CN101091883A - Equipment for manufacturing composite membrane filter of polytetrafluoroethylene - Google Patents
Equipment for manufacturing composite membrane filter of polytetrafluoroethylene Download PDFInfo
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- CN101091883A CN101091883A CN 200710067992 CN200710067992A CN101091883A CN 101091883 A CN101091883 A CN 101091883A CN 200710067992 CN200710067992 CN 200710067992 CN 200710067992 A CN200710067992 A CN 200710067992A CN 101091883 A CN101091883 A CN 101091883A
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- 239000002131 composite material Substances 0.000 title claims abstract description 148
- 229920001343 polytetrafluoroethylene Polymers 0.000 title claims abstract description 71
- 239000004810 polytetrafluoroethylene Substances 0.000 title claims abstract description 71
- 239000012528 membrane Substances 0.000 title claims abstract description 69
- -1 polytetrafluoroethylene Polymers 0.000 title claims abstract description 55
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 238000001816 cooling Methods 0.000 claims abstract description 68
- 238000010438 heat treatment Methods 0.000 claims abstract description 64
- 230000005540 biological transmission Effects 0.000 claims abstract description 31
- 239000000463 material Substances 0.000 claims abstract description 31
- 238000003825 pressing Methods 0.000 claims abstract description 25
- 150000001875 compounds Chemical class 0.000 claims description 15
- 238000001914 filtration Methods 0.000 claims description 10
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 229910052736 halogen Inorganic materials 0.000 claims description 5
- 150000002367 halogens Chemical class 0.000 claims description 5
- 238000012937 correction Methods 0.000 claims description 3
- 238000005096 rolling process Methods 0.000 claims 8
- 238000004804 winding Methods 0.000 abstract description 20
- 239000012982 microporous membrane Substances 0.000 abstract description 11
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical compound FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 abstract 1
- 238000013329 compounding Methods 0.000 description 15
- 238000000034 method Methods 0.000 description 14
- 239000004677 Nylon Substances 0.000 description 5
- 229920001778 nylon Polymers 0.000 description 5
- 230000035699 permeability Effects 0.000 description 5
- 239000004743 Polypropylene Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 239000004745 nonwoven fabric Substances 0.000 description 4
- 229920000728 polyester Polymers 0.000 description 4
- 229920001155 polypropylene Polymers 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 230000001070 adhesive effect Effects 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 238000010030 laminating Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005485 electric heating Methods 0.000 description 2
- 238000003475 lamination Methods 0.000 description 2
- 239000006247 magnetic powder Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004695 Polyether sulfone Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000004627 regenerated cellulose Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本发明公开了一种聚四氟乙烯支撑复合过滤膜的制造设备,包括送料收卷传动装置、压合装置和控制装置,送料收卷传动装置包括聚四氟乙烯微孔滤膜送料滚轴、支撑材料送料滚轴、复合膜收卷滚轴、聚四氟乙烯微孔滤膜送料传动滚辊、支撑材料送料传动滚辊和复合膜收卷传动滚辊,特点是压合装置由设置有转速控制装置的加热复合滚辊和冷却复合滚辊构成,加热复合滚辊和冷却复合滚辊两者中至少一个的轴上设置有压合压力传动装置,加热复合滚辊设置有加热装置,冷却复合滚辊设置有冷却装置,并均设置有测量滚辊表面温度的测温元件,使用本发明制造的支撑复合过滤膜,既可大大改善过滤膜材料的收缩性和成型性,又可保持聚四氟乙烯微孔滤膜原有的膜形态和结构。
The invention discloses a polytetrafluoroethylene-supported composite filter membrane manufacturing equipment, which includes a feeding and winding transmission device, a pressing device and a control device. The feeding and winding transmission device includes a polytetrafluoroethylene microporous filter membrane feeding roller, The supporting material feeding roller, the composite film winding roller, the polytetrafluoroethylene microporous filter membrane feeding driving roller, the supporting material feeding driving roller and the composite film winding driving roller are characterized in that the pressing device is equipped with a rotating speed The control device consists of a heating composite roller and a cooling composite roller, at least one of the shafts of the heating composite roller and the cooling composite roller is provided with a pressing pressure transmission device, the heating composite roller is provided with a heating device, and the cooling composite roller is equipped with a heating device. The rollers are provided with cooling devices, and are equipped with temperature measuring elements for measuring the surface temperature of the rollers. Using the supported composite filter membrane manufactured by the present invention can greatly improve the shrinkage and formability of the filter membrane material, and can also maintain the The original membrane shape and structure of vinyl fluoride microporous membrane.
Description
技术领域technical field
本发明涉及一种过滤膜制造设备,尤其是涉及一种聚四氟乙烯支撑复合过滤膜的制造设备。The invention relates to a filter membrane manufacturing equipment, in particular to a polytetrafluoroethylene supported composite filter membrane manufacturing equipment.
背景技术Background technique
聚四氟乙烯(PTFE)材料在高分子材料中,性能突出;耐高温,耐酸碱、有机溶剂,又具有无毒和生物相容性。拉伸成型的聚四氟乙烯微孔滤膜用于气体或液体过滤时,具有比其它高分子材料(如再生纤维素、尼龙、聚偏氟乙烯、聚醚砜)微孔滤膜更大的开孔率,更好的微粒阻截和耐久性等综合性能,是当前化工、医疗、食品、电子等领域有广泛用途的过滤材料。但在滤膜以摺叠滤芯形式实际应用前,需将滤膜进行折叠以增加膜面积提高透量,而单一的聚四氟乙烯(PTFE)微孔滤膜膜薄、质软、易变形,不能自支撑。这样滤膜在加工中需要一层或多层其它多孔材料的支撑才能成型,但是把聚四氟乙烯微孔滤膜直接与支撑材料一起折叠,不但折叠成型困难,废品率高,而且在应用中膜与支撑材料容易脱离,影响使用效果和使用周期。因此人们考虑将聚四氟乙烯微孔滤膜与支撑材料复合在一起,但现有公开的复合设备主要采用纺织行业中广泛应用的涂胶连续复合纺织面辅料设备、塑料超声焊接设备,印刷行业应用的热压覆膜设备。但以上设备和方法对于具有高熔点、不粘接特性的聚四氟乙烯(PTFE)微孔滤膜都具有较大的缺陷,一般的胶粘剂会堵塞微孔,大大降低膜的有效过滤面积及制品的透气性能,而使用特殊的胶粘剂或可热熔性材料在合成和加工工艺上又很复杂。支撑材料与聚四氟乙烯微孔膜表面经常发生层合不够牢固,大大降低使用寿命,或支撑材料被熔化而造成废品等,复合效果难以达到高端应用需求。Among polymer materials, polytetrafluoroethylene (PTFE) material has outstanding performance; high temperature resistance, acid and alkali resistance, organic solvent, non-toxic and biocompatibility. When the stretched polytetrafluoroethylene microporous membrane is used for gas or liquid filtration, it has a larger microporous membrane than other polymer materials (such as regenerated cellulose, nylon, polyvinylidene fluoride, polyethersulfone). Open porosity, better particle interception and durability and other comprehensive properties, are currently widely used filter materials in chemical, medical, food, electronics and other fields. However, before the filter membrane is actually applied in the form of a folded filter element, the filter membrane needs to be folded to increase the membrane area and increase the permeability, and the single polytetrafluoroethylene (PTFE) microporous filter membrane is thin, soft, and easily deformed. Not self-supporting. In this way, the filter membrane needs to be supported by one or more layers of other porous materials to be formed during processing. However, if the polytetrafluoroethylene microporous filter membrane is directly folded with the support material, it is not only difficult to fold and form, but also has a high reject rate. Membrane and supporting material are easy to separate, affecting the use effect and service cycle. Therefore, people consider compounding polytetrafluoroethylene microporous filter membranes and supporting materials, but the existing disclosed composite equipment mainly adopts glue-coated continuous composite textile surface accessories equipment, plastic ultrasonic welding equipment, and printing industry widely used in the textile industry. Applied hot press lamination equipment. However, the above equipment and methods have relatively large defects for polytetrafluoroethylene (PTFE) microporous membranes with high melting point and non-adhesive properties. General adhesives will block the micropores, greatly reducing the effective filtration area of the membrane and the products. Breathable performance, and the use of special adhesives or heat-fusible materials is very complicated in synthesis and processing. The support material and the surface of the PTFE microporous membrane are often not laminated firmly enough, which greatly reduces the service life, or the support material is melted to cause waste, etc., and the composite effect is difficult to meet the needs of high-end applications.
发明内容Contents of the invention
本发明所要解决的技术问题是针对上述现有技术现状而提供一种聚四氟乙烯支撑复合过滤膜的制造设备,通过专用的制造设备能够有效地将支撑材料层合到聚四氟乙烯膜的表面上,不仅层合牢固,提高了产品的成品率和产品的使用寿命,而且不影响聚四氟乙烯微孔滤膜的透气性;本发明克服了单一聚四氟乙烯微孔滤膜不能自支撑、易变形,不利于折叠加工成常用的褶形滤芯的缺陷,并保持了原有的膜形态结构和膜的孔径,透气性影响甚少,而大大改善了过滤膜材料的收缩性和成型性。The technical problem to be solved by the present invention is to provide a manufacturing equipment for a polytetrafluoroethylene supported composite filter membrane in view of the above-mentioned current state of the art, and the support material can be effectively laminated to the polytetrafluoroethylene membrane through the special manufacturing equipment On the surface, not only the lamination is firm, but the yield of the product and the service life of the product are improved, and the air permeability of the polytetrafluoroethylene microporous filter membrane is not affected; the present invention overcomes that a single polytetrafluoroethylene microporous filter membrane cannot automatically Support, easy to deform, not conducive to folding and processing into the defects of commonly used pleated filter elements, and maintain the original membrane structure and membrane pore size, with little impact on air permeability, and greatly improve the shrinkage and molding of filter membrane materials sex.
本发明解决上述技术问题所采用的技术方案为:一种聚四氟乙烯支撑复合过滤膜的制造设备,包括送料收卷传动装置、压合装置和控制装置,所述的控制装置输出控制信号到所述的送料收卷传动装置和所述的压合装置,所述的送料收卷传动装置包括聚四氟乙烯微孔滤膜送料滚轴、支撑材料送料滚轴、复合膜收卷滚轴、聚四氟乙烯微孔滤膜送料传动滚辊、支撑材料送料传动滚辊和复合膜收卷传动滚辊,所述的压合装置由至少一个加热复合滚辊和与所述的加热复合滚辊相对的冷却复合滚辊构成,所述的加热复合滚辊和所述的冷却复合滚辊设置有转速控制装置,所述的加热复合滚辊和所述的冷却复合滚辊两者中至少一个的轴上设置有压合压力传动装置,所述的加热复合滚辊设置有加热装置,所述的冷却复合滚辊设置有冷却装置,所述的加热复合滚辊和所述的冷却复合滚辊均设置有测量滚辊表面温度的测温元件,所述的测温元件将测量信号输送到所述的控制装置。The technical scheme adopted by the present invention to solve the above-mentioned technical problems is: a kind of manufacturing equipment of polytetrafluoroethylene supported composite filter membrane, comprising a feeding and winding transmission device, a pressing device and a control device, and the control device outputs a control signal to The described feeding and winding transmission device and the described pressing device, the described feeding and winding transmission device includes a polytetrafluoroethylene microporous filter membrane feeding roller, a supporting material feeding roller, a composite film winding roller, PTFE microporous membrane feeding drive rollers, support material feeding drive rollers and composite film winding drive rollers, the pressing device consists of at least one heating composite roller and the heating composite roller The opposite cooling composite roller is formed, the heating composite roller and the cooling composite roller are provided with a speed control device, and at least one of the heating composite roller and the cooling composite roller The shaft is provided with a pressing pressure transmission device, the heating composite roller is provided with a heating device, the cooling composite roller is provided with a cooling device, and the heating composite roller and the cooling composite roller are both A temperature-measuring element is provided for measuring the surface temperature of the roller, and the temperature-measuring element sends a measurement signal to the control device.
所述的加热装置可以是设置于加热复合滚辊内部且均匀分布的多根卤素灯,也可以是以油、水、气为介质的电热管或加热元件,或是采用燃气、红外、微波、高频、辐射和蒸汽等方式进行加热的加热装置。加热装置可以设置在复合滚辊外部,也可以设置在复合滚辊内部或内外同时设置。The heating device can be a plurality of halogen lamps arranged inside the heating composite roller and evenly distributed, or an electric heating tube or a heating element with oil, water, or gas as the medium, or gas, infrared, microwave, etc. Heating devices for heating by means of high frequency, radiation and steam. The heating device can be arranged outside the composite roller, also can be arranged inside the composite roller or both inside and outside.
所述的冷却装置可以是在所述的冷却复合滚辊的一侧沿所述的冷却复合滚辊的轴向并列设置的多个风扇来进行强制风冷,也可以采用水冷或油冷的方式。在特定条件下,如当所处环境温度较低,合适的复合工艺参数使得冷却复合滚辊表面温度不需强制冷却也可稳定在所述方法要求的温度区间时,可不使用冷却装置。The cooling device can be a plurality of fans arranged side by side along the axial direction of the cooling composite roller on one side of the cooling composite roller for forced air cooling, or it can be water-cooled or oil-cooled. . Under certain conditions, such as when the ambient temperature is relatively low, and suitable compounding process parameters make the surface temperature of the cooling compound roll stable in the temperature range required by the method without forced cooling, the cooling device may not be used.
所述的测温元件可以是直接接触测量的热电偶,也可以是直接接触测量的热电阻,还可以是非接触式的红外测温元件。The temperature measuring element can be a thermocouple for direct contact measurement, a thermal resistance for direct contact measurement, or a non-contact infrared temperature measuring element.
所述的加热复合滚辊的表面最好包覆镜面不锈钢,而所述的冷却复合滚辊可以是在不锈钢内层外包覆橡胶外层。The surface of the heating composite roller is preferably coated with mirror-finished stainless steel, and the cooling composite roller can be coated with a rubber outer layer on the stainless steel inner layer.
所述的送料收卷传动装置还可以设置有张力和纠偏控制装置,如由磁粉张力控制机构、力矩电机与自动张力控制器组成。The feeding and winding transmission device can also be provided with a tension and deviation correction control device, such as composed of a magnetic powder tension control mechanism, a torque motor and an automatic tension controller.
与现有技术相比,本发明的优点在于通过设置在加热复合滚辊内的加热装置使与聚四氟乙烯微孔滤膜贴近的加热复合滚辊的表面温度高于支撑材料的熔点温度,而通过设置在冷却复合滚辊下方的冷却装置使与支撑材料贴近的冷却复合滚辊的表面温度低于支撑材料的热变形温度,这样能够将与聚四氟乙烯微孔滤膜粘合的支撑材料的表面部分熔化,既能够保证聚四氟乙烯微孔滤膜与支撑材料有效地粘合并复合为一体,又不致于将支撑材料全部熔化或使支撑材料热变形;使用本发明制造的聚四氟乙烯支撑复合过滤膜克服了单一聚四氟乙烯微孔滤膜不能自支撑、易变形,不利于折叠加工成常用的褶形滤芯的缺陷,并大大改善了过滤膜材料的收缩性和成型性;复合膜同样有着优良的耐溶剂、可高温灭菌的物化特性,复合设备的结构紧凑、复合参数可调节、能满足聚四氟乙烯微孔膜大批量连续复合的工业生产要求;将多根发热均匀的卤素灯均匀分布在滚辊内部,可以保证合理的升温速率及温度均匀性。根据生产要求,本发明设备既可结合在聚四氟乙烯微孔膜生产过程中的拉伸定型之后与收卷之前进行膜与支撑材料的在线复合,也可独立对聚四氟乙烯微孔膜复合。Compared with the prior art, the advantage of the present invention is that the surface temperature of the heating composite roller close to the polytetrafluoroethylene microporous filter membrane is higher than the melting point temperature of the supporting material by the heating device arranged in the heating composite roller, And make the surface temperature of the cooling composite roller close to the support material lower than the heat distortion temperature of the support material by the cooling device arranged below the cooling composite roller, so that the support bonded with the polytetrafluoroethylene microporous filter membrane can be Partial melting of the surface of the material can ensure that the polytetrafluoroethylene microporous filter membrane and the support material are effectively bonded and compounded into one, and will not completely melt the support material or cause the support material to be thermally deformed; The tetrafluoroethylene supported composite filter membrane overcomes the defect that a single PTFE microporous filter membrane cannot be self-supporting and easily deformed, which is not conducive to folding and processing into commonly used pleated filter elements, and greatly improves the shrinkage and molding of the filter membrane material The composite membrane also has excellent solvent resistance and high temperature sterilization properties. The composite equipment has a compact structure and adjustable composite parameters, which can meet the industrial production requirements of large-scale continuous composite of polytetrafluoroethylene microporous membranes; The halogen lamps with even heating are evenly distributed inside the roller, which can ensure a reasonable heating rate and temperature uniformity. According to the production requirements, the equipment of the present invention can be combined with the on-line compounding of the membrane and the support material after stretching and setting in the production process of the polytetrafluoroethylene microporous membrane and before winding, and can also independently complex.
采用本发明的设备,优化复合工艺条件进行连续化生产,获得的聚四氟乙烯(PTFE)支撑复合过滤膜性能稳定,干、湿状态的剥离强度高,与复合前的聚四氟乙烯(PTFE)微孔滤膜相比,一方面保持了膜的原有形态结构和孔径,另一方面透气性下降少,可保持在原有膜透气量的85%以上。Adopt equipment of the present invention, optimize composite process condition and carry out continuous production, the polytetrafluoroethylene (PTFE) that obtains supports composite filtration membrane performance is stable, the peeling strength of dry and wet state is high, and polytetrafluoroethylene (PTFE) before compounding ) microporous membrane, on the one hand, it maintains the original morphological structure and pore size of the membrane;
附图说明Description of drawings
图1为本发明实施例一的结构示意图;FIG. 1 is a schematic structural view of
图2为本发明实施例二的结构示意图;FIG. 2 is a schematic structural diagram of
图3为本发明压合装置与液压传动装置配合的结构示意图;Fig. 3 is a structural schematic diagram of the cooperation between the pressing device and the hydraulic transmission device of the present invention;
图4为本发明液压传动装置的结构示意图;Fig. 4 is the structural representation of hydraulic transmission device of the present invention;
图5为本发明压合装置及测温元件和控制装置的结构示意图;Fig. 5 is a structural schematic diagram of a pressing device, a temperature measuring element and a control device of the present invention;
图6为本发明风扇构成的冷却装置的结构示意图。Fig. 6 is a schematic structural diagram of a cooling device composed of a fan according to the present invention.
具体实施方式Detailed ways
以下结合附图实施例对本发明作进一步详细描述。The present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments.
实施例一:聚四氟乙烯支撑复合过滤膜使用的制造设备,其结构包括送料收卷传动装置1、压合装置2和控制装置3,控制装置3输出控制信号到送料收卷传动装置1和压合装置2,送料收卷传动装置1包括聚四氟乙烯微孔滤膜送料滚轴11、支撑材料送料滚轴12、复合膜收卷滚轴13、聚四氟乙烯微孔滤膜送料传动滚辊14、支撑材料送料传动滚辊15和复合膜收卷传动滚辊16,压合装置2由一个加热复合滚辊21和与加热复合滚辊21相对的冷却复合滚辊22上下排列构成,加热复合滚辊21的表面包覆有镜面不锈钢,冷却复合滚辊22是在不锈钢内层外包覆橡胶外层,加热复合滚辊21和冷却复合滚辊22由调速电机(未显示)带动转动,它们的转速由控制装置3输出到调速电机的控制信号来加以控制,冷却复合滚辊22的轴上设置有液压压力传动装置23,如图所示,液压压力传动装置23包括两块对称设置的竖直方向运动滑块231、压力表232、液压管路系统233和手动增压手柄234,加热复合滚辊21内部设置有由均匀分布的18根卤素灯构成的加热装置24,冷却复合滚辊22的下方沿冷却复合滚辊22的轴向并列设置有5个风扇构成了冷却装置25,加热复合滚辊21和冷却复合滚辊22均设置有测温元件热电偶26来测量滚辊表面的温度,温度测量信号输送到控制装置3,送料收卷传动装置1设置有由磁粉张力控制机构、力矩电机与自动张力控制器组成的张力和纠偏控制装置(未显示)。Embodiment 1: The manufacturing equipment used by polytetrafluoroethylene support composite filter membrane, its structure includes feeding and
实施例二:聚四氟乙烯支撑复合过滤膜使用的制造设备,基本结构与实施例一相同,不同之处为压合装置2由两个加热复合滚辊21和与加热复合滚辊21相对的两个冷却复合滚辊22上下排列构成。Embodiment two: the manufacturing equipment that polytetrafluoroethylene support composite filter membrane is used, basic structure is identical with embodiment one, and difference is that
上述实施例中,加热装置24无特别要求,可以是以油、水、气为介质的电热管,或采用燃气加热、红外加热、微波加热、高频加热、辐射加热、蒸汽加热等方式,加热装置24可以设置在加热复合滚辊21内部,也可以设置在加热复合滚辊21外部,或内外同时设置。In the above embodiments, the
冷却装置25无特别要求,也可以采用水冷或油冷的方式。There is no special requirement for the
测温元件热电偶26无特别要求,也可以用直接接触测量的热电阻或非接触式的红外测温元件来替代。The temperature measuring
控制装置3无特别要求,可以采用现有工业自动控制技术中与被控制的工艺参数相配的通用控制元件(如继电器、计时器、传感器、调节器、显示器)来实现,也可进一步通过数据采集转换控制通讯卡来实现计算机监控。The
以下实施例为采用上述设备,调节设备结构参数,进行聚四氟乙烯微孔膜的复合过程及应用。The following examples use the above-mentioned equipment, adjust the structural parameters of the equipment, and carry out the compounding process and application of the polytetrafluoroethylene microporous membrane.
实施例三:通过将聚四氟乙烯微孔滤膜与一层聚丙烯筛网叠合在一起制造而成,调节设备的参数,进行复合:①将设置在聚四氟乙烯微孔滤膜送料滚轴上的聚四氟乙烯微孔滤膜和设置在支撑材料送料滚轴上的聚丙烯筛网通过传动控制系统输送到由上下排列的加热复合滚辊和冷却复合滚辊构成的压合装置中,使聚四氟乙烯微孔滤膜与加热复合滚辊贴近,使聚丙烯筛网与冷却复合滚辊贴近;②通过由均匀设置在加热复合滚辊内的18根卤素灯构成的加热装置使加热复合滚辊的表面温度为300℃,通过设置在冷却复合滚辊下方沿冷却复合滚辊的轴向并列设置的5个风扇构成的冷却装置使冷却复合滚辊的表面温度为20℃;③通过设置在冷却复合滚辊轴上的液压压力传动装置以液压传递方式在加热复合滚辊和冷却复合滚辊之间提供3MPa的压合压力,将聚四氟乙烯微孔滤膜和聚丙烯筛网机械压合在一起;④通过控制调速电机的转速控制膜的复合线速度为5米/分钟;⑤通过复合膜收卷滚轴将复合后的支撑复合过滤膜卷绕到复合膜收卷滚辊上。Embodiment 3: It is manufactured by laminating a polytetrafluoroethylene microporous filter membrane with a layer of polypropylene screen, adjusting the parameters of the equipment, and compounding: ① Feed the polytetrafluoroethylene microporous filter membrane The polytetrafluoroethylene microporous filter membrane on the roller and the polypropylene screen set on the supporting material feeding roller are conveyed to the pressing device composed of heating composite rollers and cooling composite rollers arranged up and down through the transmission control system In the process, make the polytetrafluoroethylene microporous filter membrane close to the heating composite roller, and make the polypropylene screen mesh close to the cooling composite roller; ②Through the heating device composed of 18 halogen lamps evenly arranged in the heating composite roller Make the surface temperature of the heating composite roller be 300°C, and make the surface temperature of the cooling composite roller be 20°C by being arranged under the cooling composite roller along the cooling device composed of 5 fans arranged side by side in the axial direction of the cooling composite roller; ③Through the hydraulic pressure transmission device set on the shaft of the cooling composite roller, a pressing pressure of 3 MPa is provided between the heating composite roller and the cooling composite roller in the form of hydraulic transmission, and the polytetrafluoroethylene microporous filter membrane and polypropylene The screens are mechanically pressed together; ④ Control the composite linear speed of the membrane to 5 m/min by controlling the speed of the speed-regulating motor; Roll on a roll.
实施例四:调节设备的参数,进行复合。基本工艺与实施例三相同,不同之处是在步骤②中加热复合滚辊的表面温度为180℃,冷却复合滚辊的表面温度为85℃,步骤③中加热复合滚辊和冷却复合滚辊之间的压合压力为20MPa,步骤④中复合线速度为15米/分钟。Embodiment 4: Adjusting the parameters of the equipment and compounding. The basic process is the same as in Example 3, except that the surface temperature of the heated composite roll is 180°C in
实施例五:调节设备的参数,进行复合。基本工艺与实施例三相同,不同之处是在步骤②中加热复合滚辊的表面温度为230℃,冷却复合滚辊的表面温度为40℃,步骤③中加热复合滚辊和冷却复合滚辊之间的压合压力为10MPa,步骤④中复合线速度为30米/分钟。Embodiment 5: Adjusting the parameters of the equipment and compounding. The basic process is the same as in Example 3, except that the surface temperature of the heated composite roll is 230°C in
实施例六:通过将聚四氟乙烯微孔滤膜与一层聚酯无纺布叠合在一起制造而成,调节设备的参数,进行复合:①将设置在聚四氟乙烯微孔滤膜送料滚轴上的聚四氟乙烯微孔滤膜和设置在支撑材料送料滚轴上的聚酯无纺布通过传动控制系统输送到由上下排列的加热复合滚辊和冷却复合滚辊构成的压合装置中,使聚四氟乙烯微孔滤膜与加热复合滚辊贴近,使聚酯无纺布与冷却复合滚辊贴近;②通过由均匀设置在加热复合滚辊内的16根卤素灯构成的加热装置使加热复合滚辊的表面温度为270℃,通过设置在冷却复合滚辊下方沿冷却复合滚辊的轴向并列设置的4个风扇构成的冷却装置使冷却复合滚辊的表面温度为15℃;③通过设置在冷却复合滚辊轴上的液压压力传动装置以液压传递方式在加热复合滚辊和冷却复合滚辊之间提供5MPa的压合压力,将聚四氟乙烯微孔滤膜和聚酯无纺布机械压合在一起;④通过控制调速电机的转速控制膜的复合线速度为5米/分钟;⑤通过复合膜收卷滚轴将复合后的支撑复合过滤膜卷绕到复合膜收卷滚辊上。Embodiment 6: It is manufactured by laminating a polytetrafluoroethylene microporous filter membrane with a layer of polyester non-woven fabric, adjusting the parameters of the equipment, and compounding: ① place the polytetrafluoroethylene microporous filter membrane The polytetrafluoroethylene microporous filter membrane on the feeding roller and the polyester non-woven fabric set on the supporting material feeding roller are transported to the press composed of heating composite rollers and cooling composite rollers arranged up and down through the transmission control system. In the combined device, the polytetrafluoroethylene microporous filter membrane is brought close to the heating compound roller, and the polyester non-woven fabric is brought close to the cooling compound roller; The heating device makes the surface temperature of the heating composite roller be 270 ℃, and the cooling device composed of 4 fans arranged side by side along the axial direction of the cooling composite roller under the cooling composite roller makes the surface temperature of the cooling composite roller be 15°C; ③A pressing pressure of 5 MPa is provided between the heating composite roller and the cooling composite roller through the hydraulic pressure transmission device set on the cooling composite roller shaft, and the polytetrafluoroethylene microporous filter membrane Press together with polyester non-woven fabric mechanically; ④ Control the composite line speed of the membrane by controlling the speed of the speed-regulating motor to 5 m/min; ⑤ Wind the composite support composite filter membrane through the composite membrane winding roller To the composite film take-up roll.
实施例七:调节设备的参数,进行复合。基本工艺与实施例六相同,不同之处是在步骤②中加热复合滚辊的表面温度为290℃,冷却复合滚辊的表面温度为60℃,步骤③中加热复合滚辊和冷却复合滚辊之间的压合压力为17MPa,步骤④中复合线速度为12米/分钟。Embodiment 7: Adjusting the parameters of the equipment and compounding. The basic process is the same as in Example 6, except that the surface temperature of the heated composite roll in
实施例八:调节设备的参数,进行复合。基本工艺与实施例六相同,不同之处是在步骤②中加热复合滚辊的表面温度为300℃,冷却复合滚辊的表面温度为40℃,步骤③中加热复合滚辊和冷却复合滚辊之间的压合压力为9MPa,步骤④中复合线速度为28米/分钟。Embodiment 8: Adjusting the parameters of the equipment and compounding. The basic process is the same as in Example 6, except that the surface temperature of the heated composite roll is 300°C in
实施例九:通过将聚四氟乙烯微孔滤膜与一层尼龙筛网叠合在一起制造而成,调节设备的参数,进行复合:①将设置在聚四氟乙烯微孔滤膜送料滚轴上的聚四氟乙烯微孔滤膜和设置在支撑材料送料滚轴上的尼龙筛网通过传动控制系统输送到由上下排列的加热复合滚辊和冷却复合滚辊构成的压合装置中,使聚四氟乙烯微孔滤膜与加热复合滚辊贴近,使尼龙筛网与冷却复合滚辊贴近;②通过由均匀设置在加热复合滚辊内的16根卤素灯构成的加热装置使加热复合滚辊的表面温度为300℃,通过设置在冷却复合滚辊下方沿冷却复合滚辊的轴向并列设置的4个风扇构成的冷却装置使冷却复合滚辊的表面温度为10℃;③通过设置在冷却复合滚辊轴上的液压压力传动装置以液压传递方式在加热复合滚辊和冷却复合滚辊之间提供5.0MPa的压合压力,将聚四氟乙烯微孔滤膜和尼龙筛网机械压合在一起;④通过控制调速电机的转速控制膜的复合线速度为30米/分钟;⑤通过复合膜收卷滚轴将复合后的支撑复合过滤膜卷绕到复合膜收卷滚辊上。Embodiment 9: Manufactured by laminating a polytetrafluoroethylene microporous filter membrane with a layer of nylon screen, adjusting the parameters of the equipment, and compounding: ① put the polytetrafluoroethylene microporous filter membrane on the feeding roller The polytetrafluoroethylene microporous filter membrane on the shaft and the nylon screen set on the supporting material feeding roller are transported to the pressing device composed of heating composite rollers and cooling composite rollers arranged up and down through the transmission control system. Make the polytetrafluoroethylene microporous filter membrane close to the heating composite roller, and make the nylon screen mesh close to the cooling composite roller; The surface temperature of the roller is 300°C, and the cooling device composed of four fans arranged side by side along the axial direction of the cooling composite roller is arranged under the cooling composite roller to make the surface temperature of the cooling composite roller 10°C; ③ by setting The hydraulic pressure transmission device on the cooling composite roller shaft provides a pressing pressure of 5.0MPa between the heating composite roller and the cooling composite roller in a hydraulic transmission mode, and the polytetrafluoroethylene microporous filter membrane and the nylon screen are mechanically Press together; ④ Control the composite line speed of the membrane to 30 m/min by controlling the speed of the speed-regulating motor; ⑤ Wind the composite supporting composite filter membrane to the composite membrane winding roller through the composite membrane winding roller superior.
实施例十:调节设备的参数,进行复合。基本工艺与实施例九相同,不同之处是在步骤②中加热复合滚辊的表面温度为250℃,冷却复合滚辊的表面温度为30℃,步骤③中加热复合滚辊和冷却复合滚辊之间的压合压力为20MPa,步骤④中复合线速度为1米/分钟。Embodiment 10: Adjusting the parameters of the equipment and compounding. The basic process is the same as in Example 9, except that the surface temperature of the heated composite roll is 250°C in
实施例十一:调节设备的参数,进行复合。基本工艺与实施例九相同,不同之处是在步骤②中加热复合滚辊的表面温度为225℃,冷却复合滚辊的表面温度为40℃,步骤③中加热复合滚辊和冷却复合滚辊之间的压合压力为10MPa,步骤④中复合线速度为10米/分钟。Embodiment 11: Adjusting the parameters of the equipment and compounding. The basic process is the same as in Example 9, except that the surface temperature of the heated composite roll is 225°C in
采用本发明的设备,调节设备的参数,进行复合连续化生产,获得的聚四氟乙烯(PTFE)支撑复合过滤膜性能稳定,干、湿状态的剥离强度高,与复合前的聚四氟乙烯(PTFE)微孔滤膜相比,一方面保持了膜的原有形态结构和孔径,另一方面透气性下降少,可保持在原有膜透气量的85%以上。Adopt the equipment of the present invention, adjust the parameter of equipment, carry out composite continuous production, the performance of polytetrafluoroethylene (PTFE) supporting composite filtration membrane obtained is stable, the peeling strength of dry and wet state is high, and the polytetrafluoroethylene before compounding Compared with (PTFE) microporous membrane, on the one hand, it maintains the original morphology and pore size of the membrane, and on the other hand, the air permeability decreases less, and can maintain more than 85% of the original membrane air permeability.
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CN101091883B (en) | 2011-02-09 |
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