CN111690195A - Nano microporous membrane, and preparation method and application thereof - Google Patents
Nano microporous membrane, and preparation method and application thereof Download PDFInfo
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- CN111690195A CN111690195A CN202010372403.4A CN202010372403A CN111690195A CN 111690195 A CN111690195 A CN 111690195A CN 202010372403 A CN202010372403 A CN 202010372403A CN 111690195 A CN111690195 A CN 111690195A
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- 239000012982 microporous membrane Substances 0.000 title claims abstract description 19
- 238000002360 preparation method Methods 0.000 title claims 2
- 229920000098 polyolefin Polymers 0.000 claims abstract description 38
- 239000002994 raw material Substances 0.000 claims abstract description 25
- 239000004014 plasticizer Substances 0.000 claims abstract description 19
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 17
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 15
- 239000000314 lubricant Substances 0.000 claims abstract description 15
- 239000006057 Non-nutritive feed additive Substances 0.000 claims abstract description 14
- -1 polyethylene Polymers 0.000 claims description 23
- 239000005662 Paraffin oil Substances 0.000 claims description 20
- 238000001125 extrusion Methods 0.000 claims description 18
- 239000004698 Polyethylene Substances 0.000 claims description 14
- 238000005266 casting Methods 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 14
- 229920000573 polyethylene Polymers 0.000 claims description 14
- 239000012528 membrane Substances 0.000 claims description 10
- 229920000642 polymer Polymers 0.000 claims description 10
- 238000000605 extraction Methods 0.000 claims description 9
- 239000004743 Polypropylene Substances 0.000 claims description 8
- 229920001155 polypropylene Polymers 0.000 claims description 8
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 6
- 239000003153 chemical reaction reagent Substances 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
- 125000001931 aliphatic group Chemical group 0.000 claims description 5
- 230000002155 anti-virotic effect Effects 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 5
- 150000002148 esters Chemical class 0.000 claims description 5
- 150000003014 phosphoric acid esters Chemical class 0.000 claims description 4
- 239000002904 solvent Substances 0.000 claims description 4
- 235000021355 Stearic acid Nutrition 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 3
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical group CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 3
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 3
- 239000002530 phenolic antioxidant Substances 0.000 claims description 3
- 150000003021 phthalic acid derivatives Chemical class 0.000 claims description 3
- 239000008117 stearic acid Substances 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 2
- 239000003381 stabilizer Substances 0.000 claims 1
- 239000003039 volatile agent Substances 0.000 claims 1
- 239000011148 porous material Substances 0.000 abstract description 19
- 239000000463 material Substances 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 5
- 230000009471 action Effects 0.000 abstract description 2
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- 241000700605 Viruses Species 0.000 description 10
- 239000000306 component Substances 0.000 description 8
- 238000009835 boiling Methods 0.000 description 5
- 239000004744 fabric Substances 0.000 description 5
- YEVQZPWSVWZAOB-UHFFFAOYSA-N 2-(bromomethyl)-1-iodo-4-(trifluoromethyl)benzene Chemical compound FC(F)(F)C1=CC=C(I)C(CBr)=C1 YEVQZPWSVWZAOB-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 4
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 4
- PEJVLWCOQVHCAF-UHFFFAOYSA-N dioctyl oxalate Chemical compound CCCCCCCCOC(=O)C(=O)OCCCCCCCC PEJVLWCOQVHCAF-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000004750 melt-blown nonwoven Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
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- 229910019142 PO4 Inorganic materials 0.000 description 1
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- 238000002955 isolation Methods 0.000 description 1
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- 238000005259 measurement Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
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- 238000000465 moulding Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 125000005498 phthalate group Chemical class 0.000 description 1
- 239000008029 phthalate plasticizer Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
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- A—HUMAN NECESSITIES
- A41—WEARING APPAREL
- A41D—OUTERWEAR; PROTECTIVE GARMENTS; ACCESSORIES
- A41D13/00—Professional, industrial or sporting protective garments, e.g. surgeons' gowns or garments protecting against blows or punches
- A41D13/05—Professional, industrial or sporting protective garments, e.g. surgeons' gowns or garments protecting against blows or punches protecting only a particular body part
- A41D13/11—Protective face masks, e.g. for surgical use, or for use in foul atmospheres
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- A—HUMAN NECESSITIES
- A41—WEARING APPAREL
- A41D—OUTERWEAR; PROTECTIVE GARMENTS; ACCESSORIES
- A41D31/00—Materials specially adapted for outerwear
- A41D31/04—Materials specially adapted for outerwear characterised by special function or use
- A41D31/30—Antimicrobial, e.g. antibacterial
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/001—Combinations of extrusion moulding with other shaping operations
- B29C48/0018—Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C71/00—After-treatment of articles without altering their shape; Apparatus therefor
- B29C71/0009—After-treatment of articles without altering their shape; Apparatus therefor using liquids, e.g. solvents, swelling agents
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
- C08J7/02—Chemical treatment or coating of shaped articles made of macromolecular substances with solvents, e.g. swelling agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C71/00—After-treatment of articles without altering their shape; Apparatus therefor
- B29C71/0009—After-treatment of articles without altering their shape; Apparatus therefor using liquids, e.g. solvents, swelling agents
- B29C2071/0027—Removing undesirable residual components, e.g. solvents, unreacted monomers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/04—Condition, form or state of moulded material or of the material to be shaped cellular or porous
- B29K2105/041—Microporous
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/04—Homopolymers or copolymers of ethene
- C08J2323/06—Polyethene
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- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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- C08J2491/00—Characterised by the use of oils, fats or waxes; Derivatives thereof
- C08J2491/06—Waxes
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/10—Esters; Ether-esters
- C08K5/11—Esters; Ether-esters of acyclic polycarboxylic acids
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
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- C08K5/10—Esters; Ether-esters
- C08K5/12—Esters; Ether-esters of cyclic polycarboxylic acids
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- C—CHEMISTRY; METALLURGY
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- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
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- C08K5/52—Phosphorus bound to oxygen only
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- Manufacturing & Machinery (AREA)
- Textile Engineering (AREA)
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Abstract
本发明公开了一种纳米微孔膜、纳米微孔膜制作方法及其应用,包括纳米微孔膜采用质量分数如下的各组分原料:聚烯烃:21.3~30份,加工助剂:70~78.5份,增塑剂;0.02~0.1份;抗氧化剂;0.03~0.2份,润滑剂;0.04~0.15份,其中,所述聚烯烃的分子量为5万~150万。本发明将一定分子量的聚烯烃与加工助剂按一定比例混合,使得复合后的材料满足特定的强度要求,在分子间作用力和添加剂的作用下,聚烯烃流延基膜拉伸后形成的微孔结构的孔径大大降低,孔径可以达到纳米级别,能够实现100%防护的效果,同时微孔膜的厚度也可以减薄,用于口罩材料佩戴更舒适。The invention discloses a nano-microporous film, a method for making a nano-microporous film and an application thereof, including the following mass fractions of each component raw material used in the nano-microporous film: polyolefin: 21.3-30 parts, processing aid: 70-70 parts 78.5 parts, plasticizer; 0.02-0.1 part; antioxidant; 0.03-0.2 part, lubricant; 0.04-0.15 part, wherein the molecular weight of the polyolefin is 50,000-1.5 million. In the present invention, a certain molecular weight of polyolefin and a processing aid are mixed in a certain proportion, so that the compounded material meets specific strength requirements. Under the action of intermolecular force and additives, the polyolefin cast base film is stretched and formed The pore size of the microporous structure is greatly reduced, and the pore size can reach the nanometer level, which can achieve 100% protection effect. At the same time, the thickness of the microporous membrane can also be reduced, making it more comfortable to wear as a mask material.
Description
技术领域technical field
本发明涉及医用防病毒口罩设计领域,尤其涉及一种纳米微孔膜、纳米微孔膜制作方法及其应用。The invention relates to the field of design of medical anti-virus masks, in particular to a nano-microporous film, a method for making the nano-microporous film, and applications thereof.
背景技术Background technique
医疗用口罩一般都是多层结构,一般简称为SMS结构。材料是纺粘无纺布+ 熔喷无纺布+纺粘无纺布,简称SMS结构。目前熔喷无纺布主要材质是聚丙烯,是一种超细静电纤维布,可以捕捉粉尘。含有细菌和病毒的飞沫靠近熔喷无纺布后,会被静电吸附在无纺布表面,无法透过。这就是这种材料隔绝病菌的原理。Medical masks are generally multi-layer structures, generally referred to as SMS structures. The material is spunbond non-woven fabric + meltblown non-woven fabric + spunbond non-woven fabric, referred to as SMS structure. At present, the main material of meltblown non-woven fabric is polypropylene, which is an ultra-fine electrostatic fiber cloth that can capture dust. After the droplets containing bacteria and viruses are close to the melt-blown non-woven fabric, they will be electrostatically adsorbed on the surface of the non-woven fabric and cannot be penetrated. That's how the material keeps germs out.
口罩里面最重要的是阻隔层是熔喷层M(Meltblown),熔喷层的纤维直径在 2微米左右。熔喷层M成孔较纺粘层S小,富有静电捕捉功效,是口罩发挥功能的核心部件。但是受限于目前纺丝技术,纤维直径只能实现2微米生产,无法进一步细化,从而进一步缩小孔径,使孔径达到病毒直径范围。熔喷层M的孔径基本在100nm~200nm之间,而目前大多数病毒直径为50-100nm,恰好小于目前医用口罩孔径尺寸,为病毒的入侵埋下一定隐患。因此,寻求一种更薄、孔径更小以致能100%阻隔病毒的纳米微孔隔膜,成为高端医院口罩的重要研发方向。The most important thing in the mask is that the barrier layer is the meltblown layer M (Meltblown), and the fiber diameter of the meltblown layer is about 2 microns. The meltblown layer M has smaller pores than the spunbond layer S, and is rich in electrostatic capture effect, which is the core component of the mask function. However, limited by the current spinning technology, the fiber diameter can only be produced at 2 microns, which cannot be further refined, thereby further reducing the pore size and making the pore size reach the virus diameter range. The pore size of the meltblown layer M is basically between 100nm and 200nm, while the diameter of most viruses at present is 50-100nm, which is just smaller than the pore size of the current medical masks, which lays a certain hidden danger for the invasion of viruses. Therefore, seeking a nano-microporous membrane that is thinner and has a smaller pore size so that it can block viruses 100% has become an important research and development direction for high-end hospital masks.
发明内容SUMMARY OF THE INVENTION
为了解决现有技术中医用防病毒口罩用的熔喷层孔径比病毒孔径大,无法 100%阻隔病毒的技术问题,本发明提供了一种纳米微孔膜、纳米微孔膜制作方法及其应用来解决上述问题。In order to solve the technical problem that the pore size of the meltblown layer used in the traditional Chinese medical anti-virus mask is larger than that of the virus and cannot block the virus 100%, the present invention provides a nano-microporous film, a method for making the nano-microporous film and its application. to solve the above problems.
本发明提出一种纳米微孔膜,所述纳米微孔膜采用质量分数如下的各组分原料:聚烯烃:21.3~30份,加工助剂:70~78.5份,增塑剂;0.02~0.1份;抗氧化剂;0.03~0.2份,润滑剂;0.04~0.15份,其中,所述聚烯烃的分子量为5 万~150万。The invention provides a nano-microporous film. The nano-microporous film adopts the following raw materials by mass fraction: polyolefin: 21.3-30 parts, processing aid: 70-78.5 parts, plasticizer; 0.02-0.1 part; antioxidant; 0.03-0.2 part, lubricant; 0.04-0.15 part, wherein, the molecular weight of the polyolefin is 50,000-1.5 million.
进一步的,所述聚烯烃为聚乙烯或者聚丙烯。Further, the polyolefin is polyethylene or polypropylene.
进一步的,所述加工助剂为石蜡油,所述石蜡油的分子量为100~500g/mol。Further, the processing aid is paraffin oil, and the molecular weight of the paraffin oil is 100-500 g/mol.
进一步的,所述增塑剂为苯二甲酸酯类、脂肪族二元酸酯类、磷酸酯类中的一种或者多种混合。苯二甲酸酯类具体指邻苯二甲酸二辛酯(DOP),脂肪族二元酸酯类具体指乙二酸二辛酯(DOA),磷酸酯类具体指磷酸三辛酯(TOP)。Further, the plasticizer is a mixture of one or more of phthalic acid esters, aliphatic dibasic acid esters, and phosphoric acid esters. The phthalates specifically refer to dioctyl phthalate (DOP), the aliphatic dibasic acid esters specifically refer to dioctyl oxalate (DOA), and the phosphate esters specifically refer to trioctyl phosphate (TOP).
优选的,所述抗氧化剂为一种或者多种酚类抗氧化剂的混合,多种抗氧化剂混合可以达到协同抗氧的效果。Preferably, the antioxidant is a mixture of one or more phenolic antioxidants, and the mixture of multiple antioxidants can achieve a synergistic antioxidant effect.
优选的,所述润滑剂为硬脂酸类高分子化合物。Preferably, the lubricant is a stearic acid polymer compound.
本发明还提出一种纳米微孔膜的制作方法,包括以下几个步骤:The present invention also proposes a method for making a nano-microporous membrane, comprising the following steps:
S1:原料制作;将聚烯烃、增塑剂、抗氧化剂和润滑剂按照以上所述的纳米微孔膜中各组分的质量分数比例混合,在温度20℃~50℃下搅拌均匀后加入挤出设备中,随后按比例加入加工助剂。S1: Production of raw materials; mix polyolefin, plasticizer, antioxidant and lubricant according to the above-mentioned mass fraction ratio of each component in the nano-microporous film, stir evenly at a temperature of 20 ° C ~ 50 ° C, and add extrusion out of the equipment, and then the processing aids are added in proportion.
S2:挤出成型;步骤S1中的混合物在下从双螺杆挤出机中熔融挤出,随后经流延辊铸片成型,得到聚烯烃流延基膜。S2: extrusion molding; the mixture in step S1 is melt-extruded from a twin-screw extruder at the bottom, and then cast into sheets through a casting roll to obtain a polyolefin cast base film.
S3:拉伸;在90-110℃下,首先纵向拉伸流延基膜,接着横向拉伸,得到具有微孔结构的聚烯烃微孔膜。S3: stretching; at 90-110° C., the cast base film is firstly stretched in the longitudinal direction, and then stretched in the transverse direction to obtain a polyolefin microporous film with a microporous structure.
S4:二次拉伸:首先在聚烯烃微孔膜上添加挥发性试剂,使用萃取工艺将聚烯烃微孔膜中的高沸点溶剂白油萃取出来,接着在100-120℃下再次进行横向拉伸,经干燥、电晕处理后得到高分子纳米微孔膜。S4: Secondary stretching: First, add volatile reagents to the polyolefin microporous film, extract the high-boiling solvent white oil in the polyolefin microporous film using an extraction process, and then perform transverse stretching again at 100-120 °C stretched, dried and corona treated to obtain a polymer nanoporous membrane.
优选的,步骤S1中的挤出设备为双螺杆挤出机。Preferably, the extrusion equipment in step S1 is a twin-screw extruder.
优选的,步骤S4中的挥发性试剂为二氯甲烷。Preferably, the volatile reagent in step S4 is dichloromethane.
本发明还提出以上所述方法制备的纳米微孔膜在医用防病毒口罩中的应用。The present invention also proposes the application of the nano-microporous membrane prepared by the above method in medical anti-virus masks.
本发明的有益效果是:The beneficial effects of the present invention are:
(1)本发明将一定分子量的聚烯烃与加工助剂按一定比例混合,使得复合后的材料满足特定的强度要求,在分子间作用力和添加剂的作用下,聚烯烃流延基膜拉伸后形成的微孔结构的孔径大大降低,孔径可以达到纳米级别,能够实现100%防护的效果,同时微孔膜的厚度也可以减薄,用于口罩材料佩戴更舒适。(1) In the present invention, a certain molecular weight of polyolefin and a processing aid are mixed in a certain proportion, so that the composite material meets specific strength requirements, and under the action of intermolecular force and additives, the polyolefin casting base film is stretched The pore size of the formed microporous structure is greatly reduced, and the pore size can reach the nanometer level, which can achieve 100% protection effect. At the same time, the thickness of the microporous membrane can also be reduced, making it more comfortable to wear as a mask material.
(2)本发明在原料中添加有增塑剂和抗氧化剂,增塑剂使原料的柔韧性增强,更容易加工,抗氧化剂可以减少空气对原料性能的影响,产品稳定性更好。(2) In the present invention, plasticizers and antioxidants are added to the raw materials, and the plasticizers enhance the flexibility of the raw materials, making it easier to process, and the antioxidants can reduce the influence of air on the properties of the raw materials, resulting in better product stability.
(3)本发明所述的纳米微孔膜经两次拉伸成型,在第一次拉伸形成聚烯烃微孔膜后,采用萃取工艺萃取出高沸点的白油,纳米微孔膜中聚烯烃的比例更高,分子间作用力更大。(3) The nano-microporous film of the present invention is stretched twice, and after the first stretch to form a polyolefin microporous film, an extraction process is used to extract high-boiling white oil, and the nano-microporous film is polymerized The higher the ratio of olefins, the greater the intermolecular forces.
(4)本发明所述方法可以采用聚丙烯和聚乙烯两种主要材质加工纳米微孔膜,突破了现有技术中仅使用聚丙烯制作熔喷无纺布的局限性,提高了产品原料的可选性,从而可以大大降低产品成本。(4) The method of the present invention can use two main materials of polypropylene and polyethylene to process the nano-microporous film, which breaks through the limitation of only using polypropylene to make melt-blown non-woven fabrics in the prior art, and improves the quality of product raw materials. Optional, which can greatly reduce product costs.
具体实施方式Detailed ways
下面详细描述本发明的实施例。下面描述的实施例是示例性的,仅用于解释本发明,而不能理解为对本发明的限制。Embodiments of the present invention are described in detail below. The embodiments described below are exemplary, only for explaining the present invention, and should not be construed as limiting the present invention.
一种纳米微孔膜,所述纳米微孔膜采用质量分数如下的各组分原料:聚烯烃:21.3~30份,加工助剂:70~78.5份,增塑剂;0.02~0.1份;抗氧化剂;0.03~0.2 份,润滑剂;0.04~0.15份,其中,所述聚烯烃的分子量为5万~150万。A nano-microporous film, the nano-microporous film adopts each component raw material with the following mass fractions: polyolefin: 21.3-30 parts, processing aid: 70-78.5 parts, plasticizer; 0.02-0.1 part; Oxidant; 0.03-0.2 part, lubricant; 0.04-0.15 part, wherein the molecular weight of the polyolefin is 50,000-1.5 million.
所述加工助剂为高粘度助剂,加工助剂与一定分子量的聚烯烃混合后的原料的分子间作用力更高,韧性更好。The processing aid is a high-viscosity aid, and the raw material after the processing aid is mixed with a certain molecular weight polyolefin has higher intermolecular force and better toughness.
聚烯烃通常为聚乙烯或者聚丙烯。The polyolefin is usually polyethylene or polypropylene.
所述加工助剂可以为石蜡油,所述石蜡油的分子量优选为100~500g/mol。The processing aid may be paraffin oil, and the molecular weight of the paraffin oil is preferably 100-500 g/mol.
分子量越多,分子间的作用力越大,强度越大,结构稳定性越好,另一方面,分子量越多,熔融指数也越大,加工难度越高,因此聚烯烃和石蜡油的分子量都需要合理选择。The higher the molecular weight, the greater the intermolecular force, the greater the strength, and the better the structural stability. On the other hand, the higher the molecular weight, the greater the melt index, and the higher the processing difficulty. Reasonable choice is required.
作为优选的,所述石蜡油的碳链数在6-40之间,且是经过异构完全的低分子油,碳链数越多,石蜡油的沸点越低,纳米微孔膜加工过程中石蜡油越容易挥发,导致溶剂浓度降低;相反,碳链数越低,石蜡油的沸点越高,石蜡油的稳定性较好,但是材料成本较高,因此需要合理选择石蜡油的碳链数。Preferably, the carbon chain number of the paraffin oil is between 6-40, and it is a low molecular oil that has undergone complete isomerization. The higher the carbon chain number, the lower the boiling point of the paraffin oil. The more volatile the paraffin oil is, the lower the solvent concentration is; on the contrary, the lower the carbon chain number, the higher the boiling point of the paraffin oil, the better the stability of the paraffin oil, but the higher the material cost, so the carbon chain number of the paraffin oil needs to be selected reasonably .
增塑剂为苯二甲酸酯类、脂肪族二元酸酯类、磷酸酯类中的一种或者多种混合。增塑剂起到增塑效果,可以使原料的柔韧性增强,更容易加工。苯二甲酸酯类增塑剂优选用邻苯二甲酸二辛酯(DOP),脂肪族二元酸酯类增塑剂优选用乙二酸二辛酯(DOA),磷酸酯类增塑剂优选用磷酸三辛酯(TOP)。The plasticizer is a mixture of one or more of phthalic acid esters, aliphatic dibasic acid esters and phosphoric acid esters. The plasticizer has a plasticizing effect, which can enhance the flexibility of the raw material and make it easier to process. The phthalate plasticizer is preferably dioctyl phthalate (DOP), the aliphatic dibasic acid ester plasticizer is preferably dioctyl oxalate (DOA), and the phosphate ester plasticizer is preferably Use trioctyl phosphate (TOP).
所述抗氧化剂为一种或者多种酚类抗氧化剂的混合,多种抗氧化剂混合可以达到协同抗氧的效果。The antioxidant is a mixture of one or more phenolic antioxidants, and the mixture of multiple antioxidants can achieve a synergistic antioxidant effect.
所述润滑剂优选为硬脂酸类高分子化合物,润滑剂用于减少膜与膜之间的摩擦或者薄膜与加工设备之间的摩擦。The lubricant is preferably a stearic acid-based polymer compound, and the lubricant is used to reduce friction between films or between films and processing equipment.
一种纳米微孔膜的制作方法,包括以下几个步骤:A method for making a nano-microporous membrane, comprising the following steps:
S1:原料制作;将聚烯烃、增塑剂、抗氧化剂和润滑剂按照上述纳米微孔膜中各组分的质量分数比例混合,在温度20℃~50℃下搅拌均匀后加入挤出设备中,随后按比例加入加工助剂。S1: Production of raw materials; polyolefin, plasticizer, antioxidant and lubricant are mixed according to the mass fraction ratio of each component in the above-mentioned nano-microporous film, stirred evenly at a temperature of 20 ℃ ~ 50 ℃, and then added to the extrusion equipment , followed by proportional addition of processing aids.
S2:挤出成型;步骤S1中的混合物从双螺杆挤出机中熔融挤出,随后经流延辊铸片成型,得到聚烯烃流延基膜。S2: extrusion molding; the mixture in step S1 is melt-extruded from a twin-screw extruder, and then cast into sheets through a casting roll to obtain a polyolefin cast base film.
S3:拉伸;在90-110℃下,首先纵向拉伸流延基膜,接着横向拉伸,得到具有微孔结构的聚烯烃微孔膜。S3: stretching; at 90-110° C., the cast base film is firstly stretched in the longitudinal direction, and then stretched in the transverse direction to obtain a polyolefin microporous film with a microporous structure.
S4:二次拉伸:首先在聚烯烃微孔膜上添加挥发性试剂,使用萃取工艺将聚烯烃微孔膜中的高沸点溶剂白油萃取出来,接着在100-120℃下再次进行横向拉伸,经干燥、电晕处理后得到高分子纳米微孔膜。S4: Secondary stretching: First, add volatile reagents to the polyolefin microporous film, extract the high-boiling solvent white oil in the polyolefin microporous film using an extraction process, and then perform transverse stretching again at 100-120 °C stretched, dried and corona treated to obtain a polymer nanoporous membrane.
步骤S1中的挤出设备为双螺杆挤出机。The extrusion equipment in step S1 is a twin-screw extruder.
熔融挤出的过程如下:将步骤S1中的原料混合物采用双螺杆挤出机在 180~260℃下熔融挤出,通过流延模头或环形吹塑口模,流延成膜,冷却后(如强制冷却)以一定的速度牵引,得到厚度均匀的聚烯烃流延基膜。具体地,熔融挤出可以采用单螺杆或双螺杆挤出机挤出,考虑材料的成型加工和塑化性能,挤出温度不低于190℃。流延成膜用的辊温度为30~100℃,生产线速度为60~ 120kg/h,成型厚度10~40微米。The process of melt extrusion is as follows: the raw material mixture in step S1 is melted and extruded at 180-260 ° C using a twin-screw extruder, passed through a casting die or an annular blowing die, cast into a film, and after cooling ( For example, forced cooling) is drawn at a certain speed to obtain a polyolefin cast base film with uniform thickness. Specifically, the melt extrusion can be extruded by a single-screw or twin-screw extruder. Considering the molding and plasticizing properties of the material, the extrusion temperature is not lower than 190°C. The temperature of the rolls used for casting film formation is 30-100° C., the production line speed is 60-120 kg/h, and the forming thickness is 10-40 microns.
在流延成膜后,可进一步对得到的聚烯烃流延基膜进行热处理,进一步提高基膜的结晶度和晶片的完整性,热处理温度为110~150℃,热处理时间为10 分钟~15小时。After the casting film is formed, the obtained polyolefin cast base film can be further heat-treated to further improve the crystallinity of the base film and the integrity of the wafer. .
本发明首先在原料中加入具有润滑作用的试剂,有利于原料的搅拌混合,以及原料挤出时能够更加顺畅平滑,在一次拉伸后使用挥发性试剂将白油萃取出来,萃取时使用的挥发性试剂为二氯甲烷,经过萃取工艺的聚烯烃微孔膜的润滑成分降低,聚烯烃比例增加,分子间作用力也有所增加,此时可以在聚烯烃微孔膜的基础上再次进行拉伸,由于存在较大的分子间作用力,因此拉伸后的聚烯烃微孔膜的孔径仍可以保持较小尺寸。In the present invention, a reagent with lubricating effect is firstly added to the raw material, which is beneficial to the stirring and mixing of the raw material, and the raw material can be extruded more smoothly and smoothly. After one stretch, a volatile reagent is used to extract the white oil. The lubricating component of the polyolefin microporous film after the extraction process is reduced, the proportion of polyolefin is increased, and the intermolecular force is also increased. At this time, it can be stretched again on the basis of the polyolefin microporous film. , due to the large intermolecular force, the pore size of the stretched polyolefin microporous membrane can still maintain a small size.
通过以上所述方法制备的纳米微孔膜可以作为阻隔层应用在医用防病毒口罩中。The nano-microporous membrane prepared by the above method can be used as a barrier layer in medical anti-virus masks.
以下通过多个实施例来举例说明纳米微孔膜的各种适用组成、制作方法以及性能测试结果。Various suitable compositions, manufacturing methods and performance test results of the nano-microporous membrane are exemplified by various embodiments below.
实施例1Example 1
原料成分为:分子量为60万的聚乙烯,增塑剂250ppm,抗氧化剂400ppm,润滑剂500ppm,石蜡油分子量400g/mol,石蜡油与聚乙烯的质量分数比为7: 3,混合后的原料总重为20g,用双螺杆挤出机熔融挤出,流延成厚膜,挤出温度为220℃,挤出量120kg/h,流延温度为60℃,流延成型的厚膜厚度为30um。纵向拉伸倍率为10倍拉伸比,纵向拉伸温度90℃,一次横向拉伸倍率为10倍拉伸比,一次横向拉伸温度100℃,萃取温度15℃,二次横向拉伸倍率为10倍拉伸比,二次横向拉伸温度120℃,经干燥后得到高分子纳米微孔膜,纳米微孔膜的厚度为5um。经测试,本实施例制造获得的微孔膜,整体孔径在100nm以下,只有少量高于100nm,平均孔径为52nm,体现出对各种病毒的有效物理隔离。The raw material components are: polyethylene with a molecular weight of 600,000, plasticizer 250ppm, antioxidant 400ppm, lubricant 500ppm, paraffin oil molecular weight 400g/mol, the mass fraction ratio of paraffin oil and polyethylene is 7: 3, the mixed raw material The total weight is 20g, melt extruded with a twin-screw extruder, cast into a thick film, the extrusion temperature is 220°C, the extrusion rate is 120kg/h, the casting temperature is 60°C, and the thickness of the thick film formed by casting is 30um. The longitudinal stretching ratio is 10 times the stretching ratio, the longitudinal stretching temperature is 90 °C, the primary transverse stretching ratio is 10 times the stretching ratio, the primary transverse stretching temperature is 100 °C, the extraction temperature is 15 °C, and the secondary transverse stretching ratio is The stretching ratio is 10 times, the secondary transverse stretching temperature is 120°C, and the polymer nano-microporous film is obtained after drying, and the thickness of the nano-microporous film is 5um. After testing, the overall pore size of the microporous membrane produced in this example is less than 100 nm, only a small amount is higher than 100 nm, and the average pore size is 52 nm, which reflects the effective physical isolation of various viruses.
实施例2Example 2
原料成分为:分子量为150万的聚乙烯,增塑剂600ppm,抗氧化剂800ppm,润滑剂1000ppm,石蜡油分子量200g/mol,石蜡油与聚乙烯的质量分数比为7: 3,混合后的原料总重为20g,用双螺杆挤出机熔融挤出,流延成厚膜,挤出温度为220℃,挤出量60kg/h流延温度为60℃,流延成型的厚膜厚度为30um。纵向拉伸倍率为7倍拉伸比,纵向拉伸温度95℃,一次横向拉伸倍率为10倍拉伸比,一次横向拉伸温度115℃,萃取温度20℃,二次横向拉伸倍率为10倍拉伸比,二次横向拉伸温度115℃,经干燥后得到高分子纳米微孔膜,纳米微孔膜的厚度为2um。经测试,其平均孔径为64nm。The raw material components are: polyethylene with a molecular weight of 1.5 million, plasticizer 600ppm, antioxidant 800ppm, lubricant 1000ppm, paraffin oil molecular weight 200g/mol, the mass fraction ratio of paraffin oil and polyethylene is 7: 3, the mixed raw material The total weight is 20g, melt extruded with a twin-screw extruder, cast into a thick film, the extrusion temperature is 220℃, the extrusion volume is 60kg/h, the casting temperature is 60℃, and the thickness of the thick film formed by casting is 30um . The longitudinal stretching ratio is 7 times the stretching ratio, the longitudinal stretching temperature is 95 °C, the primary transverse stretching ratio is 10 times the stretching ratio, the primary transverse stretching temperature is 115 °C, the extraction temperature is 20 °C, and the secondary transverse stretching ratio is The stretching ratio is 10 times, the secondary transverse stretching temperature is 115°C, and the polymer nano-microporous film is obtained after drying, and the thickness of the nano-microporous film is 2um. After testing, its average pore size is 64nm.
实施例3Example 3
原料成分为:分子量为60万的聚乙烯(熔融指数为),增塑剂800ppm,抗氧化剂1500ppm,润滑剂1200ppm,石蜡油分子量600g/mol,石蜡油与聚乙烯的质量分数比为3:1,混合后的原料总重为20g,用双螺杆挤出机熔融挤出,流延成厚膜,挤出温度为220℃,挤出量80kg/h,流延温度为60℃,流延成型的厚膜厚度为30um。纵向拉伸倍率为8倍拉伸比,纵向拉伸温度90℃,一次横向拉伸倍率为10倍拉伸比,一次横向拉伸温度110℃,萃取温度18℃,二次横向拉伸倍率为10倍拉伸比,二次横向拉伸温度110℃,经干燥后得到高分子纳米微孔膜,纳米微孔膜的厚度为4um。经测试,平均孔径为71nm。The raw material components are: polyethylene with a molecular weight of 600,000 (melt index), plasticizer 800ppm, antioxidant 1500ppm, lubricant 1200ppm, paraffin oil molecular weight 600g/mol, and the mass fraction ratio of paraffin oil to polyethylene is 3:1 , the total weight of the mixed raw materials is 20g, melt extruded with a twin-screw extruder, cast into a thick film, the extrusion temperature is 220 ° C, the extrusion volume is 80 kg/h, the casting temperature is 60 ° C, and the casting is formed. The thickness of the thick film is 30um. The longitudinal stretching ratio is 8 times the stretching ratio, the longitudinal stretching temperature is 90 °C, the primary transverse stretching ratio is 10 times the stretching ratio, the primary transverse stretching temperature is 110 °C, the extraction temperature is 18 °C, and the secondary transverse stretching ratio is 10 times the stretching ratio, the secondary transverse stretching temperature is 110°C, and the polymer nano-microporous film is obtained after drying, and the thickness of the nano-microporous film is 4um. After testing, the average pore size is 71nm.
实施例4Example 4
原料成分为:熔融指数为2g/10min的聚丙烯,增塑剂900ppm,抗氧化剂 1800ppm,润滑剂1400ppm,石蜡油分子量200g/mol,石蜡油与聚乙烯的质量分数比为3:1,混合后的原料总重为20g,用双螺杆挤出机熔融挤出,流延成厚膜,挤出温度为220℃,挤出量70kg/h,流延温度为60℃,流延成型的厚膜厚度为30um。纵向拉伸倍率为9倍拉伸比,纵向拉伸温度100℃,一次横向拉伸倍率为10倍拉伸比,一次横向拉伸温度120℃,萃取温度20℃,二次横向拉伸倍率为10倍拉伸比,二次横向拉伸温度120℃,经干燥后得到高分子纳米微孔膜,纳米微孔膜的厚度为3um。经测试,其平均孔径为63nm。The raw material components are: polypropylene with a melt index of 2g/10min, plasticizer 900ppm, antioxidant 1800ppm, lubricant 1400ppm, paraffin oil molecular weight 200g/mol, and the mass fraction ratio of paraffin oil and polyethylene is 3:1. The total weight of the raw materials is 20g, which is melt-extruded with a twin-screw extruder, and cast into a thick film. The thickness is 30um. The longitudinal stretching ratio is 9 times the stretching ratio, the longitudinal stretching temperature is 100 °C, the primary transverse stretching ratio is 10 times the stretching ratio, the primary transverse stretching temperature is 120 °C, the extraction temperature is 20 °C, and the secondary transverse stretching ratio is The stretching ratio is 10 times, the secondary transverse stretching temperature is 120°C, and the polymer nano-microporous film is obtained after drying, and the thickness of the nano-microporous film is 3um. After testing, its average pore size is 63nm.
表1中列出了实施例1-实施例4制出的纳米微孔膜的各参数测量结果,从表中可以看出使用本发明所述的方法,在不同配比情况下制得的纳米微孔膜与现有技术相比均具有突出的优势,主要有以下几点:(1)孔径小,孔径均在100nm 以下,甚至可以达到50nm,能够100%阻隔病毒,体现更好的防护功能(现有口罩熔喷层孔径为100-200nm);(2)厚度薄,仅为2-7um,是现有口罩熔喷层厚度的十分之一,制成口罩后佩戴更舒服(现有口罩熔喷层厚度为20-40um);(3) 抗拉强度高,抗拉强度达200Mpa以上,体现更高安全性(现有口罩熔喷层强度为100MPa左右)。(4)静电效果更好,病毒捕捉能力更高。Table 1 lists the measurement results of each parameter of the nano-microporous membranes prepared in Examples 1-4. Compared with the existing technology, the microporous membrane has outstanding advantages, mainly in the following points: (1) The pore size is small, the pore size is below 100nm, and can even reach 50nm, which can block viruses 100% and reflect better protection. (The aperture of the meltblown layer of the existing mask is 100-200nm); (2) the thickness is thin, only 2-7um, which is one-tenth of the thickness of the meltblown layer of the existing mask, and it is more comfortable to wear after being made into a mask (the existing The thickness of the meltblown layer of the mask is 20-40um); (3) the tensile strength is high, and the tensile strength is above 200Mpa, reflecting higher safety (the strength of the existing mask meltblown layer is about 100MPa). (4) The electrostatic effect is better, and the virus capture ability is higher.
表1Table 1
另外,对比实施例1和实施例2,实施例2中的聚乙烯分子量较大,分子间作用力更高,韧性更好,因此实施例2可以拉伸得更薄。同理,实施例1与实施例3相比,实施例3中的聚乙烯占比较大,微孔膜整体韧性较好。实施例4 中采用聚丙烯代替聚乙烯,使用本发明所述方法同样可以制得各参数性能更加优化的纳米微孔膜。In addition, comparing Example 1 and Example 2, the polyethylene in Example 2 has a larger molecular weight, higher intermolecular force, and better toughness, so Example 2 can be stretched thinner. Similarly, compared with Example 3, Example 1 has a larger proportion of polyethylene, and the overall toughness of the microporous membrane is better. In Example 4, polypropylene is used instead of polyethylene, and nano-microporous membranes with more optimized performance of various parameters can also be obtained by using the method of the present invention.
在本说明书中,对所述术语的示意性表述不一定指的是相同的实施例。而且,描述的具体特征、结构、材料或者特点可以在任何的一个或多个实施例中以合适的方式结合。In this specification, schematic representations of such terms do not necessarily refer to the same embodiment. Furthermore, the particular features, structures, materials or characteristics described may be combined in any suitable manner in one or more embodiments.
以上述依据本发明的理想实施例为启示,通过上述的说明内容,相关工作人员完全可以在不偏离本项发明技术思想的范围内,进行多样的变更以及修改。本项发明的技术性范围并不局限于说明书上的内容,必须要根据权利要求范围来确定其技术性范围。Taking the above ideal embodiments according to the present invention as inspiration, and through the above description, relevant personnel can make various changes and modifications without departing from the technical idea of the present invention. The technical scope of the present invention is not limited to the contents in the specification, and the technical scope must be determined according to the scope of the claims.
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