CN114921046A - High-barrier polyester film and preparation method thereof - Google Patents

High-barrier polyester film and preparation method thereof Download PDF

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Publication number
CN114921046A
CN114921046A CN202210536294.4A CN202210536294A CN114921046A CN 114921046 A CN114921046 A CN 114921046A CN 202210536294 A CN202210536294 A CN 202210536294A CN 114921046 A CN114921046 A CN 114921046A
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barrier
polyester film
prepolymer
polymerization
polymer
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田有为
田其福
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Chengdu Fuquan New Material Co ltd
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Chengdu Fuquan New Material Co ltd
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    • CCHEMISTRY; METALLURGY
    • 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
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F283/00Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
    • C08F283/01Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to unsaturated polyesters
    • CCHEMISTRY; METALLURGY
    • 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
    • C08J2351/00Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • C08J2351/08Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers grafted on to macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/80Packaging reuse or recycling, e.g. of multilayer packaging

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

The invention relates to the field of film preparation, and particularly discloses a high-barrier polyester film and a preparation method thereof. Compared with the traditional PET polyester film, the high-barrier polyester film has better barrier property and good barrier effect on oxygen and water vapor.

Description

High-barrier polyester film and preparation method thereof
Technical Field
The invention relates to the field of film preparation, in particular to a high-barrier polyester film and a preparation method thereof.
Background
With the progress of society and the improvement of living standard, the requirements of people on food safety and sanitation are also improved to a new height, and the pure edible requirement is changed into the pursuit of food freshness, taste and quality. The PET film is limited by the structure thereof, and the development and the application of the PET film in the high-end important fields of military and civilian such as food and medicine are subjected to bottlenecks. Therefore, the barrier property, especially the oxygen barrier property, of the PET is improved, and the PET has a vital function and profound significance for the application of the PET in the field of packaging materials.
According to "Dolli. research, modification and application progress of PET [ J ]. Shandong chemical engineering 2021,50(8): 71-72", it is known that methods for improving barrier properties of polyester films in the prior art include surface treatment, laminar blending, nano material blending, multilayer compounding and the like. For example, CN202010210399.1 in China discloses a PET film with excellent gas barrier property and a preparation process thereof, the invention takes epoxy organosilane and methoxysilane as resin matrixes, and takes an active diluent, a cross-linking agent, a photoinitiator, a coinitiator, an adhesion regulator, a thermal curing agent and a nano polymer filler as raw materials to prepare a film with good gas and moisture barrier properties, and then the PET film is modified by utilizing a surface coating modification method, so that the barrier property of the PET film is further improved. The invention CN202110849954.X in China is a polyester film with high barrier property obtained by adopting a multilayer compounding method.
However, the existing high-barrier polyester film has the defects of numerous required raw materials and high preparation cost, or surface treatment, layered blending, nano material blending or multi-layer compounding is required, the preparation method is complicated, and no high-barrier polyester film which has good barrier property without further treatment is available.
Therefore, there is a need for a high barrier polyester film with simple preparation method, low preparation cost and good barrier property.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provide a high-barrier polyester film so as to at least achieve the effect that the barrier property is superior to that of the traditional PET film.
The purpose of the invention is realized by the following technical scheme:
a high-barrier polyester film is prepared from the prepolymer prepared from dicarboxylic acid and butenediol through polymerizing with cyclic diene.
Further, the dicarboxylic acids include: the dicarboxylic acids include: phthalic acid and its substitution products; the phthalic acid comprises one or more of phthalic acid, isophthalic acid, and terephthalic acid.
Further, the cyclic diene comprises one or more of cyclohexadiene, cyclopentadiene, divinylbenzene, diallyl maleate and butadiene.
Further, the molar ratio of the dicarboxylic acid to the butylene glycol is 4: 1 to 8; the mass ratio of the prepolymer to the cyclic diene is 15-19: 1-5.
Furthermore, the molecular weight of the prepolymer is 800-3600 g/mol.
It should be noted that if the molecular weight of the prepolymer is too low, the hard segment and the crosslinking point of the polymer formed subsequently are too many, the coating is too brittle, and the adverse effect is easily caused, so that the barrier property is damaged, and the molecular weight is too high, and the segments are easily entangled, so that the viscosity of the system is too high, which is not favorable for practical operation.
Another object of the present invention is to provide a method for preparing the high-barrier polyester film, comprising the steps of:
step one, polymerizing the dicarboxylic acid and the butenediol to form the prepolymer;
polymerizing the prepolymer and the cyclic diene to obtain a high-barrier polymer;
and step three, extruding and granulating the high-barrier polymer, melting the high-barrier polymer, and then stretching the high-barrier polymer to form a film.
Further, in the second step, the polymerization method is solution polymerization, photo-initiated polymerization or bulk polymerization.
Further, the solvent adopted by the solution polymerization comprises one or more of toluene, tetrahydrofuran, ethyl acetate and butanone; the initiator adopted by the solution polymerization comprises one or more of isophenylene hydroperoxide and benzoyl peroxide.
Further, the photoinitiator used for the photo-initiated polymerization includes photoinitiator 184 and/or photoinitiator TPO.
Further, the initiator used for the bulk polymerization comprises azobisisobutyronitrile and/or benzoyl peroxide.
It should be noted that PET is a high molecular polymer with linear structure, and from the viewpoint of molecular structure, it is the alternate existence of rigid chain segment and flexible chain segment, and although the existence of benzene ring has a certain restriction effect on the rotation of the chain segment, the C-O-C bond and CH in the structural unit 2 -CH 2 The limited effect of partial chain segments is small, the rotation is easy to occur, and the barrier of the small molecules of the permeate is not facilitated. The invention is through the ring shapeThe diene enables different polyester molecule chain segments to be interacted to form a large network structure, reduces the chain rotation and displacement of the flexible chain segment, and further inhibits the activity of the molecule chain segment. Meanwhile, the free volume of the molecular chain segment is smaller, and the barrier property of the polyester is effectively improved.
The invention has the beneficial effects that:
1. the preparation method of the high-barrier polyester film is simple, the raw materials are easy to obtain, the cost is low, and the preparation method is suitable for large-scale production.
2. Compared with the traditional PET polyester film, the high-barrier polyester film has better barrier property and good barrier effect on oxygen and water vapor.
Detailed Description
The technical solutions of the present invention are described in further detail below, but the scope of the present invention is not limited to the following.
Example 1
Step one, carrying out prepolymerization on 10 parts by mass of terephthalic acid and 20 parts by mass of butylene glycol to obtain a prepolymer;
and step two, carrying out free radical polymerization on the prepolymer obtained in the step one and 10 parts by mass of cyclohexadiene by using N-methyl pyrrolidone and iso-phenylpropyl hydrogen peroxide as initiators in a solvent polymerization manner to obtain a polymer.
And step three, carrying out vacuum filtration on the polymer obtained in the step two, removing the solvent, carrying out extrusion granulation on the obtained solid, and stretching the obtained particles to form a film.
Example 2
Step one, pre-polymerizing 20 parts by mass of isophthalic acid and 20 parts by mass of butylene glycol to obtain a prepolymer;
and step two, taking azobisisobutyronitrile as an initiator, and carrying out bulk polymerization on the prepolymer obtained in the step one and 10 parts by mass of cyclopentadiene to obtain a solid polymer.
And step three, extruding and granulating the solid obtained in the step two, and stretching the obtained particles to form a film.
Example 3
Step one, pre-polymerizing 20 parts by mass of phthalic acid and 10 parts by mass of butylene glycol to obtain a prepolymer;
and step two, taking 184 as a photoinitiator, and carrying out photoinitiated polymerization on the prepolymer obtained in the step one and 5 parts by mass of cyclohexadiene to obtain a polymer.
And step three, extruding and granulating the polymer obtained in the step two, and stretching the obtained particles to form a film.
Example 4
Step one, carrying out prepolymerization on 30 parts by mass of terephthalic acid and 10 parts by mass of butylene glycol to obtain a prepolymer;
and step two, using toluene as a solvent and benzoyl peroxide as an initiator, and carrying out free radical polymerization on the prepolymer obtained in the step one and 5 parts by mass of cyclohexadiene in a solvent polymerization manner to obtain a polymer.
And step three, carrying out vacuum filtration on the polymer obtained in the step two, removing the solvent, carrying out extrusion granulation on the obtained solid, and stretching the obtained particles to form a film.
Example 5
Step one, pre-polymerizing 40 parts by mass of isophthalic acid and 10 parts by mass of butylene glycol to obtain a prepolymer;
and step two, taking benzoyl peroxide as an initiator, and carrying out bulk polymerization on the prepolymer obtained in the step one and 5 parts by mass of cyclopentadiene to obtain a solid polymer.
And step three, extruding and granulating the solid obtained in the step two, and stretching the obtained particles to form a film.
Example 6
Step one, pre-polymerizing 40 parts by mass of phthalic acid and 10 parts by mass of butylene glycol to obtain a pre-polymer;
and step two, taking 184 as a photoinitiator, and carrying out photoinitiated polymerization on the prepolymer obtained in the step one and 2.5 parts by mass of cyclohexadiene to obtain a polymer.
And step three, extruding and granulating the polymer obtained in the step two. The resulting particles were stretched to form a film.
Comparative example 1: a conventional PET polyester film (brand manufacturer: DuPont, Foshan, model: 100 HN-A4).
Comparative example 2: a high-resistance polyester film was prepared in the same manner as in example 1, except that: butylene glycol was replaced with ethylene glycol.
Comparative example 3: a high-resistance polyester film was prepared in the same manner as in example 1, except that: the phthalic acid was replaced with malonic acid.
Examples of the experiments
The oxygen and water vapor barrier properties were tested for examples 1-6 and comparative examples. The oxygen transmission was tested via the plant using the national standard GBT1038-2000 and the water vapor transmission was tested via the plant using the national standard GBT 1037-1998. Oxygen transmission in cm 3 /m 2 24 h.0.1 MPa, water vapor transmission in g/m 2 24h, the lower the test value, the stronger the oxygen barrier capacity, and the experimental results are shown in Table 1.
TABLE 1
Figure BDA0003648363740000041
Therefore, the oxygen transmission rate of the high-barrier polyester film prepared by the method is 1/3-1/6 of that of the traditional PET polyester film, and the water vapor transmission rate is about 1/2 of that of the traditional PET polyester film, namely compared with the traditional PET polyester film, the oxygen transmission rate of the high-barrier polyester film is at least improved by 2 times, and the water vapor transmission rate of the high-barrier polyester film is improved by 1 time. In addition, after the butylene glycol is replaced by the ethylene glycol, the barrier property to oxygen and moisture is obviously reduced, which is probably because the symmetric hydrogen activity of the ethylene glycol is insufficient and a free radical can hardly be formed, and the double bond between two carbon atoms of the butylene glycol is an initiation point of a subsequent free radical, which is beneficial to a subsequent polymerization reaction. After the phthalic acid is replaced by the malonic acid, the blocking effect is reduced in response, which is probably because the phthalic acid contains benzene rings, and the benzene rings have a certain limiting effect on the rotation of the chain segments connected with the benzene rings, so that the activity of the chain segments can be inhibited, the permeation of small molecules is reduced, and the blocking performance is improved.
The foregoing is illustrative of the preferred embodiments of this invention, and it is to be understood that the invention is not limited to the precise form disclosed herein and that various other combinations, modifications, and environments may be resorted to, falling within the scope of the concept as disclosed herein, either as described above or as apparent to those skilled in the relevant art. And that modifications and variations may be effected by those skilled in the art without departing from the spirit and scope of the invention as defined by the appended claims.

Claims (10)

1. A high-barrier polyester film characterized by: the rubber is prepared by forming a prepolymer by dicarboxylic acid and butylene glycol and then polymerizing the prepolymer and cyclic diene.
2. The high barrier polyester film according to claim 1, wherein the dicarboxylic acid comprises: phthalic acid and its substitution products; the phthalic acid comprises one or more of phthalic acid, isophthalic acid, and terephthalic acid.
3. The high-barrier polyester film according to claim 1, wherein: the cyclic diene comprises one or more of cyclohexadiene, cyclopentadiene, divinylbenzene, diallyl maleate and butadiene.
4. The high-barrier polyester film according to claim 1, wherein: the mass ratio of the dicarboxylic acid to the butenediol is 4: 1-8; the mass ratio of the prepolymer to the cyclic diene is 15-19: 1-5.
5. The high-barrier polyester film according to claim 1, wherein: the molecular weight of the prepolymer is 800-3600 g/mol.
6. The method for preparing a high barrier polyester film according to any one of claims 1 to 5, comprising the steps of:
step one, polymerizing the dicarboxylic acid and the butenediol to form the prepolymer;
polymerizing the prepolymer and the cyclic diene to obtain a high-barrier polymer;
and step three, extruding and granulating the high-barrier polymer, melting the high-barrier polymer, and then stretching the high-barrier polymer to form a film.
7. The method of claim 6, wherein: in the second step, the polymerization method is solution polymerization, photoinitiated polymerization or bulk polymerization.
8. The method of claim 7, wherein: the solvent adopted by the solution polymerization comprises one or more of toluene, tetrahydrofuran, ethyl acetate and butanone; the initiator adopted by the solution polymerization comprises one or more of isophenylene hydroperoxide and benzoyl peroxide.
9. The method of claim 7, wherein: the photoinitiator used for the photoinitiated polymerization includes photoinitiator 184 and/or photoinitiator TPO.
10. The method for producing according to claim 7, characterized in that: the initiator adopted by the bulk polymerization comprises azobisisobutyronitrile and/or benzoyl peroxide.
CN202210536294.4A 2022-05-17 2022-05-17 High-barrier polyester film and preparation method thereof Pending CN114921046A (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001009998A (en) * 1999-06-25 2001-01-16 Teijin Ltd Gas barrier polyester film
US20080161465A1 (en) * 2006-12-28 2008-07-03 Jason Christopher Jenkins Oxygen-scavenging polyester compositions useful for packaging
CN113045873A (en) * 2021-03-17 2021-06-29 宜兴博雅新材料科技有限公司 Graphene oxide high-barrier composite film and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001009998A (en) * 1999-06-25 2001-01-16 Teijin Ltd Gas barrier polyester film
US20080161465A1 (en) * 2006-12-28 2008-07-03 Jason Christopher Jenkins Oxygen-scavenging polyester compositions useful for packaging
CN113045873A (en) * 2021-03-17 2021-06-29 宜兴博雅新材料科技有限公司 Graphene oxide high-barrier composite film and preparation method thereof

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