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WO2010002205A2 - Biodegradable flexible film - Google Patents

Biodegradable flexible film Download PDF

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Publication number
WO2010002205A2
WO2010002205A2 PCT/KR2009/003621 KR2009003621W WO2010002205A2 WO 2010002205 A2 WO2010002205 A2 WO 2010002205A2 KR 2009003621 W KR2009003621 W KR 2009003621W WO 2010002205 A2 WO2010002205 A2 WO 2010002205A2
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WO
WIPO (PCT)
Prior art keywords
film
pha
longitudinal
sheet
poly
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/KR2009/003621
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French (fr)
Other versions
WO2010002205A3 (en
Inventor
Kyung-Youn Kim
Sang Il Kim
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SKC Co Ltd
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SKC Co Ltd
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Publication of WO2010002205A2 publication Critical patent/WO2010002205A2/en
Publication of WO2010002205A3 publication Critical patent/WO2010002205A3/en
Anticipated expiration legal-status Critical
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Classifications

    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0018Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/10Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
    • B29C55/12Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D7/00Producing flat articles, e.g. films or sheets
    • B29D7/01Films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/04Polyesters derived from hydroxycarboxylic acids, e.g. lactones
    • 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
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/04Polyesters derived from hydroxy carboxylic acids, e.g. lactones
    • 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
    • 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
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/06Biodegradable
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/10Transparent films; Clear coatings; Transparent materials
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/16Applications used for films

Definitions

  • the present invention relates to a biodegradable flexible film having improved flexibility, transparency, and mechanical properties, which is useful for environmentally friendly packaging.
  • plastic films such as polyvinyl chloride, polyethylene and polypropylene films are not completely satisfactory in terms of their performance characteristics.
  • polyvinyl chloride films generate toxic pollutants when incinerated, and polyethylene films have been employed only for low-grade packaging materials due to their relatively poor dimensional and mechanical properties.
  • Polypropylene films have satisfactory mechanical properties, but generate products that are not biodegradable and accumulate in the soil when disposed.
  • biodegradable aliphatic polyesters particularly polylactic acid films. While such films have satisfactory mechanical properties and transparency, they have poor flexibility due to their high crystallinity, making them unsuitable for packaging. In case of using such films for wrapping cold-storage materials or frozen foods at a low temperature, they break easily during storage or handling due to insufficient pin-hole resistance.
  • H09-157408 and 2004-010900 disclose a polylactic acid film which is prepared by blending polylactic acid (having an L-lactic acid to D-lactic acid weight ratio of 100:0-94:6 or 6:94-0: 100) and a biodegradable aliphatic polyester having a glass transition temperature (T g ) of 0 o C or less at a weight ratio of 100 : 3 to 100 : 70, and the film obtained from the blend is drawn at least once in the transverse or longitudinal direction and heat-treated.
  • T g glass transition temperature
  • the polylactic acid films thus produced have problems in that the miscibility of the polyester with polylactic acid is poor, leading to increased haze of the film, which is not suitable for use as a transparent wrapping material.
  • T g of the polyester resin is 0 o C or less, adhesion of the film to a casting roll occurs frequently during the processing, the thermal stability resistance of the film is unsatisfactorily low, and the degree of heat shrinkage of the film is too high for use in an application that requires dimensional stability.
  • biodegradable flexible film having improved flexibility, transparency, pin-hole resistance, and mechanical properties which can be advantageously used for packaging.
  • a biodegradable flexible film comprising 20 to 90 wt% of polylactic acid and 1 to 80 wt% of a polyhydroxyalkanoate (PHA), which exhibits a biodegradability of at least
  • a wrapping material comprising the biodegradable flexible film according to the present invention.
  • a method for preparing the inventive biodegradable flexible film comprising the steps of: (a) melt-extruding a polymer blend composed of 20 to 99 wt% of polylactic acid and 1 to 80 wt% of a PHA, to prepare a sheet; (b) drawing the sheet in the longitudinal and transverse directions to prepare a biaxially oriented film; and (c) heat-setting the biaxially oriented film.
  • the biodegradable flexible film according to the present invention can be efficiently used as an environmentally friendly wrapping material due to its superior flexibility, transparency, pin-hole resistance, mechanical properties, and biodegradability.
  • the biodegradable flexible film of the present invention comprises 20 to 90 wt% of polylactic acid and 1 to 80 wt% of a polyhydroxyalkanoate (PHA).
  • PHA polyhydroxyalkanoate
  • the inventive film may comprise 50 to 90 wt% of polylactic acid and 10 to 50 wt% of a PHA.
  • the inventive film has a biodegradability of 90 % or more.
  • biodegradability refers to a ratio of biodegradation of test material to that of standard material (e.g., cellulose) over a same period of time.
  • standard material e.g., cellulose
  • the Ministry of Environment in Korea regulates that the biodegradability of a particular material relative to that of a standard material should be 90 % or more.
  • the inventive film has an initial elastic modulus determined based on a stress-strain curve of 50 to 350 kgf/mm 2 .
  • the initial elastic modulus of the film is less than 50 kgf/mm 2 , problems occur during printing or laminating process due to the occurrence of wrinkles in the driving direction which is caused by insufficient resistance against a mechanical tension, while when is more than 350 kgf/mm 2 , the film may be easily broken or rupture due to an increased stiffness.
  • the inventive film may have an initial elastic modulus determined based on a stress-strain curve of 150 to 250 kgf/mm 2 .
  • the inventive film has a haze of 20 % or less.
  • a transparency of the film significantly decreases which is not suitable for a transparent wrapping material.
  • the inventive film may have a haze of 10 % or less.
  • the PHA used in the inventive film may be a heteropolymer or copolymer which consists of one or more repeating units of formulas I and II:
  • Rl is methyl or ethyl
  • R2 is ethyl, propyl, pentyl, or heptyl
  • the PHA used in the inventive film may be selected from the group consisting of polyhydroxybutyrate (PHB), polyhydroxybutyrate valerate (PHBV), poly(3 -hydroxybutyrate-co-3 -hydroxy valerate) (P(3HB-co-3HV)), poly(3 -hydroxybutyrate-co-3 -hydroxyhexanoate) (P(3HB-co-3HH)), poly (3 -hy droxybutyrate-co- 3 -hydroxy octanoate) (P(3HB-co-3HO)), poly-3 -hydroxyvalerate (PHV), and a mixture thereof.
  • the PHA used in the inventive film may further comprise a glycolide repeating unit of formula III in an amount of 0 to 50 wt% based on the weight of the PHA.
  • a glycolide repeating unit of formula III in an amount of 0 to 50 wt% based on the weight of the PHA.
  • PHA may comprise the glycolide in an amount of 20 wt% or less.
  • the inventive film may further comprise other additives such as an anti- blocking agent, a cross-linking agent, antioxidant, heat stabilizer, UV absorber and plasticizers to the extent they do not adversely affect the film properties.
  • additives such as an anti- blocking agent, a cross-linking agent, antioxidant, heat stabilizer, UV absorber and plasticizers to the extent they do not adversely affect the film properties.
  • the inventive film has improved pin-hole resistance, preferably, the inventive film may have 100 or less pin-holes per 100 cm 2 when stressed repeatedly at ambient temperature.
  • a film having pin-hole number exceeding 100 in the test may become brittle to rupture easily during shipping, and may be susceptible to actual pin-hole generation when wrinkled repeatedly, particularly in winter.
  • the inventive film may have pin-hole number of 50 or less in the test.
  • the heat shrinkability of the inventive film measured at 100 o C for 5 min may be 70 % or less in either the longitudinal or transverse direction.
  • heat shrinkability of a film exceeds 70 %, heat shrinkage may occur excessively in the longitudinal and transverse directions during printing or laminating process and the film may be curled after printing.
  • the biodegradable flexible film of the present invention is prepared by a method comprising the steps of: (a) melt-extruding a polymer blend composed of 20 to 99 wt% of polylactic acid and 1 to 80 wt% of a PHA, to prepare a sheet; (b) drawing the sheet in the longitudinal and transverse directions to prepare a biaxially oriented film; and (c) heat-setting the biaxially oriented film.
  • the melt-extruding may be performed at 180 to 25O o C.
  • the longitudinal drawing and the transverse drawing may be performed at draw ratios of 2 to 4 and 3 to 5, respectively. Further, the longitudinal drawing and the transverse drawing may be conducted at temperature ranges of 40 to 90 o C and 50 to 90 o C, respectively.
  • the heat-setting may be carried at 50 to 150 o C.
  • Example 1 Polylactic acid resin (4032D, Nature Works LLC) having a melting point of
  • Rl is CH 3 and R2 is CH 2 CH 3 ) and glycolide, were blended at a weight ratio of 90 : 10.
  • the polymer blend was melt-extruded at 230 o C and then cooled on a casting roll kept at 15 o C to prepare a sheet.
  • the sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 70 o C and then drawn at a draw ratio of 3.7 in the transverse direction at 85 o C.
  • the drawn sheet was heat-set at 100 o C, to obtain a biaxially drawn polyester film having a thickness of 20 ⁇ m.
  • Polylactic acid resin 4032D, Nature Works LLC having a melting point of 170 o C and a polyhydroxyalkanoate copolymer resin (P(3HB-co-3HH), Rl is CH 3 and R2 is CH 2 CH 2 CH 3 ) (troflexTM, Danimer scientific LLC) having a melting point of 140 o C, were blended at a weight ratio of 80 : 20.
  • the polymer blend was melt-extruded at 220 o C and then cooled on a casting roll kept at 15 o C to prepare a sheet.
  • the sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 75 o C and then drawn at a draw ratio of 3.7 in the transverse direction at 80 o C.
  • the drawn sheet was heat-set at 100 o C, to obtain a biaxially drawn polyester film having a thickness of 20 ⁇ m.
  • Polylactic acid resin 4032D, Nature Works LLC having a melting point of 170 o C and a polyhydroxyalkanoate copolymer resin (P(3HB-co-3HO), Rl is CH 3 and R2 is (CH 2 ) 4 CH 3 ) (troflexTM, Danimer scientific LLC) having a melting point of 100 o C, were blended at a weight ratio of 70 : 30.
  • the polymer blend was melt-extruded at 210 o C and then cooled on a casting roll kept at 15 o C to prepare a sheet.
  • the sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 70 o C and then drawn at a draw ratio of 3.7 in the transverse direction at 75 o C.
  • the drawn sheet was heat-set at 140 o C, to obtain a biaxially drawn polyester film having a thickness of 20 ⁇ m.
  • Polylactic acid resin (4032D, Nature Works LLC) having a melting point of 170 o C was melt-extruded at 240 o C and then cooled on a casting roll kept at 18 o C to prepare a sheet.
  • the sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 85 o C and then drawn at a draw ratio of 3.7 in the transverse direction at 90 o C.
  • the drawn sheet was heat-set at 140 o C, to obtain a biaxially drawn polyester film having a thickness of 20 /m.
  • Polylactic acid resin 4032D, Nature Works LLC having a melting point of 170 o C and polybutylene succinate (PBS) (G4560, IRe Chemical Ltd., Korea) having a melting point of 115 o C were blended at a weight ratio of 95 : 5.
  • PBS polybutylene succinate
  • the polymer blend resin was melt-extruded at 220 o C and then cooled on a casting roll kept at 15 o C to prepare a sheet.
  • the sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 75 o C and then drawn at a draw ratio of 3.7 in the transverse direction at 80 o C.
  • the drawn sheet was heat-set at 100 o C, to obtain a biaxially drawn polyester film having a thickness of 20 ⁇ m.
  • Polylactic acid resin 4032D 5 Nature Works LLC having a melting point of 170 o C and a polyhydroxyalkanoate (PHB, Rl is CH 3 ) (troflexTM, Danimer scientific LLC) having a melting point of 180 o C, were blended at a weight ratio of 15 : 85.
  • the polymer blend resin was melt-extruded at 200 o C and then cooled on a casting roll kept at 9 o C to prepare a sheet.
  • the sheet was drawn at a draw ratio of 2.5 in the longitudinal direction at 60 o C and then drawn at a draw ratio of 3.0 in the transverse direction at 65 o C.
  • the drawn sheet was heat-set at 100 o C, to obtain a biaxially drawn polyester film having a thickness of 20 ⁇ m.
  • a polymer sample dissolved in a 4: 1 mixture of deutro-chloroform and trifluoroacetic acid was subjected to quantitative NMR analysis with JSM-LA300 type 1 H-NMR (Jeol Inc., Japan). Relative areas of characteristic peaks based on a read out were converted into weight%.
  • a biodegradability of a film sample was evaluated according to KS M3100- 1 (2003), and the ratio of biodegradability value of the film sample and that of a standard material over a period of 180 days was calculated according to the following equation:
  • Biodegradability (%) [ (degree of biodegradation of film sample) / (degree of biodegradation of standard material) ] x 100
  • An initial elastic modulus was determined according to ASTM D 882 by measuring the modulus of elasticity using a film sample having the size of 100 mm (length) x 15 mm (width) with Universal Tester (UTM 4206-001 , Instron Inc.), wherein the interval between chucks is set at 50 mm and the elongation speed at 200 mm/min, and calculating an average value therefrom. (4) Haze (%)
  • a haze of a film specimen was measured with a hazemeter (Model: SEP-H, Nihohn Semitsu Kogaku, Japan) using a C-light source.
  • a sample film was subjected to a flex crack resistance test using Gelbo-Flex tester (Gelbo Inc., USA) consisting of a 165 mm sample fixing plate, a 88 mm sample fixing diameter and a 125 mm traveling distance, at an angle of 420 degrees for 450 cycles.
  • the sample film was placed flat on a white paper, whereon an oily nitroglycerin-based ink was applied with a doctor blade.
  • the numbers of ink dots appeared on the white paper was represented as the pin-hole number.
  • An average value derived from 3 tests was taken to represent each sample.
  • a film sample was cut into a 200 mm (length) x 15 mm (width) piece, maintained at 100 o C in a circulating air oven for 5 minutes, and the change in the film length was measured. Using the following equation, the degrees of shrinkage in each of the longitudinal and transverse directions were calculated:
  • Heat shrinkage (%) [ ( length before heat treatment - length after heat treatment ) / length before heat treatment ] x 100
  • the inventive films exhibit improved properties in terms of flexibility, transparency, pin-hole resistance, and mechanical properties, etc., whereas the films that fall out the scope of the present invention showed deteriorated properties.

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  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
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  • Biological Depolymerization Polymers (AREA)
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Abstract

A biodegradable flexible film, comprising 20 to 90 wt% of polylactic acid and 1 to 80 wt% of a polyhydroxyalkanoate, exhibits a biodegradability of at least 90 %, an initial elastic modulus determined based on a stress-strain curve of 50 to 350 kgf/mm2, and a haze of 20 % or less.

Description

BIODEGRADABLE FLEXIBLE FILM
FIELD OF THE INVENTION
The present invention relates to a biodegradable flexible film having improved flexibility, transparency, and mechanical properties, which is useful for environmentally friendly packaging.
BACKGROUND OF THE INVENTION
Conventional plastic films such as polyvinyl chloride, polyethylene and polypropylene films are not completely satisfactory in terms of their performance characteristics. For example, polyvinyl chloride films generate toxic pollutants when incinerated, and polyethylene films have been employed only for low-grade packaging materials due to their relatively poor dimensional and mechanical properties. Polypropylene films, on the other hand, have satisfactory mechanical properties, but generate products that are not biodegradable and accumulate in the soil when disposed.
In order to solve such problems, there have been employed biodegradable aliphatic polyesters, particularly polylactic acid films. While such films have satisfactory mechanical properties and transparency, they have poor flexibility due to their high crystallinity, making them unsuitable for packaging. In case of using such films for wrapping cold-storage materials or frozen foods at a low temperature, they break easily during storage or handling due to insufficient pin-hole resistance. Japanese Laid-open Patent Publication Nos. H09-157408 and 2004-010900 disclose a polylactic acid film which is prepared by blending polylactic acid (having an L-lactic acid to D-lactic acid weight ratio of 100:0-94:6 or 6:94-0: 100) and a biodegradable aliphatic polyester having a glass transition temperature (Tg) of 0 oC or less at a weight ratio of 100 : 3 to 100 : 70, and the film obtained from the blend is drawn at least once in the transverse or longitudinal direction and heat-treated. However, the polylactic acid films thus produced have problems in that the miscibility of the polyester with polylactic acid is poor, leading to increased haze of the film, which is not suitable for use as a transparent wrapping material. Further, when Tg of the polyester resin is 0 oC or less, adhesion of the film to a casting roll occurs frequently during the processing, the thermal stability resistance of the film is unsatisfactorily low, and the degree of heat shrinkage of the film is too high for use in an application that requires dimensional stability.
SUMMARY OF THE INVENTION
Accordingly, it is an object of the present invention to provide a biodegradable flexible film having improved flexibility, transparency, pin-hole resistance, and mechanical properties which can be advantageously used for packaging.
It is another object of the present invention to provide an improved wrapping material .
It is a further object of the present invention to provide a preparation method of the inventive biodegradable flexible film.
In accordance with one aspect of the present invention, there is provided a biodegradable flexible film comprising 20 to 90 wt% of polylactic acid and 1 to 80 wt% of a polyhydroxyalkanoate (PHA), which exhibits a biodegradability of at least
90 %, an initial elastic modulus determined based on a stress-strain curve of 50 to
350 kgf/mm2, and a haze of 20 % or less.
In accordance with another aspect of the present invention, there is provided a wrapping material comprising the biodegradable flexible film according to the present invention.
In accordance with a further aspect of the present invention, there is provided a method for preparing the inventive biodegradable flexible film comprising the steps of: (a) melt-extruding a polymer blend composed of 20 to 99 wt% of polylactic acid and 1 to 80 wt% of a PHA, to prepare a sheet; (b) drawing the sheet in the longitudinal and transverse directions to prepare a biaxially oriented film; and (c) heat-setting the biaxially oriented film. The biodegradable flexible film according to the present invention can be efficiently used as an environmentally friendly wrapping material due to its superior flexibility, transparency, pin-hole resistance, mechanical properties, and biodegradability.
DETAILED DESCRIPTION OF THE INVENTION
The biodegradable flexible film of the present invention comprises 20 to 90 wt% of polylactic acid and 1 to 80 wt% of a polyhydroxyalkanoate (PHA). When the amount of the PHA is less than 1 wt%, it fails to slow down the crystallization of the polylactic acid so that the film has insufficient flexibility, while when is more than 80 wt%, the crystallization of the polylactic acid becomes slow to make it difficult to draw, and the film has poor mechanical properties. Preferably, the inventive film may comprise 50 to 90 wt% of polylactic acid and 10 to 50 wt% of a PHA.
The inventive film has a biodegradability of 90 % or more. As used herein, the term "biodegradability" refers to a ratio of biodegradation of test material to that of standard material (e.g., cellulose) over a same period of time. The Ministry of Environment in Korea regulates that the biodegradability of a particular material relative to that of a standard material should be 90 % or more.
The inventive film has an initial elastic modulus determined based on a stress-strain curve of 50 to 350 kgf/mm2. When the initial elastic modulus of the film is less than 50 kgf/mm2, problems occur during printing or laminating process due to the occurrence of wrinkles in the driving direction which is caused by insufficient resistance against a mechanical tension, while when is more than 350 kgf/mm2, the film may be easily broken or rupture due to an increased stiffness. Preferably, the inventive film may have an initial elastic modulus determined based on a stress-strain curve of 150 to 250 kgf/mm2.
The inventive film has a haze of 20 % or less. When the haze is more than 20 %, a transparency of the film significantly decreases which is not suitable for a transparent wrapping material. Preferably, the inventive film may have a haze of 10 % or less.
The PHA used in the inventive film may be a heteropolymer or copolymer which consists of one or more repeating units of formulas I and II:
Figure imgf000005_0001
wherein, Rl is methyl or ethyl, and R2 is ethyl, propyl, pentyl, or heptyl.
The PHA used in the inventive film may be selected from the group consisting of polyhydroxybutyrate (PHB), polyhydroxybutyrate valerate (PHBV), poly(3 -hydroxybutyrate-co-3 -hydroxy valerate) (P(3HB-co-3HV)), poly(3 -hydroxybutyrate-co-3 -hydroxyhexanoate) (P(3HB-co-3HH)), poly (3 -hy droxybutyrate-co- 3 -hydroxy octanoate) (P(3HB-co-3HO)), poly-3 -hydroxyvalerate (PHV), and a mixture thereof.
The PHA used in the inventive film may further comprise a glycolide repeating unit of formula III in an amount of 0 to 50 wt% based on the weight of the PHA. When the content of the glycolide repeating unit exceeds 50 wt%, the crystallizing may become slow to make it difficult to form a film. Preferably, the
PHA may comprise the glycolide in an amount of 20 wt% or less.
Figure imgf000005_0002
The inventive film may further comprise other additives such as an anti- blocking agent, a cross-linking agent, antioxidant, heat stabilizer, UV absorber and plasticizers to the extent they do not adversely affect the film properties.
The inventive film has improved pin-hole resistance, preferably, the inventive film may have 100 or less pin-holes per 100 cm2 when stressed repeatedly at ambient temperature. A film having pin-hole number exceeding 100 in the test may become brittle to rupture easily during shipping, and may be susceptible to actual pin-hole generation when wrinkled repeatedly, particularly in winter. Preferably, the inventive film may have pin-hole number of 50 or less in the test.
The heat shrinkability of the inventive film measured at 100 oC for 5 min may be 70 % or less in either the longitudinal or transverse direction. When such heat shrinkability of a film exceeds 70 %, heat shrinkage may occur excessively in the longitudinal and transverse directions during printing or laminating process and the film may be curled after printing.
The biodegradable flexible film of the present invention is prepared by a method comprising the steps of: (a) melt-extruding a polymer blend composed of 20 to 99 wt% of polylactic acid and 1 to 80 wt% of a PHA, to prepare a sheet; (b) drawing the sheet in the longitudinal and transverse directions to prepare a biaxially oriented film; and (c) heat-setting the biaxially oriented film.
In the inventive method, the melt-extruding may be performed at 180 to 25OoC.
The longitudinal drawing and the transverse drawing may be performed at draw ratios of 2 to 4 and 3 to 5, respectively. Further, the longitudinal drawing and the transverse drawing may be conducted at temperature ranges of 40 to 90 oC and 50 to 90 oC, respectively.
The heat-setting may be carried at 50 to 150 oC.
EXAMPLE
The following Examples are intended to further illustrate the present invention without limiting its scope.
Example 1 Polylactic acid resin (4032D, Nature Works LLC) having a melting point of
170 oC and a copolymer resin (troflex™, Danimer scientific LLC) having a melting point of 150 oC which is a copolymer of polyhydroxyalkanoate (P(3HB-co-3HV),
Rl is CH3 and R2 is CH2CH3) and glycolide, were blended at a weight ratio of 90 : 10.
The polymer blend was melt-extruded at 230 oC and then cooled on a casting roll kept at 15 oC to prepare a sheet. The sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 70 oC and then drawn at a draw ratio of 3.7 in the transverse direction at 85 oC. The drawn sheet was heat-set at 100 oC, to obtain a biaxially drawn polyester film having a thickness of 20 μm.
Example 2
Polylactic acid resin (4032D, Nature Works LLC) having a melting point of 170 oC and a polyhydroxyalkanoate copolymer resin (P(3HB-co-3HH), Rl is CH3 and R2 is CH2CH2CH3) (troflex™, Danimer scientific LLC) having a melting point of 140 oC, were blended at a weight ratio of 80 : 20.
The polymer blend was melt-extruded at 220 oC and then cooled on a casting roll kept at 15 oC to prepare a sheet. The sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 75 oC and then drawn at a draw ratio of 3.7 in the transverse direction at 80 oC. The drawn sheet was heat-set at 100 oC, to obtain a biaxially drawn polyester film having a thickness of 20 μm.
Example 3
Polylactic acid resin (4032D, Nature Works LLC) having a melting point of 170 oC and a polyhydroxyalkanoate copolymer resin (P(3HB-co-3HO), Rl is CH3 and R2 is (CH2)4CH3) (troflex™, Danimer scientific LLC) having a melting point of 100 oC, were blended at a weight ratio of 70 : 30. The polymer blend was melt-extruded at 210 oC and then cooled on a casting roll kept at 15 oC to prepare a sheet. The sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 70 oC and then drawn at a draw ratio of 3.7 in the transverse direction at 75 oC. The drawn sheet was heat-set at 140 oC, to obtain a biaxially drawn polyester film having a thickness of 20 μm.
Comparative Example 1
Polylactic acid resin (4032D, Nature Works LLC) having a melting point of 170 oC was melt-extruded at 240 oC and then cooled on a casting roll kept at 18 oC to prepare a sheet. The sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 85 oC and then drawn at a draw ratio of 3.7 in the transverse direction at 90 oC. The drawn sheet was heat-set at 140 oC, to obtain a biaxially drawn polyester film having a thickness of 20 /m.
Comparative Example 2
Polylactic acid resin (4032D, Nature Works LLC) having a melting point of 170 oC and polybutylene succinate (PBS) (G4560, IRe Chemical Ltd., Korea) having a melting point of 115 oC were blended at a weight ratio of 95 : 5.
The polymer blend resin was melt-extruded at 220 oC and then cooled on a casting roll kept at 15 oC to prepare a sheet. The sheet was drawn at a draw ratio of 3.0 in the longitudinal direction at 75 oC and then drawn at a draw ratio of 3.7 in the transverse direction at 80 oC. The drawn sheet was heat-set at 100 oC, to obtain a biaxially drawn polyester film having a thickness of 20 μm.
Comparative Example 3
Polylactic acid resin (4032D5 Nature Works LLC) having a melting point of 170 oC and a polyhydroxyalkanoate (PHB, Rl is CH3) (troflex™, Danimer scientific LLC) having a melting point of 180 oC, were blended at a weight ratio of 15 : 85. The polymer blend resin was melt-extruded at 200 oC and then cooled on a casting roll kept at 9 oC to prepare a sheet. The sheet was drawn at a draw ratio of 2.5 in the longitudinal direction at 60 oC and then drawn at a draw ratio of 3.0 in the transverse direction at 65 oC. The drawn sheet was heat-set at 100 oC, to obtain a biaxially drawn polyester film having a thickness of 20 μm.
The polyester films obtained in Examples 1 to 3 and Comparative Examples
1 to 3 were each evaluated as follows. The results are shown in Table 1.
(1) Composition
A polymer sample dissolved in a 4: 1 mixture of deutro-chloroform and trifluoroacetic acid was subjected to quantitative NMR analysis with JSM-LA300 type 1H-NMR (Jeol Inc., Japan). Relative areas of characteristic peaks based on a read out were converted into weight%.
(2) Biodegradability (%)
A biodegradability of a film sample was evaluated according to KS M3100- 1 (2003), and the ratio of biodegradability value of the film sample and that of a standard material over a period of 180 days was calculated according to the following equation:
Biodegradability (%) = [ (degree of biodegradation of film sample) / (degree of biodegradation of standard material) ] x 100
(3) Initial elastic modulus (kgf/mm2)
An initial elastic modulus was determined according to ASTM D 882 by measuring the modulus of elasticity using a film sample having the size of 100 mm (length) x 15 mm (width) with Universal Tester (UTM 4206-001, Instron Inc.), wherein the interval between chucks is set at 50 mm and the elongation speed at 200 mm/min, and calculating an average value therefrom. (4) Haze (%)
A haze of a film specimen was measured with a hazemeter (Model: SEP-H, Nihohn Semitsu Kogaku, Japan) using a C-light source.
(5) Pin-hole resistance
A sample film was subjected to a flex crack resistance test using Gelbo-Flex tester (Gelbo Inc., USA) consisting of a 165 mm sample fixing plate, a 88 mm sample fixing diameter and a 125 mm traveling distance, at an angle of 420 degrees for 450 cycles.
Next, the sample film was placed flat on a white paper, whereon an oily nitroglycerin-based ink was applied with a doctor blade. The numbers of ink dots appeared on the white paper was represented as the pin-hole number. An average value derived from 3 tests was taken to represent each sample.
(6) Heat shrinkage (%)
A film sample was cut into a 200 mm (length) x 15 mm (width) piece, maintained at 100 oC in a circulating air oven for 5 minutes, and the change in the film length was measured. Using the following equation, the degrees of shrinkage in each of the longitudinal and transverse directions were calculated:
Heat shrinkage (%) = [ ( length before heat treatment - length after heat treatment ) / length before heat treatment ] x 100
Figure imgf000011_0001
As shown in Table 1, the inventive films exhibit improved properties in terms of flexibility, transparency, pin-hole resistance, and mechanical properties, etc., whereas the films that fall out the scope of the present invention showed deteriorated properties.
While the invention has been described with respect to the above specific embodiments, it should be recognized that various modifications and changes may be made to the invention by those skilled in the art which also fall within the scope of the invention as defined by the appended claims.

Claims

WHAT IS CLAIMED IS;
1. A biodegradable flexible film comprising 20 to 90 wt% of polylactic acid and 1 to 80 wt% of a polyhydroxyalkanoate (PHA), which exhibits a biodegradability of at least 90 %, an initial elastic modulus determined based on a stress-strain curve of 50 to 350 lcgf/mm2, and a haze of 20 % or less.
2. The film of claim I, wherein the PHA is a heteropolymer or copolymer which comprises one or more repeating units of formulas (I) and (II):
Figure imgf000013_0001
wherein, Rl is methyl or ethyl, and R2 is ethyl, propyl, pentyl, or heptyl.
3. The film of claim 2, wherein the PHA further comprises a glycolide repeating unit of formula III in an amount of 0 to 50 wt% based on the weight of the PHA:
Figure imgf000013_0002
4. The film of claim 1, wherein the PHA is selected from the group consisting of polyhydroxybutyrate (PHB), polyhydroxybutyrate valerate (PHBV), poly(3-hydroxybutyrate-co-3 -hydroxy valerate) (P(3HB-co-3HV)), poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (P(3HB-co-3HH)), poly(3-hydroxybutyrate-co-S -hydroxyoctanoate) (P(3HB-CO-3HO)), poly-3-hydroxyvalerate (PHV), and a mixture thereof.
5. The film of claim I, wherein the heat shrinkability of the film measured at 100oC for 5 min is 70 % or less in either the longitudinal or transverse direction.
6. A wrapping material comprising the biodegradable flexible film according to any one of claims 1 to 5.
7. A method for preparing the biodegradable flexible film of claim 1 comprising the steps of:
(a) melt-extruding a polymer blend composed of 20 to 99 wt% of polylactic acid and 1 to 80 wt% of a PHA, to prepare a sheet;
(b) drawing the sheet in the longitudinal and transverse directions to prepare a biaxially oriented film; and
(c) heat-setting the biaxially oriented film.
8. The method of claim 7, wherein the melt-extruding is performed at 180 to 25O oC.
9. The method of claim 7, wherein the longitudinal drawing and the transverse drawing are performed at draw ratios of 2 to 4 and 3 to 5, respectively.
10. The method of claim 1, wherein the longitudinal drawing and the transverse drawing are conducted at temperature ranges of 40 to 90 oC and 50 to 90 oC, respectively.
11. The method of claim 7, the heat-setting is carried at 50 to 150 oC.
PCT/KR2009/003621 2008-07-03 2009-07-02 Biodegradable flexible film Ceased WO2010002205A2 (en)

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