CN110452402A - A kind of method that Mechanical Method prepares hydrophobic high permeable fiber film - Google Patents

A kind of method that Mechanical Method prepares hydrophobic high permeable fiber film Download PDF

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CN110452402A
CN110452402A CN201910724350.5A CN201910724350A CN110452402A CN 110452402 A CN110452402 A CN 110452402A CN 201910724350 A CN201910724350 A CN 201910724350A CN 110452402 A CN110452402 A CN 110452402A
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cellulose
hydrophobic
permeable fiber
highly air
fiber membrane
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刘杨
姚明珠
赵辉
易锬
黄崇杏
陆光海
禹业帆
蒙香江
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Guangxi University
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Abstract

本发明公开了一种机械法制备疏水高透气纤维膜的方法,属于生物质绿色纤维材料及环保材料领域。本发明将纤维素原料依次通过酶解预处理、机械研磨和成型干燥等步骤最终得到疏水高透气纤维膜。本发明方法制备的纤维素膜结构密实,机械性能优异,透明度高,疏水性强,水接触角平均值可至106°,透气性可达75.77s/(in2·100cc·1.22KPa);本发明的纤维素膜制备过程中未使用化学药品,不需要复杂的化学反应过程,无需复杂的工艺和高昂的设备投入;所得纤维素膜的水接触角可达106°,具有较好的耐水性,可在高湿度环境中使用。

The invention discloses a method for mechanically preparing a hydrophobic and highly air-permeable fiber membrane, which belongs to the field of biomass green fiber materials and environmental protection materials. In the invention, the cellulose raw material is sequentially subjected to enzymatic hydrolysis pretreatment, mechanical grinding, forming and drying steps to finally obtain a hydrophobic and highly air-permeable fiber membrane. The cellulose film prepared by the method of the present invention has a compact structure, excellent mechanical properties, high transparency, strong hydrophobicity, an average water contact angle of up to 106°, and an air permeability of up to 75.77s/(in 2 ·100cc·1.22KPa); No chemicals are used in the preparation process of the invented cellulose membrane, no complex chemical reaction process is required, no complicated process and high equipment investment are required; the water contact angle of the obtained cellulose membrane can reach 106°, which has good water resistance , can be used in high humidity environment.

Description

一种机械法制备疏水高透气纤维膜的方法A method for mechanically preparing hydrophobic and highly air-permeable fiber membranes

技术领域technical field

本发明属于绿色纤维材料及环保微纳米材料领域,具体地说是一种机械法制备疏水高透气纤维膜的方法。The invention belongs to the field of green fiber materials and environment-friendly micro-nano materials, in particular to a method for mechanically preparing hydrophobic and highly air-permeable fiber membranes.

背景技术Background technique

纤维素是地球上最丰富的生物高分子,它主要存在于高等植物的细胞壁中。微纳米纤维素不仅具有原材料来源广、强度高、比表面积大、生物相容性好、可生物降解、可再生循环利用等优点;同时由于直径在几到几十纳米尺寸范围、长度在几到几十微米尺度,直径小、长径比大,还兼具优异的力学性能。这些显著的特性使其有潜力制成透明微纳米纤维素薄膜纸,用于包装、耐高温柔性电子元器件基底、微流体芯片等高端领域。Cellulose is the most abundant biopolymer on earth, and it is mainly found in the cell walls of higher plants. Micro-nano cellulose not only has the advantages of wide source of raw materials, high strength, large specific surface area, good biocompatibility, biodegradability, renewable recycling, etc. Tens of microns scale, small diameter, large aspect ratio, and excellent mechanical properties. These remarkable properties make it possible to make transparent micro-nanocellulose film paper for high-end fields such as packaging, high-temperature-resistant flexible electronic component substrates, and microfluidic chips.

然而,纳米纤维素表面含有大量功能基团-羟基,极易吸水,致使透明纳米纸吸水性高,在包装、电子器件、微流体芯片等领域的直接应用受到限制。However, the surface of nanocellulose contains a large number of functional groups - hydroxyl groups, which are very easy to absorb water, resulting in high water absorption of transparent nanopaper, which limits the direct application in packaging, electronic devices, microfluidic chips and other fields.

目前,常见方法制得的纤维素纳米膜表面有大量亲水基团的存在,纤维素膜材料通常对湿度敏感、对水耐受性差,纤维素膜在吸湿后会出现润胀变形、强度降低和阻隔性变差等问题。另外,在制备复合材料时,亲水的纤维素也存在与其它疏水性基质兼容性差的问题。针对纳米纤维素的疏水改性已有大量文献报道,物理吸附和化学改性是常用的方法。物理表面吸附主要是通过水性亲和力、静电吸引、氢键或者范德华力的作用,在CNF表面吸附表面活性剂、电性相反物质或者聚合物电解质来实现。化学改性是通过共价键链接的方式在纤维素表面引入各种小分子或者大分子。然而,这些处理方法一般都需要加热或者较长的处理时间,有时需要加入一些有毒性的化学试剂,而且处理效率不高,难以规模化生产。At present, there are a large number of hydrophilic groups on the surface of the cellulose nanomembrane prepared by common methods. The cellulose membrane material is usually sensitive to humidity and has poor water tolerance. After absorbing moisture, the cellulose membrane will swell and deform and reduce its strength. and poor barrier properties. In addition, when preparing composite materials, hydrophilic cellulose also has the problem of poor compatibility with other hydrophobic matrices. A large number of literatures have been reported on the hydrophobic modification of nanocellulose, and physical adsorption and chemical modification are commonly used methods. Physical surface adsorption is mainly achieved by adsorbing surfactants, electrically opposite substances or polymer electrolytes on the surface of CNF through the action of water affinity, electrostatic attraction, hydrogen bond or van der Waals force. Chemical modification is to introduce various small molecules or macromolecules on the surface of cellulose through covalent linkage. However, these treatment methods generally require heating or long treatment time, and sometimes need to add some toxic chemical reagents, and the treatment efficiency is not high, making it difficult to scale production.

综上所述,纤维素膜的疏水性研究过程依然存在很多问题,纤维素微纤化过程依然存在很多问题阻碍着其规模化的生产和应用,如:预处理过程周期长、不环保、化学药品昂贵、难回收,制备成本高等问题。另外,传统方法制备的纤维素纳米膜耐水性较差,不易在潮湿环境下使用。若要进行疏水改性,需要进行复杂、成本高或环境不友好的后续处理。因此,迫切需要开发一种高效、可持续、低成本且对环境友好的方法来制备高性能的纤维素膜。故本发明提出一种机械法制备疏水高透气纤维膜的制备方法,以克服上述诸多问题,实现生产过程绿色、节能、环保,使新材料有望广泛应用于包装、微流体芯片、耐高温柔性电子元器件基底等高端领域。In summary, there are still many problems in the research process of the hydrophobicity of cellulose membranes, and there are still many problems in the process of cellulose microfibrillation that hinder its large-scale production and application, such as: long pretreatment cycle, not environmentally friendly, chemical Drugs are expensive, difficult to recycle, and have high preparation costs. In addition, cellulose nanomembranes prepared by traditional methods have poor water resistance and are not easy to use in humid environments. Complicated, costly or environmentally unfriendly subsequent treatments are required for hydrophobic modification. Therefore, there is an urgent need to develop an efficient, sustainable, low-cost, and environmentally friendly method to prepare high-performance cellulose membranes. Therefore, the present invention proposes a method for mechanically preparing hydrophobic and highly air-permeable fiber membranes to overcome the above-mentioned problems, realize green, energy-saving, and environmentally friendly production processes, and make new materials widely used in packaging, microfluidic chips, and high-temperature-resistant flexible electronics. High-end fields such as component substrates.

公开于该背景技术部分的信息仅仅旨在增加对本发明的总体背景的理解,而不应当被视为承认或以任何形式暗示该信息构成已为本领域一般技术人员所公知的现有技术。The information disclosed in this Background section is only for enhancing the understanding of the general background of the present invention and should not be taken as an acknowledgment or any form of suggestion that the information constitutes the prior art that is already known to those skilled in the art.

发明内容Contents of the invention

针对现有技术中存在的上述不足之处,本发明的目的是用简单的工艺制备一种疏水性高透气纤维膜,解决了现有方法制备的高能耗、高成本、无法大批量生产的技术问题。Aiming at the above-mentioned deficiencies existing in the prior art, the object of the present invention is to prepare a kind of hydrophobic and highly air-permeable fiber membrane with a simple process, which solves the high energy consumption, high cost, and inability to mass-produce the technology prepared by the existing method. question.

为实现上述目的,本发明所采用的技术方案如下:In order to achieve the above object, the technical scheme adopted in the present invention is as follows:

一种机械法制备疏水高透气纤维膜的方法,包括以下步骤:A method for mechanically preparing a hydrophobic and highly air-permeable fiber membrane, comprising the following steps:

(1)酶解预处理:将纤维素原料用纤维素酶在水浴加热条件下进行酶解预处理,得到浆料;(1) Enzymolysis pretreatment: the cellulose raw material is subjected to enzymolysis pretreatment with cellulase under the condition of heating in a water bath to obtain a slurry;

(2)机械法研磨:将步骤(1)所得浆料冲洗后,利用高浓盘磨机对纤维素进行盘磨机械法研磨处理,使纤维素微纤化并实现纤维素部分无定形区的破坏、纤维素表面分子的部分溶解和半纤维素的溶出,得到微米/纳米纤维素悬浮液;(2) Mechanical grinding: After rinsing the slurry obtained in step (1), use a high-concentration disc refiner to perform mechanical grinding on the cellulose to microfibrillate the cellulose and realize the formation of the amorphous region of the cellulose. Destruction, partial dissolution of cellulose surface molecules and dissolution of hemicelluloses to obtain micro/nano cellulose suspensions;

(3)成型干燥:将步骤(2)所得微米/纳米纤维素悬浮液采用流延法进行成型处理,干燥后即得到所述疏水高透气纤维膜。(3) Molding and drying: the micron/nanocellulose suspension obtained in step (2) is molded by casting method, and the hydrophobic and highly air-permeable fiber membrane is obtained after drying.

作为优选,步骤(1)中所述纤维素原料为甘蔗渣、棉花、麦草、芦苇、桑皮或黄麻;所述纤维素原料采用纤维素舒解机40000rpm进行分散预处理。Preferably, the cellulose raw material in step (1) is bagasse, cotton, wheat straw, reed, mulberry bark or jute; and the cellulose raw material is dispersed and pretreated with a cellulose decomposing machine at 40,000 rpm.

作为优选,步骤(1)中所述纤维素酶预处理条件为:酶解时间为30min,酶解温度50℃。Preferably, the cellulase pretreatment conditions in step (1) are: enzymolysis time is 30 minutes, and enzymolysis temperature is 50°C.

作为优选,步骤(2)中采用高浓盘磨机处理纤维素悬浮液时,高浓盘磨机磨盘之间的间距为0.01-0.07mm;纤维素悬浮液中纤维素含量为5-30wt%;研磨次数为5-30次。As preferably, when adopting high-concentration disc mill to process cellulose suspension in step (2), the distance between the discs of high-concentration disc mill is 0.01-0.07mm; the cellulose content in the cellulose suspension is 5-30wt% ; Grinding frequency is 5-30 times.

作为优选,步骤(3)中所述流延法成型前对步骤(2)所得微米/纳米纤维素悬浮液进行超声处理和磁力搅拌处理;所述磁力搅拌转速为600rpm;所述微米/纳米纤维素悬浮液定量为15g/cm2As preferably, the micron/nanocellulose suspension obtained in step (2) is subjected to ultrasonic treatment and magnetic stirring treatment before the tape casting method described in step (3); the magnetic stirring speed is 600rpm; the micron/nanofiber The quantitative value of the plain suspension is 15g/cm 2 .

作为优选,步骤(3)中所述干燥处理在鼓风干燥箱中进行。As a preference, the drying treatment in step (3) is carried out in a blast drying oven.

作为优选,所述鼓风干燥箱干燥温度为35-45℃。Preferably, the drying temperature of the blast drying oven is 35-45°C.

与现有技术相比,本发明的有益效果在于:Compared with prior art, the beneficial effect of the present invention is:

本发明所制备的纤维素膜性能优异,结构密实、强度高、透明度高,疏水性好,透气性高达75.77s/(in2.100cc.1.22KPa);并且本发明的纤维素膜未经过任何疏水改性处理,不需要复杂的化学反应、不需要昂贵的化学试剂和仪器设备,在机械处理和成膜过程中纤维素表面可发生分子重排和重结晶;所得纳米纤维素膜的水接触角可达106°,可在高湿度环境下使用。The cellulose film prepared by the present invention has excellent properties, compact structure, high strength, high transparency, good hydrophobicity, and air permeability as high as 75.77s/(in2.100cc.1.22KPa); and the cellulose film of the present invention has not undergone any hydrophobic Modification treatment does not require complicated chemical reactions, expensive chemical reagents and equipment, and molecular rearrangement and recrystallization can occur on the cellulose surface during mechanical treatment and film formation; the water contact angle of the obtained nanocellulose film Up to 106°, can be used in high humidity environment.

附图说明Description of drawings

图1为实施例1中所得疏水高透气纤维素膜的疏水角图片;Fig. 1 is the picture of the hydrophobic angle of the hydrophobic highly air-permeable cellulose film obtained in Example 1;

图2为实施例1中所得疏水高透气纤维素膜的扫描电镜图片;Fig. 2 is the scanning electron microscope picture of the obtained hydrophobic highly air-permeable cellulose film in embodiment 1;

图3为实施例2中所得疏水高透气纤维素膜的疏水角图片;Fig. 3 is the picture of the hydrophobic angle of the hydrophobic highly air-permeable cellulose film obtained in Example 2;

图4为实施例2中所得疏水高透气纤维素膜的扫描电镜图片;Fig. 4 is the scanning electron microscope picture of the obtained hydrophobic highly air-permeable cellulose film in embodiment 2;

图5为实施例3中所得疏水高透气纤维素膜的疏水角图片;Fig. 5 is the picture of the hydrophobic angle of the hydrophobic highly air-permeable cellulose film obtained in Example 3;

图6为实施例3中所得疏水高透气纤维素膜的扫描电镜图片。6 is a scanning electron microscope picture of the hydrophobic and highly air-permeable cellulose membrane obtained in Example 3.

具体实施方式Detailed ways

参考下列实施例将更容易理解本发明,给出的实施例不是限制本发明的范围。The present invention will be more readily understood with reference to the following examples, which are given without limiting the scope of the invention.

实施例1Example 1

(1)将蔗渣浆料采用纤维素舒解机40000rpm进行分散预处理,待疏解后,用纤维素酶在50℃水浴加热条件下,利用纤维素酶进行酶解30min;(1) Disperse and pretreat the bagasse slurry with a cellulose decomposing machine at 40,000 rpm. After decomposing, use cellulase to perform enzymatic hydrolysis for 30 minutes under the condition of heating in a water bath at 50° C.;

(2)将酶解后的纤维素浆料用大量蒸馏水冲洗,除去酶液,利用高浓盘磨机对纤维素进行盘磨机械法研磨处理,高浓盘磨机磨盘之间的间距为0.07mm;纤维素悬浮液中纤维素含量为30wt%;研磨次数为20次。研磨使纤维素微纤化并实现纤维素部分无定形区的破坏、纤维素表面分子的部分溶解和半纤维素的溶出,得到微米/纳米纤维素悬浮液;(2) Rinse the enzymatically hydrolyzed cellulose slurry with a large amount of distilled water, remove the enzyme liquid, and use a high-concentration disc mill to grind the cellulose mechanically. The distance between the discs of the high-concentration disc mill is 0.07. mm; the cellulose content in the cellulose suspension is 30 wt%; the number of grinding times is 20 times. Grinding makes cellulose microfibrillation and achieves the destruction of the amorphous region of cellulose, the partial dissolution of cellulose surface molecules and the dissolution of hemicellulose to obtain a micro/nano cellulose suspension;

(3)将微米/纳米纤维素悬浮液进行磁力搅拌处理,磁力搅拌转速为600rpm,以微米/纳米纤维素悬浮液定量为15g/cm2采用流延法进行成型处理,鼓风干燥箱进行干燥处理,干燥温度为35℃,干燥后即得到所述疏水高透气纤维膜。(3) The micron/nano cellulose suspension is subjected to magnetic stirring treatment, the magnetic stirring speed is 600rpm, and the micron/nano cellulose suspension is quantitatively 15g/cm 2 is molded by tape casting, and dried in a blast drying oven treatment, the drying temperature is 35° C., and the hydrophobic and highly air-permeable fiber membrane can be obtained after drying.

实施例2Example 2

(1)将蔗渣浆料采用纤维素舒解机40000rpm进行分散预处理,待疏解后,用纤维素酶在50℃水浴加热条件下,利用纤维素酶进行酶解30min;(1) Disperse and pretreat the bagasse slurry with a cellulose decomposing machine at 40,000 rpm. After decomposing, use cellulase to perform enzymatic hydrolysis for 30 minutes under the condition of heating in a water bath at 50° C.;

(2)将酶解后的纤维素浆料用大量蒸馏水冲洗,除去酶液,利用高浓盘磨机对纤维素进行盘磨机械法研磨处理,高浓盘磨机磨盘之间的间距为0.07mm;纤维素悬浮液中纤维素含量为30wt%;研磨次数为25次。研磨使纤维素微纤化并实现纤维素部分无定形区的破坏、纤维素表面分子的部分溶解和半纤维素的溶出,得到微米/纳米纤维素悬浮液;(2) Rinse the enzymatically hydrolyzed cellulose slurry with a large amount of distilled water, remove the enzyme liquid, and use a high-concentration disc mill to grind the cellulose mechanically. The distance between the discs of the high-concentration disc mill is 0.07. mm; the cellulose content in the cellulose suspension is 30 wt%; the number of grinding times is 25 times. Grinding makes cellulose microfibrillation and achieves the destruction of the amorphous region of cellulose, the partial dissolution of cellulose surface molecules and the dissolution of hemicellulose to obtain a micro/nano cellulose suspension;

(3)将微米/纳米纤维素悬浮液进行磁力搅拌处理,磁力搅拌转速为600rpm,以微米/纳米纤维素悬浮液定量为15g/cm2采用流延法进行成型处理,鼓风干燥箱进行干燥处理,干燥温度为35℃,干燥后即得到所述疏水高透气纤维膜。(3) The micron/nano cellulose suspension is subjected to magnetic stirring treatment, the magnetic stirring speed is 600rpm, and the micron/nano cellulose suspension is quantitatively 15g/cm 2 is molded by tape casting, and dried in a blast drying oven treatment, the drying temperature is 35° C., and the hydrophobic and highly air-permeable fiber membrane can be obtained after drying.

实施例3Example 3

(1)将蔗渣浆料采用纤维素舒解机40000rpm进行分散预处理,待疏解后,用纤维素酶在50℃水浴加热条件下,利用纤维素酶进行酶解30min;(1) Disperse and pretreat the bagasse slurry with a cellulose decomposing machine at 40,000 rpm. After decomposing, use cellulase to perform enzymatic hydrolysis for 30 minutes under the condition of heating in a water bath at 50° C.;

(2)将酶解后的纤维素浆料用大量蒸馏水冲洗,除去酶液,利用高浓盘磨机对纤维素进行盘磨机械法研磨处理,高浓盘磨机磨盘之间的间距为0.07mm;纤维素悬浮液中纤维素含量为30wt%;研磨次数为30次。研磨使纤维素微纤化并实现纤维素部分无定形区的破坏、纤维素表面分子的部分溶解和半纤维素的溶出,得到微米/纳米纤维素悬浮液;(2) Rinse the enzymatically hydrolyzed cellulose slurry with a large amount of distilled water, remove the enzyme liquid, and use a high-concentration disc mill to grind the cellulose mechanically. The distance between the discs of the high-concentration disc mill is 0.07. mm; the cellulose content in the cellulose suspension is 30 wt%; the number of grinding times is 30 times. Grinding makes cellulose microfibrillation and achieves the destruction of the amorphous region of cellulose, the partial dissolution of cellulose surface molecules and the dissolution of hemicellulose to obtain a micro/nano cellulose suspension;

(3)将微米/纳米纤维素悬浮液进行磁力搅拌处理,磁力搅拌转速为600rpm,以微米/纳米纤维素悬浮液定量为15g/cm2采用流延法进行成型处理,鼓风干燥箱进行干燥处理,干燥温度为35℃,干燥后即得到所述疏水高透气纤维膜。(3) The micron/nano cellulose suspension is subjected to magnetic stirring treatment, the magnetic stirring speed is 600rpm, and the micron/nano cellulose suspension is quantitatively 15g/cm 2 is molded by tape casting, and dried in a blast drying oven treatment, the drying temperature is 35° C., and the hydrophobic and highly air-permeable fiber membrane can be obtained after drying.

性能测试试验performance testing test

分别测试本发明实施例1-3所得纤维素膜的厚度、弹性模量、耐折度、接触角和透气性,试验结果见下表1。The thickness, elastic modulus, folding endurance, contact angle and air permeability of the cellulose films obtained in Examples 1-3 of the present invention were tested respectively, and the test results are shown in Table 1 below.

表1本发明实施例1-3所得纤维素膜性能测试Table 1 The performance test of the cellulose film obtained in Examples 1-3 of the present invention

从表1可以看出,本发明所制备的纤维素膜性能优异,结构密实,强度高,透明度高,疏水性好,透气性高达75.77s/(in2.100cc.1.22KPa)。As can be seen from Table 1, the cellulose film prepared by the present invention has excellent properties, compact structure, high strength, high transparency, good hydrophobicity, and air permeability as high as 75.77s/(in2.100cc.1.22KPa).

前述对本发明的具体示例性实施方案的描述是为了说明和例证的目的。这些描述并非想将本发明限定为所公开的精确形式,并且很显然,根据上述教导,可以进行很多改变和变化。对示例性实施例进行选择和描述的目的在于解释本发明的特定原理及其实际应用,从而使得本领域的技术人员能够实现并利用本发明的各种不同的示例性实施方案以及各种不同的选择和改变。本发明的范围意在由权利要求书及其等同形式所限定。The foregoing descriptions of specific exemplary embodiments of the present invention have been presented for purposes of illustration and description. These descriptions are not intended to limit the invention to the precise form disclosed, and obviously many modifications and variations are possible in light of the above teaching. The exemplary embodiments were chosen and described in order to explain the specific principles of the invention and its practical application, thereby enabling others skilled in the art to make and use various exemplary embodiments of the invention, as well as various Choose and change. It is intended that the scope of the invention be defined by the claims and their equivalents.

Claims (7)

1.一种机械法制备疏水高透气纤维膜的方法,其特征在于,包括以下步骤:1. A method for mechanically preparing hydrophobic and highly air-permeable fiber membranes, characterized in that, may further comprise the steps: (1)酶解预处理:将纤维素原料用纤维素酶在水浴加热条件下进行酶解预处理,得到浆料;(1) Enzymolysis pretreatment: the cellulose raw material is subjected to enzymolysis pretreatment with cellulase under the condition of heating in a water bath to obtain a slurry; (2)机械研磨:将步骤(1)所得浆料冲洗后,利用高浓盘磨机对纤维素进行盘磨机械法研磨处理,使纤维素微纤化并实现纤维素部分无定形区的破坏、纤维素表面分子的部分溶解和半纤维素的溶出,得到微米/纳米纤维素悬浮液;(2) Mechanical grinding: After rinsing the slurry obtained in step (1), use a high-concentration disc refiner to perform disc grinding mechanical grinding on the cellulose to microfibrillate the cellulose and destroy the amorphous region of the cellulose , Partial dissolution of cellulose surface molecules and dissolution of hemicellulose to obtain micro/nano cellulose suspension; (3)成型干燥:将步骤(2)所得微米/纳米纤维素悬浮液采用流延法进行成型处理,干燥后即得到所述疏水高透气纤维膜。(3) Molding and drying: the micron/nanocellulose suspension obtained in step (2) is molded by casting method, and the hydrophobic and highly air-permeable fiber membrane is obtained after drying. 2.根据权利要求1所述的机械法制备疏水高透气纤维膜的方法,其特征在于,步骤(1)中所述纤维素原料为甘蔗渣、棉花、麦草、芦苇、桑皮或黄麻;所述纤维素原料采用纤维素舒解机40000rpm进行分散预处理。2. mechanical method according to claim 1 prepares the method for hydrophobic highly air-permeable fiber membrane, it is characterized in that, the cellulose raw material described in step (1) is bagasse, cotton, wheat straw, reed, mulberry bark or jute; The above-mentioned cellulose raw material adopts the 40000rpm of cellulose unwinding machine to carry out dispersion pretreatment. 3.根据权利要求1所述的机械法制备疏水高透气纤维膜的方法,其特征在于,步骤(1)中所述纤维素酶预处理条件为:酶解时间为30min,酶解温度50℃。3. The method for mechanically preparing a hydrophobic and highly air-permeable fiber membrane according to claim 1, wherein the cellulase pretreatment conditions described in step (1) are: enzymolysis time is 30min, and enzymolysis temperature is 50°C . 4.根据权利要求1所述的机械法制备疏水高透气纤维膜的方法,其特征在于,步骤(2)中采用高浓盘磨机处理纤维素悬浮液时,高浓盘磨机磨盘之间的间距为0.01-0.07mm;纤维素悬浮液中纤维素含量为5-30wt%;研磨次数为5-30次。4. mechanical method according to claim 1 prepares the method for hydrophobic highly air-permeable fiber film, it is characterized in that, when adopting high-concentration disc mill to process cellulose suspension in step (2), between the high-concentration disc mill grinding discs The pitch of the cellulose is 0.01-0.07mm; the cellulose content in the cellulose suspension is 5-30wt%; the grinding frequency is 5-30 times. 5.根据权利要求1所述的机械法制备疏水高透气纤维膜的方法,其特征在于,步骤(3)中所述流延法成型前对步骤(2)所得微米/纳米纤维素悬浮液进行超声处理和磁力搅拌处理;所述磁力搅拌转速为600rpm;所述微米/纳米纤维素悬浮液定量为15g/cm25. mechanical method according to claim 1 prepares the method for hydrophobic highly air-permeable fiber membrane, it is characterized in that, step (2) gained micron/nanometer cellulose suspension is carried out before casting method molding described in step (3). Ultrasonic treatment and magnetic stirring treatment; the rotational speed of the magnetic stirring is 600 rpm; the quantitative value of the micro/nano cellulose suspension is 15 g/cm 2 . 6.根据权利要求1所述的机械法制备疏水高透气纤维膜的方法,其特征在于,步骤(3)中所述干燥处理在鼓风干燥箱中进行。6. The method for mechanically preparing hydrophobic and highly air-permeable fiber membranes according to claim 1, characterized in that, the drying treatment in step (3) is carried out in a blast drying oven. 7.根据权利要求6所述的机械法制备疏水高透气纤维膜的方法,其特征在于,所述鼓风干燥箱干燥温度为35-45℃。7 . The method for mechanically preparing a hydrophobic and highly air-permeable fiber membrane according to claim 6 , wherein the drying temperature of the blast drying oven is 35-45° C.
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Application publication date: 20191115