CN109401225A - A kind of biodegradable preservative film and preparation method thereof - Google Patents

A kind of biodegradable preservative film and preparation method thereof Download PDF

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CN109401225A
CN109401225A CN201811189636.XA CN201811189636A CN109401225A CN 109401225 A CN109401225 A CN 109401225A CN 201811189636 A CN201811189636 A CN 201811189636A CN 109401225 A CN109401225 A CN 109401225A
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preservative film
parts
biodegradable
temperature
film according
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CN109401225B (en
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魏志国
梁世丰
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Guangdong Jusu Technology Co ltd
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Guangdong Huateng Biological Co Ltd
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2401/00Characterised by the use of cellulose, modified cellulose or cellulose derivatives
    • C08J2401/08Cellulose derivatives
    • C08J2401/26Cellulose ethers
    • C08J2401/28Alkyl ethers
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    • C08J2403/00Characterised by the use of starch, amylose or amylopectin or of their derivatives or degradation products
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2467/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
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    • C08J2467/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2467/04Polyesters derived from hydroxy carboxylic acids, e.g. lactones
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    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
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Abstract

The present invention relates to biodegradated polymer materal technical fields, more particularly to a kind of biodegradable preservative film and preparation method thereof, raw material is mainly made of 50-65 portions of PBAT, 15-30 portions of modified starches, 20-40 parts of polylactic acid, 3-10 parts of Biodegradable aliphatic-aromatic copolyesters, 3-10 parts of methylhydroxypropylcellulose ethers, 2-8 parts of nano talcs, 0.1-0.5 parts of chain extenders, 0.2-0.8 parts of antioxidant and 0.2-0.6 parts of lubricants.The present invention greatly reduces cost, to be conducive to large-scale production and application while improving preservative film toughness of products, plasticity, intensity and degradability by the synergistic effect of each component.

Description

A kind of biodegradable preservative film and preparation method thereof
Technical field
The present invention relates to biodegradated polymer materal technical fields, and in particular to a kind of biodegradable preservative film and its Preparation method.
Background technique
With the continuous development of China's economy, the demand of the packaging materials such as preservative film is also increasing.Traditional preservative film Material is mainly derived from the petroleum based materials such as polyethylene (PE), is difficult after discarded processed.If by the way of burning Reason can then generate a large amount of toxic by-products;If handled by the way of burying, due to conventional petroleum sill degradation cycle Very long, some is even more than 100 years, this can bring about serious " white pollution " problem.Therefore, environment amenable biology Degradation material is the hot spot studied at present.
Polylactic acid (PLA) is a kind of thermoplasticity biodegradable material, intensity and modulus with higher, in recent years by people Be considered as a kind of environmental-friendly packaging material with great potential.But polylactic acid is semi-crystalline polymer, vitrifying The shortcomings that transition temperature is high, and there are poor toughness, brittleness greatly, poor heat resistance, to affect its processing performance and application;It is another Thermoplastic biodegradable material is polyadipate/butylene terephthalate (PBAT), has preferable ductility, extension at break Rate and impact property, but likewise, pure PBAT there is also hardness it is partially soft, film forming is poor the disadvantages of.Starch is that nature is only secondary In the second largest natural biological copolymer of cellulose, extremely low cost and Wholly-degradable cause people and greatly close Note.The existing much research in terms of polylactic acid and starch blending material and report both at home and abroad.For example, Chinese patent CN102408690A discloses a kind of thermoplastic starch modified polylactic acid material, forms starch by simple be directly blended and gathers The co-mixing system of lactic acid, but starch is incompatible with polylactic acid, co-mixing system interface adhesion is poor, causes product toughness, plastic Property etc. physical mechanical properties reduce;Chinese patent CN101831155A discloses a kind of preparation side of starch/polylactic acid mixture Method, used chain extender are to have virose diisocyanate compound, limit its in disposable food packing and Application in terms of tableware;For another example Chinese patent CN101781448A discloses a kind of enhanced polylactic acid of fully biodegradable Acid/starch blend preparation method, this method improve the mechanics of blend and resistance to by adding thermoplastic elastic toughener Hot property, but used thermoplastic elastic toughener is liquid rubber or thermoplastic elastomer (TPE), for not biodegradable composition, Affect blend can degradable property.Therefore there are still following defects: (1) starch for current starch conversion poly-lactic acid material The heat resisting temperature of itself is limited, and starch is made in process carbonization to occur and decompose because temperature is excessively high;(2) polylactic acid with The compatibility of starch is not good enough, causes the physical mechanical properties such as the toughness, intensity, plasticity of material poor.For this purpose, the prior art Mostly by adding various high-cost auxiliary agents to improve the performance of product, will lead to product in this way, cost has risen considerably, and And the degradability of material is caused to reduce;In addition, the prior art using coating method increase preservative film anti-microbial property, i.e., at One layer of antimicrobial coating is coated on the film of type, using solidifying.Although this mode simple process, coating can be with Environment changes the passage with the time and anti-microbial property is caused to decline, and the antibacterial time limit is short.
Summary of the invention
It is an object of the invention to provide a kind of biodegradable preservative film and its system aiming at the shortcomings in the prior art Preparation Method, prepared preservative film are obviously improved on plasticity, toughness, intensity and degradability, Er Qieyuan Various additives dosage is few in material, and modified starch dosage is more, reduces costs while improving product comprehensive performance.
The purpose of the present invention is achieved through the following technical solutions:
A kind of biodegradable preservative film is provided, is mainly made of raw material from the following weight:
Wherein, the modified starch is by 45-60 portions of tapiocas, 45-60 parts of distilled water, 2-8 parts of glycerol and 0.2-1 parts Made of maleic anhydride is modified by gelatinization.
Wherein, the modified starch is by 45-60 portions of tapiocas, 45-60 parts of distilled water, 2-8 parts of glycerol and 0.2-1 parts Made of maleic anhydride is modified by gelatinization.By carrying out gelatinization modification to tapioca, para arrowroot is on the one hand substantially increased The surface compatability and plasticizing capacity of powder, enable it is compatible with polylactic acid and PBAT well, so that improves product can Plasticity, toughness and tensile strength, another aspect modified starch heat resisting temperature get a promotion, and solve tapioca in process It is middle that the problem of carbonization is decomposed occurs because temperature is excessively high.Modified starch usage amount of the invention is larger, and raw material is cheap and easy to get, energy Cost is enough significantly reduced, although the dosage for increasing modified starch will also result in its object while improving product degradability The decline of mechanical performance is managed, but the present invention can guarantee not influencing product properties by the synergistic effect of other components Under the premise of, it is reduced cost also.
In above-mentioned technical proposal, a kind of biodegradable preservative film is mainly made of raw material from the following weight:
Further include the antibacterial agent of 0.8-1.5 parts by weight in above-mentioned technical proposal, the antibacterial agent by nisin and Tea polyphenols are according to weight ratio (2-3): (1-3) is compounded.
In above-mentioned technical proposal, the Biodegradable aliphatic-aromatic copolyester and methylhydroxypropylcellulose ether Weight ratio is (0.5-2): 1.It is improved using methylhydroxypropylcellulose ether and Biodegradable aliphatic-aromatic copolyester altogether The plasticity and toughening effect of mixed object, while making it have excellent mechanical performance and processability, both raw materials are all It is completely biodegradable material, the degradation property without will affect product;Specifically, being conducive to by the amount ratio of the two The compatibility in blend between each component is improved, the comprehensive performance of product is further increased.
In above-mentioned technical proposal, the Biodegradable aliphatic-aromatic copolyester be poly terephthalic acid-co- oneself two Sour butanediol ester, poly terephthalic acid-co- ethylene glycol adipate, poly terephthalic acid-co- EGS ethylene glycol succinate and poly- At least one of terephthalic acid (TPA)-co- succinic acid-butanediol ester.
In above-mentioned technical proposal, the average grain diameter of the nano talc is 50-80nm.The nanoscale of the particle size range is sliding Mountain flour particle can improve dispersion and interfacial adhesion problem in high temperature resistant substrate, and then be conducive to improve the strong of composite material Degree and toughness;In addition, also to control the partial size and dosage of nano talc, when dosage is very few, product is not achieved and finally uses The requirement of performance, when dosage is excessive, because nano-scale particle is easy to influence product due to occurring to reunite when high-temperature fusion is blended Can, while can also dramatically increase material cost.
In above-mentioned technical proposal, the chain extender is that marque is in ADR-4368C, ADR-4368CS and ADR-4370 At least one.The chain extender can be with the functional group reactions in polylactic acid chain, so that polylactic acid molecule chain forms long-branched knot Structure increases its molecular weight simultaneously, and the lactic acid composite material finally prepared not only greatly strengthens toughness, but also has better Thermal stability;The antioxidant is at least one of tert-butylhydroquinone, catechol and hydroquinone;The lubrication Agent is zinc stearate, N, any one in N'- ethylenebisstearamide and polyethylene wax, lubricant plays improvement polymer Rheological property effect.
The present invention also provides a kind of above-mentioned preparation methods of biodegradable preservative film, comprising the following steps:
Step a, formula ratio is pressed, under the conditions of 20-25 DEG C, after tapioca and distilled water are mixed and stirred for uniformly, is added Enter glycerol and maleic anhydride, and be stirred continuously the mixture to form colloidal, is subsequently placed in water-bath or oil bath pan and is added Heat gelatinization, heating temperature are 85-100 DEG C, and time 10-30min obtains thick colloid, then by drying, crushing, are obtained It is spare to modified starch;
Step b, formula ratio is pressed, weighs modified starch, PBAT, polylactic acid, biodegradable fatty race-aromatic copolyester respectively Ester, methylhydroxypropylcellulose ether and nano talc, dry 4-5h at 75-85 DEG C, make the moisture content of each component≤ 0.08%, be conducive to each component and carry out dry-mixed and subsequent melt polymerization reaction;Then by drying in addition to nano talc Component be stirred dry-mixed to uniform, obtain premix, be subsequently added into the chain extender of formula ratio, antioxidant, lubricant and Antibacterial agent continues to stir evenly, obtains blend;
Step c, screw extruder is added by spout in blend, and the nano talc of drying is added in screw downstream Enter screw extruder to squeeze out through high-temperature fusion, then be cooled down after Blown Film to get the preservative film is arrived, wherein screw extruder The temperature of each heating region is as follows:
Screw rod front: 175-180 DEG C, screw rod middle part: 170-175 DEG C, screw rod rear portion: 155-160 DEG C, nozzle temperature 180- 185℃。
In above-mentioned technical proposal, in step a, after thick colloid is toasted 10-30min at 100-120 DEG C, it will dry Solid be crushed to 100-300 mesh, obtain modified starch.
In above-mentioned technical proposal, in step c, the feeding revolving speed of screw extruder is 0.8-1.4rpm, by the temperature of feeding section Degree control is at 60-90 DEG C, to prevent the premature melting of chain extender and generation gel.In addition, nano talc is in spiral shell in step c Screw extruder is added in bar downstream, and other components are to nano-talc powder particles during can avoiding melt blending to the maximum extent Shearing and dispersion process impact.
Beneficial effects of the present invention:
A kind of biodegradable preservative film of the invention and preparation method thereof, wherein raw material mainly by 50-65 parts of PBAT, 15-30 portions of modified starches, 20-40 parts of polylactic acid, 3-10 parts of Biodegradable aliphatic-aromatic copolyesters, 3-10 parts of methyl hydroxyls Propyl cellulose ether, 2-8 part nano talc, 0.1-0.5 parts of chain extenders, 0.2-0.8 parts of antioxidant and 0.2-0.6 parts of lubricants It is made.Compared with prior art, the invention has the following advantages that
(1) present invention carries out gelatinization modification to tapioca using special process, substantially increases the surface of tapioca Compatibility and plasticizing capacity, enable it is compatible with polylactic acid and PBAT well, to improve the flexibility of product, tension Intensity and plasticity are stretched, and modified starch heat resisting temperature gets a promotion, makes tapioca in process will not be because of temperature It spends high and carbonization occurs and decomposes;
(2) present invention further utilizes methylhydroxypropylcellulose ether and Biodegradable aliphatic-aromatic copolyester, Firm connection layer is formed between fiber and aliphatic-aromatic copolyester, so that the intensity and ductility of material are improved, and this Two kinds of raw materials are all Biodegradable materials;On the other hand, pass through control modified starch, methylhydroxypropylcellulose ether and biology Degrading aliphatic-aromatic copolyester three amount ratio, further increases the compatibility in blend between each component;
(3) nano talc is used in inventive formulation, nanoscale talcum powder particle can improve in high temperature resistant base Dispersion and interfacial adhesion problem in material, and then be conducive to improve the intensity and toughness of composite material;By nano talc in spiral shell Screw extruder is added in bar downstream, and other components are to nano-talc powder particles during can avoiding melt blending to the maximum extent Shearing and dispersion process impact;
(4) additionally use chain extender in inventive formulation, in Screw Extrusion, chain extender can in polylactic acid chain Functional group reactions, so that polylactic acid molecule chain forms long-branched structure, increases its molecular weight simultaneously, the biology finally prepared can Degradable material not only greatly strengthens toughness, but also has better thermal stability;
(5) it is added to antibacterial agent in inventive formulation, which is dissolved in polylactic acid and PBAT co-mixing system, makes lactic acid chain Coccus peptide and tea polyphenols are embedded in polymer surfaces securely, coating method compared with prior art, and antibacterial effect is more lasting;
(6) in raw material of the invention, relative to polylactic acid and PBAT, the usage amount of various additives is less, and is modified shallow lake The content of powder is higher, by the synergistic effect of each component, thus improving preservative film toughness of products, plasticity, intensity and can While degradability, cost is greatly reduced, and preparation process is simple, easily controllable, be conducive to large-scale production and application.
Specific embodiment
The invention will be further described with the following Examples.
Embodiment 1:
A kind of preservative film of the present embodiment, preparation method are following (following each component is in parts by weight):
Step a, after at 20 °C, 50 portions of tapiocas and 50 parts of distilled water are mixed and stirred for uniformly, 4 parts are added Glycerol, 0.6 part of maleic anhydride, and it is stirred continuously the mixture to form colloidal;It is subsequently placed in water-bath or oil bath pan and carries out Heat Gelatinization, heating temperature are 95 DEG C, and time 25min obtains thick colloid;Thick colloid is placed in baking oven, is dried Dry temperature is 100 DEG C, after toasting 15min, the solid of drying is crushed to 200 mesh, obtains modified starch.
Step b, 20 portions of modified starches, 50 parts of PBAT, 25 parts of polylactic acid, 3 parts of biodegradable fatty race-fragrance are weighed respectively Race's copolyesters, 5 parts of methylhydroxypropylcellulose ethers and 5 parts of nano talcs (average grain diameter 50nm), dry 4h at 75 DEG C, Make moisture content≤0.08% of each component;Then the component in addition to nano talc of drying is stirred dry-mixed to equal It is even, obtain premix;It is subsequently added into 0.2 part of chain extender ADR-4368C, 0.4 part of tert-butylhydroquinone, 0.2 part of stearic acid Zinc and 1 part of antibacterial agent, continue to stir evenly, obtain blend;
In the step, Biodegradable aliphatic-aromatic copolyester be poly terephthalic acid-co- tetramethylene adipate, Poly terephthalic acid-co- ethylene glycol adipate and poly terephthalic acid-co- EGS ethylene glycol succinate are 2 according to weight ratio: The mixture of 2:1 compounding;Antibacterial agent is compounded by nisin and tea polyphenols according to weight ratio 3:1.
Step c, screw extruder is added by spout in blend, and the nano talc of drying is added in screw downstream Enter screw extruder to squeeze out through high-temperature fusion, then be cooled down after Blown Film to get preservative film is arrived.In the step, Screw Extrusion The feeding revolving speed of machine is 1.4rpm, by the control of the temperature of feeding section at 60 DEG C, the temperature setting of each heating region of screw extruder It is as shown in table 1:
The temperature of each heating region of 1. screw extruder of table
Embodiment 2:
A kind of preservative film of the present embodiment, preparation method are following (following each component is in parts by weight):
Step a, under the conditions of 22 DEG C, after 45 portions of tapiocas and 55 parts of distilled water are mixed and stirred for uniformly, 2 parts are added Glycerol, 0.4 part of maleic anhydride, and it is stirred continuously the mixture to form colloidal;It is subsequently placed in water-bath or oil bath pan and carries out Heat Gelatinization, heating temperature are 85 DEG C, and time 30min obtains thick colloid;Thick colloid is placed in baking oven, is dried Dry temperature is 110 DEG C, after toasting 20min, the solid of drying is crushed to 100 mesh, obtains modified starch.
Step b, weigh respectively 15 portions of modified starches, 60 parts of PBAT, 35 parts of polylactic acid, 5 parts of poly terephthalic acid-co- oneself Naphthalate, 3 parts of methylhydroxypropylcellulose ethers and 6 parts of nano talcs (average grain diameter 70nm), dry at 78 DEG C Dry 5h, makes moisture content≤0.08% of each component;Then the component in addition to nano talc of drying is stirred dry-mixed To uniform, premix is obtained;It is subsequently added into 0.1 part of chain extender ADR-4370,0.2 part of hydroquinone, 0.4 part of N, the Asia N'- second Base bis-stearamides and 1.2 parts of antibacterial agents, continue to stir evenly, obtain blend;
In the step, antibacterial agent is compounded by nisin and tea polyphenols according to weight ratio 1:1.
Step c, screw extruder is added by spout in blend, and the nano talc of drying is added in screw downstream Enter screw extruder to squeeze out through high-temperature fusion, then be cooled down after Blown Film to get preservative film is arrived.In the step, Screw Extrusion The feeding revolving speed of machine is 1.0rpm, by the control of the temperature of feeding section at 90 DEG C, the temperature setting of each heating region of screw extruder It is as shown in table 2:
The temperature of each heating region of 2. screw extruder of table
Embodiment 3:
A kind of preservative film of the present embodiment, preparation method are following (following each component is in parts by weight):
Step a, under the conditions of 25 DEG C, after 60 portions of tapiocas and 45 parts of distilled water are mixed and stirred for uniformly, 8 parts are added Glycerol, 1 part of maleic anhydride, and it is stirred continuously the mixture to form colloidal;It is subsequently placed in water-bath or oil bath pan and is added Heat gelatinization, heating temperature are 100 DEG C, and time 10min obtains thick colloid;Thick colloid is placed in baking oven, is dried Temperature is 120 DEG C, after toasting 10min, the solid of drying is crushed to 230 mesh, obtains modified starch.
Step b, 25 portions of modified starches, 56 parts of PBAT, 30 parts of polylactic acid, 10 parts of biodegradable fatty race-virtues are weighed respectively Fragrant race's copolyesters, 10 parts of methylhydroxypropylcellulose ethers and 8 parts of nano talcs (average grain diameter 60nm), dry at 80 DEG C 4.5h makes moisture content≤0.08% of each component, is then stirred the component in addition to nano talc of drying dry-mixed To uniform, premix is obtained, 0.2 part of chain extender ADR-4368C, 0.1 part of chain extender ADR-4370,0.3 part of spy are subsequently added into Butylhydroquinone, 0.5 part of catechol and 0.6 part of polyethylene wax, continue to stir evenly, obtain blend;
In the step, Biodegradable aliphatic-aromatic copolyester is poly terephthalic acid-co- EGS ethylene glycol succinate The mixture compounded with poly terephthalic acid-co- succinic acid-butanediol ester according to weight ratio 1:2.
Step c, screw extruder is added by spout in blend, and the nano talc of drying is added in screw downstream Enter screw extruder to squeeze out through high-temperature fusion, then be cooled down after Blown Film to get preservative film is arrived.In the step, Screw Extrusion The feeding revolving speed of machine is 0.8rpm, by the control of the temperature of feeding section at 80 DEG C, the temperature setting of each heating region of screw extruder It is as shown in table 3:
The temperature of each heating region of 3. screw extruder of table
Embodiment 4:
A kind of preservative film of the present embodiment, preparation method are following (following each component is in parts by weight):
Step a, under the conditions of 21 DEG C, after 56 portions of tapiocas and 60 parts of distilled water are mixed and stirred for uniformly, 6 parts are added Glycerol, 0.2 part of maleic anhydride, and it is stirred continuously the mixture to form colloidal;It is subsequently placed in water-bath or oil bath pan and carries out Heat Gelatinization, heating temperature are 90 DEG C, and time 15min obtains thick colloid;Thick colloid is placed in baking oven, is dried Dry temperature is 105 DEG C, after toasting 30min, the solid of drying is crushed to 300 mesh, obtains modified starch;
Step b, 30 portions of modified starches, 65 parts of PBAT, 40 parts of polylactic acid, 8 parts of biodegradable fatty race-fragrance are weighed respectively Race's copolyesters, 7 parts of methylhydroxypropylcellulose ethers and 3 parts of nano talcs (average grain diameter 80nm), dry 4h at 85 DEG C, Make moisture content≤0.08% of each component, is then stirred the component in addition to nano talc of drying dry-mixed to equal It is even, premix is obtained, 0.2 part of chain extender ADR-4368C, 0.2 part of chain extender ADR-4368CS, 0.1 part of chain extension are subsequently added into It is equal to continue stirring for agent ADR-4370,0.4 part of catechol, 0.2 part of hydroquinone, 0.3 part of zinc stearate and 0.8 part of antibacterial agent It is even, obtain blend;
In the step, Biodegradable aliphatic-aromatic copolyester is poly terephthalic acid-co- tetramethylene adipate The mixture compounded with poly terephthalic acid-co- EGS ethylene glycol succinate according to weight ratio 3:2;Antibacterial agent is by streptococcus lactis Peptide and tea polyphenols are compounded according to weight ratio 2:1.
Step c, screw extruder is added by spout in blend, and the nano talc of drying is added in screw downstream Enter screw extruder to squeeze out through high-temperature fusion, then be cooled down after Blown Film to get preservative film is arrived.In the step, Screw Extrusion The feeding revolving speed of machine is 1.2rpm, by the control of the temperature of feeding section at 70 DEG C, the temperature setting of each heating region of screw extruder It is as shown in table 4:
The temperature of each heating region of 4. screw extruder of table
Following performance detection is carried out respectively to the preservative film of embodiment 1 to 4:
1, tensile strength is tested:
According to the method for GB/T1040.1-2006, the sample of embodiment 1 to 4 is subjected to tensile strength test respectively.
2, elongation at break is tested:
According to the method for GB/T1040.1-2006, the sample of embodiment 1 to 4 is subjected to elongation at break test respectively.
3, tearing strength test:
According to the method for GB/T16578.1-2008, the sample of embodiment 1 to 4 is subjected to tearing strength test respectively.
4, degradation property is tested:
The sample of embodiment 1 to 4 is used into mounding respectively, dry known weight (W1) the sample embedment to constant weight is contained Have and keep high humility in the containers of mixtures such as sand, gardens soil, be protected from light, after a period of time, takes out soil and bury sample, clean table Face soil, it is dry to constant weight (W2), degradation rate: degradation rate=(W1-W2)/W1 × 100% is calculated according to calculation formula.
Test result is as shown in table 5:
The performance test of the preservative film of 5. embodiment 1 to 4 of table
It follows that preservative film of the invention has excellent plasticity, toughness, intensity and degradability, Er Qieyuan Various additives dosage is few in material, and modified starch dosage is more, reduces costs while improving product properties.
The present embodiment is merely illustrative of the technical solution of the present invention, rather than limiting the scope of the invention, although ginseng The present invention is explained in detail according to preferred embodiment, those skilled in the art should understand that, it can be to the present invention Technical solution be modified or replaced equivalently, without departing from the spirit and scope of technical solution of the present invention.

Claims (10)

1. a kind of biodegradable preservative film, it is characterised in that: be mainly made of raw material from the following weight:
Wherein, the modified starch is by 45-60 portions of tapiocas, 45-60 parts of distilled water, 2-8 parts of glycerol and 0.2-1 parts of Malaysias Made of acid anhydrides is modified by gelatinization.
2. a kind of biodegradable preservative film according to claim 1, it is characterised in that: mainly by the original of following parts by weight Material is made:
3. a kind of biodegradable preservative film according to claim 1 or 2, it is characterised in that: further include 0.8-1.5 weight The antibacterial agent of part, the antibacterial agent is by nisin and tea polyphenols according to weight ratio (2-3): (1-3) is compounded.
4. a kind of biodegradable preservative film according to claim 1, it is characterised in that: the biodegradable fatty race- The weight ratio of aromatic copolyester and methylhydroxypropylcellulose ether is (0.5-2): 1.
5. a kind of biodegradable preservative film according to claim 1, it is characterised in that: the nano talc is averaged Partial size is 50-80nm.
6. a kind of biodegradable preservative film according to claim 1, it is characterised in that: the biodegradable fatty race- Aromatic copolyester be poly terephthalic acid-co- tetramethylene adipate, poly terephthalic acid-co- ethylene glycol adipate, At least one of poly terephthalic acid-co- EGS ethylene glycol succinate and poly terephthalic acid-co- succinic acid-butanediol ester.
7. a kind of biodegradable preservative film according to claim 1, it is characterised in that: the chain extender is marque For at least one of ADR-4368C, ADR-4368CS and ADR-4370;The antioxidant is tert-butylhydroquinone, adjacent benzene At least one of diphenol and hydroquinone;The lubricant is zinc stearate, N,N' ethylene bis stearmide and polyethylene Any one in wax.
8. a kind of preparation method of biodegradable preservative film as described in claim 3 to 7 any one, it is characterised in that: The following steps are included:
Step a, formula ratio is pressed, under the conditions of 20-25 DEG C, after tapioca and distilled water are mixed and stirred for uniformly, is added sweet Oil and maleic anhydride, and it is stirred continuously the mixture to form colloidal, it is subsequently placed in water-bath or oil bath pan and carries out heating paste Change, heating temperature is 85-100 DEG C, and time 10-30min obtains thick colloid, then by drying, crushing, is changed Property starch, it is spare;
Step b, press formula ratio, weigh respectively modified starch, PBAT, polylactic acid, Biodegradable aliphatic-aromatic copolyester, Methylhydroxypropylcellulose ether and nano talc dry 4-5h at 75-85 DEG C, make moisture content≤0.08% of each component, Then the component in addition to nano talc of drying is stirred dry-mixed to uniform, obtains premix, is subsequently added into and matches Chain extender, antioxidant, lubricant and the antibacterial agent just measured, continue to stir evenly, obtain blend;
Step c, screw extruder is added by spout in blend, and spiral shell is added in screw downstream in the nano talc of drying Bar extruder is squeezed out through high-temperature fusion, is then cooled down after Blown Film to get the preservative film is arrived, wherein screw extruder respectively adds The temperature of thermal region is as follows:
Screw rod front: 175-180 DEG C, screw rod middle part: 170-175 DEG C, screw rod rear portion: 155-160 DEG C, nozzle temperature 180-185 ℃。
9. a kind of preparation method of biodegradable preservative film according to claim 8, it is characterised in that:, will in step a After thick colloid toasts 10-30min at 100-120 DEG C, the solid of drying is crushed to 100-300 mesh, obtains modified shallow lake Powder.
10. a kind of preparation method of biodegradable preservative film according to claim 8, it is characterised in that: in step c, The feeding revolving speed of screw extruder is 0.8-1.4rpm, and the temperature of feeding section is controlled at 60-90 DEG C.
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