CN107901566A - Breathable acrylonitrile-ethylene-styrene copolymer film composite paper and preparation method thereof - Google Patents
Breathable acrylonitrile-ethylene-styrene copolymer film composite paper and preparation method thereof Download PDFInfo
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- CN107901566A CN107901566A CN201711142830.8A CN201711142830A CN107901566A CN 107901566 A CN107901566 A CN 107901566A CN 201711142830 A CN201711142830 A CN 201711142830A CN 107901566 A CN107901566 A CN 107901566A
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- calcium carbonate
- film
- acrylonitrile
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- 238000002360 preparation method Methods 0.000 title claims abstract description 44
- 229920001923 acrylonitrile-ethylene-styrene Polymers 0.000 title claims abstract description 31
- 239000002131 composite material Substances 0.000 title abstract description 27
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims abstract description 67
- 239000002245 particle Substances 0.000 claims abstract description 39
- 229920001046 Nanocellulose Polymers 0.000 claims abstract description 31
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910000019 calcium carbonate Inorganic materials 0.000 claims abstract description 14
- 239000007822 coupling agent Substances 0.000 claims abstract description 11
- 238000002156 mixing Methods 0.000 claims abstract description 10
- 239000003960 organic solvent Substances 0.000 claims abstract description 9
- 238000001035 drying Methods 0.000 claims abstract description 5
- 238000007731 hot pressing Methods 0.000 claims abstract description 3
- 238000003490 calendering Methods 0.000 claims description 15
- 238000009826 distribution Methods 0.000 claims description 13
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 11
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 11
- 238000001125 extrusion Methods 0.000 claims description 7
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 claims description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical group OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 6
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 4
- -1 caprylyl titanate esters Chemical class 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 238000012545 processing Methods 0.000 claims description 3
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- 239000008187 granular material Substances 0.000 claims 5
- IJHFPIYBJZCNJS-UHFFFAOYSA-N C(=C)C=CC1=CC=CC=C1.C(=C)C#N Chemical compound C(=C)C=CC1=CC=CC=C1.C(=C)C#N IJHFPIYBJZCNJS-UHFFFAOYSA-N 0.000 claims 2
- FLKPEMZONWLCSK-UHFFFAOYSA-N diethyl phthalate Chemical compound CCOC(=O)C1=CC=CC=C1C(=O)OCC FLKPEMZONWLCSK-UHFFFAOYSA-N 0.000 claims 2
- PNWJXICONNROSM-UHFFFAOYSA-N ethene;prop-2-enenitrile;styrene Chemical compound C=C.C=CC#N.C=CC1=CC=CC=C1 PNWJXICONNROSM-UHFFFAOYSA-N 0.000 claims 2
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims 2
- VIZORQUEIQEFRT-UHFFFAOYSA-N Diethyl adipate Chemical compound CCOC(=O)CCCCC(=O)OCC VIZORQUEIQEFRT-UHFFFAOYSA-N 0.000 claims 1
- 229920001577 copolymer Polymers 0.000 claims 1
- 150000002148 esters Chemical class 0.000 claims 1
- 238000007765 extrusion coating Methods 0.000 claims 1
- 229920001519 homopolymer Polymers 0.000 claims 1
- 238000005304 joining Methods 0.000 claims 1
- ULWHHBHJGPPBCO-UHFFFAOYSA-N propane-1,1-diol Chemical class CCC(O)O ULWHHBHJGPPBCO-UHFFFAOYSA-N 0.000 claims 1
- 239000010453 quartz Substances 0.000 abstract description 24
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 24
- 239000000843 powder Substances 0.000 abstract description 23
- ZBBLRPRYYSJUCZ-GRHBHMESSA-L (z)-but-2-enedioate;dibutyltin(2+) Chemical compound [O-]C(=O)\C=C/C([O-])=O.CCCC[Sn+2]CCCC ZBBLRPRYYSJUCZ-GRHBHMESSA-L 0.000 abstract description 7
- LTMRRSWNXVJMBA-UHFFFAOYSA-L 2,2-diethylpropanedioate Chemical compound CCC(CC)(C([O-])=O)C([O-])=O LTMRRSWNXVJMBA-UHFFFAOYSA-L 0.000 abstract description 7
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 238000005096 rolling process Methods 0.000 abstract 1
- 239000000123 paper Substances 0.000 description 30
- 230000000052 comparative effect Effects 0.000 description 25
- 230000035699 permeability Effects 0.000 description 23
- 230000005540 biological transmission Effects 0.000 description 19
- 238000000034 method Methods 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 10
- 238000009998 heat setting Methods 0.000 description 6
- 239000002985 plastic film Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 235000012055 fruits and vegetables Nutrition 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000005022 packaging material Substances 0.000 description 3
- 229920006255 plastic film Polymers 0.000 description 3
- 229920005672 polyolefin resin Polymers 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- 230000003078 antioxidant effect Effects 0.000 description 2
- 239000012459 cleaning agent Substances 0.000 description 2
- 239000002270 dispersing agent Substances 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000010954 inorganic particle Substances 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical group CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000012438 extruded product Nutrition 0.000 description 1
- 235000021022 fresh fruits Nutrition 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920002285 poly(styrene-co-acrylonitrile) Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000001132 ultrasonic dispersion Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/06—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the heating method
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/002—Methods
-
- 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
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/22—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of indefinite length
- B29C43/24—Calendering
-
- 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
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/32—Component parts, details or accessories; Auxiliary operations
- B29C43/58—Measuring, controlling or regulating
-
- 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
- B29C48/0011—Combinations of extrusion moulding with other shaping operations combined with compression moulding
-
- 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
-
- 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
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- 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
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/10—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
- B29C55/12—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/10—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of paper or cardboard
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
- B32B27/302—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising aromatic vinyl (co)polymers, e.g. styrenic (co)polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B33/00—Layered products characterised by particular properties or particular surface features, e.g. particular surface coatings; Layered products designed for particular purposes not covered by another single class
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/10—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the pressing technique, e.g. using action of vacuum or fluid pressure
-
- 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
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/32—Component parts, details or accessories; Auxiliary operations
- B29C43/58—Measuring, controlling or regulating
- B29C2043/5816—Measuring, controlling or regulating temperature
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2007/00—Flat articles, e.g. films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/724—Permeability to gases, adsorption
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Laminated Bodies (AREA)
Abstract
Description
技术领域technical field
本发明涉及透气薄膜,具体地,涉及透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸及其制备方法。The invention relates to a breathable film, in particular to a breathable acrylonitrile-ethylene-styrene copolymer film composite paper and a preparation method thereof.
背景技术Background technique
任何一种包装材料包括塑料薄膜或可食用薄膜,对氧气、氮气、二氧化碳以及水蒸气的通透性测定十分重要,特别是用于果蔬保鲜的包装材料,其透气性非常重要,这是因为具有合适透气性的薄膜,才能对果蔬后的生理代谢获得起到一定的调控作用,从而提高果蔬的食用品质、延长果蔬的架货寿命,对此,为了获得具有良好透气性的材料,人们进行了广泛的研究。Any kind of packaging material, including plastic film or edible film, is very important to determine the permeability of oxygen, nitrogen, carbon dioxide and water vapor, especially the packaging material used for fresh fruit and vegetable preservation, its air permeability is very important, because it has A film with suitable air permeability can regulate the physiological metabolism of fruits and vegetables to a certain extent, thereby improving the eating quality of fruits and vegetables and prolonging the shelf life of fruits and vegetables. In this regard, in order to obtain materials with good air permeability, people have carried out Extensive research.
中国专利申请201110203184.8公开了一种低透气量透气膜的组合物及其制备方法,其组分包括:聚烯烃树脂混合物、透气量调节剂、表面改性的微米级无机粒子、抗氧剂、润滑剂和偶联剂。其优点在于纳微米无机填料能够提高透气膜的力学性能,同时表面偶联改性的无机粒子增加了与聚烯烃基体树脂的相容性,但不足之处在于高添加量(30%-55%)的微米无机粒子不能够很好地均匀分散在基体树脂中,从而影响了薄膜材料的透气均匀性。Chinese patent application 201110203184.8 discloses a composition and a preparation method of a low-air-permeable air-permeable membrane. agents and coupling agents. Its advantage is that the nano-micron inorganic filler can improve the mechanical properties of the breathable film, and the surface coupling modified inorganic particles increase the compatibility with the polyolefin matrix resin, but the disadvantage is that the high addition amount (30%-55% ) micron inorganic particles can not be uniformly dispersed in the matrix resin, thus affecting the uniformity of air permeability of the film material.
中国专利申请201110125458.6公开了一种聚烯烃薄膜及其制备方法,其组分包括:聚烯烃树脂、成孔剂和萃取剂。其优点在于所采用传统湿法制备的聚丙烯烃薄膜的结构小、数量多,但其采用两步高体积百分比浓度的萃取过程,其萃取溶剂为N,N’-二甲基甲酰胺、二氯甲烷、三氯甲烷等属于高污染、有毒溶剂,可对人体和环境造成巨大伤害。Chinese patent application 201110125458.6 discloses a polyolefin film and its preparation method, the components of which include: polyolefin resin, pore forming agent and extractant. Its advantage is that the polypropylene hydrocarbon film prepared by the traditional wet method has a small structure and a large number, but it adopts a two-step extraction process with a high volume percentage concentration, and the extraction solvent is N, N'-dimethylformamide, dichloro Methane, chloroform, etc. are highly polluting and toxic solvents, which can cause great harm to the human body and the environment.
中国专利申请201710110501.9公开了一种透气性复合薄膜及其制备方法,该复合薄膜由如下重量百分比的组分制备而成:60%-82%的聚烯烃树脂聚合物、2%-8%微纳米晶纤维素粒子、0.4%-1%抗氧剂、15%-30%分散剂、0.1%-0.5%润滑剂、0.2%-1%偶联剂。其制备方法如下:将微纳米晶纤维素水分散液和偶联剂分散均匀;再加入分散剂混合均匀,并干燥得预处理填料;将所得到的预处理填料、聚烯烃树脂、抗氧剂、润滑剂添加到双螺杆挤出机中,经过熔融挤出、冷却和造粒得透气性复合薄膜组成物,热压延制备平整薄膜;再浸入清洗剂中,超声、干燥;双向拉伸并进行热定型处理,得透气性复合薄膜。该复合薄膜透气性能高效、机械性能优良。缺点是需要浸入清洗剂中,处理过程较繁琐。Chinese patent application 201710110501.9 discloses a breathable composite film and its preparation method. The composite film is prepared from the following components by weight percentage: 60%-82% polyolefin resin polymer, 2%-8% micronano Crystalline cellulose particles, 0.4%-1% antioxidant, 15%-30% dispersant, 0.1%-0.5% lubricant, 0.2%-1% coupling agent. The preparation method is as follows: uniformly disperse the micro-nanocrystalline cellulose aqueous dispersion and the coupling agent; then add the dispersant and mix evenly, and dry to obtain the pretreated filler; the obtained pretreated filler, polyolefin resin, antioxidant , Lubricant is added to the twin-screw extruder, and the breathable composite film composition is obtained through melt extrusion, cooling and granulation, and the flat film is prepared by hot calendering; then immersed in the cleaning agent, ultrasonicated, and dried; two-way stretching and Heat-setting treatment to obtain a breathable composite film. The composite film has high air permeability and excellent mechanical properties. The disadvantage is that it needs to be immersed in the cleaning agent, and the processing process is cumbersome.
因此,非常有必要提供一种制备方法简单且具有良好的透气性的薄膜。Therefore, it is very necessary to provide a film with simple preparation method and good air permeability.
发明内容Contents of the invention
本发明的目的是提供一种透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸及其制备方法,该透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸的薄膜层既具有良好的抗拉强度,又具有良好的透气性,并且制备方法简单,易于实现。The purpose of this invention is to provide a kind of breathable acrylonitrile-ethylene-styrene copolymer film composite paper and preparation method thereof, the film layer of this breathable acrylonitrile-ethylene-styrene copolymer film composite paper has good tensile strength , and has good gas permeability, and the preparation method is simple and easy to realize.
为了实现上述目的,本发明提供了透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸的制备方法,包括以下步骤:(1)将碳酸钙、有机溶剂和钛酸酯偶联剂超声分散,烘干,得到改性碳酸钙;(2)将改性碳酸钙、微纳米晶纤维素粒子、多孔粉石英、丙烯腈-乙烯-苯乙烯共聚物、丙二酸二乙酯和马来酸二丁基锡共混,挤出;(3)将挤出物进行压延,双向拉伸,制得薄膜;(4)将薄膜进行加热并热压于纸质层的表面上;其中,改性碳酸钙、微纳米晶纤维素粒子和多孔粉石英的质量比为1:1-2:2-4。In order to achieve the above object, the present invention provides a preparation method of air-permeable acrylonitrile-ethylene-styrene copolymer film composite paper, comprising the following steps: (1) calcium carbonate, organic solvent and titanate coupling agent are ultrasonically dispersed, baked Dry to obtain modified calcium carbonate; (2) modify calcium carbonate, micro-nanocrystalline cellulose particles, porous powder quartz, acrylonitrile-ethylene-styrene copolymer, diethyl malonate and dibutyltin maleate blending and extruding; (3) calendering and biaxially stretching the extrudate to obtain a film; (4) heating and pressing the film on the surface of the paper layer; wherein, modified calcium carbonate, micro The mass ratio of nanocrystalline cellulose particles to porous powder quartz is 1:1-2:2-4.
本发明还提供一种根据前文所述的制备方法制备得到的透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸。The present invention also provides a breathable acrylonitrile-ethylene-styrene copolymer film composite paper prepared according to the above-mentioned preparation method.
通过上述技术方案,本发明通过对碳酸钙进行改性,又通过将改性碳酸钙、微纳米晶纤维素粒子、多孔粉石英进行配比并添加进丙烯腈-乙烯-苯乙烯共聚物为基体的薄膜制备原料中,通过挤出,压延,双向拉伸工艺,制备了具有抗拉强度良好并且具有良好透气性的薄膜,将薄膜进行加热并热压于纸质层的表面上制得薄膜复合纸,该制备方法简单,易于实现,具有较好的推广价值。Through the above technical scheme, the present invention modifies the calcium carbonate, and mixes the modified calcium carbonate, micro-nanocrystalline cellulose particles, and porous powder quartz and adds it into the acrylonitrile-ethylene-styrene copolymer as the matrix Among the raw materials for film preparation, a film with good tensile strength and good air permeability is prepared through extrusion, calendering, and biaxial stretching processes, and the film is heated and hot-pressed on the surface of the paper layer to obtain a film composite paper, the preparation method is simple, easy to implement, and has good promotion value.
本发明的其他特征和优点将在随后的具体实施方式部分予以详细说明。Other features and advantages of the present invention will be described in detail in the following detailed description.
具体实施方式Detailed ways
以下对本发明的具体实施方式进行详细说明。应当理解的是,此处所描述的具体实施方式仅用于说明和解释本发明,并不用于限制本发明。Specific embodiments of the present invention will be described in detail below. It should be understood that the specific embodiments described here are only used to illustrate and explain the present invention, and are not intended to limit the present invention.
在本文中所披露的范围的端点和任何值都不限于该精确的范围或值,这些范围或值应当理解为包含接近这些范围或值的值。对于数值范围来说,各个范围的端点值之间、各个范围的端点值和单独的点值之间,以及单独的点值之间可以彼此组合而得到一个或多个新的数值范围,这些数值范围应被视为在本文中具体公开。Neither the endpoints nor any values of the ranges disclosed herein are limited to such precise ranges or values, and these ranges or values are understood to include values approaching these ranges or values. For numerical ranges, between the endpoints of each range, between the endpoints of each range and individual point values, and between individual point values can be combined with each other to obtain one or more new numerical ranges, these values Ranges should be considered as specifically disclosed herein.
本发明提供了透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸的制备方法,包括以下步骤:(1)将碳酸钙、有机溶剂和钛酸酯偶联剂超声分散,烘干,得到改性碳酸钙;(2)将改性碳酸钙、微纳米晶纤维素粒子、多孔粉石英、丙烯腈-乙烯-苯乙烯共聚物、丙二酸二乙酯和马来酸二丁基锡共混,挤出;(3)将挤出物进行压延,双向拉伸,制得薄膜;(4)将薄膜进行加热并热压于纸质层的表面上;其中,改性碳酸钙、微纳米晶纤维素粒子和多孔粉石英的质量比为1:1-2:2-4。The invention provides a method for preparing air-permeable acrylonitrile-ethylene-styrene copolymer film composite paper, comprising the following steps: (1) ultrasonically dispersing calcium carbonate, an organic solvent and a titanate coupling agent, and drying to obtain a modified Calcium carbonate; (2) Modified calcium carbonate, micro-nanocrystalline cellulose particles, porous powder quartz, acrylonitrile-ethylene-styrene copolymer, diethyl malonate and dibutyltin maleate are blended, extruded (3) calendering and biaxially stretching the extruded product to obtain a film; (4) heating the film and hot pressing it on the surface of the paper layer; wherein, modified calcium carbonate, micro-nanocrystalline cellulose particles The mass ratio to porous powder quartz is 1:1-2:2-4.
通过上述技术方案,本发明通过对碳酸钙进行改性,又通过将改性碳酸钙、微纳米晶纤维素粒子、多孔粉石英进行配比并添加进丙烯腈-乙烯-苯乙烯共聚物为基体的薄膜制备原料中,通过挤出,压延,双向拉伸工艺,制备了具有抗拉强度良好并且具有良好透气性的薄膜,该制备方法简单,易于实现,具有较好的推广价值。Through the above technical scheme, the present invention modifies the calcium carbonate, and mixes the modified calcium carbonate, micro-nanocrystalline cellulose particles, and porous powder quartz and adds it into the acrylonitrile-ethylene-styrene copolymer as the matrix Among the raw materials for film preparation, a film with good tensile strength and good air permeability is prepared through extrusion, calendering and biaxial stretching processes. The preparation method is simple, easy to implement, and has good promotion value.
在上述技术方案中,只要按照上述配比即可得到具有良好透气性的薄膜,对于各组分的添加量,本领域技术人员可在较宽范围内进行调整。为了使薄膜既具有良好的抗拉强度,又具有良好的透气性,优选地,相对于100重量份的丙烯腈-乙烯-苯乙烯共聚物,添加的改性碳酸钙、微纳米晶纤维素粒子和多孔粉石英的总重量份为15-25份。In the above technical solution, as long as the above ratio is followed, a film with good air permeability can be obtained, and the addition amount of each component can be adjusted within a wide range by those skilled in the art. In order to make the film have both good tensile strength and good air permeability, preferably, relative to 100 parts by weight of acrylonitrile-ethylene-styrene copolymer, the added modified calcium carbonate, micro-nanocrystalline cellulose particles and the total weight of porous powder quartz is 15-25 parts.
对于本发明的制备工艺的具体条件,本领域技术人员可灵活调整,为了提高材料的抗拉强度,并使薄膜具有良好的透气性,并降低挤压过程中的粘杆现象,优选地,步骤(3)中压延的条件包括:将挤出物在200-220℃以20t-40t的压力下进行热压延。For the specific conditions of the preparation process of the present invention, those skilled in the art can adjust flexibly. In order to improve the tensile strength of the material, and make the film have good air permeability, and reduce the sticking phenomenon in the extrusion process, preferably, the step (3) Conditions for middle calendering include: hot calendering the extrudate at 200-220° C. under a pressure of 20t-40t.
对于本发明的制备工艺的具体条件,本领域技术人员可灵活调整,为了提高材料的抗拉强度,并使薄膜具有良好的透气性,优选地,双向拉伸的条件包括:将压延后得到的薄膜进行双向拉伸,拉伸倍率为1.2-1.8,然后在130-160℃进行热定型处理,热定型处理时间为5-15min。For the specific conditions of the preparation process of the present invention, those skilled in the art can adjust flexibly. In order to improve the tensile strength of the material and make the film have good air permeability, preferably, the conditions of biaxial stretching include: The film is biaxially stretched with a stretch ratio of 1.2-1.8, and then subjected to heat setting treatment at 130-160° C., and the heat setting treatment time is 5-15 minutes.
对于碳酸钙的改性,本领域技术人员可在较宽范围内进行调整,为了提高改性碳酸钙与微纳米晶纤维素粒子、多孔粉石英配比后能够提高薄膜的透气性,并不降低薄膜的抗拉强度,优选地,步骤(1)中,碳酸钙、有机溶剂和钛酸酯偶联剂的质量比为1:2-3:0.4-0.6。For the modification of calcium carbonate, those skilled in the art can adjust in a wide range. In order to improve the ratio of modified calcium carbonate to micro-nanocrystalline cellulose particles and porous powder quartz, the air permeability of the film can be improved without reducing The tensile strength of the film, preferably, in step (1), the mass ratio of calcium carbonate, organic solvent and titanate coupling agent is 1:2-3:0.4-0.6.
对于碳酸钙的改性的具体工艺,本领域技术人员可在较宽范围内进行调整,为了提高改性碳酸钙与微纳米晶纤维素粒子、多孔粉石英配比后能够提高薄膜的透气性,并不降低薄膜的抗拉强度,优选地,超声分散时间为10-20min,烘干温度为40-90℃。For the specific process of the modification of calcium carbonate, those skilled in the art can adjust in a wide range, in order to improve the air permeability of the film after improving the ratio of modified calcium carbonate and micro-nanocrystalline cellulose particles, porous powder quartz, Without reducing the tensile strength of the film, preferably, the ultrasonic dispersion time is 10-20 min, and the drying temperature is 40-90°C.
在上述技术方案中,钛酸酯偶联剂可在较宽范围内进行选择,为了提高改性碳酸钙与微纳米晶纤维素粒子、多孔粉石英配比后能够提高薄膜的透气性,并不降低薄膜的抗拉强度,优选地,钛酸酯偶联剂为异丙基三异硬脂基钛酸酯和/或异丙基三辛酰基钛酸酯。In the above technical scheme, the titanate coupling agent can be selected in a wide range. In order to improve the air permeability of the film after improving the ratio of modified calcium carbonate to micro-nanocrystalline cellulose particles and porous powder quartz, it does not To reduce the tensile strength of the film, preferably, the titanate coupling agent is isopropyl triisostearyl titanate and/or isopropyl trioctanoyl titanate.
在上述技术方案中,有机溶剂可在较宽范围内进行选择,优选地,有机溶剂为甲醇、乙醇、丙二醇、二乙二醇、丙酮、四氢呋喃、季戊四醇中的一种或多种。In the above technical solution, the organic solvent can be selected in a wide range. Preferably, the organic solvent is one or more of methanol, ethanol, propylene glycol, diethylene glycol, acetone, tetrahydrofuran, and pentaerythritol.
在上述技术方案中,纸质层可在较宽范围内进行选择,为了使薄膜层于纸质层结合性较好,优选地,纸质层为牛皮纸或波纹纸。In the above technical solution, the paper layer can be selected in a wide range. In order to make the film layer better bonded to the paper layer, preferably, the paper layer is kraft paper or corrugated paper.
当然,对于各组分的添加量,本领域技术人员可在较宽范围内进行调整,为了使得到的薄膜具有良好的抗拉强度和透气性,优选地,以重量份计,相对于100份的丙烯腈-乙烯-苯乙烯共聚物,改性碳酸钙3-4份,微纳米晶纤维素粒子4-6份,多孔粉石英8-12份,丙二酸二乙酯3-6份,马来酸二丁基锡1-2份。Of course, those skilled in the art can adjust the addition amount of each component in a wide range. In order to make the obtained film have good tensile strength and air permeability, preferably, in parts by weight, relative to 100 parts Acrylonitrile-ethylene-styrene copolymer, 3-4 parts of modified calcium carbonate, 4-6 parts of micro-nanocrystalline cellulose particles, 8-12 parts of porous powder quartz, 3-6 parts of diethyl malonate, 1-2 parts of dibutyltin maleate.
其中,为了使得到的薄膜具有良好的抗拉强度和透气性,优选地,微纳米晶纤维素粒子的粒径分布为100nm-50μm。Wherein, in order to make the obtained film have good tensile strength and air permeability, preferably, the particle size distribution of the micro-nanocrystalline cellulose particles is 100nm-50μm.
其中,为了使得到的薄膜具有良好的抗拉强度和透气性,优选地,多孔粉石英的平均直径为不大于0.8μm。Wherein, in order to make the obtained film have good tensile strength and gas permeability, preferably, the average diameter of the porous powdered quartz is not greater than 0.8 μm.
对于步骤(2)中的共混条件,本领域技术人员可在较宽范围内进行调整,为了提高混合的均匀性,优选地,步骤(2)中:共混温度为180-195℃,混炼时间为30-40min。For the blending conditions in step (2), those skilled in the art can adjust within a wide range. In order to improve the uniformity of mixing, preferably, in step (2): the blending temperature is 180-195° C. Refining time is 30-40min.
更进一步,为了提高薄膜的抗拉强度,优选地,步骤(2)中的挤出温度为200-215℃。Furthermore, in order to increase the tensile strength of the film, preferably, the extrusion temperature in step (2) is 200-215°C.
本发明还提供一种根据前文所述的制备方法制备得到的透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸。该薄膜既具有抗拉强度并且具有良好透气性,将薄膜进行加热并热压于纸质层的表面上,即可得该薄膜复合纸,该薄膜复合纸既具有良好的抗拉强度,又具有良好的透气性,非常适合作为果蔬的包装材料。The present invention also provides a breathable acrylonitrile-ethylene-styrene copolymer film composite paper prepared according to the above-mentioned preparation method. The film has both tensile strength and good air permeability, and the film is heated and hot-pressed on the surface of the paper layer to obtain the film composite paper. The film composite paper not only has good tensile strength, but also has Good air permeability, very suitable as packaging materials for fruits and vegetables.
以下将通过实施例对本发明进行详细描述。The present invention will be described in detail below by way of examples.
乙烯-丙烯-苯乙烯-丙烯腈共聚物来自于常州市安得鑫化工有限公司;微纳米晶纤维素粒子购自上海三思科技材料有限公司;其他为常规市售品。Ethylene-propylene-styrene-acrylonitrile copolymer was purchased from Changzhou Andexin Chemical Co., Ltd.; micro-nanocrystalline cellulose particles were purchased from Shanghai Sansi Technology Materials Co., Ltd.; others were commercially available.
制备例1Preparation Example 1
以重量份计,将1份碳酸钙,2份乙醇和0.4份异丙基三辛酰基钛酸酯超声分散20min,于90℃烘干,得到改性碳酸钙。In parts by weight, 1 part of calcium carbonate, 2 parts of ethanol and 0.4 part of isopropyl tricaprylyl titanate were ultrasonically dispersed for 20 minutes, and dried at 90° C. to obtain modified calcium carbonate.
制备例2Preparation example 2
以重量份计,将1份碳酸钙,3份乙醇和0.6份异丙基三异硬脂基钛酸酯超声分散10min,于40℃烘干,得到改性碳酸钙。In parts by weight, 1 part of calcium carbonate, 3 parts of ethanol and 0.6 part of isopropyl triisostearyl titanate were ultrasonically dispersed for 10 minutes, and dried at 40° C. to obtain modified calcium carbonate.
制备例3Preparation example 3
以重量份计,将1份碳酸钙,2.5份乙醇和0.5份异丙基三异硬脂基钛酸酯超声分散15min,于70℃烘干,得到改性碳酸钙。In parts by weight, 1 part of calcium carbonate, 2.5 parts of ethanol and 0.5 part of isopropyl triisostearyl titanate were ultrasonically dispersed for 15 minutes, and dried at 70° C. to obtain modified calcium carbonate.
实施例1Example 1
透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸的制备方法,包括以下步骤:The preparation method of breathable acrylonitrile-ethylene-styrene copolymer film composite paper comprises the following steps:
(1)以重量份计,将100份的丙烯腈-乙烯-苯乙烯共聚物,制备例1中的改性碳酸钙3份,微纳米晶纤维素粒子(粒径分布为10μm-50μm)4份,多孔粉石英(平均直径为不大于0.8μm)8份,丙二酸二乙酯3份,马来酸二丁基锡1份于180℃共混,混炼时间为30min,于200℃挤出;(1) In parts by weight, with 100 parts of acrylonitrile-ethylene-styrene copolymer, 3 parts of modified calcium carbonate in Preparation Example 1, micro-nanocrystalline cellulose particles (particle size distribution is 10 μm-50 μm) 4 Parts, 8 parts of porous powder quartz (average diameter not greater than 0.8 μm), 3 parts of diethyl malonate, 1 part of dibutyltin maleate were blended at 180°C, the mixing time was 30min, and extruded at 200°C ;
(2)将挤出物在200℃以20t的压力下进行热压延,将压延后得到的薄膜进行双向拉伸,拉伸倍率为1.2,然后在130℃进行热定型处理,热定型处理时间为5min;(2) The extrudate is hot-calendered at 200°C under a pressure of 20t, and the film obtained after calendering is biaxially stretched to a stretch ratio of 1.2, and then heat-set at 130°C for a heat-setting time of 5min;
(3)将拉伸后的薄膜进行加热并于180℃热压于纸质层的表面上。(3) The stretched film is heated and hot-pressed on the surface of the paper layer at 180°C.
实施例2Example 2
透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸的制备方法,包括以下步骤:The preparation method of breathable acrylonitrile-ethylene-styrene copolymer film composite paper comprises the following steps:
(1)以重量份计,将100份的丙烯腈-乙烯-苯乙烯共聚物,制备例2中的改性碳酸钙4份,微纳米晶纤维素粒子(粒径分布为100nm-20μm)6份,多孔粉石英(平均直径为不大于0.8μm)12份,丙二酸二乙酯6份,马来酸二丁基锡2份于195℃共混,混炼时间为40min,于215℃挤出;(1) In parts by weight, with 100 parts of acrylonitrile-ethylene-styrene copolymer, 4 parts of modified calcium carbonate in Preparation Example 2, micro-nanocrystalline cellulose particles (particle size distribution is 100nm-20 μm) 6 Parts, 12 parts of porous powder quartz (average diameter not greater than 0.8μm), 6 parts of diethyl malonate, 2 parts of dibutyltin maleate were blended at 195°C, the mixing time was 40min, and extruded at 215°C ;
(2)将挤出物在220℃以40t的压力下进行热压延,将压延后得到的薄膜进行双向拉伸,拉伸倍率为1.8,然后在160℃进行热定型处理,热定型处理时间为15min;(2) The extrudate is hot-calendered at 220°C under a pressure of 40t, and the film obtained after calendering is biaxially stretched to a stretch ratio of 1.8, and then heat-set at 160°C for a heat-setting time of 15min;
(3)将拉伸后的薄膜进行加热并于170℃热压于纸质层的表面上。(3) The stretched film is heated and hot-pressed on the surface of the paper layer at 170°C.
实施例3Example 3
透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸的制备方法,包括以下步骤:The preparation method of breathable acrylonitrile-ethylene-styrene copolymer film composite paper comprises the following steps:
(1)以重量份计,将100份的丙烯腈-乙烯-苯乙烯共聚物,制备例3中的改性碳酸钙3.5份,微纳米晶纤维素粒子(粒径分布为10-30μm)5份,多孔粉石英(平均直径为不大于0.8μm)10份,丙二酸二乙酯4.5份,马来酸二丁基锡1.5份于188℃共混,混炼时间为35min,于205℃挤出;(1) In parts by weight, with 100 parts of acrylonitrile-ethylene-styrene copolymer, 3.5 parts of modified calcium carbonate in Preparation Example 3, micro-nanocrystalline cellulose particles (particle size distribution is 10-30 μm) 5 parts Parts, 10 parts of porous powder quartz (average diameter not greater than 0.8 μm), 4.5 parts of diethyl malonate, 1.5 parts of dibutyltin maleate were blended at 188 ° C, the mixing time was 35 minutes, and extruded at 205 ° C ;
(2)将挤出物在210℃以30t的压力下进行热压延,将压延后得到的薄膜进行双向拉伸,拉伸倍率为1.5,然后在145℃进行热定型处理,热定型处理时间为10min;(2) The extrudate is hot-calendered at 210°C under a pressure of 30t, and the film obtained after calendering is biaxially stretched to a stretch ratio of 1.5, and then heat-set at 145°C for a heat-setting time of 10min;
(3)将拉伸后的薄膜进行加热并于190℃热压于纸质层的表面上。(3) The stretched film was heated and hot-pressed on the surface of the paper layer at 190°C.
实施例4Example 4
按照实施例3的方法制备透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸,不同的是,制备例3中的改性碳酸钙2份,微纳米晶纤维素粒子(粒径分布为粒径分布为10-30μm)4份,多孔粉石英(平均直径为不大于0.8μm)8份。Prepare air-permeable acrylonitrile-ethylene-styrene copolymer film composite paper according to the method of embodiment 3, the difference is that 2 parts of modified calcium carbonate in preparation example 3, micro-nanocrystalline cellulose particles (particle size distribution is particle size The distribution is 10-30 μm) 4 parts, porous powder quartz (average diameter is not more than 0.8 μm) 8 parts.
实施例5Example 5
按照实施例3的方法制备透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸,不同的是,制备例3中的改性碳酸钙5份,微纳米晶纤维素粒子(粒径分布为粒径分布为10-30μm)5份,多孔粉石英(平均直径为不大于0.8μm)20份。Prepare air-permeable acrylonitrile-ethylene-styrene copolymer film composite paper according to the method of embodiment 3, the difference is that 5 parts of modified calcium carbonate in preparation example 3, micro-nanocrystalline cellulose particles (particle size distribution is particle size The distribution is 10-30μm) 5 parts, porous powder quartz (average diameter is not more than 0.8μm) 20 parts.
实施例6Example 6
按照实施例3的方法制备透气丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸,不同的是,制备例3中的改性碳酸钙1份,微纳米晶纤维素粒子(粒径分布为粒径分布为10-30μm)2份,多孔粉石英(平均直径为不大于0.8μm)4份。Prepare air-permeable acrylonitrile-ethylene-styrene copolymer film composite paper according to the method of embodiment 3, the difference is, 1 part of modified calcium carbonate in preparation example 3, micro-nanocrystalline cellulose particle (particle size distribution is particle size The distribution is 10-30μm) 2 parts, porous powder quartz (average diameter is not more than 0.8μm) 4 parts.
对比例1Comparative example 1
按照实施例3的方法制备丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸,不同的是,将实施例3中所用的改性碳酸钙3.5份变更为未改性的碳酸钙3.5份。According to the method for embodiment 3, acrylonitrile-ethylene-styrene copolymer film composite paper is prepared, and difference is that 3.5 parts of modified calcium carbonate used in embodiment 3 are changed into 3.5 parts of unmodified calcium carbonate.
对比例2Comparative example 2
按照实施例3的方法制备丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸,不同的是,将添加的改性碳酸钙、微纳米晶纤维素粒子和多孔粉石英变更为:Acrylonitrile-ethylene-styrene copolymer film composite paper is prepared according to the method of Example 3, and the difference is that the added modified calcium carbonate, micro-nanocrystalline cellulose particles and porous powder quartz are changed to:
制备例3中的改性碳酸钙5份,微纳米晶纤维素粒子(粒径分布为粒径分布为10-30μm)2份,多孔粉石英(平均直径为不大于0.8μm)7份。5 parts of modified calcium carbonate in Preparation Example 3, 2 parts of micro-nanocrystalline cellulose particles (the particle size distribution is 10-30 μm), and 7 parts of porous powder quartz (average diameter is not more than 0.8 μm).
对比例3Comparative example 3
按照实施例3的方法制备丙烯腈-乙烯-苯乙烯共聚物薄膜复合纸,不同的是,将添加的改性碳酸钙、微纳米晶纤维素粒子和多孔粉石英变更为:Acrylonitrile-ethylene-styrene copolymer film composite paper is prepared according to the method of Example 3, and the difference is that the added modified calcium carbonate, micro-nanocrystalline cellulose particles and porous powder quartz are changed to:
制备例3中的改性碳酸钙2份,微纳米晶纤维素粒子(粒径分布为粒径分布为10-30μm)8份,多孔粉石英(平均直径为不大于0.8μm)3份。2 parts of modified calcium carbonate in Preparation Example 3, 8 parts of micro-nanocrystalline cellulose particles (the particle size distribution is 10-30 μm), and 3 parts of porous powder quartz (average diameter is not more than 0.8 μm).
检测例1Test example 1
氧气透过率(单位为mL/m2,天,标准大气压)测试采用型号为8001的氧气透过率测试仪进行测定,对应标准为GB/T1038-2000塑料薄膜和薄片气体透过性试验方法。Oxygen transmission rate (unit: mL/m 2 , day, standard atmospheric pressure) is measured by an oxygen transmission rate tester model 8001, and the corresponding standard is GB/T1038-2000 Plastic Film and Sheet Gas Permeability Test Method .
经对实施例1-6以及对比例1-3中的制备的薄膜进行检测,发现氧气透过率从高到低的顺序依次是:实施例5、实施例3、实施例2、实施例1、实施例4、实施例6、对比例2、对比例1、对比例3,其中,实施例5的氧气透过率最高,为2950mL/m2,实施例3、实施例2和实施例1的氧气透过率接近,其中实施例3的氧气透过率为1952mL/m2,实施例4和实施例6的氧气透过率接近,实施例6为1710mL/m2;对比例2、对比例1和对比例3中薄膜的氧气透过率较低,其中,对比例2的氧气透过率仅为1518mL/m2。After detecting the films prepared in Examples 1-6 and Comparative Examples 1-3, it was found that the order of oxygen transmission rate from high to low is: Example 5, Example 3, Example 2, Example 1 , Example 4, Example 6, Comparative Example 2, Comparative Example 1, and Comparative Example 3, wherein the oxygen transmission rate of Example 5 is the highest at 2950mL/m 2 , and Example 3, Example 2 and Example 1 The oxygen transmission rate is close, wherein the oxygen transmission rate of embodiment 3 is 1952mL/m 2 , the oxygen transmission rate of embodiment 4 and embodiment 6 is close, and embodiment 6 is 1710mL/m 2 ; The oxygen transmission rate of the film in Example 1 and Comparative Example 3 is relatively low, and the oxygen transmission rate of Comparative Example 2 is only 1518mL/m 2 .
检测例2Test example 2
水蒸气透过率(单位为mL/m2)测试采用型号为Model 3/33水蒸气透过率测试仪进行检测,对应标准为GB/T 30412-2013塑料薄膜和薄片水蒸气透过率的测定。The water vapor transmission rate (unit: mL/m 2 ) is tested with a Model 3/33 water vapor transmission rate tester, and the corresponding standard is GB/T 30412-2013 Water vapor transmission rate of plastic films and sheets Determination.
经对实施例1-6以及对比例1-3中的制备的薄膜进行检测,发现水蒸气透过率从高到低的顺序依次是:实施例5、实施例3、实施例2、实施例1、实施例4、实施例6、对比例2、对比例1、对比例3,其中,实施例5的水蒸气透过率最高,为8.6mL/m2,实施例3、实施例2和实施例1的水蒸气透过率接近,其中实施例3的水蒸气透过率为7.2mL/m2,实施例4和实施例6的水蒸气透过率接近,实施例6为6.4mL/m2;对比例2、对比例1和对比例3中薄膜的水蒸气透过率较低,其中,对比例2的水蒸气透过率仅为4.6mL/m2。After detecting the films prepared in Examples 1-6 and Comparative Examples 1-3, it was found that the order of water vapor transmission rate from high to low is: Example 5, Example 3, Example 2, Example 1. Example 4, Example 6, Comparative Example 2, Comparative Example 1, and Comparative Example 3. Among them, Example 5 has the highest water vapor transmission rate of 8.6mL/m 2 , and Example 3, Example 2 and The water vapor transmission rate of embodiment 1 is close, wherein the water vapor transmission rate of embodiment 3 is 7.2mL/m 2 , the water vapor transmission rate of embodiment 4 and embodiment 6 is close, and embodiment 6 is 6.4mL/m m 2 ; the water vapor transmission rate of the films in Comparative Example 2, Comparative Example 1 and Comparative Example 3 was low, and the water vapor transmission rate of Comparative Example 2 was only 4.6mL/m 2 .
检测例3Test example 3
抗拉强度(单位为MPa)参数是通过GB/T1040.1-2006塑料拉伸性能的测定第1部分进行检测。The parameter of tensile strength (in MPa) is detected by the first part of GB/T1040.1-2006 Determination of tensile properties of plastics.
经对实施例1-6以及对比例1-3中的制备的薄膜进行检测,发现抗拉强度从高到低的顺序依次是:对比例3、实施例3、实施例2、实施例1、实施例6、实施例4、实施例5、对比例1、对比例2,其中,对比例3的抗拉强度最高,为19.2MPa,实施例3、实施例2和实施例1的抗拉强度接近,其中实施例3的抗拉强度为17.8MPa,实施例4、实施例5和实施例6的抗拉强度接近,实施例5为14.9MPa;对比例2、对比例1中薄膜的抗拉强度较低,其中,对比例2的抗拉强度仅为11.5MPa。After detecting the films prepared in Examples 1-6 and Comparative Examples 1-3, it was found that the order of tensile strength from high to low is: Comparative Example 3, Example 3, Example 2, Example 1, Embodiment 6, embodiment 4, embodiment 5, comparative example 1, comparative example 2, wherein, the tensile strength of comparative example 3 is the highest, is 19.2MPa, the tensile strength of embodiment 3, embodiment 2 and embodiment 1 Close, wherein the tensile strength of embodiment 3 is 17.8MPa, the tensile strength of embodiment 4, embodiment 5 and embodiment 6 is close, and embodiment 5 is 14.9MPa; The tensile strength of film in comparative example 2, comparative example 1 The strength is low, and the tensile strength of Comparative Example 2 is only 11.5MPa.
以上详细描述了本发明的优选实施方式,但是,本发明并不限于上述实施方式中的具体细节,在本发明的技术构思范围内,可以对本发明的技术方案进行多种简单变型,这些简单变型均属于本发明的保护范围。The preferred embodiments of the present invention have been described in detail above, but the present invention is not limited to the specific details in the above embodiments. Within the scope of the technical concept of the present invention, various simple modifications can be made to the technical solutions of the present invention. These simple modifications All belong to the protection scope of the present invention.
另外需要说明的是,在上述具体实施方式中所描述的各个具体技术特征,在不矛盾的情况下,可以通过任何合适的方式进行组合,为了避免不必要的重复,本发明对各种可能的组合方式不再另行说明。In addition, it should be noted that the various specific technical features described in the above specific embodiments can be combined in any suitable way if there is no contradiction. The combination method will not be described separately.
此外,本发明的各种不同的实施方式之间也可以进行任意组合,只要其不违背本发明的思想,其同样应当视为本发明所公开的内容。In addition, various combinations of different embodiments of the present invention can also be combined arbitrarily, as long as they do not violate the idea of the present invention, they should also be regarded as the disclosed content of the present invention.
Claims (10)
- A kind of 1. preparation method of ventilative acrylonitrile ethylene styrene copolymer Film laminated paper, it is characterised in that including with Lower step:(1) by calcium carbonate, organic solvent and titanate coupling agent ultrasonic disperse, drying, obtains modified calcium carbonate;(2) by modified calcium carbonate, micro nanocrystalline cellulose granules, porous konilite, acrylonitrile ethylene styrene copolymer, third Diethyl adipate and dibutyitin maleate blending, extrusion;(3) extrudate is rolled, biaxial tension, film is made;(4) film heat and hot pressing is on the surface of paper layer;Wherein, the mass ratio of modified calcium carbonate, micro nanocrystalline cellulose granules and porous konilite is 1:1-2:2-4.
- 2. preparation method according to claim 1, wherein, it is common relative to acrylonitrile-vinyl-styrene of 100 parts by weight Polymers, the total weight parts of the modified calcium carbonate of addition, micro nanocrystalline cellulose granules and porous konilite are 15-25 parts.
- 3. preparation method according to claim 1 or 2, wherein, the condition of calendering includes in step (3):Extrudate is existed 200-220 DEG C under the pressure of 20t-40t to carry out hot calender.
- 4. preparation method according to claim 1 or 2, wherein, the condition of biaxial tension includes:It is thin by what is obtained after calendering Film carries out biaxial tension, and stretching ratio 1.2-1.8, then carries out thermal finalization processing, thermal finalization processing time at 130-160 DEG C For 5-15min.
- 5. preparation method according to claim 1 or 2, wherein, in step (1), calcium carbonate, organic solvent and titanate esters are even The mass ratio for joining agent is 1:2-3:0.4-0.6;And/or the ultrasonic disperse time is 10-20min, drying temperature is 40-90 DEG C.
- 6. preparation method according to claim 5, wherein,Titanate coupling agent is three caprylyl titanate esters of three iso stearyl titanate esters of isopropyl and/or isopropyl;And/orOrganic solvent is methanol, the one or more in ethanol, propane diols, diethylene glycol, acetone, tetrahydrofuran, pentaerythrite;And/or paper layer is brown paper or corrugated paper.
- 7. preparation method according to claim 1 or 2, wherein, in parts by weight, relative to 100 parts of acrylonitrile-second Alkene-styrol copolymer, 3-4 parts of modified calcium carbonate, 4-6 parts of micro nanocrystalline cellulose granules, porous konilite 8-12 parts, the third two 3-6 parts of diethyl phthalate, 1-2 parts of dibutyitin maleate.
- 8. preparation method according to claim 7, wherein, the particle diameter distribution of micro nanocrystalline cellulose granules is 100nm-50 μm;And/or the average diameter of porous konilite is no more than 0.8 μm.
- 9. preparation method according to claim 1 or 2, wherein, in step (2):Blending temperature is 180-195 DEG C, is kneaded Time is 30-40min;And/or extrusion temperature is 200-215 DEG C.
- It is 10. common according to ventilative acrylonitrile-vinyl-styrene that claim 1-9 any one of them preparation methods are prepared Homopolymer film extrusion coating paper.
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Application publication date: 20180413 |