CN104558751A - Composition and method for preparing ultrathin gas-permeable film - Google Patents

Composition and method for preparing ultrathin gas-permeable film Download PDF

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CN104558751A
CN104558751A CN201310512388.9A CN201310512388A CN104558751A CN 104558751 A CN104558751 A CN 104558751A CN 201310512388 A CN201310512388 A CN 201310512388A CN 104558751 A CN104558751 A CN 104558751A
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weight
parts
density polyethylene
polyethylene
ultra
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CN104558751B (en
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权慧
张师军
李�杰
初立秋
高达利
吕芸
刘建叶
徐萌
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Sinopec Beijing Research Institute of Chemical Industry
China Petroleum and Chemical Corp
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Sinopec Beijing Research Institute of Chemical Industry
China Petroleum and Chemical Corp
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0807Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
    • C08L23/0815Copolymers of ethene with aliphatic 1-olefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/002Physical properties
    • C08K2201/003Additives being defined by their diameter
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/16Applications used for films
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/06Properties of polyethylene
    • C08L2207/066LDPE (radical process)

Abstract

The invention provides a composition and a method for preparing an ultrathin gas-permeable film. The gas-permeable film composition comprises a polyethylene blend, inorganic filler, a dispersant, an antioxidant and processing additives, wherein the polyethylene blend comprises medium-density polyethylene and linear low-density polyethylene, and can also comprise low-density polyethylene; the inorganic filler is micron or nano-scale calcium carbonate; and the dispersant is superfine fully-vulcanized powder rubber. The composition has better processing performance and mechanical properties, the casting and elongation rate are increased and meanwhile the gram weight can be further decreased to reduce the costs; the superfine fully-vulcanized powder rubber can assist the uniform dispersion of the inorganic filler in the resin so that the uniformity of the gas-permeable film is ensured.

Description

A kind of composition and method thereof preparing ultra-thin breathable film
Technical field
The present invention relates to processing modified plastics field, be specifically related to a kind of polyethylene composition possessing high working property for ultra-thin breathable film, and the preparation method of ultra-thin breathable film.
Background technology
Air-permeable envelope also claims " waterproof and breathable microporous membrane ", has the feature of permeable watertight, and gas can be allowed to pass through, and can intercept again the liquid as water simultaneously; It not only breathes freely but also soft as fabric, moisture content can be isolated again as plastics bag, therefore be called as " film that can breathe ", be widely used in as the sanitary product such as baby paper diaper and women sanitary articles, with fields such as medical treatment, food product pack, agricultural, weaving, buildings, it is the novel material developed rapidly in the world.
Air-permeable envelope is succeeded in developing by Japan the earliest, and is greatly developed in Korea S, and product is exported to all over the world in a large number, and wherein China is maximum product demand ground.Gordian technique---the air-permeable envelope resin that current air-permeable envelope is produced, rests in several overseas enterprise's hands.
Air-permeable envelope utilizes thermoplastic, polymeric materials for raw material, by filling inorganic mineral filler, such as nano-calcium carbonate etc., preparation becomes air-permeable envelope master batch, then, after curtain coating or blown film make film, be prepared from through unidirectional or stretch processes between the softening temperature and melt temperature of polymkeric substance.Under stretching action, around inorganic particulate, form the space of certain size, become the Waterproof Breathable microporous membrane with intercommunication network shape structure.Air-permeable envelope can allow the gas such as water vapour, air to pass through, but does not allow liquid to pass through.
The most frequently used thermoplastic polymer preparing air-permeable envelope is polyolefine material, can cause difficulty to fast filming and stretching owing to adding high amount of inorganic filler, therefore air-permeable envelope has higher requirement to a series of links such as raw material, weighting material, process for treating surface, curtain coating, stretchings; And along with the improving constantly of product quality, being growing more intense of market competition, and the enhancing of people's environmental consciousness, market proposes light-weighted requirement to air-permeable envelope; Lightweight can reduce product cost, improve the comfort of human body, but has higher requirement to the various aspects of performance of air-permeable envelope resin.
Patent WO-A-01/79343 discloses a kind ofly has stronger resistance to impact shock and the higher water vapor microporous thermoplastic's film through filter, by the calcium carbonate of 40 ~ 60%, 30 ~ 40% linear low density polyethylene (LLDPE) and 1 ~ 10% Low Density Polyethylene (LDPE) blended after progressively stretching make.
Chinese patent 03812642.7 discloses a kind of air-permeable envelope with higher water vapour permeability, good mechanical properties and processing characteristics, adopts bimodal LLDPE as matrix resin, add a certain amount of ion filler blended after be filmed.Bimodal LLDPE can the physical strength of Balanced films and processing characteristics, thus can reduce grammes per square metre or the thickness of air-permeable envelope to a certain extent, but due to the existence of low molecular weight polyethylene a part of in system, the physical strength of air-permeable envelope will be affected.
Chinese patent 200810220057.7 discloses a kind of mixture for the preparation of high-strength polyolefin permeable membrane and method thereof, and component comprises: polyolefin resin, micron order and nano sized inorganic fillers, oxidation inhibitor, processing aid, coupling agent.Wherein nanometer inorganic filler can improve the mechanical property of polyolefin permeable membrane, reduce the thickness of air-permeable envelope, and can be prepared the air-permeable envelope of high strength highly air-permeable by adjusting process condition; But because the consistency of nanometer inorganic filler and polyolefin resin is poor, the ventilative ununiformity of material can be caused and affect the use of air-permeable envelope.
Chinese patent 200810110060.3 discloses a kind of composition of melt-processable, comprises particle fillers, LDPE, LLDPE, dispersion agent and fluoropolymer.After surface modification is carried out to weighting material, while guaranteeing its high dispersing, effectively can reduce metal defects in the course of processing, avoid in extrusion, at high temperature there is charing and accumulate in die head aperture place in dispersion agent, causes instability, the product extruded to occur the phenomenon such as uneven.But operation is more complicated, tooling cost is higher.
Summary of the invention
In order to overcome the deficiency that prior art exists, the invention provides a kind of composition for high working property, ultra-thin breathable film, and the preparation method of ultra-thin breathable film; While the permeability ensureing air-permeable envelope, improve its mechanical property, obtain thinner air-permeable envelope, and there is good processing characteristics.
A kind of composition preparing ultra-thin breathable film of the present invention is achieved in that
A kind of composition preparing ultra-thin breathable film, contain in described composition: polyethylene blend, mineral filler, oxidation inhibitor and processing aid: be 100 parts in the gross weight of described polyethylene blend and described mineral filler, the weight of described polyethylene blend is 40 ~ 60 parts, the weight of described mineral filler is 40 ~ 60 parts, the weight of described oxidation inhibitor is 0.5 ~ 3 part, and the weight of described processing aid is 0.2 ~ 1.0 part;
Medium-density polyethylene (MDPE) containing wide distribution in described polyethylene blend and linear low density polyethylene (LLDPE);
The medium-density polyethylene of described wide distribution, its density is 0.935g/cm 3~ 0.945g/cm 3, melt flow rate (MFR) (MFR) is 0.1g/10min ~ 8g/10min(190 DEG C, 2.16kg), molecular weight distribution is 8 ~ 20; Be 100 parts in the gross weight of described polyethylene blend, the weight of the medium-density polyethylene of described wide distribution is 30 ~ 70 parts;
Described linear low density polyethylene, its comonomer is butylene, hexene or octene, and catalyzer is Zieglor-Natta catalyzer or metallocene catalyst; Its density is 0.890g/cm 3~ 0.925g/cm 3, melt flow rate (MFR) (MFR) is 1g/10min ~ 10g/10min(2.16kg, 190 DEG C); Be 100 parts in the gross weight of described polyethylene blend, the weight of described linear low density polyethylene is 70 ~ 30 parts;
Described mineral filler is selected from: one or more in calcium carbonate, barium sulfate, talcum powder or silicon-dioxide, and its particle diameter is 0.1 μm ~ 50 μm.
In the specific implementation, the medium-density polyethylene of described wide distribution, its melt flow rate (MFR) (MFR) is 2g/10min ~ 5g/10min(190 DEG C, 2.16kg), molecular weight distribution is 8 ~ 12; Be 100 parts in the gross weight of described polyethylene blend, the weight of the medium-density polyethylene of described wide distribution is 45 ~ 55 parts; Described linear low density polyethylene, its melt flow rate (MFR) (MFR) is 2g/10min ~ 5g/10min(2.16kg, 190 DEG C); Be 100 parts in the gross weight of described polyethylene blend, the weight of described linear low density polyethylene is 45 ~ 55 parts.
In the specific implementation, also Low Density Polyethylene (LDPE) is contained in described polyethylene blend; Described Low Density Polyethylene, its melt flow rate (MFR) (MFR) is 2g/cm 3~ 20g/cm 3(190 DEG C, 2.16kg), preferably 4g/cm 3~ 7g/cm 3; Be 100 parts in the gross weight of described polyethylene blend, the weight of described Low Density Polyethylene is 1 ~ 20 part, and the weight of the medium-density polyethylene of described wide distribution is 40 ~ 55 parts, and the weight of described linear low density polyethylene is 40 ~ 55 parts.
In the specific implementation, described mineral filler is calcium carbonate, and its particle diameter is 0.1 μm ~ 3 μm; Be 100 parts in the gross weight of described polyethylene blend and described mineral filler, the weight of described mineral filler is 45 ~ 55 parts, and the weight of described polyethylene blend is 45 ~ 55 parts; Described mineral filler uses silane coupling agent or stearic acid to carry out surface modification; Described oxidation inhibitor is selected from: pentaerythritol tetrathioglycollate, four [methyl-β-(3,5-di-tert-butyl-hydroxy phenyl) propionic ester] pentaerythritol ester (antioxidant 1010), three (2,4-di-t-butyl) phenyl-phosphite (irgasfos 168), propionic acid octadecyl, 1, one or more in 3 three (2-methyl-4-hydroxyl-5-tert-butyl-phenyl) butane or alkylation polyphenol; Preferred described oxidation inhibitor is antioxidant 1010 and irgasfos 168, and the amount ratio of antioxidant 1010 and irgasfos 168 is 2:1 ~ 1:2(weight).Described processing aid is white oil or polyethylene wax.
In the specific implementation, also containing dispersion agent in described composition, for the patented product of the Sinopec Beijing Chemical Research Institute that patent US6423760 and CN00816450 etc. introduce, be 100 parts in the gross weight of described polyethylene blend and described mineral filler, the weight of described dispersion agent is 0.5 ~ 3.0 part;
Described dispersion agent is ultra-fine fully vulcanized powder rubber, be selected from: one or more in full sulfuration styrene-butadiene rubber(SBR), full sulfuration carboxylic styrene-butadiene rubber, full vulcanized acrylate rubber, full-sulfurized nitrile rubber, full sulfuration carboxy nitrile rubber, full sulphurated siliastic or full sulfuration vinylpyridiene-styrene-butadiene rubber, preferred described dispersion agent is that full sulfuration styrene-butadiene rubber(SBR) is or/and full sulfuration carboxylic styrene-butadiene rubber; The gel content of described ultra-fine fully vulcanized powder rubber is greater than 60wt%, particle diameter is 50 ~ 2000nm, preferred particle diameter is 100 ~ 1000nm, preferred particle diameter is 150 ~ 500nm.
Another subject matter of the present invention: a kind of preparation method of ultra-thin breathable film is achieved in that
Use the described composition of one of claim 1 ~ 8 to prepare a method for ultra-thin breathable film, the method comprises the following steps:
(1) by described polyethylene blend, described mineral filler, described oxidation inhibitor and described processing aid, or by described polyethylene blend, described mineral filler, described oxidation inhibitor, described processing aid and described dispersion agent, mix through high speed mixer;
(2) material mixed is added twin screw extruder, extrudes, pelletizing drying, obtain the ultra-thin breathable film composition of high working property;
(3) the ultra-thin breathable film composition curtain coating of described high working property is become film, then longitudinally stretch, stretch ratio is 1.5 ~ 5, preferred stretch ratio is 1.5 ~ 2.5, obtain ultra-thin breathable film.
High working property provided by the invention, ultra-thin breathable film composition have the following advantages: the matrix resin selected is the blend of wide distribution medium-density polyethylene and linear low density polyethylene, the polyethylene of wide distribution has higher mechanical property and preferably processibility simultaneously, low molecular weight part can provide good processing characteristics, high molecular weight moieties can provide good mechanical property, therefore, it is possible to obtain good processibility in the production process of air-permeable envelope, improve curtain coating and draw speed, and can grammes per square metre be reduced further reduce costs.In addition, ultra-fine fully vulcanized powder rubber can be used as dispersed in resin of dispersion agent microwaveassisted inorganic filler, ensures the homogeneity of air-permeable envelope product.
Embodiment
Be described in further detail technical scheme of the present invention below in conjunction with embodiment, protection scope of the present invention is not limited to following embodiment.
Embodiment 1
Be 0.937g/cm by wide distribution MDPE(density 3, MFR is 4.5g/10min, molecular weight distribution is 15) be 2.0g/10min with LLDPE(MFR), calcium carbonate (particle diameter 0.1 μm ~ 3 μm, surface is through coupling agent treatment), oxidation inhibitor and processing aid carry out blended, the composition (mass ratio 1:1) of what wherein oxidation inhibitor was selected is antioxidant 1010 and irgasfos 168, what processing aid was selected is white oil.The parts by weight of each component are as shown in table 1.
Twin screw extruder is added after each component being mixed in homogenizer, extrusion temperature is 230 DEG C, extrude, pelletizing, obtain the composition of high working property, ultra-thin breathable film after drying, be 1.5 times of initial length after also longitudinally being stretched by casting machine curtain coating, obtain air-permeable envelope product, the performance of gained film is as shown in table 2.
Embodiment 2
Metallocene LLDPE(MFR is selected to be 3.0g/10min) LLDPE in alternate embodiment 1, other blend components are identical with embodiment 1, and the parts by weight of each component are as shown in table 1; Film-forming method is identical with embodiment 1, and the performance of gained film is as shown in table 2.
Result shows, and the LLDPE adopting metallocene LLDPE to substitute Zieglor-Natta catalysis can improve the mechanical property of air-permeable envelope further, thus reduces grammes per square metre further.
Embodiment 3
Blend components is identical with embodiment 1, and the parts by weight of each component are as shown in table 1; Twin screw extruder is added after each component being mixed in homogenizer, extrusion temperature is 230 DEG C, extrude, pelletizing, obtain the composition of high working property, ultra-thin breathable film after drying, be 2.0 times of initial length after also longitudinally being stretched by casting machine curtain coating, obtain air-permeable envelope product, the performance of gained film is as shown in table 2.
Embodiment 4
In blend components, also contain LDPE(MFR is 7.0g/10min), other blend components are identical with embodiment 1, and the parts by weight of each component are as shown in table 1; Film-forming method is identical with embodiment 1, and the performance of gained film is as shown in table 2.
Embodiment 5
Also containing ultra-fine form of finely divided powder, mehtod styrene-butadiene rubber(SBR) (patented product for the Sinopec Beijing Chemical Research Institute that patent US6423760 and CN00816450 etc. introduce) in blend components, other blend components are identical with embodiment 1, and the parts by weight of each component are as shown in table 1; Film-forming method is identical with embodiment 1, and the performance of gained film is as shown in table 2.
Rubber latex is obtained by spray drying process sulfuration by described form of finely divided powder, mehtod styrene-butadiene rubber(SBR), and product grade is VP101, and Beijing Chemical Research Institute produces, and its gel content is greater than 60wt%, swelling index is not more than 15.Form of finely divided powder, mehtod styrene-butadiene rubber(SBR) is nano level, can unrestricted flow and without the need to by separant, therefore there is good dispersiveness, join in high air-permeable envelope of filling, better can isolate mineral filler, thus obtain better dispersion effect, also there is certain lubrication simultaneously, the friction between melt and screw rod can be alleviated in the course of processing, improve the stability of processing and the efficiency of production.
Embodiment 6
Also containing LDPE(trade mark 1C7A in blend components, density is g/cm 3mFR is 7.0g/10min) and ultra-fine form of finely divided powder, mehtod styrene-butadiene rubber(SBR) (patented product for the Sinopec Beijing Chemical Research Institute that patent US6423760 and CN00816450 etc. introduce), other blend components are identical with embodiment 1, and the parts by weight of each component are as shown in table 1; Film-forming method is identical with embodiment 1, and the performance of gained film is as shown in table 2.
Table 1
Embodiment 1 2 3 4 5 6
Wide distribution MDPE 25 25 25 20 26 18
LLDPE 25 25 25 20 29 22
LDPE 0 0 0 10 0 5
Mineral filler 50 50 50 50 45 55
Dispersion agent 0 0 0 0 1 1
Oxidation inhibitor 0.3 0.3 0.3 0.3 0.3 0.3
Processing aid 0.7 0.7 0.7 0.7 0.7 0.7
Table 2
Embodiment 1 2 3 4 5 6
Stretch ratio 1.5 1.5 2.0 1.5 1.5 1.5
Longitudinal tensile strength, MPa 16.5 22.3 15.9 15.5 16.2 16.0
Longitudinal tensile strain rate, % 310 490 290 320 380 370
Transverse tensile strength, MPa 9.5 12.1 9.2 8.9 9.3 9.2
Cross direction elongation, % 440 580 300 450 460 450
Grammes per square metre, g/m 2 23 18 17 20 24 20
Water vapour permeability, g/m 2/24h 2800 3850 4000 3100 2500 3550

Claims (10)

1. prepare the composition of ultra-thin breathable film for one kind, contain in described composition: polyethylene blend, mineral filler, oxidation inhibitor and processing aid: be 100 parts in the gross weight of described polyethylene blend and described mineral filler, the weight of described polyethylene blend is 40 ~ 60 parts, the weight of described mineral filler is 40 ~ 60 parts, the weight of described oxidation inhibitor is 0.5 ~ 3 part, and the weight of described processing aid is 0.2 ~ 1.0 part;
Medium-density polyethylene containing wide distribution in described polyethylene blend and linear low density polyethylene;
The medium-density polyethylene of described wide distribution, its density is 0.935g/cm 3~ 0.945g/cm 3, melt flow rate (MFR) is 0.1g/10min ~ 8g/10min(190 DEG C, 2.16kg), molecular weight distribution is 8 ~ 20; Be 100 parts in the gross weight of described polyethylene blend, the weight of the medium-density polyethylene of described wide distribution is 30 ~ 70 parts;
Described linear low density polyethylene, its comonomer is butylene, hexene or octene, and catalyzer is Zieglor-Natta catalyzer or metallocene catalyst; Its density is 0.890g/cm 3~ 0.925g/cm 3, melt flow rate (MFR) is 1g/10min ~ 10g/10min(2.16kg, 190 DEG C); Be 100 parts in the gross weight of described polyethylene blend, the weight of described linear low density polyethylene is 30 ~ 70 parts;
Described mineral filler is selected from: one or more in calcium carbonate, barium sulfate, talcum powder or silicon-dioxide, and its particle diameter is 0.1 μm ~ 50 μm.
2. composition according to claim 1, is characterized in that:
The medium-density polyethylene of described wide distribution, its melt flow rate (MFR) is 2g/10min ~ 5g/10min(190 DEG C, 2.16kg), molecular weight distribution is 8 ~ 12; Be 100 parts in the gross weight of described polyethylene blend, the weight of the medium-density polyethylene of described wide distribution is 45 ~ 55 parts;
Described linear low density polyethylene, its melt flow rate (MFR) is 2g/10min ~ 5g/10min(2.16kg, 190 DEG C); Be 100 parts in the gross weight of described polyethylene blend, the weight of described linear low density polyethylene is 45 ~ 55 parts.
3. composition according to claim 1, is characterized in that:
Also containing Low Density Polyethylene in described polyethylene blend; Described Low Density Polyethylene, its melt flow rate (MFR) is 2g/cm 3~ 20g/cm 3(190 DEG C, 2.16kg);
Be 100 parts in the gross weight of described polyethylene blend, the weight of described Low Density Polyethylene is 1 ~ 20 part, and the weight of the medium-density polyethylene of described wide distribution is 40 ~ 55 parts, and the weight of described linear low density polyethylene is 40 ~ 55 parts.
4. composition according to claim 3, is characterized in that:
Described Low Density Polyethylene, its melt flow rate (MFR) is 4g/cm 3~ 7g/cm 3(190 DEG C, 2.16kg).
5. composition according to claim 1, is characterized in that:
Described mineral filler uses silane coupling agent or stearic acid to carry out surface modification; Be 100 parts in the gross weight of described polyethylene blend and described mineral filler, the weight of described mineral filler is 45 ~ 55 parts, and the weight of described polyethylene blend is 45 ~ 55 parts;
Described oxidation inhibitor is selected from: pentaerythritol tetrathioglycollate, four [methyl-β-(3,5-di-tert-butyl-hydroxy phenyl) propionic ester] pentaerythritol ester, three (2,4-di-t-butyl) phenyl-phosphite, propionic acid octadecyl, 1, one or more in 3 three (2-methyl-4-hydroxyl-5-tert-butyl-phenyl) butane or alkylation polyphenol.
6. composition according to claim 5, is characterized in that:
Described oxidation inhibitor is [methyl-β-(3,5-di-tert-butyl-hydroxy phenyl) propionic ester] pentaerythritol ester and three (2,4-di-t-butyl) phenyl-phosphite, [methyl-β-(3,5-di-tert-butyl-hydroxy phenyl) propionic ester] weight ratio of pentaerythritol ester and three (2,4-di-t-butyl) phenyl-phosphite is 2:1 ~ 1:2.
Described mineral filler is calcium carbonate, and its particle diameter is 0.1 μm ~ 3 μm;
Described processing aid is white oil or polyethylene wax.
7. composition according to claim 1, is characterized in that:
Also containing dispersion agent in described composition, be 100 parts in the gross weight of described polyethylene blend and described mineral filler, the weight of described dispersion agent is 0.5 ~ 3.0 part;
Described dispersion agent is ultra-fine fully vulcanized powder rubber, is selected from: one or more in full sulfuration styrene-butadiene rubber(SBR), full sulfuration carboxylic styrene-butadiene rubber, full vulcanized acrylate rubber, full-sulfurized nitrile rubber, full sulfuration carboxy nitrile rubber, full sulphurated siliastic or full sulfuration vinylpyridiene-styrene-butadiene rubber; The gel content of described ultra-fine fully vulcanized powder rubber is greater than 60wt%, particle diameter is 50 ~ 2000nm.
8. composition according to claim 7, is characterized in that:
Described ultra-fine fully vulcanized powder rubber is that full sulfuration styrene-butadiene rubber(SBR) is or/and full sulfuration carboxylic styrene-butadiene rubber; The particle diameter of described ultra-fine fully vulcanized powder rubber is 150 ~ 500nm.
9. adopt the described composition of one of claim 1 ~ 8 to prepare a method for ultra-thin breathable film, the method comprises the following steps:
1) by described polyethylene blend, described mineral filler, described oxidation inhibitor and described processing aid, or by described polyethylene blend, described mineral filler, described oxidation inhibitor, described processing aid and described dispersion agent, mix through high speed mixer;
2) material mixed is added twin screw extruder, extrudes, pelletizing drying, obtain the ultra-thin breathable film composition of high working property;
3) the ultra-thin breathable film composition curtain coating of described high working property is become film, then longitudinally stretch, stretch ratio is 1.5 ~ 5, obtains ultra-thin breathable film.
10. the method preparing ultra-thin breathable film according to claim 9, is characterized in that:
Described stretch ratio is 1.5 ~ 2.5.
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