WO2023115599A1 - Degradable high-barrier composite film and preparation method therefor - Google Patents
Degradable high-barrier composite film and preparation method therefor Download PDFInfo
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- WO2023115599A1 WO2023115599A1 PCT/CN2021/141572 CN2021141572W WO2023115599A1 WO 2023115599 A1 WO2023115599 A1 WO 2023115599A1 CN 2021141572 W CN2021141572 W CN 2021141572W WO 2023115599 A1 WO2023115599 A1 WO 2023115599A1
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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
- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29D—PRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
- B29D7/00—Producing flat articles, e.g. films or sheets
- B29D7/01—Films or sheets
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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
- 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
- B32B27/08—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 synthetic resin
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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
- 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
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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
- 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
- B32B27/20—Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents
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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
- B32B29/00—Layered products comprising a layer of paper or cardboard
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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
- B32B9/00—Layered products comprising a layer of a particular substance not covered by groups B32B11/00 - B32B29/00
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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
- B32B9/00—Layered products comprising a layer of a particular substance not covered by groups B32B11/00 - B32B29/00
- B32B9/04—Layered products comprising a layer of a particular substance not covered by groups B32B11/00 - B32B29/00 comprising such particular substance as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B9/045—Layered products comprising a layer of a particular substance not covered by groups B32B11/00 - B32B29/00 comprising such particular substance as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
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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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- 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
- B32B2307/716—Degradable
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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
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/724—Permeability to gases, adsorption
- B32B2307/7242—Non-permeable
- B32B2307/7246—Water vapor barrier
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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
- B32B2439/00—Containers; Receptacles
- B32B2439/70—Food packaging
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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
- C08J2303/00—Characterised by the use of starch, amylose or amylopectin or of their derivatives or degradation products
- C08J2303/02—Starch; Degradation products thereof, e.g. dextrin
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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
- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
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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
- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/04—Polyesters derived from hydroxy carboxylic acids, e.g. lactones
-
- 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
- C08J2371/00—Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
- C08J2371/08—Polyethers derived from hydroxy compounds or from their metallic derivatives
-
- 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
- C08J2403/00—Characterised by the use of starch, amylose or amylopectin or of their derivatives or degradation products
- C08J2403/02—Starch; Degradation products thereof, e.g. dextrin
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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
- C08J2467/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2467/04—Polyesters derived from hydroxy carboxylic acids, e.g. lactones
-
- 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
- C08J2471/00—Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
- C08J2471/08—Polyethers derived from hydroxy compounds or from their metallic derivatives
Definitions
- the invention relates to a degradable high-barrier composite film and a preparation method thereof, belonging to the field of packaging films.
- High barrier packaging is critical to extending the shelf life and shelf life of food, pharmaceuticals and cosmetics.
- usually high-barrier packaging uses aluminum foil and plastic film as the barrier layer, polyethylene or polypropylene as the heat-sealing layer and printing layer, and paper as the middle layer , Composite materials formed by dry or extrusion compounding processes.
- the rapid marketization of paper-aluminum-plastic composite flexible packaging has provided great convenience to people’s daily life, but at the same time, composite flexible packaging with different materials and characteristics is difficult to separate and recycle through physical means, and is basically a disposable packaging material.
- Biodegradable composite flexible packaging is an environmentally friendly packaging material that combines fully biodegradable materials of different materials and functions to give the contents good protection and aesthetics. This type of composite flexible packaging can be directly buried after being discarded. Under specific composting conditions and It can be completely degraded into biomass, carbon dioxide and water within a degradable time limit, providing a solution for reducing the carbon footprint of composite plastic flexible packaging.
- CN113427867A discloses a high-barrier polylactic acid-based film with a five-layer composite structure.
- the barrier layer is ethylene-vinyl alcohol copolymer (EVOH) or ethylene-vinyl acetate copolymer (EVA), this composite film combines degradable materials with high barrier traditional plastic EVOH.
- EVOH ethylene-vinyl alcohol copolymer
- EVA ethylene-vinyl acetate copolymer
- CN112706484A discloses a high-barrier polyvinyl alcohol (PVA) composite film, including a functional layer and an outer layer, and the functional layer is an alternating structure of thermoplastic polyvinyl alcohol two-dimensional nano-layers and EVOH two-dimensional nano-layers assembled by multiple layers.
- the EVOH in these solutions is a non-degradable material, and the resulting composite flexible packaging still needs to be separated and recycled after disposal, which cannot completely solve the plastic pollution problem caused by the composite flexible packaging, and also makes the degradable components in it meaningless.
- CN112159544A discloses a kind of environmental protection degradable high barrier film of three-layer structure, and barrier layer is positioned at the middle of two base layers, and barrier layer is made of propylene carbonate, nano mesoporous material and dispersant, and base layer is then made of butylene adipate - Composition of butylene terephthalate copolymer, plasticizer, polyacrylate, polypropylene carbonate and polycaprolactone/polyvinylpyrrolidone blend, formed by melt extrusion processing and biaxial stretching process Three-layer coextruded structural membrane. In this process, in order to improve the tensile strength of the film, a biaxial stretching process is used to process the biodegradable film. This process and equipment are expensive and complicated, and
- the purpose of the present invention is to solve a series of shortcomings in the background technology, and specifically solve the problems of complex processing, difficult recycling of different materials and high prices in the field of food composite packaging.
- the present invention provides a degradable high barrier composite film, which has a layer structure of one of A/B, A/C, A/B/C and A/B/A/C
- the A layer is a modified polybutylene terephthalate-adipate copolymer, comprising the following mass components: 50-103 parts of polybutylene terephthalate-adipate copolymer, 20-109 parts of thermoplastic starch, 2-10 parts of compatibilizer, 0.5-10 parts of tackifier, 1.5-42 parts of auxiliary materials
- the B layer is paper or cellulose film
- the C layer is a composite material, including the following Quality components: 40-150 parts of fully biodegradable polymer, 12-60 parts of reinforcing filler, 2-16 parts of antistatic agent, 0.1-15 parts of ultraviolet absorber.
- thermoplastic starch plasticizer is at least two of glycerin, citric acid, stearic acid, formamide, urea, sorbitol, ethylene glycol, acetyl tributyl citrate and epoxidized soybean oil.
- the gelatinization temperature of the thermoplastic starch is 50-120°C.
- the compatibilizer is succinic anhydride, maleic anhydride grafted polyterephthalic acid-adipate-butylene copolymer, ethylene-methyl acrylate-glycidyl methacrylate, ⁇ -aminopropyl At least one of triethoxysilane, ⁇ -glycidyloxypropyltrimethoxysilane, ⁇ -(methacryloyloxy)propyltrimethoxysilane, titanate coupling agent.
- the tackifier is at least one of ethylene-vinyl acetate copolymer, ethylene-acrylic acid copolymer, sodium lignosulfonate, diphenylmethane diisocyanate and DuPont's Biomax strong 120.
- the fully biodegradable polymer is polyhydroxyalkanoate, poly ⁇ -caprolactone, polybutylene succinate, polysuccinate-adipate-butylene copolymer, polylactic acid - at least two of caprolactone copolymer, polyglyceryl sebacate, polybutylene terephthalate-co-succinate and polypropylene carbonate.
- the reinforcing filler is carbon nanotubes, graphene, white lignin, cellulose nanocrystals, nano-intercalation montmorillonite, kaolin, nano-calcium carbonate, cellulose nano-whiskers, amorphous nano-scale white carbon black , at least one of food-grade talcum powder.
- the antistatic agent is trihydroxyethylmethyl quaternary ammonium methyl sulfate, octadecyl dimethyl quaternary ammonium nitrate, alkylamide nonionic surfactant, alkyl phosphate, Alkyl Sulfate, Stearyl Trimethyl Ammonium Chloride and Stearyl Dimethyl Ammonium Chloride, (Lauramidopropyl Trimethylamine) Sulfate Potassium Ester Salt, N,N-Bis(2- Hydroxyethyl)-N-(3'dodecyloxy-2'hydroxypropyl)methanamine potassium sulfate, trihydroxyethyl methyl quaternary ammonium sulfate potassium ester, N,N-hexadecyl At least one of ethyl morpholine sulfate ethyl ester salts.
- the ultraviolet absorber is phenyl o-hydroxybenzoate, 2,4-dihydroxybenzophenone, 2-hydroxyl-4-methoxybenzophenone, 2-hydroxyl-4-n-octyloxy benzophenone, 2-(2'-hydroxy-3',5'-di-tert-phenyl)-5-chlorinated benzotriazole, resorcinol monobenzoate, 2'-2'- Thiobis(4-tert-octylphenoxy)nickel, tris(1,2,2,6,6-pentamethylpiperidinyl)phosphite, 4-benzoyloxy-2,2,6 , at least one of 6-tetramethylpiperidine, 2,4,6-tris(2'-butoxyphenyl)-1,3,5-triazine, and hexamethylphosphoric triamide.
- the present invention provides a method for preparing a degradable high-barrier composite film, comprising the following steps: S1: dry the starch at 60°C for 12-48 hours and weigh it with a plasticizer in a ratio of 100:(10-40) Add to the high-speed mixer and stir for 2-10 minutes. During the mixing process, cooling water is passed through the inner wall of the machine to cool the material temperature. Put the mixed material into the extruder for melting, mixing, cooling and pelletizing. The temperature from the feeding section to the extruder head is 80-150°C, the feeding speed is 3-10rpm, and the screw speed is 50-400rpm/min.
- the melt pressure is 2-10MPa
- the traction and pelletizing speeds are 20-60rpm/min and 7-20rpm/min respectively
- a thermoplastic material for modifying polybutylene terephthalate adipate copolymer is obtained.
- thermoplastic starch granules described in S1 Polybutylene terephthalate adipate, compatibilizer, tackifier and auxiliary materials, extrude and granulate, and then blow mold into a film through an extruder, blow the film
- the operating temperature of each temperature zone of the machine is 80-200°C
- the speed of the main machine is 40-200rpm/min, and sequentially undergoes melting, plasticizing, pressurizing, cooling, pulling, trimming and winding to obtain the A layer;
- S10 Corona, winding, cutting, and packaging are performed on the materials obtained in S3, S5, S7, and S9 to obtain the degradable high-barrier composite film.
- thermoplastic starch to fill polybutylene terephthalate adipate copolymer reduces the production cost of degradable resins and increases its barrier properties to water vapor, and can ensure its durability in the natural environment that can indicate a deadline Compostability;
- the composite film has good barrier properties and high interlayer peel strength, and can be applied to the packaging field of liquid and fresh foods.
- composition of each layer of A, B, and C in Examples 1-5 is shown in Table 1.
- a biodegradable high-barrier composite film has an A/C double-layer structure.
- the layer A has a thickness of 50 ⁇ m and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle size of 1 mm, an intrinsic viscosity ([ ⁇ ]) of 0.9 dl/g, and a molecular weight of 150,000 become.
- the A layer includes the following components in parts by weight: 50 parts of polybutylene terephthalate-adipate copolymer, 60 parts of thermoplastic starch, 2 parts of ethylene-methyl acrylate-glycidyl methacrylate , 3.1 parts of ethylene-vinyl acetate copolymer, 1.5 parts of auxiliary materials.
- the C layer has a thickness of 6 ⁇ m and contains the following components in parts by mass: 23 parts of polyglycerol sebacate, 17 parts of polylactic acid-caprolactone copolymer, 4 parts of cellulose nanocrystals, and 9 parts of carbon nanotubes , 12.8 parts of trihydroxyethylmethyl quaternary ammonium methyl sulfate, 3.2 parts of N,N-hexadecyl ethyl morpholine ethyl sulfate salt and tris(1,2,2,6,6-pentamethylpipene 0.1 part of pyridyl) phosphite.
- the preparation method of above-mentioned degradable high-barrier composite film comprises the following steps:
- thermoplastic starch granules described in S1 polybutylene terephthalate-adipate, ethylene-methyl acrylate-glycidyl methacrylate, ethylene-vinyl acetate copolymer, antibacterial agent, anti-blocking agent and water
- the lubricant is mixed, it is extruded and granulated, and then blown into a film by the extruder. Traction, edge trimming and winding to obtain the A layer;
- S3 Polyglyceryl sebacate, polylactic acid-caprolactone copolymer, cellulose nanocrystals, carbon nanotubes, trihydroxyethylmethyl quaternary ammonium methosulfate, N,N-hexadecyl ethyl Morpholine ethyl sulfate and tris(1,2,2,6,6-pentamethylpiperidinyl) phosphite are added to the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into In the first extruder of the multi-layer composite production line, the pellets are melted and plasticized to form a uniform fluid, and a cast film is formed through a flat die as the C layer;
- S5 Winding, cutting, and packaging the material obtained in S4 to obtain the degradable high-barrier composite film.
- a biodegradable high-barrier composite film has an A/B/C three-layer structure.
- the layer A has a thickness of 55 ⁇ m, and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle diameter of 3 mm, an intrinsic viscosity ([ ⁇ ]) of 1.2 dl/g, and a molecular weight of 100,000 become.
- the A layer includes the following components in parts by weight: 103 parts of polybutylene terephthalate-adipate copolymer, 20 parts of thermoplastic starch, 3 parts of ⁇ -aminopropyltriethoxysilane, seaweed 0.5 parts of sodium bicarbonate, 26.3 parts of auxiliary materials.
- the B layer has a thickness of 400 ⁇ m and is made of cellulose film.
- the C layer has a thickness of 230 ⁇ m and contains the following components in parts by mass: 12 parts of polylactic acid-caprolactone copolymer, 50 parts of polyhydroxyalkanoate, 10 parts of nano-intercalated montmorillonite, 2 parts of carbon nanotubes 5.6 parts of N,N-hexadecylethylmorpholine ethyl sulfate and 5 parts of tris(1,2,2,6,6-pentamethylpiperidinyl)phosphite.
- the preparation method of above-mentioned degradable high-barrier composite film comprises the following steps:
- thermoplastic starch granules described in S1 After mixing the thermoplastic starch granules described in S1, polybutylene terephthalate-adipate, ⁇ -aminopropyltriethoxysilane, sodium alginate, antibacterial agent, anti-blocking agent and slip agent Extrusion granulation, and then blown into film by extruder.
- the operating temperature of each temperature zone of the blown film machine is 110-140 °C, the main engine speed is 400Hz, and it undergoes melting, plasticizing, pressurizing, cooling, pulling, and trimming in sequence. and winding to obtain the A layer;
- S3 Polylactic acid-caprolactone copolymer, polyhydroxyalkanoate, nano-intercalation montmorillonite, carbon nanotubes, N,N-hexadecyl ethyl morpholine ethyl sulfate salt and three (1, 2,2,6,6-Pentamethylpiperidinyl) phosphite is added to the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into the first extruder of the multi-layer composite production line , to melt and plasticize the pellets to form a uniform fluid, and form a cast film through a flat die as the C layer;
- S5 Heat and cool the layer A film obtained in S2 for stretch transfer, and then perform secondary calendering and compounding with the B/C structure composite film obtained in S4 to obtain the A/B/C structure composite film.
- S6 Corona, winding, cutting, and packaging are performed on the material obtained in S3 to obtain the degradable high-barrier composite film.
- a biodegradable high-barrier composite film has an A/B double-layer structure.
- the layer A has a thickness of 100 ⁇ m, and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle size of 2 mm, an intrinsic viscosity ([ ⁇ ]) of 1.5 dl/g, and a molecular weight of 180,000 become.
- the A layer includes the following components in parts by weight: 80 parts of polybutylene terephthalate-adipate copolymer, 30 parts of thermoplastic starch, 6 parts of ⁇ -aminopropyltriethoxysilane, ethylene - 8.6 parts of vinyl acetate copolymer, 35.5 parts of auxiliary materials.
- the B layer has a thickness of 300 ⁇ m and is made of paper.
- the preparation method of above-mentioned degradable high-barrier composite film comprises the following steps:
- thermoplastic starch granules described in S1 polybutylene terephthalate-adipate copolymer, thermoplastic starch, ⁇ -aminopropyltriethoxysilane, ethylene-vinyl acetate copolymer, antibacterial agent, The anti-blocking agent and slip agent are mixed, extruded and granulated, and then blown into a film by the extruder. Pressing, cooling, pulling, edge trimming and winding to obtain the A layer;
- S4 Corona, winding, cutting, and packaging are performed on the material obtained in S3 to obtain the degradable high-barrier composite film.
- a biodegradable high-barrier composite film has an A/B/A/C four-layer structure.
- the A layer has a thickness of 80 ⁇ m, and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle diameter of 4 mm, an intrinsic viscosity ([ ⁇ ]) of 1.3 dl/g, and a molecular weight of 120,000. become.
- the A layer includes the following components in parts by weight: 85 parts of polybutylene terephthalate-adipate copolymer, 80 parts of thermoplastic starch, 10 parts of ethylene-methyl acrylate-glycidyl methacrylate, 10 parts of sodium alginate, 42 parts of auxiliary materials.
- the thickness of the B layer is 260 ⁇ m, and the material is cellulose film.
- the C layer has a thickness of 300 ⁇ m and contains the following components in parts by mass: 130 parts of polyglycerol sebacate, 20 parts of polyhydroxyalkanoate, 5 parts of cellulose nanocrystals, and 15 parts of nano-intercalated montmorillonite , 30 parts of carbon nanotubes, 2 parts of N,N-hexadecyl ethyl morpholine ethyl sulfate, 2.9 parts of phenyl o-hydroxybenzoate and tris(1,2,2,6,6-pentamethylpipene 12.1 parts of pyridyl) phosphite.
- the preparation method of above-mentioned degradable high-barrier composite film comprises the following steps:
- thermoplastic starch granules described in S1 polybutylene terephthalate-adipate copolymer, thermoplastic starch, ethylene-methyl acrylate-glycidyl methacrylate, sodium alginate, antibacterial agent, opening
- the film blowing machine is blown into a film after being mixed with the lubricant and slip agent, and then blown into a film. , cooling, traction, edge trimming and winding to obtain the A layer;
- S3 Polyglyceryl sebacate, polyhydroxyalkanoate, cellulose nanocrystals, nanointercalation montmorillonite, carbon nanotubes, N,N-hexadecylethylmorpholine ethyl sulfate, ortho Phenyl hydroxybenzoate and tris(1,2,2,6,6-pentamethylpiperidinyl) phosphite are added to the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into multi-layer In the first extruder of the composite production line, the pellets are melted and plasticized to form a uniform fluid, and a cast film is formed through a flat die as the C layer;
- S6 performing corona, winding, cutting, and packaging on the material obtained in S5 to obtain the degradable high-barrier composite film.
- a biodegradable high-barrier composite film has an A/B/A/C four-layer structure.
- the layer A has a thickness of 95 ⁇ m, and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle diameter of 5 mm, an intrinsic viscosity ([ ⁇ ]) of 1.5 dl/g, and a molecular weight of 140,000. become.
- the A layer includes the following components in parts by weight: 80 parts of polybutylene terephthalate-adipate copolymer, 109 parts of thermoplastic starch, 7 parts of ⁇ -aminopropyltriethoxysilane, alginic acid 6.4 parts of sodium, 31.2 parts of excipients.
- the thickness of the B layer is 50 ⁇ m, and the material is cellulose film.
- the C layer has a thickness of 160 ⁇ m and contains the following components in parts by mass: 45 parts of polyglycerol sebacate, 65 parts of polylactic acid-caprolactone copolymer, 10 parts of cellulose nanocrystals, nano-intercalation montmorillonite 50 parts of soil, 9.7 parts of trihydroxyethylmethyl quaternary ammonium methosulfate, and 8.5 parts of tris(1,2,2,6,6-pentamethylpiperidinyl) phosphite.
- the preparation method of above-mentioned degradable high-barrier composite film comprises the following steps:
- thermoplastic starch granules described in S1 polybutylene terephthalate-adipate copolymer, ⁇ -aminopropyltriethoxysilane, sodium alginate, antibacterial agent, anti-blocking agent and slip agent After extruding and granulating, it is blown into film by extruder. Edge and winding, to obtain the A layer;
- S3 Polyglyceryl sebacate, polylactic acid-caprolactone copolymer, cellulose nanocrystals, nanointercalation montmorillonite, trihydroxyethylmethyl quaternary ammonium methosulfate and tris(1,2, 2,6,6-pentamethylpiperidinyl) phosphite is added to the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into the first extruder of the multi-layer composite production line to make The pellets are melted and plasticized to form a uniform fluid, and a cast film is formed through a flat die as the C layer;
- S6 performing corona, winding, cutting, and packaging on the material obtained in S5 to obtain the degradable high-barrier composite film.
- the biodegradation rate of the composite film in Examples 1-5 is ⁇ 74% within 6 months, which meets the requirement in GB/T 20197-2006 that the biodegradation rate of biodegradable plastics should be ⁇ 61%.
- the oxygen transmission rate and water vapor transmission rate of this type of composite film are in line with the requirements of food packaging films in GB/T 28117-2011.
- the oxygen transmission rate and water vapor transmission rate should be lower than 20cm 3 /m 2 ⁇ 24h ⁇ 0.1MPa and 30 (g/m 2 ⁇ 24h) requirements.
- the peel strength of the food composite packaging film should generally be ⁇ 3.0N/15mm, and the peel strength between the layers of the composite films in Examples 1-5 all meet the requirements. Therefore, the degradable high-barrier composite film of the present invention has the potential to be applied to food packaging that requires higher barrier properties.
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Abstract
Description
本发明涉及一种可降解高阻隔复合膜及其制备方法,属于包装薄膜领域。The invention relates to a degradable high-barrier composite film and a preparation method thereof, belonging to the field of packaging films.
高阻隔性包装对延长食品、药品和化妆品的保质期和货架期至关重要。为了实现隔水、阻氧、直立、避光、低温热封等多重功能,通常高阻隔包装以铝箔和塑料薄膜为阻隔层,聚乙烯或聚丙烯为热封层和印刷层,纸为中间层,通过干式或挤出复合等工艺形成的复合材料。纸铝塑复合软包装的快速市场化给人们的日常生活提供了极大便捷性,但与此同时,不同材质和特性的复合软包装难以通过物理方式分离和回收,基本属于一次性包材,绝大部分作为一般生活垃圾被填埋或焚烧,给环境带来巨大压力;而用于制备复合包装材料的长纤维纸浆、聚乙烯及优质铝材在使用后仍具有较高使用价值,直接丢弃也造成大量资源浪费。因此,开发新型复合软包装材料具有深远而重要的社会意义及经济价值。High barrier packaging is critical to extending the shelf life and shelf life of food, pharmaceuticals and cosmetics. In order to achieve multiple functions such as water barrier, oxygen barrier, upright, light-proof, low-temperature heat sealing, etc., usually high-barrier packaging uses aluminum foil and plastic film as the barrier layer, polyethylene or polypropylene as the heat-sealing layer and printing layer, and paper as the middle layer , Composite materials formed by dry or extrusion compounding processes. The rapid marketization of paper-aluminum-plastic composite flexible packaging has provided great convenience to people’s daily life, but at the same time, composite flexible packaging with different materials and characteristics is difficult to separate and recycle through physical means, and is basically a disposable packaging material. Some of them are landfilled or incinerated as general domestic waste, which brings great pressure to the environment; while the long-fiber pulp, polyethylene and high-quality aluminum materials used to prepare composite packaging materials still have high use value after use, and direct disposal also causes A lot of resources are wasted. Therefore, the development of new composite flexible packaging materials has far-reaching and important social significance and economic value.
生物可降解复合软包装是将不同材质和功能的全生物降解材料结合,赋予内容物以良好保护特性和美观性的环保包装材料,这类复合软包装废弃后可直接堆埋,在特定堆肥条件下和可表明期限的降解时间内完全降解成生物质,二氧化碳和水,为减少复合塑料软包装碳足迹提供解决方案。Biodegradable composite flexible packaging is an environmentally friendly packaging material that combines fully biodegradable materials of different materials and functions to give the contents good protection and aesthetics. This type of composite flexible packaging can be directly buried after being discarded. Under specific composting conditions and It can be completely degraded into biomass, carbon dioxide and water within a degradable time limit, providing a solution for reducing the carbon footprint of composite plastic flexible packaging.
但由于可降解材料自身阻隔性能不够,因此很多技术方案次采用了与传统不可降解材料复合的方案,如CN113427867A公开了一种具有五层复合结构的高阻隔聚乳酸基薄膜,其中外层为高分子量聚乳酸,阻隔层为乙烯-乙烯醇共聚物(EVOH)或乙烯-醋酸乙烯共聚物(EVA),该复合薄膜将可降解材料与高阻隔的传统塑料EVOH相结合。CN112706484A公开了一种高阻隔性聚乙烯醇(PVA)复合薄膜,包括功能层和外层,功能层为多层组装的热塑性聚乙烯醇二维纳米层 与EVOH二维纳米层交替结构。这些方案中的EVOH为不可降解材料,所得复合软包装废弃后仍需做分离和回收后处理,不能彻底解决复合软包装造成的塑料污染问题,也使得其中的可降解成份失去了意义。However, due to the insufficient barrier performance of the degradable material itself, many technical solutions have adopted a composite solution with traditional non-degradable materials. For example, CN113427867A discloses a high-barrier polylactic acid-based film with a five-layer composite structure. Molecular weight polylactic acid, the barrier layer is ethylene-vinyl alcohol copolymer (EVOH) or ethylene-vinyl acetate copolymer (EVA), this composite film combines degradable materials with high barrier traditional plastic EVOH. CN112706484A discloses a high-barrier polyvinyl alcohol (PVA) composite film, including a functional layer and an outer layer, and the functional layer is an alternating structure of thermoplastic polyvinyl alcohol two-dimensional nano-layers and EVOH two-dimensional nano-layers assembled by multiple layers. The EVOH in these solutions is a non-degradable material, and the resulting composite flexible packaging still needs to be separated and recycled after disposal, which cannot completely solve the plastic pollution problem caused by the composite flexible packaging, and also makes the degradable components in it meaningless.
采用全降解成份,并达到阻隔性能要求的方案也有少量公开报道,但基本都涉及到新研发的专用加工设备,辅以复杂工艺实现,现阶段难以工业化。例如CN112159544A公开了一种三层结构的环保可降解高阻隔薄膜,阻隔层位于两基层中间,阻隔层由碳酸亚丙酯、纳米介孔材料和分散剂构成,基层则由己二酸丁二醇酯-对苯二甲酸丁二醇酯共聚物、增塑剂、聚丙烯酸酯、聚碳酸亚丙酯和聚己内酯/聚乙烯吡咯烷酮共混物组成,通过熔融挤出加工、双向拉伸工艺形成三层共挤出结构膜片。该工艺中为了提高薄膜的拉伸强度采用双向拉伸工艺加工生物可降解薄膜,该工艺和设备价格高昂、工艺复杂,在生物降解薄膜加工领域尚不成熟。There are also a small number of public reports on the use of fully degradable components to meet the barrier performance requirements, but basically all involve newly developed special processing equipment, supplemented by complex processes, and it is difficult to industrialize at this stage. For example CN112159544A discloses a kind of environmental protection degradable high barrier film of three-layer structure, and barrier layer is positioned at the middle of two base layers, and barrier layer is made of propylene carbonate, nano mesoporous material and dispersant, and base layer is then made of butylene adipate - Composition of butylene terephthalate copolymer, plasticizer, polyacrylate, polypropylene carbonate and polycaprolactone/polyvinylpyrrolidone blend, formed by melt extrusion processing and biaxial stretching process Three-layer coextruded structural membrane. In this process, in order to improve the tensile strength of the film, a biaxial stretching process is used to process the biodegradable film. This process and equipment are expensive and complicated, and are not yet mature in the field of biodegradable film processing.
发明内容Contents of the invention
本发明的目的是为解决背景技术中的一系列缺点,具体解决了目前食品复合包装领域加工过程复杂,不同材料难回收和价格高昂的问题。The purpose of the present invention is to solve a series of shortcomings in the background technology, and specifically solve the problems of complex processing, difficult recycling of different materials and high prices in the field of food composite packaging.
为实现上述目的,第一方面,本发明提供一种可降解高阻隔复合膜,具有A/B、A/C、A/B/C和A/B/A/C四者之一的层结构,所述A层为改性聚对苯二甲酸-己二酸-丁二酯共聚物,包含以下质量组分:聚对苯二甲酸-己二酸丁二醇酯共聚物50-103份,热塑性淀粉20-109份,相容剂2-10份,增粘剂0.5-10份,辅料1.5-42份;所述B层为纸或纤维素膜;所述C层为复合材料,包含以下质量组分:全生物降解聚合物40-150份,增强填料12-60份,抗静电剂2-16份,紫外线吸收剂0.1-15份。In order to achieve the above object, in the first aspect, the present invention provides a degradable high barrier composite film, which has a layer structure of one of A/B, A/C, A/B/C and A/B/A/C , the A layer is a modified polybutylene terephthalate-adipate copolymer, comprising the following mass components: 50-103 parts of polybutylene terephthalate-adipate copolymer, 20-109 parts of thermoplastic starch, 2-10 parts of compatibilizer, 0.5-10 parts of tackifier, 1.5-42 parts of auxiliary materials; the B layer is paper or cellulose film; the C layer is a composite material, including the following Quality components: 40-150 parts of fully biodegradable polymer, 12-60 parts of reinforcing filler, 2-16 parts of antistatic agent, 0.1-15 parts of ultraviolet absorber.
进一步地,所述热塑性淀粉的增塑剂为甘油、柠檬酸、硬脂酸、甲酰胺、尿素、山梨醇、乙二醇、乙酰柠檬酸三丁酯和环氧大豆油中的至少两种。Further, the thermoplastic starch plasticizer is at least two of glycerin, citric acid, stearic acid, formamide, urea, sorbitol, ethylene glycol, acetyl tributyl citrate and epoxidized soybean oil.
进一步地,所述热塑性淀粉的糊化温度为50-120℃。Further, the gelatinization temperature of the thermoplastic starch is 50-120°C.
进一步地,所述相容剂为琥珀酸酐、马来酸酐接枝聚对苯二甲酸-己二酸-丁二酯共聚物、乙烯-丙烯酸甲酯-甲基丙烯酸缩水甘油酯、γ-氨丙基三乙氧基硅烷、γ-缩水甘油醚氧丙基三甲氧基硅烷、γ-(甲基丙烯酰氧)丙基三甲氧基硅烷、钛酸酯偶联剂中的至少一种。Further, the compatibilizer is succinic anhydride, maleic anhydride grafted polyterephthalic acid-adipate-butylene copolymer, ethylene-methyl acrylate-glycidyl methacrylate, γ-aminopropyl At least one of triethoxysilane, γ-glycidyloxypropyltrimethoxysilane, γ-(methacryloyloxy)propyltrimethoxysilane, titanate coupling agent.
进一步地,所述增粘剂为乙烯-醋酸乙烯共聚物、乙烯-丙烯酸共聚物、木质素磺酸钠、二苯甲烷二异氰酸酯和杜邦公司的Biomax strong 120中的至少一种。Further, the tackifier is at least one of ethylene-vinyl acetate copolymer, ethylene-acrylic acid copolymer, sodium lignosulfonate, diphenylmethane diisocyanate and DuPont's Biomax strong 120.
进一步地,所述全生物降解聚合物为聚羟基脂肪酸酯、聚ε-己内酯、聚丁二酸丁二醇酯、聚丁二酸-己二酸-丁二酯共聚物、聚乳酸-己内酯共聚物、癸二酸聚甘油酯、聚对苯二甲酸-共-丁二酸丁二醇酯和聚碳酸亚丙酯中的至少两种。Further, the fully biodegradable polymer is polyhydroxyalkanoate, polyε-caprolactone, polybutylene succinate, polysuccinate-adipate-butylene copolymer, polylactic acid - at least two of caprolactone copolymer, polyglyceryl sebacate, polybutylene terephthalate-co-succinate and polypropylene carbonate.
进一步地,所述增强填料为碳纳米管、石墨烯、白木质素、纤维素纳米晶体、纳米插层蒙脱土、高岭土、纳米碳酸钙、纤维素纳米晶须、无定形纳米级白炭黑、食品级滑石粉中的至少一种。Further, the reinforcing filler is carbon nanotubes, graphene, white lignin, cellulose nanocrystals, nano-intercalation montmorillonite, kaolin, nano-calcium carbonate, cellulose nano-whiskers, amorphous nano-scale white carbon black , at least one of food-grade talcum powder.
进一步地,所述抗静电剂为三羟乙基甲基季铵甲基硫酸盐、十八烷基二甲基季铵硝酸盐、烷基酰胺类非离子型表面活性剂、烷基磷酸酯、烷基硫酸酯、硬脂酰三甲基氯化铵和硬脂酰二甲基戊基氯化铵、(月桂酰胺丙基三甲基胺)硫酸钾酯盐、N,N-双(2-羟乙基)-N-(3’十二烷氧基-2’羟基丙基)甲胺硫酸钾酯盐、三羟乙基甲基季胺硫酸钾酯盐、N,N-十六烷基乙基吗啉硫酸乙酯盐中的至少一种。Further, the antistatic agent is trihydroxyethylmethyl quaternary ammonium methyl sulfate, octadecyl dimethyl quaternary ammonium nitrate, alkylamide nonionic surfactant, alkyl phosphate, Alkyl Sulfate, Stearyl Trimethyl Ammonium Chloride and Stearyl Dimethyl Ammonium Chloride, (Lauramidopropyl Trimethylamine) Sulfate Potassium Ester Salt, N,N-Bis(2- Hydroxyethyl)-N-(3'dodecyloxy-2'hydroxypropyl)methanamine potassium sulfate, trihydroxyethyl methyl quaternary ammonium sulfate potassium ester, N,N-hexadecyl At least one of ethyl morpholine sulfate ethyl ester salts.
进一步地,所述紫外线吸收剂为邻羟基苯甲酸苯酯、2,4-二羟基二苯甲酮、2-羟基-4-甲氧基二苯甲酮、2-羟基-4-正辛氧基二苯甲酮、2-(2’-羟基-3’,5’-二叔苯基)-5-氯化苯并三唑、单苯甲酸间苯二酚酯、2’-2’-硫代双(4-叔辛基酚氧基)镍、三(1,2,2,6,6-五甲哌啶基)亚磷酸酯、4-苯甲酰氧 基-2,2,6,6-四甲基哌啶、2,4,6-三(2’正丁氧基苯基)-1,3,5-三嗪、六甲基磷酰三胺中的至少一种。Further, the ultraviolet absorber is phenyl o-hydroxybenzoate, 2,4-dihydroxybenzophenone, 2-hydroxyl-4-methoxybenzophenone, 2-hydroxyl-4-n-octyloxy benzophenone, 2-(2'-hydroxy-3',5'-di-tert-phenyl)-5-chlorinated benzotriazole, resorcinol monobenzoate, 2'-2'- Thiobis(4-tert-octylphenoxy)nickel, tris(1,2,2,6,6-pentamethylpiperidinyl)phosphite, 4-benzoyloxy-2,2,6 , at least one of 6-tetramethylpiperidine, 2,4,6-tris(2'-butoxyphenyl)-1,3,5-triazine, and hexamethylphosphoric triamide.
第二方面,本发明提供一种可降解高阻隔复合膜的制备方法,包括如下步骤:S1:将淀粉在60℃下干燥12-48h后与增塑剂按100:(10-40)比例称重并加入高速混合机搅拌2-10min,混合过程中机器内壁通冷却水进行料温冷却。将混合物料加入挤出机进行熔融、混炼、冷却和切粒,从喂料段到挤出机头的温度为80-150℃,喂料转速3-10rpm,螺杆转速50-400rpm/min,熔体压力2-10MPa,牵引和切粒速度分别为20-60rpm/min和7-20rpm/min,经切粒后得到用于改性聚对苯二甲酸己二酸丁二酯共聚物的热塑性淀粉;In a second aspect, the present invention provides a method for preparing a degradable high-barrier composite film, comprising the following steps: S1: dry the starch at 60°C for 12-48 hours and weigh it with a plasticizer in a ratio of 100:(10-40) Add to the high-speed mixer and stir for 2-10 minutes. During the mixing process, cooling water is passed through the inner wall of the machine to cool the material temperature. Put the mixed material into the extruder for melting, mixing, cooling and pelletizing. The temperature from the feeding section to the extruder head is 80-150°C, the feeding speed is 3-10rpm, and the screw speed is 50-400rpm/min. The melt pressure is 2-10MPa, the traction and pelletizing speeds are 20-60rpm/min and 7-20rpm/min respectively, and after pelletizing, a thermoplastic material for modifying polybutylene terephthalate adipate copolymer is obtained. starch;
S2:将S1所述热塑性淀粉颗粒、聚对苯二甲酸己二酸丁二酯、相容剂、增粘剂和辅料混合后挤出造粒,再经挤出机吹塑成膜,吹膜机各温区操作温度为80-200℃,主机转速40-200rpm/min,并依次经过熔融、塑化、增压、冷却、牵引、切边和收卷,即得所述A层;S2: Mix the thermoplastic starch granules described in S1, polybutylene terephthalate adipate, compatibilizer, tackifier and auxiliary materials, extrude and granulate, and then blow mold into a film through an extruder, blow the film The operating temperature of each temperature zone of the machine is 80-200°C, the speed of the main machine is 40-200rpm/min, and sequentially undergoes melting, plasticizing, pressurizing, cooling, pulling, trimming and winding to obtain the A layer;
S3:在S2所得A层膜上方放卷B层,对A层进行加热后与B层同时经过冷却复合辊进行拉伸转移,通过压延辊压合在一起,获得A/B结构复合膜;S3: Unwind layer B above the layer A film obtained in S2, heat layer A and layer B through cooling composite rolls for stretch transfer, and press together through calender rolls to obtain A/B structure composite film;
S4:将全生物降解聚合物、增强填料、抗静电剂和紫外线吸收剂加入多路喂料挤出系统进行熔融共混造粒,冷却后的粒料投入多层复合生产线的第一台挤出机中,使粒料熔融、塑化形成均匀流体,通过平口模形成流延薄膜作为C层;S4: Add fully biodegradable polymers, reinforcing fillers, antistatic agents and UV absorbers into the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into the first extrusion of the multi-layer composite production line In the machine, the pellets are melted and plasticized to form a uniform fluid, and a cast film is formed through a flat die as the C layer;
S5:将S4所得流延膜拉伸转移,同时流延膜上方放置S2所得A层膜,两者通过压延辊压合在一起,获得A/C结构复合膜;S5: Stretch and transfer the cast film obtained in S4, and place the A-layer film obtained in S2 above the cast film, and the two are pressed together by a calender roll to obtain an A/C structure composite film;
S6:在S4所得层流延膜上方放卷B层,两者通过压延辊压合在一起,获得B/C结构复合膜;S6: Unwind layer B above the cast film obtained in S4, and press the two together through calender rolls to obtain a composite film with a B/C structure;
S7:将S2所得A层膜加热、冷却复合辊进行拉伸转移后与S6所得B/C复 合膜进行二次压延复合,即得所述A/B/C结构复合膜;S7: After heating and cooling the composite roll of the A-layer film obtained in S2, carrying out stretch transfer with the B/C composite film obtained in S6 for secondary calendering and compounding, the composite film of the A/B/C structure is obtained;
S8:将S2所得A层膜放卷于B层膜两侧,其中B层膜为主放卷,对S2所得A层膜加热、拉伸转移后与B层膜压延复合,即得A/B/A结构复合膜;S8: Unwind the A-layer film obtained in S2 on both sides of the B-layer film, in which the B-layer film is the main unwinding, heat the A-layer film obtained in S2, stretch and transfer it, and calender and compound it with the B-layer film to obtain A/B /A structure composite film;
S9:对S8所得A/B/A复合膜A面进行电晕处理后与S4所得材料分别拉伸转移至第二副加热和冷却复合辊,通过复合辊压延在一起即得所述A/B/A/C结构复合材料,S9: After performing corona treatment on the A side of the A/B/A composite film obtained in S8, the material obtained in S4 is stretched and transferred to the second secondary heating and cooling composite roll, and rolled together by the composite roll to obtain the A/B /A/C Structural Composite Materials,
S10:对S3、S5、S7、S9所得材料进行电晕、收卷、分切、包装即得所述可降解高阻隔复合膜。S10: Corona, winding, cutting, and packaging are performed on the materials obtained in S3, S5, S7, and S9 to obtain the degradable high-barrier composite film.
与现有技术相比,本发明的有益效果为:Compared with prior art, the beneficial effect of the present invention is:
(1)利用热塑性淀粉填充聚对苯二甲酸己二酸丁二酯共聚物降低可降解树脂的生产成本并增加其对水蒸汽的阻隔性,并能保证其在可表明期限的自然环境中的堆肥可降解性;(1) The use of thermoplastic starch to fill polybutylene terephthalate adipate copolymer reduces the production cost of degradable resins and increases its barrier properties to water vapor, and can ensure its durability in the natural environment that can indicate a deadline Compostability;
(2)当复合软包装材料在使用期结束后,复合膜无需进行化学分离,直接通过堆肥处理,有助于解决目前复合软包装回收材料难回收的问题;(2) When the composite flexible packaging material has expired, the composite film does not need to be chemically separated, and it can be directly processed through composting, which helps to solve the problem that the current composite flexible packaging recycled materials are difficult to recycle;
(3)该复合膜具有良好的阻隔性、较高层间剥离强度,可应用于液态和生鲜类食品的包装领域。(3) The composite film has good barrier properties and high interlayer peel strength, and can be applied to the packaging field of liquid and fresh foods.
现在结合实施例对本发明作进一步详细的说明,本发明的应用并不局限于下面的实施例,对本发明所做的任何形式上的变通都将落入本发明的保护范围。The present invention is described in further detail in conjunction with embodiment now, and the application of the present invention is not limited to following embodiment, and any form modification of the present invention all will fall into protection domain of the present invention.
实施例1-5中A、B、C各层的成分如表1所示。The composition of each layer of A, B, and C in Examples 1-5 is shown in Table 1.
表1实施例1-5中A、B、C层成分A, B, C layer composition in the embodiment 1-5 of table 1
实施例1Example 1
一种生物可降解高阻隔复合膜,该复合膜具有A/C双层结构。A biodegradable high-barrier composite film has an A/C double-layer structure.
所述A层厚度为50μm,由平均粒径1mm,特性黏度([η])0.9dl/g,分子量为15万的改性聚对苯二甲酸-己二酸丁二酯共聚物颗粒加工而成。所述A层包括以下重量份计的组分:聚对苯二甲酸-己二酸丁二醇酯共聚物50份,热塑性淀粉60份,乙烯-丙烯酸甲酯-甲基丙烯酸缩水甘油酯2份,乙烯-醋酸乙烯共聚物3.1份,辅料1.5份。The layer A has a thickness of 50 μm and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle size of 1 mm, an intrinsic viscosity ([η]) of 0.9 dl/g, and a molecular weight of 150,000 become. The A layer includes the following components in parts by weight: 50 parts of polybutylene terephthalate-adipate copolymer, 60 parts of thermoplastic starch, 2 parts of ethylene-methyl acrylate-glycidyl methacrylate , 3.1 parts of ethylene-vinyl acetate copolymer, 1.5 parts of auxiliary materials.
所述C层厚度为6μm,包含以下质量份数计的组分:癸二酸聚甘油酯23份、聚乳酸-己内酯共聚物17份、纤维素纳米晶体4份、碳纳米管9份、三羟乙基甲基季胺甲基硫酸盐12.8份、N,N-十六烷基乙基吗啉硫酸乙酯盐3.2份和三(1,2,2,6,6-五甲哌啶基)亚磷酸酯0.1份。The C layer has a thickness of 6 μm and contains the following components in parts by mass: 23 parts of polyglycerol sebacate, 17 parts of polylactic acid-caprolactone copolymer, 4 parts of cellulose nanocrystals, and 9 parts of carbon nanotubes , 12.8 parts of trihydroxyethylmethyl quaternary ammonium methyl sulfate, 3.2 parts of N,N-hexadecyl ethyl morpholine ethyl sulfate salt and tris(1,2,2,6,6-pentamethylpipene 0.1 part of pyridyl) phosphite.
上述可降解高阻隔复合膜的制备方法,包括以下步骤:The preparation method of above-mentioned degradable high-barrier composite film, comprises the following steps:
S1:将直链度为20%的淀粉在60℃下干燥12h后与甘油和硬脂酸按40:15:5比例称重并加入高速混合机搅拌2min,混合过程中机器内壁通冷却水,使糊化温度保持在50℃。将混合物料加入挤出机进行熔融、混炼、冷却和切粒,从喂料段到挤出机头的温度为110-150℃,喂料转速5rpm,螺杆转速400rpm/min,熔体压力2-5MPa,牵引和切粒速度分别为20rpm/min和19rpm/min。经切粒后得到用于改性聚对苯二甲酸己二酸丁二酯共聚物的热塑性淀粉;S1: Dry the starch with a linearity of 20% at 60°C for 12 hours, weigh it with glycerin and stearic acid in a ratio of 40:15:5, add it to a high-speed mixer and stir for 2 minutes, and pass cooling water through the inner wall of the machine during the mixing process. The gelatinization temperature was maintained at 50°C. Put the mixed material into the extruder for melting, mixing, cooling and pelletizing. The temperature from the feeding section to the extruder head is 110-150°C, the feeding speed is 5rpm, the screw speed is 400rpm/min, and the melt pressure is 2 -5MPa, traction and pelletizing speeds are 20rpm/min and 19rpm/min respectively. Obtain the thermoplastic starch for modified polybutylene terephthalate adipate copolymer after pelletizing;
S2:将S1所述热塑性淀粉颗粒、聚对苯二甲酸-己二酸丁二酯,乙烯-丙烯酸甲酯-甲基丙烯酸缩水甘油酯、乙烯-醋酸乙烯共聚物、抗菌剂、开口剂和爽滑剂混合后挤出造粒,再经挤出机吹塑成膜,吹膜机各温区操作温度为110-160℃,主机转速200Hz,并依次经过熔融、塑化、增压、冷却、牵引、切边和收卷,即得所述A层;S2: The thermoplastic starch granules described in S1, polybutylene terephthalate-adipate, ethylene-methyl acrylate-glycidyl methacrylate, ethylene-vinyl acetate copolymer, antibacterial agent, anti-blocking agent and water After the lubricant is mixed, it is extruded and granulated, and then blown into a film by the extruder. Traction, edge trimming and winding to obtain the A layer;
S3:将癸二酸聚甘油酯、聚乳酸-己内酯共聚物、纤维素纳米晶体、碳纳米管、三羟乙基甲基季胺甲基硫酸盐、N,N-十六烷基乙基吗啉硫酸乙酯盐和三(1,2,2,6,6-五甲哌啶基)亚磷酸酯加入多路喂料挤出系统进行熔融共混造粒,冷却 后的粒料投入多层复合生产线的第一台挤出机中,使粒料熔融、塑化形成均匀流体,通过平口模形成流延薄膜作为C层;S3: Polyglyceryl sebacate, polylactic acid-caprolactone copolymer, cellulose nanocrystals, carbon nanotubes, trihydroxyethylmethyl quaternary ammonium methosulfate, N,N-hexadecyl ethyl Morpholine ethyl sulfate and tris(1,2,2,6,6-pentamethylpiperidinyl) phosphite are added to the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into In the first extruder of the multi-layer composite production line, the pellets are melted and plasticized to form a uniform fluid, and a cast film is formed through a flat die as the C layer;
S4:所得流延膜拉伸转移,同时流延膜上方放置A层,两者通过压延辊压合在一起,获得A/C结构复合膜;S4: Stretching transfer of the obtained cast film, and at the same time, layer A is placed on the cast film, and the two are pressed together by a calender roll to obtain an A/C structure composite film;
S5:对S4所得材料进行收卷、分切、包装即得所述可降解高阻隔复合膜。S5: Winding, cutting, and packaging the material obtained in S4 to obtain the degradable high-barrier composite film.
实施例2Example 2
一种生物可降解高阻隔复合膜,该复合膜具有A/B/C三层结构。A biodegradable high-barrier composite film has an A/B/C three-layer structure.
所述A层厚度为55μm,由平均粒径3mm,特性黏度([η])1.2dl/g,分子量为10万的改性聚对苯二甲酸-己二酸丁二酯共聚物颗粒加工而成。所述A层包括以下重量份计的组分:聚对苯二甲酸-己二酸丁二醇酯共聚物103份,热塑性淀粉20份,γ-氨丙基三乙氧基硅烷3份,海藻酸钠0.5份,辅料26.3份。The layer A has a thickness of 55 μm, and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle diameter of 3 mm, an intrinsic viscosity ([η]) of 1.2 dl/g, and a molecular weight of 100,000 become. The A layer includes the following components in parts by weight: 103 parts of polybutylene terephthalate-adipate copolymer, 20 parts of thermoplastic starch, 3 parts of γ-aminopropyltriethoxysilane, seaweed 0.5 parts of sodium bicarbonate, 26.3 parts of auxiliary materials.
所述B层厚度为400μm,材质为纤维素膜。The B layer has a thickness of 400 μm and is made of cellulose film.
所述C层厚度为230μm,包含以下质量份数计的组分:聚乳酸-己内酯共聚物12份、聚羟基脂肪酸酯50份、纳米插层蒙脱土10份、碳纳米管2份、N,N-十六烷基乙基吗啉硫酸乙酯盐5.6份和三(1,2,2,6,6-五甲哌啶基)亚磷酸酯5份。The C layer has a thickness of 230 μm and contains the following components in parts by mass: 12 parts of polylactic acid-caprolactone copolymer, 50 parts of polyhydroxyalkanoate, 10 parts of nano-intercalated montmorillonite, 2 parts of carbon nanotubes 5.6 parts of N,N-hexadecylethylmorpholine ethyl sulfate and 5 parts of tris(1,2,2,6,6-pentamethylpiperidinyl)phosphite.
上述可降解高阻隔复合膜的制备方法,包括以下步骤:The preparation method of above-mentioned degradable high-barrier composite film, comprises the following steps:
S1:将直链度为28%的淀粉在60℃下干燥12h后与甘油和尿素按14:1:5比例称重并加入高速混合机搅拌5min,混合过程中机器内壁通冷却水,使糊化温度保持在50℃。将混合物料加入挤出机进行熔融、混炼、冷却和切粒,从喂料段到挤出机头的温度为110-130℃,喂料转速7rpm,螺杆转速300rpm/min,熔体压力3-8MPa,牵引和切粒速度分别为30rpm/min和20rpm/min。经切粒后得到用于改性聚对苯二甲酸己二酸丁二酯共聚物的热塑性淀粉;S1: Dry the starch with a straight chain degree of 28% at 60°C for 12 hours, weigh it with glycerin and urea at a ratio of 14:1:5, add it to a high-speed mixer and stir for 5 minutes, and pass cooling water through the inner wall of the machine during the mixing process to make the paste The melting temperature was kept at 50 °C. Put the mixed material into the extruder for melting, mixing, cooling and pelletizing. The temperature from the feeding section to the extruder head is 110-130°C, the feeding speed is 7rpm, the screw speed is 300rpm/min, and the melt pressure is 3 -8MPa, traction and pelletizing speeds are 30rpm/min and 20rpm/min respectively. Obtain the thermoplastic starch for modified polybutylene terephthalate adipate copolymer after pelletizing;
S2:将S1所述热塑性淀粉颗粒、聚对苯二甲酸-己二酸丁二醇酯、γ-氨丙基三乙氧基硅烷、海藻酸钠、抗菌剂、开口剂和爽滑剂混合后挤出造粒,再经挤出机吹塑成膜,吹膜机各温区操作温度为110-140℃,主机转速400Hz,并依次 经过熔融、塑化、增压、冷却、牵引、切边和收卷,即得所述A层;S2: After mixing the thermoplastic starch granules described in S1, polybutylene terephthalate-adipate, γ-aminopropyltriethoxysilane, sodium alginate, antibacterial agent, anti-blocking agent and slip agent Extrusion granulation, and then blown into film by extruder. The operating temperature of each temperature zone of the blown film machine is 110-140 ℃, the main engine speed is 400Hz, and it undergoes melting, plasticizing, pressurizing, cooling, pulling, and trimming in sequence. and winding to obtain the A layer;
S3:将聚乳酸-己内酯共聚物、聚羟基脂肪酸酯、纳米插层蒙脱土、碳纳米管、N,N-十六烷基乙基吗啉硫酸乙酯盐和三(1,2,2,6,6-五甲哌啶基)亚磷酸酯加入多路喂料挤出系统进行熔融共混造粒,冷却后的粒料投入多层复合生产线的第一台挤出机中,使粒料熔融、塑化形成均匀流体,通过平口模形成流延薄膜作为C层;S3: Polylactic acid-caprolactone copolymer, polyhydroxyalkanoate, nano-intercalation montmorillonite, carbon nanotubes, N,N-hexadecyl ethyl morpholine ethyl sulfate salt and three (1, 2,2,6,6-Pentamethylpiperidinyl) phosphite is added to the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into the first extruder of the multi-layer composite production line , to melt and plasticize the pellets to form a uniform fluid, and form a cast film through a flat die as the C layer;
S4:在C层流延膜上方放卷B层,两者通过压延辊压合在一起,获得B/C结构复合膜;S4: Unwind layer B above the cast film of layer C, and press the two together by calender rolls to obtain a composite film of B/C structure;
S5:将S2所得A层膜加热、冷却复合辊进行拉伸转移后与S4所得的B/C结构复合膜进行二次压延复合,即得所述A/B/C结构复合膜。S5: Heat and cool the layer A film obtained in S2 for stretch transfer, and then perform secondary calendering and compounding with the B/C structure composite film obtained in S4 to obtain the A/B/C structure composite film.
S6:对S3所得材料进行电晕、收卷、分切、包装即得所述可降解高阻隔复合膜。S6: Corona, winding, cutting, and packaging are performed on the material obtained in S3 to obtain the degradable high-barrier composite film.
实施例3Example 3
一种生物可降解高阻隔复合膜,该复合膜具有A/B双层结构。A biodegradable high-barrier composite film has an A/B double-layer structure.
所述A层厚度为100μm,由平均粒径2mm,特性黏度([η])1.5dl/g,分子量为18万的改性聚对苯二甲酸-己二酸丁二酯共聚物颗粒加工而成。所述A层包括以下重量份计的组分:聚对苯二甲酸-己二酸丁二醇酯共聚物80份,热塑性淀粉30份,γ-氨丙基三乙氧基硅烷6份,乙烯-醋酸乙烯共聚物8.6份,辅料35.5份。The layer A has a thickness of 100 μm, and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle size of 2 mm, an intrinsic viscosity ([η]) of 1.5 dl/g, and a molecular weight of 180,000 become. The A layer includes the following components in parts by weight: 80 parts of polybutylene terephthalate-adipate copolymer, 30 parts of thermoplastic starch, 6 parts of γ-aminopropyltriethoxysilane, ethylene - 8.6 parts of vinyl acetate copolymer, 35.5 parts of auxiliary materials.
所述B层厚度为300μm,材质为纸。The B layer has a thickness of 300 μm and is made of paper.
上述可降解高阻隔复合膜的制备方法,包括以下步骤:The preparation method of above-mentioned degradable high-barrier composite film, comprises the following steps:
S1:将直链度为25%的淀粉在60℃下干燥48h后与硬脂酸和尿素按30:9:4比例称重并加入高速混合机搅拌8min,混合过程中机器内壁通冷却水,使糊化温度保持在120℃。将混合物料加入挤出机进行熔融、混炼、冷却和切粒,从喂料段到挤出机头的温度为110-150℃,喂料转速10rpm,螺杆转速400rpm/min, 熔体压力8-10MPa,牵引和切粒速度分别为35rpm/min和20rpm/min。经切粒后得到用于改性聚对苯二甲酸己二酸丁二酯共聚物的热塑性淀粉;S1: Dry the starch with a linearity of 25% at 60°C for 48 hours, weigh it with stearic acid and urea at a ratio of 30:9:4, add it to a high-speed mixer and stir for 8 minutes, and pass cooling water through the inner wall of the machine during the mixing process. The gelatinization temperature was maintained at 120°C. Put the mixed material into the extruder for melting, mixing, cooling and pelletizing. The temperature from the feeding section to the extruder head is 110-150°C, the feeding speed is 10rpm, the screw speed is 400rpm/min, and the melt pressure is 8 -10MPa, traction and pelletizing speeds are 35rpm/min and 20rpm/min respectively. Obtain the thermoplastic starch for modified polybutylene terephthalate adipate copolymer after pelletizing;
S2:将S1所述热塑性淀粉颗粒、聚对苯二甲酸-己二酸丁二醇酯共聚物、热塑性淀粉、γ-氨丙基三乙氧基硅烷、乙烯-醋酸乙烯共聚物、抗菌剂、开口剂和爽滑剂混合后挤出造粒,再经挤出机吹塑成膜,吹膜机各温区操作温度为90-140℃,主机转速200Hz,并依次经过熔融、塑化、增压、冷却、牵引、切边和收卷,即得所述A层;S2: The thermoplastic starch granules described in S1, polybutylene terephthalate-adipate copolymer, thermoplastic starch, γ-aminopropyltriethoxysilane, ethylene-vinyl acetate copolymer, antibacterial agent, The anti-blocking agent and slip agent are mixed, extruded and granulated, and then blown into a film by the extruder. Pressing, cooling, pulling, edge trimming and winding to obtain the A layer;
S3:在A层膜上方放卷B层,对A层进行加热后与B层同时经过冷却复合辊进行拉伸转移,通过压延辊压合在一起,获得A/B结构复合膜;S3: Unwind layer B above layer A, heat layer A and layer B through cooling composite rolls for stretch transfer, and press together through calender rolls to obtain A/B structure composite films;
S4:对S3所得材料进行电晕、收卷、分切、包装即得所述可降解高阻隔复合膜。S4: Corona, winding, cutting, and packaging are performed on the material obtained in S3 to obtain the degradable high-barrier composite film.
实施例4Example 4
一种生物可降解高阻隔复合膜,该复合膜具有A/B/A/C四层结构。A biodegradable high-barrier composite film has an A/B/A/C four-layer structure.
所述A层厚度为80μm,由平均粒径4mm,特性黏度([η])1.3dl/g,分子量为12万的改性聚对苯二甲酸-己二酸丁二酯共聚物颗粒加工而成。所述A层包括以下重量份计的组分:聚对苯二甲酸-己二酸丁二酯共聚物85份,热塑性淀粉80份,乙烯-丙烯酸甲酯-甲基丙烯酸缩水甘油酯10份,海藻酸钠10份,辅料42份。The A layer has a thickness of 80 μm, and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle diameter of 4 mm, an intrinsic viscosity ([η]) of 1.3 dl/g, and a molecular weight of 120,000. become. The A layer includes the following components in parts by weight: 85 parts of polybutylene terephthalate-adipate copolymer, 80 parts of thermoplastic starch, 10 parts of ethylene-methyl acrylate-glycidyl methacrylate, 10 parts of sodium alginate, 42 parts of auxiliary materials.
所述B层厚度为260μm,材质为纤维素膜。The thickness of the B layer is 260 μm, and the material is cellulose film.
所述C层厚度为300μm,包含以下质量份数计的组分:癸二酸聚甘油酯130份、聚羟基脂肪酸酯20份、纤维素纳米晶体5份、纳米插层蒙脱土15份、碳纳米管30份、N,N-十六烷基乙基吗啉硫酸乙酯盐2份、邻羟基苯甲酸苯酯2.9份和三(1,2,2,6,6-五甲哌啶基)亚磷酸酯12.1份。The C layer has a thickness of 300 μm and contains the following components in parts by mass: 130 parts of polyglycerol sebacate, 20 parts of polyhydroxyalkanoate, 5 parts of cellulose nanocrystals, and 15 parts of nano-intercalated montmorillonite , 30 parts of carbon nanotubes, 2 parts of N,N-hexadecyl ethyl morpholine ethyl sulfate, 2.9 parts of phenyl o-hydroxybenzoate and tris(1,2,2,6,6-pentamethylpipene 12.1 parts of pyridyl) phosphite.
上述可降解高阻隔复合膜的制备方法,包括以下步骤:The preparation method of above-mentioned degradable high-barrier composite film, comprises the following steps:
S1:将直链度为22%的淀粉在60℃下干燥36h后与硬脂酸和尿素按51:22:7比例称重并加入高速混合机搅拌10min,混合过程中机器内壁通冷却水,使糊 化温度保持在100℃。将混合物料加入挤出机进行熔融、混炼、冷却和切粒,从喂料段到挤出机头的温度为100-140℃,喂料转速3rpm,螺杆转速200rpm/min,熔体压力2-4MPa,牵引和切粒速度分别为15rpm/min和8rpm/min。经切粒后得到用于改性聚对苯二甲酸己二酸丁二酯共聚物的热塑性淀粉;S1: Dry the starch with a linearity of 22% at 60°C for 36 hours, weigh it with stearic acid and urea in a ratio of 51:22:7, add it to a high-speed mixer and stir for 10 minutes, and pass cooling water through the inner wall of the machine during the mixing process. The gelatinization temperature was maintained at 100°C. Put the mixed material into the extruder for melting, mixing, cooling and pelletizing. The temperature from the feeding section to the extruder head is 100-140°C, the feeding speed is 3rpm, the screw speed is 200rpm/min, and the melt pressure is 2 -4MPa, traction and pelletizing speeds are 15rpm/min and 8rpm/min respectively. Obtain the thermoplastic starch for modified polybutylene terephthalate adipate copolymer after pelletizing;
S2:将S1所述热塑性淀粉颗粒、聚对苯二甲酸-己二酸丁二酯共聚物、热塑性淀粉、乙烯-丙烯酸甲酯-甲基丙烯酸缩水甘油酯、,海藻酸钠、抗菌剂、开口剂和爽滑剂混合后挤出造粒,再经挤出机吹塑成膜,吹膜机各温区操作温度为145-190℃,主机转速200Hz,并依次经过熔融、塑化、增压、冷却、牵引、切边和收卷,即得所述A层;S2: The thermoplastic starch granules described in S1, polybutylene terephthalate-adipate copolymer, thermoplastic starch, ethylene-methyl acrylate-glycidyl methacrylate, sodium alginate, antibacterial agent, opening The film blowing machine is blown into a film after being mixed with the lubricant and slip agent, and then blown into a film. , cooling, traction, edge trimming and winding to obtain the A layer;
S3:将癸二酸聚甘油酯、聚羟基脂肪酸酯、纤维素纳米晶体、纳米插层蒙脱土、碳纳米管、N,N-十六烷基乙基吗啉硫酸乙酯盐、邻羟基苯甲酸苯酯和三(1,2,2,6,6-五甲哌啶基)亚磷酸酯加入多路喂料挤出系统进行熔融共混造粒,冷却后的粒料投入多层复合生产线的第一台挤出机中,使粒料熔融、塑化形成均匀流体,通过平口模形成流延薄膜作为C层;S3: Polyglyceryl sebacate, polyhydroxyalkanoate, cellulose nanocrystals, nanointercalation montmorillonite, carbon nanotubes, N,N-hexadecylethylmorpholine ethyl sulfate, ortho Phenyl hydroxybenzoate and tris(1,2,2,6,6-pentamethylpiperidinyl) phosphite are added to the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into multi-layer In the first extruder of the composite production line, the pellets are melted and plasticized to form a uniform fluid, and a cast film is formed through a flat die as the C layer;
S4:将S2所得A层膜放卷于B层膜两侧,其中B层膜为主放卷,对S2所得A层膜加热、拉伸转移后与B层膜压延复合,即得A/B/A结构复合膜。S4: Unwind the A-layer film obtained in S2 on both sides of the B-layer film, in which the B-layer film is the main unwinding, heat, stretch and transfer the A-layer film obtained in S2, and then calender and compound it with the B-layer film to obtain A/B /A structure composite film.
S5:对S4所得A/B/A复合膜A面进行电晕处理后与S3所得材料分别拉伸转移至第二副加热和冷却复合辊,通过复合辊压延在一起即得所述A/B/A/C结构复合材料。S5: After performing corona treatment on the A side of the A/B/A composite film obtained in S4, the material obtained in S3 is stretched and transferred to the second secondary heating and cooling composite roll, and rolled together by the composite roll to obtain the A/B /A/C Structural Composite.
S6:对S5所得材料进行电晕、收卷、分切、包装即得所述可降解高阻隔复合膜。S6: performing corona, winding, cutting, and packaging on the material obtained in S5 to obtain the degradable high-barrier composite film.
实施例5Example 5
一种生物可降解高阻隔复合膜,该复合膜具有A/B/A/C四层结构。A biodegradable high-barrier composite film has an A/B/A/C four-layer structure.
所述A层厚度为95μm,由平均粒径5mm,特性黏度([η])1.5dl/g,分子量为14 万的改性聚对苯二甲酸-己二酸丁二酯共聚物颗粒加工而成。所述A层包括以下重量份计的组分:聚对苯二甲酸-己二酸丁二酯共聚物80份,热塑性淀粉109份,γ-氨丙基三乙氧基硅烷7份,海藻酸钠6.4份,辅料31.2份。The layer A has a thickness of 95 μm, and is processed from modified polybutylene terephthalate-adipate copolymer particles with an average particle diameter of 5 mm, an intrinsic viscosity ([η]) of 1.5 dl/g, and a molecular weight of 140,000. become. The A layer includes the following components in parts by weight: 80 parts of polybutylene terephthalate-adipate copolymer, 109 parts of thermoplastic starch, 7 parts of γ-aminopropyltriethoxysilane, alginic acid 6.4 parts of sodium, 31.2 parts of excipients.
所述B层厚度为50μm,材质为纤维素膜。The thickness of the B layer is 50 μm, and the material is cellulose film.
所述C层厚度为160μm,包含以下质量份数计的组分:癸二酸聚甘油酯45份、聚乳酸-己内酯共聚物65份、纤维素纳米晶体10份、纳米插层蒙脱土50份、三羟乙基甲基季铵甲基硫酸盐9.7份、和三(1,2,2,6,6-五甲哌啶基)亚磷酸酯8.5份。The C layer has a thickness of 160 μm and contains the following components in parts by mass: 45 parts of polyglycerol sebacate, 65 parts of polylactic acid-caprolactone copolymer, 10 parts of cellulose nanocrystals, nano-intercalation montmorillonite 50 parts of soil, 9.7 parts of trihydroxyethylmethyl quaternary ammonium methosulfate, and 8.5 parts of tris(1,2,2,6,6-pentamethylpiperidinyl) phosphite.
上述可降解高阻隔复合膜的制备方法,包括以下步骤:The preparation method of above-mentioned degradable high-barrier composite film, comprises the following steps:
S1:将直链度为27%的淀粉在60℃下干燥48h后与甘油和尿素按80:11:18比例称重并加入高速混合机搅拌7min,混合过程中机器内壁通冷却水,使糊化温度保持在120℃。将混合物料加入挤出机进行熔融、混炼、冷却和切粒,从喂料段到挤出机头的温度为80-130℃,喂料转速5rpm,螺杆转速340rpm/min,熔体压力2-5MPa,牵引和切粒速度分别为7rpm/min和10rpm/min。经切粒后得到用于改性聚对苯二甲酸己二酸丁二酯共聚物的热塑性淀粉;S1: Dry starch with a straight chain degree of 27% at 60°C for 48 hours, weigh it with glycerin and urea at a ratio of 80:11:18, add it to a high-speed mixer and stir for 7 minutes, and pass cooling water through the inner wall of the machine during the mixing process to make the paste The melting temperature was maintained at 120 °C. Put the mixed material into the extruder for melting, mixing, cooling and pelletizing. The temperature from the feeding section to the extruder head is 80-130°C, the feeding speed is 5rpm, the screw speed is 340rpm/min, and the melt pressure is 2 -5MPa, traction and pelletizing speeds are 7rpm/min and 10rpm/min respectively. Obtain the thermoplastic starch for modified polybutylene terephthalate adipate copolymer after pelletizing;
S2:将S1所述热塑性淀粉颗粒、聚对苯二甲酸-己二酸丁二酯共聚物、γ-氨丙基三乙氧基硅烷、海藻酸钠、抗菌剂、开口剂和爽滑剂混合后挤出造粒,再经挤出机吹塑成膜,吹膜机各温区操作温度为80-135℃,主机转速300Hz,并依次经过熔融、塑化、增压、冷却、牵引、切边和收卷,即得所述A层;S2: Mix the thermoplastic starch granules described in S1, polybutylene terephthalate-adipate copolymer, γ-aminopropyltriethoxysilane, sodium alginate, antibacterial agent, anti-blocking agent and slip agent After extruding and granulating, it is blown into film by extruder. Edge and winding, to obtain the A layer;
S3:将癸二酸聚甘油酯、聚乳酸-己内酯共聚物、纤维素纳米晶体、纳米插层蒙脱土、三羟乙基甲基季铵甲基硫酸盐和三(1,2,2,6,6-五甲哌啶基)亚磷酸酯加入多路喂料挤出系统进行熔融共混造粒,冷却后的粒料投入多层复合生产线的第一台挤出机中,使粒料熔融、塑化形成均匀流体,通过平口模形成流延薄膜作为C层;S3: Polyglyceryl sebacate, polylactic acid-caprolactone copolymer, cellulose nanocrystals, nanointercalation montmorillonite, trihydroxyethylmethyl quaternary ammonium methosulfate and tris(1,2, 2,6,6-pentamethylpiperidinyl) phosphite is added to the multi-feed extrusion system for melt blending and granulation, and the cooled pellets are put into the first extruder of the multi-layer composite production line to make The pellets are melted and plasticized to form a uniform fluid, and a cast film is formed through a flat die as the C layer;
S4:将S2所得A层膜放卷于B层膜两侧,其中B层膜为主放卷,对S2所得A层膜加热、拉伸转移后与B层膜压延复合,即得A/B/A结构复合膜。S4: Unwind the A-layer film obtained in S2 on both sides of the B-layer film, in which the B-layer film is the main unwinding, heat, stretch and transfer the A-layer film obtained in S2, and then calender and compound it with the B-layer film to obtain A/B /A structure composite film.
S5:对S4所得A/B/A复合膜A面进行电晕处理后与S3所得材料分别拉伸转移至第二副加热和冷却复合辊,通过复合辊压延在一起即得所述A/B/A/C结构复合材料。S5: After performing corona treatment on the A side of the A/B/A composite film obtained in S4, the material obtained in S3 is stretched and transferred to the second secondary heating and cooling composite roll, and rolled together by the composite roll to obtain the A/B /A/C Structural Composite.
S6:对S5所得材料进行电晕、收卷、分切、包装即得所述可降解高阻隔复合膜。S6: performing corona, winding, cutting, and packaging on the material obtained in S5 to obtain the degradable high-barrier composite film.
实验例Experimental example
按本实施例方法制备A/C、A/B/C、A/B和A/B/A/C复合膜,随后将复合膜置于既定温度和湿度条件下进行阻隔性、降解性及层间剥离测试。生物降解率、水蒸气透过率、氧气透过率和剥离强度测试结果如表2所示。Prepare A/C, A/B/C, A/B and A/B/A/C composite films according to the method of this example, and then place the composite films under the conditions of predetermined temperature and humidity Peel test. The test results of biodegradation rate, water vapor transmission rate, oxygen transmission rate and peel strength are shown in Table 2.
表2实施例1-5中多层复合膜的生物分解率、氧气透过量、水蒸气透过量和剥离强度Biodegradation rate, oxygen transmission rate, water vapor transmission rate and peel strength of multilayer composite film in table 2 embodiment 1-5
实施例1-5中复合膜在6个月之内的生物分解率≥74%,符合GB/T 20197-2006中关于生物可降解塑料的生物分解率应≥61%的要求。该类复合薄膜的氧气透过量和水蒸气透过量均符合GB/T 28117-2011中食品包装薄膜的要求氧气透过量和水蒸气透过量应低于20cm 3/m 2·24h·0.1MPa和30(g/m 2·24h)的要求。食品复合包装薄膜的剥离强度一般应≥3.0N/15mm,实施例1-5的复合膜各层间剥离强度均符合要求。因此,本发明所述的可降解高阻隔复合膜有应用于对阻隔性要求较高的食品包装的潜力。 The biodegradation rate of the composite film in Examples 1-5 is ≥74% within 6 months, which meets the requirement in GB/T 20197-2006 that the biodegradation rate of biodegradable plastics should be ≥61%. The oxygen transmission rate and water vapor transmission rate of this type of composite film are in line with the requirements of food packaging films in GB/T 28117-2011. The oxygen transmission rate and water vapor transmission rate should be lower than 20cm 3 /m 2 ·24h·0.1MPa and 30 (g/m 2 ·24h) requirements. The peel strength of the food composite packaging film should generally be ≥ 3.0N/15mm, and the peel strength between the layers of the composite films in Examples 1-5 all meet the requirements. Therefore, the degradable high-barrier composite film of the present invention has the potential to be applied to food packaging that requires higher barrier properties.
以上所述,仅是本发明的原理示意方案,并非对本发明的结构作其它形式上的限制。未表述的部分默认为采用本领域公知的方案,凡是依据本发明的技 术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明的技术方案的范围内。The above description is only a schematic scheme of the principle of the present invention, and does not impose other formal restrictions on the structure of the present invention. The unexpressed part defaults to adopting schemes known in the art, and any simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention still belong to the scope of the technical scheme of the present invention.
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