CN116808853A - Hydrophobic oleophobic PTFE membrane and preparation method and application thereof - Google Patents
Hydrophobic oleophobic PTFE membrane and preparation method and application thereof Download PDFInfo
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- 229920001343 polytetrafluoroethylene Polymers 0.000 title claims abstract description 176
- 239000004810 polytetrafluoroethylene Substances 0.000 title claims abstract description 176
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- 238000002360 preparation method Methods 0.000 title claims abstract description 46
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- QTRSWYWKHYAKEO-UHFFFAOYSA-N 1,1,2,2,3,3,4,4,5,5,6,6,7,7,8,8,9,9,10,10,10-henicosafluorodecyl-tris(1,1,2,2,2-pentafluoroethoxy)silane Chemical compound FC(F)(F)C(F)(F)O[Si](OC(F)(F)C(F)(F)F)(OC(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F QTRSWYWKHYAKEO-UHFFFAOYSA-N 0.000 description 2
- NKAMGQZDVMQEJL-UHFFFAOYSA-N 3,3,4,4,5,5,6,6,7,7,8,8,9,9,10,10,10-heptadecafluorodec-1-ene Chemical group FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C=C NKAMGQZDVMQEJL-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
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- WORVDWQJHXUFFO-UHFFFAOYSA-N 1,1,2,2,3,3,4,4,4-nonafluorobutyl-tris(1,1,2,2,2-pentafluoroethoxy)silane Chemical compound FC(F)(F)C(F)(F)O[Si](OC(F)(F)C(F)(F)F)(OC(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F WORVDWQJHXUFFO-UHFFFAOYSA-N 0.000 description 1
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- FYQFWFHDPNXORA-UHFFFAOYSA-N 3,3,4,4,5,5,6,6,7,7,8,8,8-tridecafluorooct-1-ene Chemical group FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C=C FYQFWFHDPNXORA-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
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- BIGPRXCJEDHCLP-UHFFFAOYSA-N ammonium bisulfate Chemical compound [NH4+].OS([O-])(=O)=O BIGPRXCJEDHCLP-UHFFFAOYSA-N 0.000 description 1
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- 229920001485 poly(butyl acrylate) polymer Polymers 0.000 description 1
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- ZLDJTZCGPNHTGL-UHFFFAOYSA-N tris(1,1,2,2,2-pentafluoroethoxy)-(1,1,2,2,3,3,4,4,5,5,6,6,6-tridecafluorohexyl)silane Chemical compound FC(F)(F)C(F)(F)O[Si](OC(F)(F)C(F)(F)F)(OC(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F ZLDJTZCGPNHTGL-UHFFFAOYSA-N 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/30—Polyalkenyl halides
- B01D71/32—Polyalkenyl halides containing fluorine atoms
- B01D71/36—Polytetrafluoroethene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/54—Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms
- B01D46/543—Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms using membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/38—Hydrophobic membranes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Laminated Bodies (AREA)
- Filtering Materials (AREA)
Abstract
Description
技术领域Technical field
本发明涉及高分子材料技术领域,且特别涉及一种疏水疏油PTFE膜及制备方法、应用。The invention relates to the technical field of polymer materials, and in particular to a hydrophobic and oleophobic PTFE membrane and its preparation method and application.
背景技术Background technique
随着国家对大气污染物治理的要求日益严苛,为实现超低排放,覆膜滤料应用越来越广泛。PTFE膜(聚四氟乙烯微孔膜)是采用聚四氟乙烯分散树脂,经预混、挤压、压延、双向拉伸等特殊工艺生产的微孔性薄膜,具有独特的节点原纤性、表面光滑、耐化学物质、透气不透水、透气量大、阻燃、耐高温、抗强酸碱、无毒等特性,PTFE覆膜处理的过滤材料过滤效率高,可达99.99%,具有孔径小、相对密度小、薄膜强度高、透湿防水、耐化学腐蚀、生物相容性高等特点,被广泛用于生物医用材料、服装、工业过滤材料等领域;As the country's requirements for air pollutant control become increasingly stringent, in order to achieve ultra-low emissions, membrane-coated filter materials are increasingly used. PTFE membrane (polytetrafluoroethylene microporous membrane) is a microporous film produced by special processes such as premixing, extrusion, calendering, and biaxial stretching using polytetrafluoroethylene dispersion resin. It has unique node fibrillation, It has the characteristics of smooth surface, chemical resistance, breathable and impermeable, large air permeability, flame retardant, high temperature resistance, strong acid and alkali resistance, non-toxic, etc. The filter material coated with PTFE has high filtration efficiency, up to 99.99%, and has small pore size. , low relative density, high film strength, breathable and waterproof, chemical corrosion resistance, high biocompatibility, etc., and are widely used in biomedical materials, clothing, industrial filter materials and other fields;
目前已公开专利的技术方案中采用混合--压延--脱油--横拉拉膜的工艺生产,具体步骤是:将PTFE树脂与润滑剂置于高温混料机中混合并熟化,得到糊料;将糊料经挤出机设备挤出成型得到初料;将初料在150-350℃温度下先经过纵向拉伸制备成基膜,然后在横向拉伸机上拉伸成宽幅为1-3m的PTFE双向拉伸微孔膜;在NaOH的碱性催化下采用聚丙烯酸丁脂的乙醇溶液浸润PEFT膜,对PEFT膜表面进行水解改性;PTFE微孔复合膜表面喷涂氟树脂悬浮乳液并烘干;烧结定型。但由于常规的防水拒油剂无法在PTFE膜表面形成物理交联作用,导致覆膜滤料表面无法实现高等级防水拒油,与低表面张力液体(硫酸氢铵、石油焦、重油等)接触时,防液封性能差,这类低表面张力液体会附着并堵塞PTFE微孔膜,降低其透气量,并可能导致其严重损坏。另一方面,这类液体附着在膜表面与粉尘发生团聚,粉尘再与液体团聚,最终会形成糊袋情况,导致滤袋的阻力不断上升,最终失效。这在一定程度上限制了PTFE覆膜滤料的使用,对此类工业锅炉实现超低排放造成了一定的阻碍,增加了企业的成本及环保风险。The currently disclosed patented technical solution adopts the process of mixing - calendering - deoiling - transverse stretching of the film. The specific steps are: place the PTFE resin and lubricant in a high-temperature mixer to mix and mature to obtain a paste. material; the paste is extruded through the extruder equipment to obtain the primary material; the primary material is first longitudinally stretched at a temperature of 150-350°C to prepare a base film, and then stretched on a transverse stretching machine to a width of 1 -3m PTFE biaxially stretched microporous membrane; under the alkaline catalysis of NaOH, the PEFT membrane is infiltrated with an ethanol solution of polybutyl acrylate to hydrolyze the surface of the PEFT membrane; the surface of the PTFE microporous composite membrane is sprayed with fluororesin suspension emulsion And drying; sintering and shaping. However, because conventional waterproof and oil-repellent agents cannot form physical cross-linking on the surface of the PTFE membrane, the surface of the membrane-coated filter material cannot achieve high-level waterproofing and oil-repellent, and it comes into contact with low surface tension liquids (ammonium bisulfate, petroleum coke, heavy oil, etc.) When used, the liquid-proof sealing performance is poor. This type of low surface tension liquid will adhere to and block the PTFE microporous membrane, reduce its air permeability, and may cause serious damage to it. On the other hand, this type of liquid adheres to the surface of the membrane and agglomerates with dust. The dust then agglomerates with the liquid, eventually forming a sticky bag situation, causing the resistance of the filter bag to continue to rise and eventually fail. This limits the use of PTFE-coated filter media to a certain extent, hinders the realization of ultra-low emissions from such industrial boilers, and increases the company's costs and environmental risks.
发明内容Contents of the invention
本发明的目的在于提供一种疏水疏油PTFE膜,具有良好的抵抗低表面张力液体的作用,从而保障了高粉尘工况下PTFE覆膜滤料长期运行。The purpose of the present invention is to provide a hydrophobic and oleophobic PTFE membrane that has good resistance to low surface tension liquids, thereby ensuring long-term operation of the PTFE-coated filter material under high dust conditions.
本发明的另一目的在于提供一种疏水疏油PTFE膜的制备方法,该制备方法工艺简单,适宜工业化生产。Another object of the present invention is to provide a method for preparing a hydrophobic and oleophobic PTFE membrane, which has a simple process and is suitable for industrial production.
本发明的第三个目的在于提供一种疏水疏油PTFE膜的应用,PTFE滤膜可用于空气过滤领域中,微孔结构明显,具有很好的疏水疏油特性,适用于含油气体的气固分离。The third object of the present invention is to provide an application of a hydrophobic and oleophobic PTFE membrane. The PTFE filter membrane can be used in the field of air filtration. It has an obvious microporous structure and good hydrophobic and oleophobic properties, and is suitable for gas-solid separation of oil-containing gases. separation.
本发明解决其技术问题是采用以下技术方案来实现的。The present invention solves its technical problems by adopting the following technical solutions.
本发明提出一种疏水疏油PTFE膜的制备方法,包括以下步骤:The invention proposes a preparation method of a hydrophobic and oleophobic PTFE membrane, which includes the following steps:
S1,混料:将聚四氟乙烯树脂粉末、航空煤油、交联剂混合搅拌后,加入硅烷类防水拒油剂继续混合搅拌,并于30Hz超声处理2h,制得混料A;S1, mixing: After mixing polytetrafluoroethylene resin powder, aviation kerosene, and cross-linking agent, add silane waterproof and oil-repellent agent, continue mixing and stirring, and ultrasonic treatment at 30Hz for 2 hours to prepare mixture A;
S2,挤出:将混料A通过挤出机挤出呈柱状模料;S2, extrusion: Extrude the mixture A through the extruder into a columnar mold material;
S3,压延:将柱状模料经过压延机制成聚四氟乙烯膜片后,加热,去除航空煤油;S3, Calendering: After passing the cylindrical mold material through a calender to form a polytetrafluoroethylene diaphragm, it is heated to remove aviation kerosene;
S4,双向拉伸:将脱除航空煤油后的聚四氟乙烯膜片同时进行横向拉伸及纵向拉伸;S4, biaxial stretching: the polytetrafluoroethylene diaphragm after removing aviation kerosene is stretched transversely and longitudinally at the same time;
S5,热定型:将双向拉伸的PTFE薄膜进行热定型,制得疏水疏油PTFE膜。S5, heat setting: heat setting the biaxially stretched PTFE film to obtain a hydrophobic and oleophobic PTFE film.
本发明还提出一种由上述制备方法制得的疏水疏油PTFE膜。The invention also proposes a hydrophobic and oleophobic PTFE membrane prepared by the above preparation method.
本发明还提出一种由上述制备方法制得的疏水疏油PTFE膜在滤料中的应用,包括以下步骤:The invention also proposes an application of the hydrophobic and oleophobic PTFE membrane prepared by the above preparation method in filter materials, which includes the following steps:
(1)制备复合滤料;(1) Prepare composite filter material;
(2)将疏水疏油PTFE膜热压在复合滤料表面,所述热压温度为250-330℃,热压压力为0.5-0.8MPa,热压时间为4-6s,制得疏水疏油PTFE覆膜复合滤料;(2) Hot-press the hydrophobic and oleophobic PTFE membrane on the surface of the composite filter material. The hot-pressing temperature is 250-330°C, the hot-pressing pressure is 0.5-0.8MPa, and the hot-pressing time is 4-6 s to obtain a hydrophobic and oleophobic membrane. PTFE coated composite filter material;
本发明制得的疏水疏油PTFE膜具有良好的抵抗低表面张力液体的作用,从而保障了高粉尘工况下PTFE覆膜滤料长期运行,阻力也不会发生明显上升的情况。The hydrophobic and oleophobic PTFE membrane produced by the invention has good resistance to low surface tension liquids, thereby ensuring long-term operation of the PTFE-coated filter material under high dust conditions, and the resistance will not increase significantly.
本发明制备的PTFE滤膜可用于空气过滤领域中,微孔结构明显,孔隙率达到85%以上,孔径集中分布在0.1-3μm,稳定性非常好,透气效果良好,127Pa条件下测试透气率为60-80mm/s,具有很好的疏水疏油特性,适用于含油气体的气固分离。The PTFE filter membrane prepared by the invention can be used in the field of air filtration. It has an obvious microporous structure, a porosity of more than 85%, a concentrated pore size distribution of 0.1-3 μm, very good stability, and good air permeability. The air permeability was tested under the condition of 127Pa. 60-80mm/s, has good hydrophobic and oleophobic properties, and is suitable for gas-solid separation of oil-containing gases.
附图说明Description of the drawings
为了更清楚地说明本发明实施例的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,应当理解,以下附图仅示出了本发明的某些实施例,因此不应被看作是对范围的限定,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他相关的附图。In order to explain the technical solutions of the embodiments of the present invention more clearly, the drawings required to be used in the embodiments will be briefly introduced below. It should be understood that the following drawings only show some embodiments of the present invention and therefore do not It should be regarded as a limitation of the scope. For those of ordinary skill in the art, other relevant drawings can be obtained based on these drawings without exerting creative efforts.
图1为本发明实施例的一种疏水疏油PTFE膜的制备流程图。Figure 1 is a flow chart for the preparation of a hydrophobic and oleophobic PTFE membrane according to an embodiment of the present invention.
具体实施方式Detailed ways
为使本发明实施例的目的、技术方案和优点更加清楚,下面将对本发明实施例中的技术方案进行清楚、完整地描述。实施例中未注明具体条件者,按照常规条件或制造商建议的条件进行。所用试剂或仪器未注明生产厂商者,均为可以通过市售购买获得的常规产品。In order to make the objectives, technical solutions, and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be described clearly and completely below. If the specific conditions are not specified in the examples, the conditions should be carried out according to the conventional conditions or the conditions recommended by the manufacturer. If the manufacturer of the reagents or instruments used is not indicated, they are all conventional products that can be purchased commercially.
下面对本发明实施例的一种疏水疏油PTFE膜及制备方法、应用进行具体说明。The following is a detailed description of a hydrophobic and oleophobic PTFE membrane according to the embodiment of the present invention, as well as its preparation method and application.
本发明实施例提供的一种疏水疏油PTFE膜的制备方法,包括以下步骤:The embodiment of the present invention provides a method for preparing a hydrophobic and oleophobic PTFE membrane, which includes the following steps:
S1,混料:将聚四氟乙烯树脂粉末、航空煤油、交联剂混合搅拌后,加入硅烷类防水拒油剂继续混合搅拌,并于30Hz超声处理2h,制得混料A;S1, mixing: After mixing polytetrafluoroethylene resin powder, aviation kerosene, and cross-linking agent, add silane waterproof and oil-repellent agent, continue mixing and stirring, and ultrasonic treatment at 30Hz for 2 hours to prepare mixture A;
S2,挤出:将混料A通过挤出机挤出呈柱状模料;S2, extrusion: Extrude the mixture A through the extruder into a columnar mold material;
S3,压延:将柱状模料经过压延机制成聚四氟乙烯膜片后,加热,去除航空煤油;S3, Calendering: After passing the cylindrical mold material through a calender to form a polytetrafluoroethylene diaphragm, it is heated to remove aviation kerosene;
S4,双向拉伸:将脱除航空煤油后的聚四氟乙烯膜片同时进行横向拉伸及纵向拉伸;S4, biaxial stretching: the polytetrafluoroethylene diaphragm after removing aviation kerosene is stretched transversely and longitudinally at the same time;
S5,热定型:将双向拉伸的PTFE薄膜进行热定型,制得疏水疏油PTFE膜。S5, heat setting: heat setting the biaxially stretched PTFE film to obtain a hydrophobic and oleophobic PTFE film.
进一步地,在本发明较佳实施例中,步骤S1中,所述硅烷类防水拒油剂,制备方法为:在氮气保护下,将全氟丁基乙烯和三乙氧基硅烷按照摩尔比为1:1.05-1.15加入到二甲苯溶液中,在0.5-1‰Pt催化下80-90℃回流20-24h,过滤,于真空度0.07-0.08Mpa,温度110-130℃条件下减压蒸馏除去溶剂,得硅烷类防水拒油剂。Further, in a preferred embodiment of the present invention, in step S1, the preparation method of the silane-based waterproof and oil-repellent agent is: under nitrogen protection, add perfluorobutylethylene and triethoxysilane according to a molar ratio of 1:1.05-1.15 is added to the xylene solution, refluxed at 80-90°C for 20-24h under the catalysis of 0.5-1‰Pt, filtered, and distilled under reduced pressure at a vacuum of 0.07-0.08Mpa and a temperature of 110-130°C. Solvent to obtain silane-based waterproof and oil-repellent agent.
进一步地,在本发明较佳实施例中,步骤S2中,所述挤出压力为5-8MPa,挤出速率为300-400mm/min。Further, in a preferred embodiment of the present invention, in step S2, the extrusion pressure is 5-8MPa, and the extrusion rate is 300-400mm/min.
优选地,将柱状毛坯放入挤出设备,通过挤出设备的油缸、挤出轴,在挤出设备的铜口模、不锈钢口模处挤出圆形条子,挤出呈柱状模料,模料的直径大小为18-25mm,将圆形条子送入到上压延滚筒与下压延滚筒之间,压延成宽度为200-300mm、厚度为0.2-0.3mm的带子,挤出压缩比为50-120,在整个过程中,物料都需要在80-90℃的温水中进行保温。Preferably, the cylindrical blank is put into the extrusion equipment, and the circular sliver is extruded at the copper die and stainless steel die of the extrusion equipment through the oil cylinder and the extrusion shaft of the extrusion equipment, and the cylindrical mold material is extruded. The diameter of the material is 18-25mm. The round sliver is fed between the upper and lower calendering rollers and is calendered into a tape with a width of 200-300mm and a thickness of 0.2-0.3mm. The extrusion compression ratio is 50- 120. During the entire process, the materials need to be kept in warm water at 80-90°C.
进一步地,在本发明较佳实施例中,步骤S3中,所述压延温度为40-70℃,压延速率为13-16m/min,加热温度为300-340℃,所述聚四氟乙烯膜片的厚度为30-50μm。Further, in a preferred embodiment of the present invention, in step S3, the rolling temperature is 40-70°C, the rolling speed is 13-16m/min, the heating temperature is 300-340°C, and the polytetrafluoroethylene film The thickness of the sheet is 30-50μm.
进一步地,在本发明较佳实施例中,步骤S4中,所述横向拉伸比为3-5倍,纵向拉伸比为5-8倍。Further, in a preferred embodiment of the present invention, in step S4, the transverse stretching ratio is 3-5 times, and the longitudinal stretching ratio is 5-8 times.
进一步地,在本发明较佳实施例中,步骤S5中,所述热定型温度为300-340℃,热定型时间为8-15min。Further, in a preferred embodiment of the present invention, in step S5, the heat setting temperature is 300-340°C, and the heat setting time is 8-15 minutes.
进一步地,在本发明较佳实施例中,步骤S1中,所述交联剂为聚异氰酸酯、聚乙烯醇缩丁醛中的一种或两种。Further, in a preferred embodiment of the present invention, in step S1, the cross-linking agent is one or both of polyisocyanate and polyvinyl butyral.
进一步地,在本发明较佳实施例中,在步骤S5还包括:将热定型后的PTFE薄膜进行收卷,所述疏水疏油PTFE膜的厚度为5-8μm。Further, in a preferred embodiment of the present invention, step S5 further includes: rolling up the heat-set PTFE film, and the thickness of the hydrophobic and oleophobic PTFE film is 5-8 μm.
本发明还提供了上述的制备方法制得的疏水疏油PTFE膜。The invention also provides a hydrophobic and oleophobic PTFE membrane prepared by the above preparation method.
本发明还提供了上述的制备方法制得的疏水疏油PTFE膜在滤料中的应用,其特征在于:包括以下步骤:The present invention also provides the application of the hydrophobic and oleophobic PTFE membrane prepared by the above preparation method in filter materials, which is characterized in that it includes the following steps:
(1)制备复合滤料;(1) Prepare composite filter material;
(2)将疏水疏油PTFE膜热压在复合滤料表面,所述热压温度为250-330℃,热压压力为0.5-0.8MPa,热压时间为4-6s,制得疏水疏油PTFE覆膜复合滤料。(2) Hot-press the hydrophobic and oleophobic PTFE membrane on the surface of the composite filter material. The hot-pressing temperature is 250-330°C, the hot-pressing pressure is 0.5-0.8MPa, and the hot-pressing time is 4-6 s to obtain a hydrophobic and oleophobic membrane. PTFE coated composite filter material.
优选的,所述复合滤料包括面层、底层和基布层,所述面层采用聚苯硫醚纤维与聚四氟乙烯纤维混纺,所述底层采用聚苯硫醚纤维与聚四氟乙烯纤维,所述基布层为聚四氟乙烯纱线经纬交织形成的网状结构;所述基布层位于面层和底层之间,通过针刺机械将面层、基布层和底层固定,再经过压光烧毛处理,制得复合滤料。Preferably, the composite filter material includes a surface layer, a bottom layer and a base fabric layer. The surface layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber blended, and the bottom layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber. Fiber, the base fabric layer is a network structure formed by interweaving warp and weft of polytetrafluoroethylene yarn; the base fabric layer is located between the surface layer and the bottom layer, and the surface layer, base fabric layer and bottom layer are fixed by a needle punching machine. Then after calendering and singeing treatment, the composite filter material is obtained.
优选的,所述聚苯硫醚纤维与聚四氟乙烯纤维的质量比为1-2:1。Preferably, the mass ratio of the polyphenylene sulfide fiber to the polytetrafluoroethylene fiber is 1-2:1.
以下结合实施例对本发明的特征和性能作进一步的详细描述。The features and performance of the present invention will be described in further detail below with reference to examples.
实施例一Embodiment 1
疏水疏油PTFE膜的制备方法Preparation method of hydrophobic and oleophobic PTFE membrane
(1)制备防水拒油剂:在氮气保护下,将全氟丁基乙烯和三乙氧基硅烷按照摩尔比为1:1.1加入到二甲苯溶液中,在0.5‰Pt催化下80℃回流22h,过滤,真空度0.07Mpa,温度110℃下减压蒸馏除去溶剂,得全氟丁基三乙氧基硅烷。其原理为硅氢化反应,含Si-H硅化合物与不饱和有机化合物发生加成反应,生成有机硅化合物。(1) Preparation of waterproof and oil-repellent agent: Under nitrogen protection, add perfluorobutylethylene and triethoxysilane to the xylene solution at a molar ratio of 1:1.1, and reflux at 80°C for 22 hours under the catalysis of 0.5‰Pt. , filtered, with a vacuum degree of 0.07Mpa, and the solvent was distilled under reduced pressure at a temperature of 110°C to obtain perfluorobutyltriethoxysilane. The principle is a hydrosilylation reaction. An addition reaction occurs between Si-H-containing silicon compounds and unsaturated organic compounds to generate organosilicon compounds.
(2)混料:将聚四氟乙烯树脂粉末、航空煤油、聚异氰酸酯混合搅拌5h后,加入防水拒油剂继续混合搅拌10h,并于30Hz超声处理2h,超声频率50Hz制得混料A。其中聚四氟乙烯树脂为经300目筛网筛分后的聚四氟乙烯颗粒,聚四氟乙烯树脂的质量为混料A质量的65%,航空煤油的质量为混料A质量的15%,聚异氰酸酯的质量为混料A质量的3%,防水拒油剂的质量为混料A质量的17%。(2) Mixing: After mixing polytetrafluoroethylene resin powder, aviation kerosene, and polyisocyanate for 5 hours, add a waterproof and oil-repellent agent and continue mixing and stirring for 10 hours, and ultrasonic treatment at 30 Hz for 2 hours at an ultrasonic frequency of 50 Hz to prepare mixture A. The polytetrafluoroethylene resin is polytetrafluoroethylene particles that have been screened with a 300-mesh screen. The mass of polytetrafluoroethylene resin is 65% of the mass of mixture A, and the mass of aviation kerosene is 15% of the mass of mixture A. , the mass of polyisocyanate is 3% of the mass of Mixture A, and the mass of waterproof and oil-repellent agent is 17% of the mass of Mixture A.
(3)挤出:将混料A通过挤出机挤出呈柱状模料,挤出压力为6MPa,出速率为300mm/min。(3) Extrusion: Extrude mixture A through an extruder into a columnar mold material, with an extrusion pressure of 6MPa and an output rate of 300mm/min.
(4)压延:将柱状模料经过压延机制成厚度为40μm的聚四氟乙烯膜片,压延机的圧延温度为60℃,压延速率为15m/min。压延成膜后继续加热,以去除航空煤油,加热温度为320℃。(4) Calendering: Pass the cylindrical mold material through a calender to form a polytetrafluoroethylene diaphragm with a thickness of 40 μm. The rolling temperature of the calender is 60°C, and the calendering speed is 15m/min. After calendering and film formation, heating is continued to remove aviation kerosene. The heating temperature is 320°C.
(5)双向拉伸:将脱除航空煤油后的聚四氟乙烯膜片同时进行横向及纵向拉伸。其中横向拉伸比为4倍,纵向拉伸比为6倍。(5) Biaxial stretching: The polytetrafluoroethylene diaphragm after removing aviation kerosene is stretched transversely and longitudinally at the same time. The transverse stretch ratio is 4 times, and the longitudinal stretch ratio is 6 times.
(6)热定型:将双向拉伸的PTFE薄膜进行热定型,制得疏水疏油PTFE膜。其中热定型温度为330℃,热定型时间8min。(6) Heat setting: Heat setting the biaxially stretched PTFE film to obtain a hydrophobic and oleophobic PTFE film. The heat setting temperature is 330°C and the heat setting time is 8 minutes.
(7)收卷成膜:将热定型后的PTFE薄膜进行收卷,疏水疏油PTFE膜的厚度为5-8μm。(7) Winding to form a film: Wind up the heat-set PTFE film. The thickness of the hydrophobic and oleophobic PTFE film is 5-8 μm.
疏水疏油PTFE覆膜复合滤料的制备:Preparation of hydrophobic and oleophobic PTFE-coated composite filter material:
(1)制备复合滤料:复合滤料包括依次层叠的面层、基布层和底层,通过针刺机械将基布层固定在面层和底层之间,再经过压光烧毛处理,压光温度250℃,热压压力为0.35MPa,热压时间为3s,制得针刺毡,即为复合滤料。其中面层采用聚苯硫醚纤维与聚四氟乙烯纤维混纺,底层采用聚苯硫醚纤维与聚四氟乙烯纤维,聚苯硫醚纤维与聚四氟乙烯纤维的质量比为2:1,纤维经过开松混合、梳理、铺网获得均匀的纤维网,基布层为聚四氟乙烯纱线经纬交织形成的网状结构。其中复合滤料的制备方法也可以采用技术。(1) Preparation of composite filter material: The composite filter material includes a surface layer, a base fabric layer and a bottom layer laminated in sequence. The base fabric layer is fixed between the surface layer and the bottom layer through a needle punching machine, and then undergoes calendering and singeing treatment. The light temperature is 250°C, the hot pressing pressure is 0.35MPa, and the hot pressing time is 3 seconds. The needle punched felt is obtained, which is the composite filter material. The surface layer is made of a blend of polyphenylene sulfide fiber and polytetrafluoroethylene fiber, and the bottom layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber. The mass ratio of polyphenylene sulfide fiber to polytetrafluoroethylene fiber is 2:1. The fibers are opened, mixed, carded, and laid to obtain a uniform fiber network. The base fabric layer is a network structure formed by interweaving the warp and weft of polytetrafluoroethylene yarns. Among them, the preparation method of composite filter material can also adopt technology.
(2)将本实施例中制得的疏水疏油PTFE膜热压在复合滤料表面,热压温度为260℃,热压压力为0.5MPa,热压时间为4s,制得疏水疏油PTFE覆膜复合滤料。(2) Hot-press the hydrophobic and oleophobic PTFE membrane prepared in this example on the surface of the composite filter material. The hot-pressing temperature is 260°C, the hot-pressing pressure is 0.5MPa, and the hot-pressing time is 4 seconds to prepare hydrophobic and oleophobic PTFE. Coated composite filter material.
实施例二Embodiment 2
疏水疏油PTFE膜的制备方法Preparation method of hydrophobic and oleophobic PTFE membrane
制备防水拒油剂:在氮气保护下,将全氟己基乙烯和三乙氧基硅烷按照摩尔比为1:1.05加入到二甲苯溶液中,在1‰Pt催化下80℃回流24h,过滤,真空度0.075Mpa,温度120℃下减压蒸馏除去溶剂,得全氟己基三乙氧基硅烷。其原理为硅氢化反应,含Si-H硅化合物与不饱和有机化合物发生加成反应,生成有机硅化合物。Preparation of waterproof and oil-repellent agent: Under nitrogen protection, add perfluorohexylethylene and triethoxysilane to the xylene solution at a molar ratio of 1:1.05, reflux at 80°C for 24 hours under the catalysis of 1‰Pt, filter, and vacuum The temperature is 0.075Mpa, and the solvent is distilled under reduced pressure at a temperature of 120°C to obtain perfluorohexyltriethoxysilane. The principle is a hydrosilylation reaction, in which Si-H-containing silicon compounds react with unsaturated organic compounds to form organosilicon compounds.
(2)混料:将聚四氟乙烯树脂粉末、航空煤油、聚乙烯醇缩丁醛混合搅拌8h后,加入防水拒油剂继续混合搅拌12h,并于50Hz超声处理3h,制得混料A。其中聚四氟乙烯树脂为经300目筛网筛分后的聚四氟乙烯颗粒,聚四氟乙烯树脂的质量为混料A质量的60%,航空煤油的质量为混料A质量的10%,聚乙烯醇缩丁醛的质量为混料A质量的6%,防水拒油剂的质量为混料A质量的23%。所述防水拒油剂为步骤(1)制备的硅烷类防水拒油剂。其中复合滤料的制备方法也可以采用技术。(2) Mixing: Mix polytetrafluoroethylene resin powder, aviation kerosene, and polyvinyl butyral for 8 hours, add a waterproof and oil-repellent agent, continue mixing and stirring for 12 hours, and ultrasonicate at 50Hz for 3 hours to prepare Mixture A. . The polytetrafluoroethylene resin is polytetrafluoroethylene particles that have been screened with a 300-mesh screen. The mass of polytetrafluoroethylene resin is 60% of the mass of mixture A, and the mass of aviation kerosene is 10% of the mass of mixture A. , the mass of polyvinyl butyral is 6% of the mass of Mixture A, and the mass of waterproof and oil-repellent agent is 23% of the mass of Mixture A. The waterproof and oil-repellent agent is the silane-based waterproof and oil-repellent agent prepared in step (1). Among them, the preparation method of composite filter material can also adopt technology.
(3)挤出:将混料A通过挤出机挤出呈柱状模料,挤出压力为6MPa,出速率为300mm/min。(3) Extrusion: Extrude mixture A through an extruder into a columnar mold material, with an extrusion pressure of 6MPa and an output rate of 300mm/min.
(4)压延:将柱状模料经过压延机制成厚度为40μm的聚四氟乙烯膜片,压延机的圧延温度为60℃,压延速率为15m/min。压延成膜后继续加热,以去除航空煤油,加热温度为320℃。(4) Calendering: Pass the cylindrical mold material through a calender to form a polytetrafluoroethylene diaphragm with a thickness of 40 μm. The rolling temperature of the calender is 60°C, and the calendering speed is 15m/min. After calendering and film formation, heating is continued to remove aviation kerosene. The heating temperature is 320°C.
(5)双向拉伸:将脱除航空煤油后的聚四氟乙烯膜片同时进行横向及纵向拉伸。其中横向拉伸比为4倍,纵向拉伸比为6倍。(5) Biaxial stretching: The polytetrafluoroethylene diaphragm after removing aviation kerosene is stretched transversely and longitudinally at the same time. The transverse stretch ratio is 4 times, and the longitudinal stretch ratio is 6 times.
(6)热定型:将双向拉伸的PTFE薄膜进行热定型,制得疏水疏油PTFE膜。其中热定型温度为330℃,热定型时间8min。(6) Heat setting: Heat setting the biaxially stretched PTFE film to obtain a hydrophobic and oleophobic PTFE film. The heat setting temperature is 330°C and the heat setting time is 8 minutes.
(7)收卷成膜:将热定型后的PTFE薄膜进行收卷,疏水疏油PTFE膜的厚度为5-8μm。(7) Winding to form a film: Wind up the heat-set PTFE film. The thickness of the hydrophobic and oleophobic PTFE film is 5-8 μm.
疏水疏油PTFE覆膜复合滤料的制备:Preparation of hydrophobic and oleophobic PTFE-coated composite filter material:
(1)制备复合滤料:复合滤料包括依次层叠的面层、基布层和底层,通过针刺机械将基布层固定在面层和底层之间,再经过压光烧毛处理,压光温度250℃,热压压力为0.35MPa,热压时间为3s,制得针刺毡,即为复合滤料。其中面层采用聚苯硫醚纤维与聚四氟乙烯纤维混纺,底层采用聚苯硫醚纤维与聚四氟乙烯纤维,聚苯硫醚纤维与聚四氟乙烯纤维的质量比为2:1,纤维经过开松混合、梳理、铺网获得均匀的纤维网,基布层为聚四氟乙烯纱线经纬交织形成的网状结构。其中复合滤料的制备方法也可以采用技术。(1) Preparation of composite filter material: The composite filter material includes a surface layer, a base fabric layer and a bottom layer laminated in sequence. The base fabric layer is fixed between the surface layer and the bottom layer through a needle punching machine, and then undergoes calendering and singeing treatment. The light temperature is 250°C, the hot pressing pressure is 0.35MPa, and the hot pressing time is 3 seconds. The needle punched felt is obtained, which is the composite filter material. The surface layer is made of a blend of polyphenylene sulfide fiber and polytetrafluoroethylene fiber, and the bottom layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber. The mass ratio of polyphenylene sulfide fiber to polytetrafluoroethylene fiber is 2:1. The fibers are opened, mixed, carded, and laid to obtain a uniform fiber network. The base fabric layer is a network structure formed by interweaving the warp and weft of polytetrafluoroethylene yarns. Among them, the preparation method of composite filter material can also adopt technology.
(2)将本实施例中制得的疏水疏油PTFE膜热压在复合滤料表面,热压温度为260℃,热压压力为0.5MPa,热压时间为4s,制得疏水疏油PTFE覆膜复合滤料。(2) Hot-press the hydrophobic and oleophobic PTFE membrane prepared in this example on the surface of the composite filter material. The hot-pressing temperature is 260°C, the hot-pressing pressure is 0.5MPa, and the hot-pressing time is 4 seconds to prepare hydrophobic and oleophobic PTFE. Coated composite filter material.
实施例三Embodiment 3
疏水疏油PTFE膜的制备方法Preparation method of hydrophobic and oleophobic PTFE membrane
(1)制备防水拒油剂:在氮气保护下,将全氟辛基乙烯和三乙氧基硅烷按照摩尔比为1:1.15加入到二甲苯溶液中,在1‰Pt催化下90℃回流20h,过滤,真空度0.08Mpa,温度130℃下减压蒸馏除去溶剂,得全氟癸基三乙氧基硅烷。其原理为硅氢化反应,含Si-H硅化合物与不饱和有机化合物发生加成反应,生成有机硅化合物。(1) Preparation of waterproof and oil-repellent agent: Under nitrogen protection, add perfluorooctylethylene and triethoxysilane to the xylene solution at a molar ratio of 1:1.15, and reflux at 90°C for 20 hours under the catalysis of 1‰Pt. , filtered, with a vacuum degree of 0.08Mpa, and the solvent was distilled under reduced pressure at a temperature of 130°C to obtain perfluorodecyltriethoxysilane. The principle is a hydrosilylation reaction, in which Si-H-containing silicon compounds react with unsaturated organic compounds to form organosilicon compounds.
(2)混料:将聚四氟乙烯树脂粉末、航空煤油、交联剂混合搅拌3h后,加入防水拒油剂继续混合搅拌12h,并超声处理3h,超声频率40Hz,制得混料A。其中聚四氟乙烯树脂为经300目筛网筛分后的聚四氟乙烯颗粒,交联剂包括聚异氰酸酯和聚乙烯醇缩丁醛,聚异氰酸酯和聚乙烯醇缩丁醛的质量比为1:1。聚四氟乙烯树脂的质量为混料A质量的69%,航空煤油的质量为混料A质量的10%,交联剂的质量为混料A质量的3%,防水拒油剂的质量为混料A质量的18%。所述防水拒油剂为步骤(1)制备的硅烷类防水拒油剂。其中复合滤料的制备方法也可以采用技术。(2) Mixing: After mixing polytetrafluoroethylene resin powder, aviation kerosene, and cross-linking agent for 3 hours, add a waterproof and oil-repellent agent and continue mixing and stirring for 12 hours, and ultrasonic treatment for 3 hours at an ultrasonic frequency of 40 Hz to prepare Mixture A. The polytetrafluoroethylene resin is polytetrafluoroethylene particles that have been screened through a 300-mesh screen. The cross-linking agent includes polyisocyanate and polyvinyl butyral. The mass ratio of polyisocyanate and polyvinyl butyral is 1 :1. The mass of polytetrafluoroethylene resin is 69% of the mass of mixture A, the mass of aviation kerosene is 10% of the mass of mixture A, the mass of cross-linking agent is 3% of the mass of mixture A, and the mass of waterproof and oil-repellent agent is 18% of the mass of Mixture A. The waterproof and oil-repellent agent is the silane-based waterproof and oil-repellent agent prepared in step (1). Among them, the preparation method of composite filter material can also adopt technology.
(3)挤出:将混料A通过挤出机挤出呈柱状模料,挤出压力为6MPa,出速率为300mm/min。(3) Extrusion: Extrude mixture A through an extruder into a columnar mold material, with an extrusion pressure of 6MPa and an output rate of 300mm/min.
(4)压延:将柱状模料经过压延机制成厚度为40μm的聚四氟乙烯膜片,压延机的圧延温度为60℃,压延速率为15m/min。压延成膜后继续加热,以去除航空煤油,加热温度为320℃。(4) Calendering: Pass the cylindrical mold material through a calender to form a polytetrafluoroethylene diaphragm with a thickness of 40 μm. The rolling temperature of the calender is 60°C, and the calendering speed is 15m/min. After calendering and film formation, heating is continued to remove aviation kerosene. The heating temperature is 320°C.
(5)双向拉伸:将脱除航空煤油后的聚四氟乙烯膜片同时进行横向及纵向拉伸。其中横向拉伸比为4倍,纵向拉伸比为6倍。(5) Biaxial stretching: The polytetrafluoroethylene diaphragm after removing aviation kerosene is stretched transversely and longitudinally at the same time. The transverse stretch ratio is 4 times, and the longitudinal stretch ratio is 6 times.
(6)热定型:将双向拉伸的PTFE薄膜进行热定型,制得疏水疏油PTFE膜。其中热定型温度为330℃,热定型时间8min。(6) Heat setting: Heat setting the biaxially stretched PTFE film to obtain a hydrophobic and oleophobic PTFE film. The heat setting temperature is 330°C and the heat setting time is 8 minutes.
(7)收卷成膜:将热定型后的PTFE薄膜进行收卷,疏水疏油PTFE膜的厚度为5-8μm。(7) Winding to form a film: Wind up the heat-set PTFE film. The thickness of the hydrophobic and oleophobic PTFE film is 5-8 μm.
疏水疏油PTFE覆膜复合滤料的制备:Preparation of hydrophobic and oleophobic PTFE-coated composite filter material:
(1)制备复合滤料:复合滤料包括依次层叠的面层、基布层和底层,通过针刺机械将基布层固定在面层和底层之间,再经过压光烧毛处理,压光温度250℃,热压压力为0.35MPa,热压时间为3s,制得针刺毡,即为复合滤料。其中面层采用聚苯硫醚纤维与聚四氟乙烯纤维混纺,底层采用聚苯硫醚纤维与聚四氟乙烯纤维,聚苯硫醚纤维与聚四氟乙烯纤维的质量比为2:1,纤维经过开松混合、梳理、铺网获得均匀的纤维网,基布层为聚四氟乙烯纱线经纬交织形成的网状结构。其中复合滤料的制备方法也可以采用技术。(1) Preparation of composite filter material: The composite filter material includes a surface layer, a base fabric layer and a bottom layer laminated in sequence. The base fabric layer is fixed between the surface layer and the bottom layer through a needle punching machine, and then undergoes calendering and singeing treatment. The light temperature is 250°C, the hot pressing pressure is 0.35MPa, and the hot pressing time is 3 seconds. The needle punched felt is obtained, which is the composite filter material. The surface layer is made of a blend of polyphenylene sulfide fiber and polytetrafluoroethylene fiber, and the bottom layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber. The mass ratio of polyphenylene sulfide fiber to polytetrafluoroethylene fiber is 2:1. The fibers are opened, mixed, carded, and laid to obtain a uniform fiber network. The base fabric layer is a network structure formed by interweaving the warp and weft of polytetrafluoroethylene yarns. Among them, the preparation method of composite filter material can also adopt technology.
(2)将本实施例中制得的疏水疏油PTFE膜热压在复合滤料表面,热压温度为260℃,热压压力为0.5MPa,热压时间为4s,制得疏水疏油PTFE覆膜复合滤料。(2) Hot-press the hydrophobic and oleophobic PTFE membrane prepared in this example on the surface of the composite filter material. The hot-pressing temperature is 260°C, the hot-pressing pressure is 0.5MPa, and the hot-pressing time is 4 seconds to prepare hydrophobic and oleophobic PTFE. Coated composite filter material.
实施例四Embodiment 4
疏水疏油PTFE膜的制备方法Preparation method of hydrophobic and oleophobic PTFE membrane
(1)制备防水拒油剂:在氮气保护下,将全氟辛基乙烯和三乙氧基硅烷按照摩尔比为1:1.15加入到二甲苯溶液中,在1‰Pt催化下90℃回流20h,过滤,真空度0.08Mpa,温度130℃下减压蒸馏除去溶剂,得全氟癸基三乙氧基硅烷。其原理为硅氢化反应,含Si-H硅化合物与不饱和有机化合物发生加成反应,生成有机硅化合物。(1) Preparation of waterproof and oil-repellent agent: Under nitrogen protection, add perfluorooctylethylene and triethoxysilane to the xylene solution at a molar ratio of 1:1.15, and reflux at 90°C for 20 hours under the catalysis of 1‰Pt. , filtered, with a vacuum degree of 0.08Mpa, and the solvent was distilled under reduced pressure at a temperature of 130°C to obtain perfluorodecyltriethoxysilane. The principle is a hydrosilylation reaction, in which Si-H-containing silicon compounds react with unsaturated organic compounds to form organosilicon compounds.
(2)混料:将聚四氟乙烯树脂粉末、航空煤油、交联剂混合搅拌3h后,加入防水拒油剂继续混合搅拌12h,并于60Hz超声处理3h,超声频率60Hz,制得混料A。其中聚四氟乙烯树脂为经300目筛网筛分后的聚四氟乙烯颗粒,交联剂包括聚异氰酸酯和聚乙烯醇缩丁醛,聚异氰酸酯和聚乙烯醇缩丁醛的质量比为1:1。聚四氟乙烯树脂的质量为混料A质量的69%,航空煤油的质量为混料A质量的10%,交联剂的质量为混料A质量的3%,防水拒油剂的质量为混料A质量的18%。所述防水拒油剂为步骤(1)制备的硅烷类防水拒油剂。(2) Mixing: After mixing polytetrafluoroethylene resin powder, aviation kerosene, and cross-linking agent for 3 hours, add a waterproof and oil-repellent agent and continue mixing and stirring for 12 hours, and ultrasonic treatment at 60 Hz for 3 hours at an ultrasonic frequency of 60 Hz to prepare the mixture. A. The polytetrafluoroethylene resin is polytetrafluoroethylene particles that have been screened through a 300-mesh screen. The cross-linking agent includes polyisocyanate and polyvinyl butyral. The mass ratio of polyisocyanate and polyvinyl butyral is 1 :1. The mass of polytetrafluoroethylene resin is 69% of the mass of mixture A, the mass of aviation kerosene is 10% of the mass of mixture A, the mass of cross-linking agent is 3% of the mass of mixture A, and the mass of waterproof and oil-repellent agent is 18% of the mass of Mixture A. The waterproof and oil-repellent agent is the silane-based waterproof and oil-repellent agent prepared in step (1).
(2)挤出:将混料A通过挤出机挤出呈柱状模料,挤出压力为8MPa,出速率为400mm/min。(2) Extrusion: Extrude mixture A through an extruder into a columnar mold material, with an extrusion pressure of 8MPa and an output rate of 400mm/min.
(3)压延:将柱状模料经过压延机制成厚度为50μm的聚四氟乙烯膜片,压延机的圧延温度为70℃,压延速率为16m/min。压延成膜后继续加热,以去除航空煤油,加热温度为340℃。(3) Calendering: Pass the cylindrical mold material through a calender to form a polytetrafluoroethylene diaphragm with a thickness of 50 μm. The rolling temperature of the calender is 70°C, and the calendering speed is 16m/min. After calendering and film formation, heating is continued to remove aviation kerosene. The heating temperature is 340°C.
(4)双向拉伸:将脱除航空煤油后的聚四氟乙烯膜片同时进行横向及纵向拉伸。其中横向拉伸比为5倍,纵向拉伸比为8倍。(4) Biaxial stretching: The polytetrafluoroethylene diaphragm after removing aviation kerosene is stretched transversely and longitudinally at the same time. The transverse stretch ratio is 5 times, and the longitudinal stretch ratio is 8 times.
(5)热定型:将双向拉伸的PTFE薄膜进行热定型,制得疏水疏油PTFE膜。其中热定型温度为340℃,热定型时间15min。(5) Heat setting: Heat setting the biaxially stretched PTFE film to obtain a hydrophobic and oleophobic PTFE film. The heat setting temperature is 340°C and the heat setting time is 15 minutes.
(6)收卷成膜:将热定型后的PTFE薄膜进行收卷,疏水疏油PTFE膜的厚度为5-8μm。(6) Rolling to form a film: Roll up the heat-set PTFE film. The thickness of the hydrophobic and oleophobic PTFE film is 5-8 μm.
疏水疏油PTFE覆膜复合滤料的制备:Preparation of hydrophobic and oleophobic PTFE-coated composite filter material:
(1)制备复合滤料:复合滤料包括依次层叠的面层、基布层和底层,通过针刺机械将基布层固定在面层和底层之间,再经过压光烧毛处理,压光温度250℃,热压压力为0.35MPa,热压时间为3s,制得针刺毡,即为复合滤料。其中面层采用聚苯硫醚纤维与聚四氟乙烯纤维混纺,底层采用聚苯硫醚纤维与聚四氟乙烯纤维,聚苯硫醚纤维与聚四氟乙烯纤维的质量比为2:1,纤维经过开松混合、梳理、铺网获得均匀的纤维网,基布层为聚四氟乙烯纱线经纬交织形成的网状结构。(1) Preparation of composite filter material: The composite filter material includes a surface layer, a base fabric layer and a bottom layer laminated in sequence. The base fabric layer is fixed between the surface layer and the bottom layer through a needle punching machine, and then undergoes calendering and singeing treatment. The light temperature is 250°C, the hot pressing pressure is 0.35MPa, and the hot pressing time is 3 seconds. The needle punched felt is obtained, which is the composite filter material. The surface layer is made of a blend of polyphenylene sulfide fiber and polytetrafluoroethylene fiber, and the bottom layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber. The mass ratio of polyphenylene sulfide fiber to polytetrafluoroethylene fiber is 2:1. The fibers are opened, mixed, carded, and laid to obtain a uniform fiber network. The base fabric layer is a network structure formed by interweaving the warp and weft of polytetrafluoroethylene yarns.
(2)将本实施例中制得的疏水疏油PTFE膜热压在复合滤料表面,热压温度为330℃,热压压力为0.8MPa,热压时间为6s,制得疏水疏油PTFE覆膜复合滤料。(2) Hot-press the hydrophobic and oleophobic PTFE membrane prepared in this example on the surface of the composite filter material. The hot-pressing temperature is 330°C, the hot-pressing pressure is 0.8MPa, and the hot-pressing time is 6 seconds to prepare hydrophobic and oleophobic PTFE. Coated composite filter material.
对比例Comparative ratio
疏水疏油PTFE膜的制备方法Preparation method of hydrophobic and oleophobic PTFE membrane
(1)混料:将聚四氟乙烯树脂粉末、航空煤油、聚异氰酸酯混合搅拌5h后,加入去离子水继续混合搅拌10h,并超声处理2h,超声频率50Hz,制得混料A。其中聚四氟乙烯树脂为经300目筛网筛分后的聚四氟乙烯颗粒,聚四氟乙烯树脂的质量为混料A质量的69%,航空煤油的质量为混料A质量的10%,聚异氰酸酯的质量为混料A质量的3%,去离子水为混料A质量的18%。(1) Mixing: After mixing polytetrafluoroethylene resin powder, aviation kerosene, and polyisocyanate for 5 hours, add deionized water and continue mixing and stirring for 10 hours, and ultrasonic treatment for 2 hours at an ultrasonic frequency of 50 Hz to prepare Mixture A. The polytetrafluoroethylene resin is polytetrafluoroethylene particles that have been screened with a 300-mesh screen. The mass of polytetrafluoroethylene resin is 69% of the mass of mixture A, and the mass of aviation kerosene is 10% of the mass of mixture A. , the mass of polyisocyanate is 3% of the mass of Mixture A, and the deionized water is 18% of the mass of Mixture A.
(2)挤出:将混料A通过挤出机挤出呈柱状模料,挤出压力为6MPa,出速率为300mm/min。(2) Extrusion: Extrude mixture A through an extruder into a columnar mold material, with an extrusion pressure of 6MPa and an output rate of 300mm/min.
(3)压延:将柱状模料经过压延机制成厚度为40μm的聚四氟乙烯膜片,压延机的圧延温度为60℃,压延速率为15m/min。压延成膜后继续加热,以去除航空煤油,加热温度为320℃。(3) Calendering: Pass the cylindrical mold material through a calender to form a polytetrafluoroethylene diaphragm with a thickness of 40 μm. The rolling temperature of the calender is 60°C, and the calendering speed is 15m/min. After calendering and film formation, heating is continued to remove aviation kerosene. The heating temperature is 320°C.
(4)双向拉伸:将脱除航空煤油后的聚四氟乙烯膜片同时进行横向及纵向拉伸。其中横向拉伸比为4倍,纵向拉伸比为6倍。(4) Biaxial stretching: The polytetrafluoroethylene diaphragm after removing aviation kerosene is stretched transversely and longitudinally at the same time. The transverse stretch ratio is 4 times, and the longitudinal stretch ratio is 6 times.
(5)热定型:将双向拉伸的PTFE薄膜进行热定型,制得疏水疏油PTFE膜。其中热定型温度为330℃,热定型时间8min。(5) Heat setting: Heat setting the biaxially stretched PTFE film to obtain a hydrophobic and oleophobic PTFE film. The heat setting temperature is 330°C and the heat setting time is 8 minutes.
(6)收卷成膜:将热定型后的PTFE薄膜进行收卷,疏水疏油PTFE膜的厚度为5-8μm。(6) Rolling to form a film: Roll up the heat-set PTFE film. The thickness of the hydrophobic and oleophobic PTFE film is 5-8 μm.
疏水疏油PTFE覆膜复合滤料的制备:Preparation of hydrophobic and oleophobic PTFE-coated composite filter material:
(1)制备复合滤料:复合滤料包括依次层叠的面层、基布层和底层,通过针刺机械将基布层固定在面层和底层之间,再经过压光烧毛处理,压光温度250℃,热压压力为0.35MPa,热压时间为3s,制得针刺毡,即为复合滤料。其中面层采用聚苯硫醚纤维与聚四氟乙烯纤维混纺,底层采用聚苯硫醚纤维与聚四氟乙烯纤维,聚苯硫醚纤维与聚四氟乙烯纤维的质量比为2:1,纤维经过开松混合、梳理、铺网获得均匀的纤维网,基布层为聚四氟乙烯纱线经纬交织形成的网状结构。(1) Preparation of composite filter material: The composite filter material includes a surface layer, a base fabric layer and a bottom layer laminated in sequence. The base fabric layer is fixed between the surface layer and the bottom layer through a needle punching machine, and then undergoes calendering and singeing treatment. The light temperature is 250°C, the hot pressing pressure is 0.35MPa, and the hot pressing time is 3 seconds. The needle punched felt is obtained, which is the composite filter material. The surface layer is made of a blend of polyphenylene sulfide fiber and polytetrafluoroethylene fiber, and the bottom layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber. The mass ratio of polyphenylene sulfide fiber to polytetrafluoroethylene fiber is 2:1. The fibers are opened, mixed, carded, and laid to obtain a uniform fiber network. The base fabric layer is a network structure formed by interweaving the warp and weft of polytetrafluoroethylene yarns.
(2)将本实施例中制得的疏水疏油PTFE膜热压在复合滤料表面,热压温度为260℃,热压压力为0.5MPa,热压时间为4s,制得PTFE复合滤料。(2) Hot-press the hydrophobic and oleophobic PTFE membrane prepared in this example on the surface of the composite filter material. The hot-pressing temperature is 260°C, the hot-pressing pressure is 0.5MPa, and the hot-pressing time is 4 s to prepare the PTFE composite filter material. .
对实施例1-实施例3、对比例中制得的复合滤料的性能进行测定。The properties of the composite filter materials prepared in Examples 1 to 3 and Comparative Examples were measured.
表1试验检测结果Table 1 Test results
采用标准《GBT4745-2012纺织品防水性能的检测和评价沾水法》、《GB/T19977-2014纺织品拒油性抗碳氢化合物试验》进行测定Measured using the standards "GBT4745-2012 Testing and Evaluation of Textile Waterproof Properties by Water Wet Method" and "GB/T19977-2014 Textile Oil Repellency and Hydrocarbon Resistance Test"
表2为实施例1-实施例3、对比例中制得的复合滤料的防水性能评价表Table 2 is the waterproof performance evaluation table of the composite filter materials prepared in Examples 1 to 3 and Comparative Examples.
从表2可以看出,实施例1制得的复合滤料其沾水等级为3级,实施例2制得的复合滤料其沾水等级为5级,实施例3制得的复合滤料其沾水等级为3级,对比例中制得的复合滤料的沾水等级为2级。当防水拒油剂的配比增加时,复合滤料的抗沾湿性能增强。It can be seen from Table 2 that the water-wetting grade of the composite filter material prepared in Example 1 is level 3, the water-wetting level of the composite filter material prepared in Example 2 is level 5, and the composite filter material prepared in Example 3 Its water-wetting grade is level 3, and the water-wetting grade of the composite filter material prepared in the comparative example is level 2. When the proportion of waterproof and oil-repellent agent is increased, the anti-wetting performance of the composite filter material is enhanced.
表3为实施例1-实施例3、对比例中制得的复合滤料的拒油性能评价表Table 3 is the oil repellent performance evaluation table of the composite filter materials prepared in Examples 1 to 3 and Comparative Examples.
从表3可以看出,实施例1制得的复合滤料其拒油等级为3级,实施例2制得的复合滤料其拒油等级为6级,实施例3制得的复合滤料其拒油等级为3级,对比例中制得的复合滤料的拒油等级为2级。当防水拒油剂的含量增加时,复合滤料的拒油等级增加。It can be seen from Table 3 that the oil repellency level of the composite filter material prepared in Example 1 is level 3, the oil repellency level of the composite filter material prepared in Example 2 is level 6, and the oil repellency level of the composite filter material prepared in Example 3 is level 6. The oil repellency level is level 3, and the oil repellency level of the composite filter material prepared in the comparative example is level 2. When the content of waterproof and oil-repellent agent increases, the oil-repellent grade of the composite filter material increases.
下面对上述技术方案的说明如下:The following description of the above technical solution is as follows:
本发明制得的疏水疏油PTFE膜具有良好的抵抗低表面张力液体的作用,从而保障了高粉尘工况下PTFE覆膜滤料长期运行,阻力也不会发生明显上升的情况。The hydrophobic and oleophobic PTFE membrane produced by the invention has good resistance to low surface tension liquids, thereby ensuring long-term operation of the PTFE-coated filter material under high dust conditions, and the resistance will not increase significantly.
当聚四氟乙烯树脂含量低于此60%时,会造成所得到的成品PTFE膜强度下降,影响其成膜性及使用寿命,试验过程中实际成膜率低于40%,当聚四氟乙烯树脂含量高于此69%时,会降低防水拒油等级及PTFE成品膜的透气性能,试验过程中实测防水小于3级,防油小于3级,透气量低于60mm/s(127Pa测试条件),防水拒油剂的含量低于15%时,成品PTFE膜的防水拒油性能会降低,试验过程中实测防水小于3级,防油小于2级,透气量低于50mm/s(127Pa测试条件),防水拒油剂的含量高于25%时,成品PTFE膜的强度会降低,试验过程中实测实际成膜率低于55%。When the polytetrafluoroethylene resin content is lower than this 60%, the strength of the finished PTFE membrane will be reduced, affecting its film-forming properties and service life. During the test, the actual film-forming rate was lower than 40%. When the vinyl resin content is higher than this 69%, it will reduce the waterproof and oil-repellent level and the breathability of the finished PTFE membrane. During the test, the actual waterproofing was less than level 3, the oil resistance was less than level 3, and the air permeability was lower than 60mm/s (127Pa test conditions ), when the content of waterproof and oil-repellent agent is less than 15%, the waterproof and oil-repellent performance of the finished PTFE membrane will be reduced. During the test, the actual measured waterproofness was less than level 3, the oil resistance was less than level 2, and the air permeability was less than 50mm/s (127Pa test Conditions), when the content of waterproof and oil-repellent agent is higher than 25%, the strength of the finished PTFE membrane will be reduced, and the actual film formation rate measured during the test was lower than 55%.
本发明制备的PTFE滤膜可用于空气过滤领域中,微孔结构明显,稳定性非常好,透气效果良好,具有很好的疏水疏油特性,适用于含油气体的气固分离。The PTFE filter membrane prepared by the invention can be used in the field of air filtration. It has obvious microporous structure, very good stability, good air permeability, good hydrophobic and oleophobic properties, and is suitable for gas-solid separation of oil-containing gases.
所述复合滤料包括面层、底层和基布层,所述面层采用聚苯硫醚纤维与聚四氟乙烯纤维混纺,所述底层采用聚苯硫醚纤维与聚四氟乙烯纤维,所述基布层为聚四氟乙烯纱线经纬交织形成的网状结构。所述基布层位于面层和底层之间,通过针刺机械将面层、基布层和底层固定,再经过压光烧毛处理,制得复合滤料。The composite filter material includes a surface layer, a bottom layer and a base fabric layer. The surface layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber blended, and the bottom layer is made of polyphenylene sulfide fiber and polytetrafluoroethylene fiber. The base fabric layer is a network structure formed by interlacing warp and weft of polytetrafluoroethylene yarns. The base fabric layer is located between the surface layer and the bottom layer. The surface layer, the base fabric layer and the bottom layer are fixed by acupuncture machinery, and then undergo a calendering and singeing treatment to obtain a composite filter material.
综上所述,实施例1制得的复合滤料其沾水等级为3级,实施例2制得的复合滤料其沾水等级为5级,实施例3制得的复合滤料其沾水等级为3级,对比例中制得的复合滤料的沾水等级为2级。当防水拒油剂的配比增加时,复合滤料的抗沾湿性能增强,实施例1制得的复合滤料其拒油等级为3级,实施例2制得的复合滤料其拒油等级为6级,实施例3制得的复合滤料其拒油等级为3级,对比例中制得的复合滤料的拒油等级为2级。当防水拒油剂的含量增加时,复合滤料的拒油等级增加。To sum up, the composite filter material prepared in Example 1 has a water-soaking grade of level 3, the composite filter material prepared in Example 2 has a water-wetting grade of level 5, and the composite filter material prepared in Example 3 has a water-soaking grade of The water level is level 3, and the water-wetting level of the composite filter material prepared in the comparative example is level 2. When the proportion of waterproof and oil-repellent agent is increased, the anti-wetting performance of the composite filter material is enhanced. The oil-repellent grade of the composite filter material prepared in Example 1 is level 3, and the oil-repellent grade of the composite filter material prepared in Example 2 is The oil repellency level of the composite filter material prepared in Example 3 is level 3, and the oil repellency level of the composite filter material prepared in the comparative example is level 2. When the content of waterproof and oil-repellent agent increases, the oil-repellent grade of the composite filter material increases.
以上实施例仅用以说明本发明的技术方案,而非对其限制。尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换。而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的精神和范围。The above embodiments are only used to illustrate the technical solution of the present invention, but not to limit it. Although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that they can still modify the technical solutions described in the foregoing embodiments, or make equivalent substitutions for some of the technical features. However, these modifications or substitutions do not cause the essence of the corresponding technical solution to deviate from the spirit and scope of the technical solution of each embodiment of the present invention.
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