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CN108824067A - A kind of p-aramid paper and preparation method thereof - Google Patents

A kind of p-aramid paper and preparation method thereof Download PDF

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CN108824067A
CN108824067A CN201810562334.6A CN201810562334A CN108824067A CN 108824067 A CN108824067 A CN 108824067A CN 201810562334 A CN201810562334 A CN 201810562334A CN 108824067 A CN108824067 A CN 108824067A
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paper
aramid
wet paper
para
drying
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CN108824067B (en
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马韵升
庹新林
陈梅梅
刘振学
张云奎
董志荣
刘余田
韩立霞
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Tsinghua University
Chambroad Chemical Industry Research Institute Co Ltd
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Chambroad Chemical Industry Research Institute Co Ltd
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H13/00Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
    • D21H13/10Organic non-cellulose fibres
    • D21H13/20Organic non-cellulose fibres from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H13/26Polyamides; Polyimides

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  • Chemical Kinetics & Catalysis (AREA)
  • Paper (AREA)

Abstract

本发明提供了一种对位芳纶纸的制备方法,包括:将对位芳纶纳米纤维料液进行上网成型,得到湿纸张;将湿纸张进行多级缓冲压榨脱水,得到脱水后的湿纸张;将脱水后的湿纸张依次进行多级低温烘干和张力辅助干燥进行干燥成型,得到对位芳纶纸;所述上网成型的方法为:将对位芳纶纳米纤维料液上浆后滤水,在成型网表面形成湿纸胚;对湿纸胚的下表面进行真空抽吸然后用上顶网成型器对湿纸胚的上表面进行脱水相结合的方式进行双向脱水,得到湿纸张。本发明采用特殊的上网成型工艺、多级缓冲压榨工艺、多级低温烘干工艺及张力辅助干燥工艺能够制备得到均匀性好、力学性能和绝缘性能优异的芳纶纸。本发明还提供了一种对位芳纶纸。The invention provides a preparation method of para-aramid paper, comprising: forming the para-aramid nanofiber material liquid on the net to obtain wet paper; dehydrating the wet paper by multi-stage buffer pressing to obtain dehydrated wet paper The dehydrated wet paper is sequentially subjected to multi-stage low-temperature drying and tension-assisted drying for drying and molding to obtain para-aramid paper; the method of online molding is: sizing the para-aramid nanofiber material liquid and then filtering , forming a wet paper embryo on the surface of the forming wire; vacuuming the lower surface of the wet paper embryo and then dehydrating the upper surface of the wet paper embryo with an upper top wire former for two-way dehydration to obtain wet paper. The present invention adopts a special net forming process, a multi-stage buffer pressing process, a multi-stage low-temperature drying process and a tension-assisted drying process to prepare the aramid paper with good uniformity, excellent mechanical properties and insulating properties. The invention also provides a para-aramid paper.

Description

一种对位芳纶纸及其制备方法A kind of para-aramid fiber paper and preparation method thereof

技术领域technical field

本发明涉及膜材料技术领域,尤其涉及一种对位芳纶纸及其制备方法。The invention relates to the technical field of film materials, in particular to a para-aramid paper and a preparation method thereof.

背景技术Background technique

对位芳纶纸(PAP)是一种高性能的特种膜材料,具有高强高模、尺寸稳定性优异、电气绝缘性能优良、耐化学腐蚀、重量轻等优点,其可作为结构材料、绝缘材料、透波以及过滤材料等广泛用于航空航天、军事装备、电子电器等行业。Para-aramid paper (PAP) is a high-performance special film material, which has the advantages of high strength and high modulus, excellent dimensional stability, excellent electrical insulation performance, chemical corrosion resistance, and light weight. It can be used as structural materials, insulating materials , wave penetration and filter materials are widely used in aerospace, military equipment, electronic appliances and other industries.

目前用于制备PAP的原料主要是对位芳纶短纤、浆粕或沉析纤维,有时还加入间位芳纶或其他热塑性树脂作为增强剂。造纸的过程也较为复杂,一般需要经过特殊工艺将纤维打成浆料,需要加入分散剂提高浆料的分散性和稳定性。即便如此,也难以制备得到性能稳定的PAP。因为PAP厚度一般在数十微米(部分特殊用途的PAP厚度在100微米以上),而对位芳纶短纤维的直径在10微米左右,浆粕和沉析纤维的主要结构尺寸也在几百纳米到数微米,一旦浆料分散不匀,极易造成PAP的不均匀,进而使PAP性能不稳定。另外,加入间位芳纶纤维和分散助剂也会恶化PAP的性能。间位芳纶吸湿性较大,会引起PAP高湿度下的尺寸稳定性下降,难以满足高精度产品的要求。而分散剂的加入,一方面不利于PAP的介电性能,另一方面也会产生大量废水,导致污染环境或提高生产成本。At present, the raw materials used to prepare PAP are mainly para-aramid short fibers, pulp or precipitated fibers, and sometimes meta-aramid fibers or other thermoplastic resins are added as reinforcing agents. The process of papermaking is also relatively complicated. Generally, the fiber needs to be beaten into a slurry through a special process, and a dispersant needs to be added to improve the dispersion and stability of the slurry. Even so, it is difficult to prepare PAP with stable performance. Because the thickness of PAP is generally tens of microns (the thickness of some PAPs for special purposes is more than 100 microns), while the diameter of para-aramid short fibers is about 10 microns, and the main structural size of pulp and precipitated fibers is also several hundred nanometers Once the slurry is dispersed unevenly, it will easily cause uneven PAP, and then make the performance of PAP unstable. In addition, the addition of meta-aramid fibers and dispersing aids will also deteriorate the performance of PAP. Meta-aramid fiber has high hygroscopicity, which will cause the dimensional stability of PAP to decrease under high humidity, and it is difficult to meet the requirements of high-precision products. The addition of dispersants is not conducive to the dielectric properties of PAP on the one hand, and on the other hand, it will also generate a large amount of waste water, which will pollute the environment or increase production costs.

而且,采用全纳米纤维造纸过程中存在着脱水难,制备的湿纸张湿强度低,在干燥的过程中尺寸收缩大等难题,严重影响了制备得到的对位芳纶纸的性能。因此,研发一种高性能的PAP的制备工艺成为本领域技术人员亟待解决的问题。Moreover, in the papermaking process of using all-nanofibers, there are difficulties such as difficult dehydration, low wet strength of the prepared wet paper, and large dimensional shrinkage during the drying process, which seriously affects the performance of the prepared para-aramid paper. Therefore, developing a high-performance PAP preparation process has become an urgent problem to be solved by those skilled in the art.

发明内容Contents of the invention

有鉴于此,本发明的目的在于提供一种对位芳纶纸及其制备方法,本发明提供的对位芳纶纸的制备方法工艺简单而且制备得到的对位芳纶纸在力学及电学性能上均较为优异。In view of this, the object of the present invention is to provide a kind of para-aramid paper and preparation method thereof, the preparation method process of the para-aramid paper provided by the present invention is simple and the prepared para-aramid paper has excellent mechanical and electrical properties. All are excellent.

本发明提供了一种对位芳纶纸的制备方法,包括:The invention provides a preparation method of para-aramid paper, comprising:

将对位芳纶纳米纤维料液进行上网成型,得到湿纸张;Forming the p-aramid nanofiber material liquid on the Internet to obtain wet paper;

对所述湿纸张进行多级缓冲压榨脱水处理,得到脱水后的湿纸张;performing multi-stage buffer press dehydration on the wet paper to obtain dehydrated wet paper;

将所述脱水后的湿纸张进行干燥和压光成型,得到对位芳纶纸。The dehydrated wet paper is dried and calendered to obtain para-aramid paper.

在本发明中,所述对位芳纶纳米纤维料液中对位芳纶纳米纤维的直径优选为10~100nm,更优选为20~80nm,更优选为30~70nm,最优选为40~60nm;所述对位芳纶纳米纤维料液中对位芳纶纳米纤维的长度优选为100nm~1000μm,更优选为500nm~800μm,更优选为800nm~600μm,最优选为1μm~500μm。In the present invention, the diameter of the para-aramid nanofiber in the para-aramid nanofiber feed solution is preferably 10-100 nm, more preferably 20-80 nm, more preferably 30-70 nm, most preferably 40-60 nm The length of the para-aramid nanofibers in the para-aramid nanofiber feed liquid is preferably 100nm-1000μm, more preferably 500nm-800μm, more preferably 800nm-600μm, and most preferably 1μm-500μm.

在本发明中,所述对位芳纶纳米纤维料液中的溶剂优选为水,更优选为去离子水。在本发明中,所述芳纶纳米纤维料液的质量浓度优选为0.5~2.5%,更优选为1~2%,最优选为1.5%。In the present invention, the solvent in the para-aramid nanofiber feed solution is preferably water, more preferably deionized water. In the present invention, the mass concentration of the aramid nanofiber feed solution is preferably 0.5-2.5%, more preferably 1-2%, and most preferably 1.5%.

本发明对所述对位芳纶纳米纤维料液的制备方法没有特殊的限制,采用本领域技术人员熟知的方法制备得到对位芳纶纳米纤维料液即可。在本发明中,所述对位芳纶纳米纤维料液的制备方法优选为:The present invention has no special limitation on the preparation method of the para-aramid nanofiber feed solution, and the para-aramid nanofiber feed solution can be prepared by a method well known to those skilled in the art. In the present invention, the preparation method of the para-aramid nanofiber feed solution is preferably:

在氯化物和聚乙二醇的作用下,将对苯二胺和对苯二甲酰氯在N-甲基吡咯烷酮中进行缩聚反应,得到反应产物;Under the action of chloride and polyethylene glycol, p-phenylenediamine and terephthaloyl chloride are subjected to polycondensation reaction in N-methylpyrrolidone to obtain a reaction product;

将所述反应产物和溶剂混合后破碎,得到混合体系;The reaction product and the solvent are mixed and crushed to obtain a mixed system;

将所述混合体系和水混合后搅拌,得到对位芳纶纳米纤维料液。The mixing system and water are mixed and then stirred to obtain a para-aramid nanofiber feed liquid.

在本发明中,所述缩聚反应优选在保护性气体如氮气的保护下进行。In the present invention, the polycondensation reaction is preferably carried out under the protection of a protective gas such as nitrogen.

在本发明中,所述氯化物优选为氯化钙、氯化锂和氯化镁中的一种或几种;所述聚乙二醇的数均分子量优选为2000~2500,更优选为2100~2200。在本发明中,所述氯化物和聚乙二醇的质量比优选为(1~3):1,更优选为(1.5~2.5):1,最优选为2:1。在本发明中,所述氯化物和聚乙二醇能够减少纤维的絮聚,提高分子活性。In the present invention, the chloride is preferably one or more of calcium chloride, lithium chloride and magnesium chloride; the number average molecular weight of the polyethylene glycol is preferably 2000-2500, more preferably 2100-2200 . In the present invention, the mass ratio of the chloride to polyethylene glycol is preferably (1-3):1, more preferably (1.5-2.5):1, most preferably 2:1. In the present invention, the chloride and polyethylene glycol can reduce fiber flocculation and improve molecular activity.

在本发明中,优选先将氯化物和聚乙二醇混合溶解,然后向得到的溶解液中先加入对苯二胺,待其溶解后再加入对苯二甲酰氯进行所述缩聚反应。在本发明中,所述混合溶解的温度优选为80~120℃,更优选为90~110℃,最优选为100℃。In the present invention, it is preferred to mix and dissolve the chloride and polyethylene glycol first, then add p-phenylenediamine to the obtained solution, and then add terephthaloyl dichloride to carry out the polycondensation reaction after it dissolves. In the present invention, the mixing and dissolving temperature is preferably 80-120°C, more preferably 90-110°C, and most preferably 100°C.

在本发明中,所述缩聚反应优选在冰水浴中进行,维持反应体系的温度不超过70℃。在本发明中,所述缩聚反应优选在搅拌的条件下进行,所述搅拌的速度优选为1500~2500r/min,更优选为1800~2200r/min,最优选为2000r/min。In the present invention, the polycondensation reaction is preferably carried out in an ice-water bath, and the temperature of the reaction system should not exceed 70°C. In the present invention, the polycondensation reaction is preferably carried out under stirring conditions, and the stirring speed is preferably 1500-2500 r/min, more preferably 1800-2200 r/min, most preferably 2000 r/min.

在本发明中,所述缩聚反应进行到反应体系形成冻胶体并出现韦森堡效应时停止反应,得到反应产物。在本发明中,所述缩聚反应的温度优选为-15~0℃,更优选为-10~-5℃。In the present invention, the polycondensation reaction is stopped when the reaction system forms a jelly body and Weissenberg effect occurs to obtain a reaction product. In the present invention, the temperature of the polycondensation reaction is preferably -15 to 0°C, more preferably -10 to -5°C.

在本发明中,所述反应产物和溶剂的质量体积比优选为1g:(35~45)mL,更优选为1g:(38~42)mL,最优选为1g:40mL。在本发明中,所述溶剂优选为N-甲基吡咯烷酮或甲醇。In the present invention, the mass volume ratio of the reaction product to the solvent is preferably 1 g:(35-45) mL, more preferably 1 g:(38-42) mL, most preferably 1 g:40 mL. In the present invention, the solvent is preferably N-methylpyrrolidone or methanol.

在本发明中,所述破碎的设备优选为组织粉碎机,所述破碎的时间优选为4~6min,更优选为5min。In the present invention, the crushing equipment is preferably a tissue grinder, and the crushing time is preferably 4-6 minutes, more preferably 5 minutes.

在本发明中,将混合体系和水混合搅拌的设备优选为组织粉碎机,所述搅拌的时间优选为8~12min,更优选为10min。在本发明中,所述水优选为去离子水。In the present invention, the equipment for mixing and stirring the mixing system and water is preferably a tissue pulverizer, and the stirring time is preferably 8-12 minutes, more preferably 10 minutes. In the present invention, the water is preferably deionized water.

在本发明中,得到对位芳纶纳米纤维料液后优选将所述对位芳纶纳米纤维料液反复洗涤,脱除其中的杂质;所述洗涤的设备优选为高速离心机或连续逆流带式洗涤机。In the present invention, after obtaining the p-aramid nanofiber feed liquid, it is preferable to repeatedly wash the p-aramid nanofiber feed liquid to remove impurities therein; the washing equipment is preferably a high-speed centrifuge or a continuous countercurrent belt washing machine.

本发明优选采用上述特殊工艺制备的对位芳纶纳米纤维料液制备对位芳纶纸,这种对位芳纶纳米纤维料液的对位芳纶纳米纤维的直径低于100nm,采用这种纳米纤维料液制备对位芳纶纸的过程中无需进行打浆,也无需添加分散剂,而且制备得到的对位芳纶纸均匀性好,力学性能和绝缘性能优异;制备方法工艺简单,获得的对位芳纶纸性能好。The present invention preferably adopts the para-aramid nanofiber material solution prepared by the above-mentioned special process to prepare para-aramid paper, and the diameter of the para-aramid nanofiber in the para-aramid nanofiber material solution is lower than 100nm. In the process of preparing para-aramid paper from nanofiber material liquid, no beating is required, and no dispersant is added, and the prepared para-aramid paper has good uniformity, excellent mechanical properties and insulation properties; the preparation method is simple and the obtained Para-aramid paper has good performance.

在本发明中,所述上网成型优选为采用斜网成型或长网成型技术将对位芳纶纳米纤维料液喷射或涂布到网上成型;所述成型设备优选为斜网成型器或长网成型器。在本发明中,所述上网成型采用的成型网孔径优选为100~300目,更优选为150~250目,最优选为200目,以避免对位芳纶纳米纤维料液从网孔漏掉。在本发明中,所述上网成型的方法优选为:In the present invention, the online forming is preferably using inclined wire forming or fourdrinier forming technology to spray or coat the para-aramid nanofiber material liquid onto the online forming; the forming equipment is preferably an inclined wire former or fourdrinier shaper. In the present invention, the aperture diameter of the forming mesh used in the online forming is preferably 100-300 mesh, more preferably 150-250 mesh, most preferably 200 mesh, so as to avoid the para-aramid nanofiber material liquid from leaking from the mesh . In the present invention, the method for forming online is preferably:

将所述对位芳纶纳米纤维料液上浆后滤水,在成型网表面形成湿纸胚;After sizing the para-aramid nanofiber feed solution, water is filtered, and a wet paper embryo is formed on the surface of the forming wire;

对所述湿纸胚的下表面进行真空抽吸然后采用上顶网成型器对湿纸胚的上表面进行脱水相结合的方式进行双向脱水,得到湿纸张。The lower surface of the wet paper embryo is subjected to vacuum suction and then the upper surface of the wet paper embryo is dehydrated by an upper top wire former to perform bidirectional dehydration to obtain wet paper.

在本发明中,所述上浆优选采用温水上浆;所述温水上浆的温度优选为40~60℃。在本发明中,所述滤水的时间优选为20~30秒,更优选为22~28秒,最优选为24~26秒。本发明在成型布浆时采用温水上浆能够减少纤维间的团聚,提高滤水效率,使滤水时间由3~5min降低至20~30s,大大缩短了网部的长度,解决了全纳米对位芳纶纤维抄造车速低的问题。In the present invention, the sizing preferably adopts warm water sizing; the temperature of the warm water sizing is preferably 40-60°C. In the present invention, the time for filtering water is preferably 20-30 seconds, more preferably 22-28 seconds, and most preferably 24-26 seconds. The invention adopts warm water sizing when forming pulp, which can reduce the agglomeration between fibers, improve the water filtration efficiency, reduce the water filtration time from 3 to 5 minutes to 20 to 30 seconds, greatly shorten the length of the net part, and solve the problem of all-nano alignment The problem of low speed of aramid fiber papermaking.

在本发明中,所述真空抽吸的真空度优选为-0.01~-0.1MPa,更优选为-0.02~-0.09MPa,最优选为-0.03~-0.06MPa。在本发明中,优选先对湿纸胚的下表面进行真空抽吸脱水然后再采用上顶网成型器对湿纸胚的上表面进行脱水,本发明提供的脱水方法将真空抽吸和上顶网成型器脱水相结合,实现了湿纸胚的双向脱水。在本发明中,所述真空抽吸脱水的真空度优选随着湿纸胚干度的增加而逐渐增大;优选真空抽吸过程中随着湿纸胚的干度从3%增加到5%,真空抽吸的真空度从-0.01MPa增加到-0.1MPa。In the present invention, the degree of vacuum of the vacuum suction is preferably -0.01 to -0.1 MPa, more preferably -0.02 to -0.09 MPa, most preferably -0.03 to -0.06 MPa. In the present invention, it is preferable to carry out vacuum suction dehydration to the lower surface of the wet paper embryo first, and then use an upper top wire former to dehydrate the upper surface of the wet paper embryo. The dehydration method provided by the invention combines vacuum suction and upper top wire Combined with the dehydration of the wire former, the two-way dehydration of the wet paper embryo is realized. In the present invention, the vacuum degree of the vacuum suction dehydration is preferably gradually increased with the increase of the dryness of the wet paper embryo; preferably during the vacuum suction process, the dryness of the wet paper embryo increases from 3% to 5%. , the vacuum degree of vacuum suction increases from -0.01MPa to -0.1MPa.

在本发明中,经过上顶网成型器脱水后得到的湿纸张的干度优选为8~10%,更优选为8.5~9.5%,最优选为9%。In the present invention, the dryness of the wet paper obtained after being dehydrated by the upper top wire former is preferably 8-10%, more preferably 8.5-9.5%, and most preferably 9%.

本发明采用上述特殊的上网成型工艺制备对位芳纶纸,上述上网成型工艺采用底部真空抽吸和顶部成型器脱水相结合的脱水方式,优选采用逐级真空抽吸(即随着湿纸胚干度的增加而逐渐增加真空抽吸的真空度的方式)与上顶网成型器脱水相结合的脱水方式,能够使成型纸张的纤维搭接严密,使本发明制备得到的对位芳纶纸的力学性能和电气绝缘性能较好。The present invention adopts the above-mentioned special online forming process to prepare para-aramid paper. The above-mentioned online forming process adopts a dehydration method combining bottom vacuum suction and top former dehydration, and preferably adopts step-by-step vacuum suction (that is, as the wet paper embryo The increase of dryness gradually increases the vacuum degree of vacuum suction) and the dehydration method combined with the dehydration of the upper top wire former can make the fibers of the formed paper overlap tightly, and make the para-aramid paper prepared by the present invention The mechanical properties and electrical insulation properties are good.

在本发明中,由于湿纸张的强度偏低,本发明优选利用真空吸附转移的方法将其与成型网剥离。本发明采用多级缓冲压榨脱水对湿纸张进行脱水处理,这种方法能够有效减少含水率,提高脱水后的湿纸张的湿强度。在本发明中,所述多级缓冲压榨脱水即为随着脱水后的湿纸张的干度的增加逐渐增加压榨脱水的压力,所述多级缓冲压榨脱水的压榨级数指的是压榨压力增加的次数。在本发明中,所述多级缓冲压榨脱水的压榨级数优选为2~5级,更优选为3~5级,最优选为4~5级。在本发明中,优选随着脱水后的湿纸张的干度从10%增加到15%,多级缓冲压榨脱水的压榨压力从0.05MPa以0.05MPa的梯度增加到0.35MPa。In the present invention, since the strength of the wet paper is relatively low, the present invention preferably uses a vacuum adsorption transfer method to peel it from the forming net. The invention adopts multi-stage buffer press dehydration to dehydrate the wet paper, and this method can effectively reduce the moisture content and improve the wet strength of the dehydrated wet paper. In the present invention, the multi-stage buffer press dehydration means gradually increasing the press dewatering pressure with the increase of the dryness of the dehydrated wet paper. times. In the present invention, the number of pressing stages of the multi-stage buffer press dehydration is preferably 2-5 stages, more preferably 3-5 stages, and most preferably 4-5 stages. In the present invention, preferably as the dryness of the dehydrated wet paper increases from 10% to 15%, the pressing pressure of the multi-stage buffer press dewatering increases from 0.05 MPa to 0.35 MPa with a gradient of 0.05 MPa.

在本发明中,所述多级缓冲压榨脱水优选为真空压榨脱水,所述真空压榨脱水的真空度优选为-20~-40KPa,更优选为-25~-35KPa,最优选为-30KPa。在本发明中,所述多级缓冲压榨脱水过程中的毛布清洗用高压水压力优选为1.5~2.5MPa,更优选为1.8~2.2MPa,最优选为2MPa。In the present invention, the multi-stage buffer press dehydration is preferably vacuum press dehydration, and the vacuum degree of the vacuum press dehydration is preferably -20 ~ -40KPa, more preferably -25 ~ -35KPa, most preferably -30KPa. In the present invention, the pressure of the high-pressure water used for cleaning the felt during the multi-stage buffer press dehydration process is preferably 1.5-2.5 MPa, more preferably 1.8-2.2 MPa, and most preferably 2 MPa.

在本发明中,所述干燥为多级低温烘干和张力辅助干燥,本发明优选先采用多级低温烘干的工艺对纸张进行烘干,然后进行纸张定型,在进行纸张定型时采用张力辅助干燥工艺进一步干燥纸张。本发明采用这种特殊的多级低温烘干以及张力辅助干燥相结合的干燥工艺能够使纸张更好的干燥,同时避免干燥过程中产生较大的尺寸收缩,使制备得到的对位芳纶纸具有良好的均匀度、力学性能以及电学性能。In the present invention, the drying is multi-stage low-temperature drying and tension-assisted drying. In the present invention, the multi-stage low-temperature drying process is preferably used to dry the paper first, and then the paper is shaped, and the tension-assisted drying is used when the paper is shaped. The drying process further dries the paper. The present invention adopts this special drying process combining multi-stage low-temperature drying and tension-assisted drying to make the paper dry better, and at the same time avoid large size shrinkage during the drying process, so that the prepared para-aramid paper It has good uniformity, mechanical properties and electrical properties.

在本发明中,所述多级低温烘干指的是随着纸张干度的增加逐渐提高烘干的温度,所述多级低温烘干的级数指的是提高烘干温度的次数。在本发明中,所述多级低温烘干的级数优选为6~10级,更优选为7~10级,最优选为9~10级。在本发明中,所述多级低温烘干的烘干方法优选为蒸汽烘干、导热油加热多组烘缸烘干或者电磁加热辊烘干。在本发明中,优选随着纸张干度从12%增加到30%将烘干温度逐渐从60℃提高到120℃。In the present invention, the multi-stage low-temperature drying refers to gradually increasing the drying temperature with the increase of paper dryness, and the number of stages of the multi-stage low-temperature drying refers to the times of increasing the drying temperature. In the present invention, the number of stages of the multi-stage low-temperature drying is preferably 6-10, more preferably 7-10, and most preferably 9-10. In the present invention, the drying method of the multi-stage low-temperature drying is preferably steam drying, heat conduction oil heating multiple sets of drying cylinders or electromagnetic heating roller drying. In the present invention, it is preferable to gradually increase the drying temperature from 60°C to 120°C as the paper dryness increases from 12% to 30%.

在本发明中,优选当纸张干度达到30%后进行纸张定型,在纸张定型时采用张力辅助干燥,所述张力辅助干燥优选为采用张紧装置对纸张进行拉伸定型的同时对纸张进行加热干燥,避免纸张产生起皱、收缩的问题。在本发明中,所述张紧装置优选为张紧力大的干网,所述张力辅助干燥的张力优选为4~10KN/m,更优选为6~9KN/m,最优选为6.5~8KN/m。在本发明中,所述加热干燥的方法优选为采用大辊径烘缸直接加热。在本发明中,所述张力辅助干燥的温度优选为120~160℃,更优选为130~150℃,最优选为135~145℃。在本发明中,所述张力辅助干燥的时间优选为0.5~15min,更优选为1~10min,更优选为2~8min,最优选为3~6min。In the present invention, it is preferable to carry out paper setting after the dryness of the paper reaches 30%, and use tension-assisted drying when the paper is fixed, and the tension-assisted drying is preferably to use a tensioning device to stretch and set the paper while heating the paper Dry to avoid paper wrinkling and shrinkage. In the present invention, the tensioning device is preferably a drying net with a large tension force, and the tension of the tension-assisted drying is preferably 4-10KN/m, more preferably 6-9KN/m, most preferably 6.5-8KN /m. In the present invention, the method of heating and drying is preferably direct heating by using a large-diameter drying cylinder. In the present invention, the temperature of the tension-assisted drying is preferably 120-160°C, more preferably 130-150°C, and most preferably 135-145°C. In the present invention, the tension-assisted drying time is preferably 0.5-15 min, more preferably 1-10 min, more preferably 2-8 min, most preferably 3-6 min.

本发明对所述压光成型的方法没有特殊的限制,采用本领域技术人员熟知的在制备对位芳纶纸时采用的常规的压光成型的技术方案即可。The present invention has no special limitation on the calendering forming method, and the conventional calendering forming technical solution well-known to those skilled in the art when preparing para-aramid paper can be used.

具体实施方式Detailed ways

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,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员经改进或润饰的所有其它实例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below. Obviously, the described embodiments are only some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other examples improved or modified by those skilled in the art belong to the protection scope of the present invention.

采用GB/T12914-1991《纸和纸板抗张强度的测定法(恒速拉伸法)》标准,测试本发明制备得到的对位芳纶纸的拉伸强度和伸长率;采用IEC60819-2:2001《电工用非纤维素纸第2部分:试验方法》测试本发明制备得到的对位芳纶纸的撕裂度。Adopt GB/T12914-1991 " the determination method of tensile strength of paper and cardboard (constant speed stretching method) " standard, test the tensile strength and elongation of para-aramid paper that the present invention prepares; Adopt IEC60819-2: 2001 "Non-Cellulose Paper for Electrical Engineering Part 2: Test Method" tested the tearing degree of the para-aramid paper prepared by the present invention.

采用GB/T1408.1-2006《绝缘材料电气强度试验方法第1部分:工频下试验》标准,检测本发明制备得到的对位芳纶纸的电气绝缘性能。The electrical insulation performance of the para-aramid paper prepared by the present invention was tested by adopting the standard of GB/T1408.1-2006 "Test Method for Electric Strength of Insulating Materials Part 1: Test under Power Frequency".

本发明以下实施例所用的对位芳纶纳米纤维悬浮液为按照下述方法制备得到的:The para-aramid nanofiber suspension used in the following examples of the present invention is prepared according to the following method:

向300mL的反应器中加入100mL的N-甲基吡咯烷酮(NMP),在氮气保护以及搅拌下加入10g的CaCl2和5g的分子量为2100的聚乙二醇(PEG),加热至100℃使二者溶解。待CaCl2和PEG完全溶解后用冰水浴将溶解液体系降至15℃后加入4.326g对苯二胺(PPD)溶解,待PPD完全溶解后加入8.178g对苯二甲酰氯(TPC)并高速搅拌(2000r/min)进行缩聚反应,聚合过程中保持冰水浴,维持体系温度不超过70℃;在上述缩聚反应进行到体系形成冻胶体并出现韦森堡效应时停止搅拌,撤去冰水浴,取出5g的冻胶体加入200mL的NMP,用组织粉碎机快速搅拌5min将已溶胀的冻胶体打碎,在NMP中形成均一稳定的混合体系。向混合体系中加入200mL的水,同样使用组织粉碎机快速搅拌10min得到均匀稳定的成膜悬浮液;为了脱除悬浮液中的NMP、CaCl2和PEG等杂质,利用连续逆流带式洗涤机将悬浮液用水反复洗涤干净,最终用去离子水将悬浮液分散成均匀浆料,得到质量浓度为0.5%的对位芳纶纳米纤维悬浮液,其中的对位芳纶纳米纤维直径在20nm左右,平均长度在100μm左右。Add 100 mL of N-methylpyrrolidone (NMP) to a 300 mL reactor, add 10 g of CaCl and 5 g of polyethylene glycol (PEG) with a molecular weight of 2100 under nitrogen protection and stirring, and heat to 100 ° C to make the two or dissolved. After the CaCl 2 and PEG are completely dissolved, use an ice-water bath to lower the solution system to 15°C, then add 4.326g of p-phenylenediamine (PPD) to dissolve, and then add 8.178g of terephthaloyl chloride (TPC) after the PPD is completely dissolved. Stir (2000r/min) for polycondensation reaction, keep an ice-water bath during the polymerization process, and keep the system temperature not exceeding 70°C; stop stirring when the above-mentioned polycondensation reaction proceeds until the system forms a jelly body and Weissenberg effect occurs, remove the ice-water bath, and take out 5 g of jelly was added to 200 mL of NMP, and the swollen jelly was broken up by rapid stirring with a tissue grinder for 5 minutes to form a uniform and stable mixed system in NMP. Add 200mL of water to the mixing system, and use a tissue pulverizer to stir rapidly for 10 minutes to obtain a uniform and stable film-forming suspension ; The suspension was repeatedly washed with water, and finally the suspension was dispersed into a uniform slurry with deionized water to obtain a suspension of para-aramid nanofibers with a mass concentration of 0.5%, wherein the diameter of the para-aramid nanofibers was about 20nm. The average length is around 100 μm.

实施例1Example 1

将上述对位芳纶纳米纤维悬浮液用斜网成型器斜网成型技术高压喷涂到斜网上成型,成型网的目数为100目,成型过程中对喷涂到斜网上的涂层先采用下部真空抽吸脱水再进行上顶网成型器脱水相结合的脱水方式进行双向脱水;在真空抽吸脱水的过程中,随着湿纸胚的干度从3%增加到5%,真空抽吸的真空度从-0.06MPa增大到-0.1MPa,得到湿纸张。The above-mentioned para-aramid nanofiber suspension is sprayed on the inclined net by high pressure using the inclined net forming technology of the inclined net former, and the mesh number of the forming net is 100 mesh. Suction dehydration combined with top wire former dehydration combined dehydration method for two-way dehydration; in the process of vacuum suction dehydration, as the dryness of wet paper embryo increases from 3% to 5%, the vacuum of vacuum suction The pressure increases from -0.06MPa to -0.1MPa to get wet paper.

将成型后的湿纸张利用真空吸附转移的方法与成型网剥离后进行真空压榨脱水,在真空压榨脱水过程中,随着湿纸张的干度增加到10%,真空压榨脱水的压力依次从0.15MPa、0.20MPa、0.25MPa、0.30MPa增加(4级缓冲真空压榨脱水),真空压榨脱水的真空度为-20KPa,真空压榨脱水过程中的毛布清洗用高压水压力为1.5MPa。After the formed wet paper is peeled off from the forming net by vacuum adsorption transfer method, vacuum press dehydration is carried out. During the vacuum press dehydration process, as the dryness of the wet paper increases to 10%, the pressure of vacuum press dehydration increases from 0.15MPa to 10%. , 0.20MPa, 0.25MPa, and 0.30MPa increase (4-stage buffer vacuum press dehydration), the vacuum degree of vacuum press dehydration is -20KPa, and the high-pressure water pressure for felt cleaning during vacuum press dehydration is 1.5MPa.

将脱水后的纸张采用8级蒸汽烘干,随着脱水后的纸张干度的增加,将烘干的温度从80℃提高到120℃,然后在张力为7.5kN/m的张紧装置的拉伸作用下将纸张进行热定型,热定型的温度130℃时间为6min,最后经过压光成型,得到对位芳纶纸。The dehydrated paper is dried with 8-level steam. With the increase of the dryness of the dehydrated paper, the drying temperature is increased from 80°C to 120°C, and then the tension of the tension device is 7.5kN/m. Under the action of stretching, the paper is heat-set, the heat-setting temperature is 130°C for 6 minutes, and finally it is calendered to obtain para-aramid paper.

本发明实施例1制备得到的对位芳纶纸厚度为50μm。按照上述方法测试其性能,测试结果为,拉伸强度为60MPa,伸长率为1.7%;撕裂度为800mN;电气绝缘性能为95kV/mm。The para-aramid paper prepared in Example 1 of the present invention has a thickness of 50 μm. Its performance was tested according to the above method, and the test results showed that the tensile strength was 60MPa, the elongation was 1.7%, the tearing degree was 800mN, and the electrical insulation performance was 95kV/mm.

实施例2:Example 2:

将上述对位芳纶纳米纤维悬浮液用斜网成型器斜网成型技术高压喷涂到斜网上成型,成型网的目数为100目,成型过程中对喷涂到斜网上的涂层先采用下部真空抽吸脱水再进行上顶网成型器脱水相结合的脱水方式进行双向脱水;在真空抽吸脱水过程中,随着湿纸胚的干度从3%增加到5%,真空抽吸脱水的真空度从-0.01MPa增加到-0.05MPa,得到湿纸张。The above-mentioned para-aramid nanofiber suspension is sprayed on the inclined net by high pressure using the inclined net forming technology of the inclined net former, and the mesh number of the forming net is 100 mesh. Suction dehydration combined with top wire former dehydration combined dehydration method for two-way dehydration; in the vacuum suction dehydration process, as the dryness of the wet paper embryo increases from 3% to 5%, the vacuum of vacuum suction dehydration The degree increases from -0.01MPa to -0.05MPa to get wet paper.

将成型后的湿纸张利用真空吸附转移的方法与成型网剥离后进行真空压榨脱水,在真空压榨脱水的过程中,随着湿纸张的干度增加到15%,真空压榨脱水的压力依次从0.15MPa、0.20MPa、0.25MPa、0.30MPa增加(4级缓冲真空压榨脱水),真空压榨脱水的真空度为-40KPa,真空压榨脱水过程中的毛布清洗用高压水压力为2.5MPa。The formed wet paper is peeled off from the forming net by vacuum adsorption transfer method and then dehydrated by vacuum press. During the process of vacuum press dehydration, as the dryness of the wet paper increases to 15%, the pressure of vacuum press dehydration is sequentially increased from 0.15 to 15%. MPa, 0.20MPa, 0.25MPa, and 0.30MPa increase (4-stage buffer vacuum press dehydration), the vacuum degree of vacuum press dehydration is -40KPa, and the pressure of high-pressure water for felt cleaning during vacuum press dehydration is 2.5MPa.

将脱水后的纸张采用8级蒸汽干燥,随着脱水后的纸张干度的增加,将烘干的温度从80℃提高到120℃,然后在张力7.5kN/m的张紧装置的拉伸作用下将纸张进行热定型,热定型的温度130℃时间为6min,最后经过压光成型,得到对位芳纶纸。Dry the dehydrated paper with 8-level steam. With the increase of the dryness of the dehydrated paper, increase the drying temperature from 80°C to 120°C, and then stretch it under the tension device with a tension of 7.5kN/m The paper is heat-set at a temperature of 130°C for 6 minutes, and finally calendered to obtain para-aramid paper.

本发明实施例2制备得到的对位芳纶纸厚度为80μm。按照上述方法测试其性能,测试结果为,拉伸强度为120MPa,伸长率为1.7%;撕裂度为1400mN;电气绝缘性能为85kV/mm。The para-aramid paper prepared in Example 2 of the present invention has a thickness of 80 μm. Its performance was tested according to the above method, and the test results showed that the tensile strength was 120MPa, the elongation was 1.7%, the tearing degree was 1400mN, and the electrical insulation performance was 85kV/mm.

实施例3:Example 3:

将上述对位芳纶纳米纤维悬浮液用斜网成型器斜网成型技术高压喷涂到斜网上成型,成型网的目数为100目,成型过程中对喷涂到斜网上的涂层先采用下部真空抽吸脱水再进行上顶网成型脱水相结合的脱水方式进行双向脱水;在真空抽吸脱水过程中,随着湿纸胚的干度从3%增加到5%,真空抽吸脱水的真空度从-0.01MPa增加到-0.05MPa,得到湿纸张。The above-mentioned para-aramid nanofiber suspension is sprayed on the inclined net by high pressure using the inclined net forming technology of the inclined net former, and the mesh number of the forming net is 100 mesh. Suction dehydration combined with top wire forming dehydration for two-way dehydration; in the process of vacuum suction dehydration, as the dryness of the wet paper embryo increases from 3% to 5%, the vacuum degree of vacuum suction dehydration Increase from -0.01MPa to -0.05MPa to get wet paper.

将成型后的湿纸张利用真空吸附转移的方法与成型网剥离后进行真空压榨脱水,在真空压榨脱水过程中,随着湿纸张的干度增加到12%,真空压榨脱水的压力依次从0.20MPa、0.25MPa、0.30MPa、0.35MPa增加(4级缓冲真空压榨脱水),真空压榨脱水的真空度为-30KPa,真空压榨脱水过程中的毛布清洗用高压水压力为2MPa。After the formed wet paper is peeled off from the forming net by vacuum adsorption transfer method, vacuum press dehydration is carried out. During the vacuum press dehydration process, as the dryness of the wet paper increases to 12%, the pressure of vacuum press dehydration increases from 0.20MPa to , 0.25MPa, 0.30MPa, and 0.35MPa increase (4-stage buffer vacuum press dehydration), the vacuum degree of vacuum press dehydration is -30KPa, and the high-pressure water pressure for felt cleaning during vacuum press dehydration is 2MPa.

将脱水后的纸张采用8级蒸汽烘干,随着脱水后的纸张干度的增加,烘干的温度从100℃提高到120℃,然后在张力7kN/m的张紧装置的拉伸作用下将纸张进行热定型,热定型的温度140℃时间为9min,最后经过压光成型,得到对位芳纶纸。The dehydrated paper is dried with 8-level steam. With the increase of the dryness of the dehydrated paper, the drying temperature is increased from 100°C to 120°C, and then under the tension of the tension device with a tension of 7kN/m The paper was heat-set at 140°C for 9 minutes, and finally calendered to obtain para-aramid paper.

本发明实施例3制备得到的对位芳纶纸厚度为120μm。按照上述方法测试其性能,测试结果为,拉伸强度为110MPa,伸长率为1.5%;撕裂度为2000mN;电气绝缘性能为70kV/mm。The para-aramid paper prepared in Example 3 of the present invention has a thickness of 120 μm. Its performance was tested according to the above method, and the test results showed that the tensile strength was 110MPa, the elongation was 1.5%, the tearing degree was 2000mN, and the electrical insulation performance was 70kV/mm.

实施例4:Example 4:

将上述对位芳纶纳米纤维悬浮液用斜网成型器斜网成型技术高压喷涂到斜网上成型,成型网的目数为100目,成型过程中对喷涂到斜网上的涂层先采用下部真空抽吸脱水再进行上顶网成型器脱水相结合的脱水方式进行双向脱水;在真空抽吸脱水的过程中,随着湿纸胚的干度从3%增加到5%,真空抽吸的真空度从-0.01MPa增加到-0.05MPa,得到湿纸张。The above-mentioned para-aramid nanofiber suspension is sprayed on the inclined net by high pressure using the inclined net forming technology of the inclined net former, and the mesh number of the forming net is 100 mesh. Suction dehydration combined with top wire former dehydration combined dehydration method for two-way dehydration; in the process of vacuum suction dehydration, as the dryness of wet paper embryo increases from 3% to 5%, the vacuum of vacuum suction The degree increases from -0.01MPa to -0.05MPa to get wet paper.

将成型后的湿纸张利用真空吸附转移的方法与成型网剥离后进行真空压榨脱水,在真空压榨脱水过程中,随着湿纸张的干度增加到13%,真空压榨脱水的压力依次从0.15MPa、0.20MPa、0.25MPa、0.30MPa增加(4级缓冲真空压榨脱水),真空压榨脱水的真空度为-35KPa,真空压榨脱水过程中的毛布清洗用高压水压力为2.2MPa。After the formed wet paper is peeled off from the forming net by vacuum adsorption transfer method, vacuum press dehydration is carried out. During the vacuum press dehydration process, as the dryness of the wet paper increases to 13%, the pressure of vacuum press dehydration increases from 0.15MPa to , 0.20MPa, 0.25MPa, and 0.30MPa increase (4-stage buffer vacuum press dehydration), the vacuum degree of vacuum press dehydration is -35KPa, and the high-pressure water pressure for felt cleaning during vacuum press dehydration is 2.2MPa.

将脱水后的纸张采用8蒸汽干燥,随着脱水后纸张干度的增加,烘干温度从100℃提高到120℃,然后在张力7kN/m的张紧装置的拉伸作用下将纸张进行热定型,热定型的温度140℃时间为12min,最后经过压光成型,得到对位芳纶纸。The dehydrated paper is dried with 8 steams. With the increase of paper dryness after dehydration, the drying temperature is increased from 100°C to 120°C, and then the paper is heated under the tension of a tensioning device with a tension of 7kN/m. Shaping, heat setting at 140°C for 12 minutes, and finally calendering to obtain para-aramid paper.

本发明实施例4制备得到的对位芳纶纸厚度为200μm。按照上述方法测试其性能,测试结果为,拉伸强度为150MPa,伸长率为1.5%;撕裂度为2000mN电气绝缘性能为60kV/mm。The para-aramid paper prepared in Example 4 of the present invention has a thickness of 200 μm. Its performance was tested according to the above method, and the test results showed that the tensile strength was 150MPa, the elongation was 1.5%; the tearing degree was 2000mN, and the electrical insulation performance was 60kV/mm.

比较例1Comparative example 1

采用市售的烟台民士达YT836对位芳纶纸。Commercially available Yantai Minshida YT836 para-aramid paper was used.

按照上述方法测试本发明比较例1的对位芳纶纸的性能,测试结果为,其拉伸强度为45MPa;伸长率为2.0%;撕裂度为1200mN;电气绝缘性能为16kV/mm。The properties of the para-aramid paper of Comparative Example 1 of the present invention were tested according to the above method. The test results showed that the tensile strength was 45 MPa; the elongation was 2.0%; the tearing degree was 1200 mN; and the electrical insulation performance was 16 kV/mm.

比较例2Comparative example 2

按照实施例1的方法制备得到对位芳纶纸,与实施例1的区别在于,上网成型的方法为直接将对位芳纶纳米纤维料液高压喷涂到斜网上成型,只进行上顶网成型器脱水。The para-aramid paper was prepared according to the method of Example 1. The difference from Example 1 is that the online forming method is to directly spray the para-aramid nanofiber material liquid on the inclined net for forming at high pressure, and only carry out upper net forming. dehydration.

本发明比较例2制备得到的对位芳纶纸厚度为50μm;按照上述方法测试本发明比较例2制备得到的对位芳纶纸的性能,测试结果为,拉伸强度为45MPa;伸长率为1.5%;撕裂度为750mN;电气绝缘性能为60kV/mm。The para-aramid paper prepared in comparative example 2 of the present invention has a thickness of 50 μm; the performance of the para-aramid paper prepared in comparative example 2 of the present invention is tested according to the above method, and the test result is that the tensile strength is 45 MPa; the elongation It is 1.5%; the tearing degree is 750mN; the electrical insulation performance is 60kV/mm.

比较例3Comparative example 3

按照实施例1的方法制备得到对位芳纶纸,与实施例1的区别在于,上网成型的方法为直接将对位芳纶纳米纤维料液高压喷涂到斜网上成型,只进行下部真空抽吸脱水。The para-aramid paper was prepared according to the method of Example 1. The difference from Example 1 is that the online forming method is to directly spray the para-aramid nanofiber material liquid on the inclined net at high pressure for forming, and only carry out the lower vacuum suction dehydration.

本发明比较例3制备得到的对位芳纶纸厚度为50μm;按照上述方法测试本发明比较例3制备得到的对位芳纶纸的性能,测试结果为,拉伸强度为40MPa;伸长率为1.4%;撕裂度为600mN;电气绝缘性能为40kV/mm。The para-aramid paper prepared in Comparative Example 3 of the present invention has a thickness of 50 μm; the performance of the para-aramid paper prepared in Comparative Example 3 of the present invention is tested according to the above method, and the test result is that the tensile strength is 40 MPa; the elongation It is 1.4%; the tearing degree is 600mN; the electrical insulation performance is 40kV/mm.

由以上实施例可知,本发明提供了一种对位芳纶纸的制备方法,包括:将对位芳纶纳米纤维料液进行上网成型,得到湿纸张;将所述湿纸张进行多级缓冲压榨脱水,得到脱水后的湿纸张;将所述脱水后的湿纸张依次进行多级低温烘干工艺和张力辅助干燥工艺进行干燥成型,得到对位芳纶纸;所述上网成型的方法为:将所述对位芳纶纳米纤维料液上浆后滤水,在成型网表面形成湿纸胚;对所述湿纸胚的下表面先进行真空抽吸脱水然后用上顶网成型器对湿纸胚的上表面脱水相结合的方式进行双向脱水,得到湿纸张。本发明采用特殊的上网成型工艺、多级缓冲压榨工艺、多级低温烘干工艺及张力辅助干燥工艺能够制备得到均匀性好、力学性能和绝缘性能优异的芳纶纸。As can be seen from the above examples, the present invention provides a method for preparing para-aramid paper, comprising: forming the para-aramid nanofiber material liquid on the Internet to obtain wet paper; performing multi-stage buffer pressing on the wet paper dehydration to obtain dehydrated wet paper; the dehydrated wet paper is sequentially subjected to a multi-stage low-temperature drying process and a tension-assisted drying process for drying and forming to obtain para-aramid paper; the method of online forming is: After the para-aramid nanofiber material liquid is sized, it is filtered, and a wet paper embryo is formed on the surface of the forming wire; the lower surface of the wet paper embryo is first vacuumed and dehydrated, and then the wet paper embryo is formed with an upper top wire former. Two-way dehydration is carried out by combining dehydration on the upper surface of the paper to obtain wet paper. The present invention adopts a special net forming process, a multi-stage buffer pressing process, a multi-stage low-temperature drying process and a tension-assisted drying process to prepare the aramid paper with good uniformity, excellent mechanical properties and insulating properties.

以上所述的仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。What has been described above is only a preferred embodiment of the present invention. It should be pointed out that for those of ordinary skill in the art, some improvements and modifications can also be made without departing from the principles of the present invention. These improvements and modifications It should also be regarded as the protection scope of the present invention.

Claims (10)

1. a kind of preparation method of p-aramid paper, including:
P-aramid fiber nanofiber feed liquid is subjected to upper net forming, obtains wet paper;
The processing of multi-buffer press dewatering is carried out to the wet paper, obtains dewatered wet paper;
The dewatered wet paper is dried and is formed with press polish, p-aramid paper is obtained;
The drying is that multistage low temperature drying and tension assist drying;
The molding method of the online is:
By drainage after the p-aramid fiber nanofiber feed liquid starching, l Water Paper embryo is formed in molding net surface;
The lower surface of the l Water Paper embryo be sucked by vacuum and is then carried out using upper surface of the upper top net former to l Water Paper embryo It is dehydrated the mode combined and carries out two-way dehydration, obtain wet paper.
2. the method according to claim 1, wherein p-aramid fiber is received in the p-aramid fiber nanofiber feed liquid The diameter of rice fiber is 10~100nm.
3. the method according to claim 1, wherein p-aramid fiber is received in the p-aramid fiber nanofiber feed liquid The length of rice fiber is 100nm~1000 μm.
4. the method according to claim 1, wherein the mass concentration of the p-aramid fiber nanofiber feed liquid is 0.5~2.5%.
5. the method according to claim 1, wherein the vacuum degree of the vacuum suction be -0.01~- 0.1MPa。
6. the method according to claim 1, wherein the mass dryness fraction of the wet paper is 8~10%.
7. the method according to claim 1, wherein the Pressing Number of the multi-buffer press dewatering is 2~5 Grade;The pressure of the multi-buffer press dewatering gradually increases within the scope of 0.05~0.35MPa.
8. the method according to claim 1, wherein it is described multistage low temperature drying drying series be 6~10 grades, The temperature of the multistage low temperature drying gradually increases within the scope of 60~120 DEG C.
9. the method according to claim 1, wherein the tension of tension auxiliary drying is 4~10kN/m, institute Stating the dry temperature of tension auxiliary is 120~160 DEG C.
10. a kind of p-aramid paper that method described in claim 1 is prepared.
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CN111218841A (en) * 2019-11-28 2020-06-02 陕西科技大学 A kind of nano-aramid fiber paper-based material and its preparation method and application
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