,计算二噁英脱除效率为91%。The obtained catalytic oxidation filter material was used to evaluate the performance of dioxin removal on the SCR dioxin removal test bench using simulated flue gas. . The flue gas at the inlet and outlet of the reactor was collected and analyzed for dioxin concentration, and the calculated dioxin removal efficiency was 91%.
按照GB/T 5453-1997测试标准,对常规PTFE滤袋+脱二噁英袋笼组合在压差200Pa下进行透气率测试,透气率为9.5m3/m2/min。According to the GB/T 5453-1997 test standard, the air permeability test was carried out on the combination of conventional PTFE filter bag + dioxin-free bag cage under a pressure difference of 200Pa, and the air permeability was 9.5m 3 /m 2 /min.
目前,采用浸渍法制备的脱二噁英催化滤袋,按照上述实施例中标准测试,透气率为4.5~7.7m3/m2/min,小于本发明的7.7~10.1m3/m2/min。由于透气率与阻力成正比,即证明常规滤袋+脱二噁英袋笼组合与脱二噁英滤袋+常规袋笼组合相比阻力更小。同时由于采用3D打印技术成型,可以通过改变模型设置,方便的制造不同结构、参数额产品。产品自由度高、多样性强,由于采用自动控制,产品质量稳定,可靠性强,适合工程推广。At present, the dioxin-removing catalytic filter bag prepared by the impregnation method is tested according to the standard in the above examples, and the air permeability is 4.5-7.7m 3 /m 2 /min, which is lower than the 7.7-10.1m 3 /m 2 /min of the present invention. min. Since the air permeability is directly proportional to the resistance, it proves that the combination of conventional filter bag + dioxin-free bag cage has lower resistance than the combination of dioxin-free filter bag + conventional bag cage. At the same time, due to the use of 3D printing technology for molding, products with different structures and parameters can be conveniently manufactured by changing the model settings. The product has a high degree of freedom and strong diversity. Due to the use of automatic control, the product quality is stable and reliable, and it is suitable for engineering promotion.
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