WO2020076749A1 - Crystallizable shrinkable films and thermoformable sheets made from resin blends - Google Patents

Crystallizable shrinkable films and thermoformable sheets made from resin blends Download PDF

Info

Publication number
WO2020076749A1
WO2020076749A1 PCT/US2019/055092 US2019055092W WO2020076749A1 WO 2020076749 A1 WO2020076749 A1 WO 2020076749A1 US 2019055092 W US2019055092 W US 2019055092W WO 2020076749 A1 WO2020076749 A1 WO 2020076749A1
Authority
WO
WIPO (PCT)
Prior art keywords
mole
film
residues
crystallizable
polyester
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/US2019/055092
Other languages
English (en)
French (fr)
Inventor
Mark Allen PETERS
Jacob E. NAPIERALA
Rondell Paul Little, Jr.
James Carl Williams
James Wesley PEER
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Eastman Chemical Co
Original Assignee
Eastman Chemical Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to JP2021544108A priority Critical patent/JP7530370B2/ja
Priority to CN201980066310.4A priority patent/CN112789156A/zh
Priority to EP19794356.6A priority patent/EP3863832A1/en
Priority to CN202410235347.8A priority patent/CN117986819A/zh
Priority to US17/250,975 priority patent/US12116452B2/en
Priority to KR1020217013768A priority patent/KR102886788B1/ko
Application filed by Eastman Chemical Co filed Critical Eastman Chemical Co
Priority to MX2021003703A priority patent/MX2021003703A/es
Publication of WO2020076749A1 publication Critical patent/WO2020076749A1/en
Anticipated expiration legal-status Critical
Priority to JP2024121143A priority patent/JP2024153767A/ja
Priority to US18/884,597 priority patent/US20250011534A1/en
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D65/00—Wrappers or flexible covers; Packaging materials of special type or form
    • B65D65/38—Packaging materials of special type or form
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29D—PRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D7/00—Producing flat articles, e.g. films or sheets
    • B29D7/01—Films or sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001—Combinations of extrusion moulding with other shaping operations
    • B29C48/0018—Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001—Combinations of extrusion moulding with other shaping operations
    • B29C48/0022—Combinations of extrusion moulding with other shaping operations combined with cutting
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07—Flat, e.g. panels
    • B29C48/08—Flat, e.g. panels flexible, e.g. films
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C51/00—Shaping by thermoforming, i.e. shaping sheets or sheet like preforms after heating, e.g. shaping sheets in matched moulds or by deep-drawing; Apparatus therefor
    • B29C51/002—Shaping by thermoforming, i.e. shaping sheets or sheet like preforms after heating, e.g. shaping sheets in matched moulds or by deep-drawing; Apparatus therefor characterised by the choice of material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/04—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16—Dicarboxylic acids and dihydroxy compounds
    • C08G63/18—Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
    • C08G63/181—Acids containing aromatic rings
    • C08G63/183—Terephthalic acids
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16—Dicarboxylic acids and dihydroxy compounds
    • C08G63/18—Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
    • C08G63/199—Acids or hydroxy compounds containing cycloaliphatic rings
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/66—Polyesters containing oxygen in the form of ether groups
    • C08G63/668—Polyesters containing oxygen in the form of ether groups derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/672—Dicarboxylic acids and dihydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18—Manufacture of films or sheets
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • C08L67/025—Polyesters derived from dicarboxylic acids and dihydroxy compounds containing polyether sequences
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/005—Shaping by stretching, e.g. drawing through a die; Apparatus therefor characterised by the choice of materials
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2067/00—Use of polyesters or derivatives thereof, as moulding material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2067/00—Use of polyesters or derivatives thereof, as moulding material
    • B29K2067/003—PET, i.e. poylethylene terephthalate
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037—Other properties
    • B29K2995/0049—Heat shrinkable
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037—Other properties
    • B29K2995/005—Oriented
    • B29K2995/0051—Oriented mono-axially
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037—Other properties
    • B29K2995/0094—Geometrical properties
    • B29K2995/0097—Thickness
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2007/00—Flat articles, e.g. films or sheets
    • B29L2007/008—Wide strips, e.g. films, webs
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2467/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2467/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend

Definitions

  • the present disclosure relates to crystallizable shrinkable films and thermoformable sheets comprising blends of polyester compositions which comprise residues of terephthalic acid, neopentyl glycol (NPG), 1 ,4- cyclohexanedimethanol (CHDM), ethylene glycol (EG), and diethylene glycol (DEG), in certain compositional ranges having certain advantages and improved properties.
  • polyester compositions which comprise residues of terephthalic acid, neopentyl glycol (NPG), 1 ,4- cyclohexanedimethanol (CHDM), ethylene glycol (EG), and diethylene glycol (DEG), in certain compositional ranges having certain advantages and improved properties.
  • shrink films that have at least one of the following desirable shrink film properties: (1 ) low onset shrinkage temperature, (2) a shrinkage percentage which increases gradually and in a controlled manner with increasing temperature over the temperature range where shrinkage occurs, (3) a shrink force low enough to prevent crushing of the underlying container, (4) a high ultimate shrinkage (shrinkage at the highest temperature), e.g. 50% or greater shrinkage in the main shrinkage direction at 95 °C, (5) low shrinkage in the direction orthogonal to the high shrinkage direction, (6) improved film toughness so as to prevent unnecessary fracturing, breaking, tearing, splitting, bubbling, or wrinkling of the film during manufacture and prior to and after shrinkage, and (7) recyclability.
  • (1 ) low onset shrinkage temperature (2) a shrinkage percentage which increases gradually and in a controlled manner with increasing temperature over the temperature range where shrinkage occurs, (3) a shrink force low enough to prevent crushing of the underlying container, (4) a high ultimate shrinkage (shrinkage at the highest temperature), e.g
  • thermoformable sheet with good properties and recyclability.
  • blends made with polyesters that contain certain combinations of glycol monomers in a shrink film resin composition can produce a film with good shrink film performance and also be crystallizable such that it does not impact the recycling of the accompanying PET flake during recycling.
  • These crystallizable shrink film resin blends can be processed with the PET bottle and end up as a component in the recyclable PET flake leaving the recycling process.
  • the choice and quantity of specific combinations of polyesters in the blends that contain certain glycol monomers are important to produce films with good shrink film properties and to produce a film that is crystallizable.
  • the optimized polyester resin blend compositions of this disclosure are amorphous but crystallizable. As such, they exhibit good properties in film application including as shrink films, but they have high strain induced crystalline melting points, so they provide superior performance in recycling processes.
  • the shrink film labels of the present disclosure do not have to be removed during the recycle process, and they do not impact the process.
  • Thermoshrinkable films must meet a variety of fitness for use criteria to perform in this application.
  • the films must be tough, must shrink in a controlled manner, and must provide enough shrink force to hold itself on the bottle without crushing the contents.
  • polyester shrink film labels must not interfere with the recycling process of the bottle. It would be advantageous if the label could be recyclable so the entire bottle, including the label, can be recycled and converted into new products without creating additional handling requirements or creating new environmental issues.
  • Thermoshrinkable films have been made from a variety of raw materials to meet a range of material demands. This disclosure describes unique and unexpected effects measured with blends of polyesters that are made with certain monomer combinations for shrink film resin compositions.
  • Polyester shrink film compositions have been used commercially as shrink film labels for food, beverage, personal care, household goods, etc. Often, these shrink films are used in combination with clear polyethylene terephthalate (PET) bottles or containers. The total package (bottle plus label) is then placed in the recycling process. In a typical recycling center, the PET and the shrink film material can end up together at the end of the process due to similarities in composition and density. Drying of the PET flake is required to remove residual water that remains with the PET through the recycling process. Typically, PET is dried at temperatures above 200 °C. At those temperatures, typical polyester shrink film resins will soften and become sticky, often creating clumps with PET flakes. These clumps must be removed before further processing. These clumps reduce the yield of PET flake from the process and create an additional handling step.
  • PET polyethylene terephthalate
  • glycol monomers in a film or sheet resin composition can produce film or sheet with good performance properties and is also crystallizable such that it does not impact the recycling of the PET flake.
  • These crystallizable film or sheet resins can be processed with recycled PET and end up as a component in the recyclable PET flake leaving the recycling process.
  • the choice and quantity of specific combinations of glycol monomers are important to produce films or sheet with good performance properties and to produce a film or sheet that is crystallizable; in other words, the polyester compositions are amorphous but are "crystallizable" in the sense that they have high strain induced crystalline melting points.
  • the crystallizable polyesters of the invention do not form clumps, which deter the normal mechanical operation of flaking, drying, and feeding of the flake into an extruder for further processing into (recycled)polyester pellets.
  • the sheet of the present disclosure does not have to be removed during the recycle process because it does not adversely impact the recycle process. (See, for example, https://www.thebalancesmb.com/recycling-polyethylene-terephthalate-pet- 2877869.)
  • One embodiment of the present disclosure is a crystallizable film comprising a blend of polyester compositions comprising: (1 ) at least one crystallizable polyester which comprises: residues of terephthalic acid, neopentyl glycol (NPG), 1 ,4-cyclohexanedimethanol (CHDM), ethylene glycol (EG), and diethylene glycol (DEG), in certain compositional ranges and (2) at least one amorphous polyester which comprises: residues of terephthalic acid, neopentyl glycol (NPG), 1 ,4-cyclohexanedimethanol (CHDM), ethylene glycol (EG), and diethylene glycol (DEG), in certain compositional ranges.
  • the crystallizable polyester blend composition comprises: (a) from 5 to 95 weight % of the crystallizable polyester compositions and (b) from 5 to 95 weight % of at least one amorphous polyester compositions.
  • One embodiment of the present disclosure is crystallizable composition comprising a blend of polyester compositions comprising:
  • (b) is a diol component comprising:
  • One embodiment of the present disclosure is a crystallizable composition comprising a blend of polyester compositions comprising:
  • a diol component comprising: about 70 mole% or greater of ethylene glycol residues and about 30 mole% or less of other glycols comprising one or more of:
  • One embodiment of the present disclosure is a crystallizable composition comprising a blend of polyester compositions comprising:
  • One embodiment of the present disclosure is a crystallizable composition comprising a blend of polyester compositions comprising:
  • a diol component comprising: (i) about 0 to about 30 mole% of neopentyl glycol residues;
  • the blend compositions have a crystalline melting point in the range of about 200 to about 255 ° C.
  • the above blends have a crystalline melting point in a range of about 220 ° to about 230 °C or in the range of about 245 ° to about 255 ° C.
  • component (1 ) has a crystalline melting point of about 220 ° to about 230 ° C.
  • One embodiment of the present disclosure is a crystallizable film of the preceding embodiments, wherein the film is stretched in at least one direction and the stretched film has a strain induced crystalline melting point of 200°C or greater.
  • thermoformed or thermoformable film or sheet comprising a blend of polyester compositions comprising: (1 ) at least one crystallizable polyester which comprises: residues of terephthalic acid, neopentyl glycol (NPG), 1 ,4-cyclohexanedimethanol (CHDM), ethylene glycol (EG), and diethylene glycol (DEG), in certain compositional ranges and (2) at least one amorphous polyester which comprises: residues of terephthalic acid, neopentyl glycol (NPG), 1 ,4- cyclohexanedimethanol (CHDM), ethylene glycol (EG), 2,2,4,4-tetramethyl-1 ,3- cyclobutanediol (TMCD), and diethylene glycol (DEG), in certain compositional ranges.
  • thermoformed or thermoformable film or sheet comprising crystallizable polyester blend compositions.
  • the thermoformed or thermoformable film or sheet comprises crystallizable polyester blend composition comprising: (a) from 5 to 95 weight % of the crystallizable polyester compositions and (b) from 5 to 95 weight % of at least one amorphous polyester compositions.
  • thermoformed sheet having a thickness of from about 0.25mm to about 6.4 mm, comprising a crystallizable composition comprising a blend of polyester compositions comprising:
  • a dicarboxylic acid component comprising: (i) about 70 to about 100 mole% of terephthalic acid residues;
  • (b) is a diol component comprising:
  • (b') is a diol component comprising:
  • thermoformed sheet having a thickness of from about 0.25mm to about 6.4 mm, comprising a crystallizable composition comprising a blend of polyester compositions comprising:
  • a diol component comprising: about 80 mole% or greater of ethylene glycol residues and about 20 mole% or less of other glycols comprising one or more of:
  • composition whether or not formed in situ
  • thermoformed sheet having a thickness of from about 0.25mm to about 6.4 mm, comprising a crystallizable composition comprising a blend of polyester compositions comprising:
  • thermoformed sheet having a thickness of from about 0.25mm to about 6.4 mm, comprising a crystallizable composition comprising a blend of polyester compositions comprising:
  • a dicarboxylic acid component comprising: (i) about 70 to about 100 mole% of terephthalic acid residues;
  • One embodiment of the present disclosure is an extruded or calendared film comprising the blends of crystallizable compositions of any of the preceding embodiments.
  • One embodiment of the present disclosure is a molded, thermoformed, or shaped article comprising or prepared from the sheet of any of the preceding embodiments.
  • One embodiment of the present disclosure is a medical device packaging, medical packaging, healthcare supplies packaging, commercial foodservice products, trays, containers, food pans, tumblers, storage boxes, bottles, food processors, blender and mixer bowls, utensils, water bottles, crisper trays, washing machine parts, refrigerator parts, vacuum cleaner parts, ophthalmic lenses and frames or toys comprising or prepared from the thermoformed or thermoformable sheet of any of the preceding embodiments.
  • One embodiment of the present disclosure is an article of manufacture comprising or prepared from the thermoformed or thermoformable sheet of any of the preceding claims.
  • thermoformed film or sheet of any of the preceding embodiments comprising: A. heating the polyester film or sheet; B. applying air pressure, vacuum and/or physical pressure to the heat softened film or sheet; C. conforming the sheet by vacuum or pressure to a mold shape; D. Cooling the thermoformed part and E. removing the thermoformed part or article from the mold.
  • APR Association for Plastic Recyclers
  • PET-CG-02 The Association for Plastic Recyclers
  • labels minimum 3% by weight
  • bottles are ground to a 1 ⁇ 4” to 1 ⁇ 2” flake size.
  • the bottle flake is then blended 50:50 with unlabeled control bottle flake.
  • the sample is then elutriated on a setting that allows no more than 1 .2% of the PET to be carried over with label.
  • the flake is washed with 0.3% Triton X-100 and 1 .0% caustic for 15 minutes at 88 °C.
  • the flake is then washed with water after removing all floating material and then strained to remove excess water.
  • the flake is elutriated again just as before. Then 2lbs of washed flake is placed in a Teflon-lined baking dish for each washed sampled and the flake is added to a layer thickness of 1 .5 inches. The pan containing the flake is place in a circulating oven at 208 °C for 1 -1 /2 hours. The flake is cooled and then passed through a sieve with 0.0625 inch openings. As the material is passed through the sieve, no material should clump and therefore become too large to pass through the sieve. This testing is followed by extrusion/pelletization and molding steps to ensure quality of the flake.
  • the crystallizable blend compositions of the present disclosure thus present an advantageous component of a PET recycle stream insofar as such compositions can accompany PET in recycle streams without additional separation steps. Accordingly, in one embodiment of the present disclosure there is provided a polyester recycle stream, comprising recycled polyethylene terephthalate) flake, having admixed therewith at least about 0.1 weight percent of the crystallizable blends of the present disclosure. In another embodiment, said stream passes the "Critical Guidance Protocol for Clear PET Articles with Labels and Closures", dated April 1 1 , 2019, Document No. PET-CG-02.
  • Figure 1 is a plot of crystallinity versus % PET clumping for blends made with resin #1 and resin #2.
  • Figure 2 is a plot of crystallinity versus % PET clumping for blends made with resin #2 and resin #3.
  • Heat-shrinkable plastic films are used as coverings, to hold objects together, and as an outer wrapping for bottles, cans and other kinds of containers.
  • such films are used for covering the cap, neck, shoulder or bulge of bottles or the entire bottle; for the purpose of labeling, protection, parceling, or increasing the value of the product; and for other reasons.
  • such films may be used as a covering to package such objects as boxes, bottles, boards, rods, or notebooks together in groups, and such films may also be attached closely as a wrapping.
  • the uses mentioned above take advantage of the shrinkability and the internal shrink stress of the film.
  • Polyester films Historically, Poly(vinyl chloride) (PVC) films dominated the shrink film market. However, polyester films have become a significant alternative because polyester films do not possess the environmental problems associated with PVC films. Polyester shrink films ideally would have properties very similar to PVC films so that the polyester can serve as a“drop-in” film replacement on that can be processed in existing shrink tunnel equipment.
  • PVC film properties that are desired for duplication include the following: (1 ) a relatively low shrinkage onset temperature, (2) a total shrinkage which increases gradually and in a controlled manner with increasing temperature, (3) a low shrink force to prevent crushing of the underlying container, (4) a high total shrinkage (for example, 50% or greater) and (5) an inherent film toughness so as to prevent unnecessary tearing and splitting of the film prior to and after shrinkage.
  • Thermoshrinkable films must meet a variety of fitness for use criteria in order to perform in this application.
  • the films must be tough, must shrink in a controlled manner, and must provide enough shrink force to hold itself on the bottle without crushing the contents.
  • these labels when applied to polyester containers, they must not interfere with the recycling process for the PET bottle. In fact, it would be advantageous, if the label was also recyclable so the entire bottle can be recycled and converted into new products without creating additional handling requirements or create new environmental issues.
  • Thermoshrinkable films have been made from a variety of raw materials to meet a range of material demands. This disclosure describes unique and unexpected effects measured with blends of polyesters that contain certain monomer combinations that improves the recyclability of the polyester shrink film label.
  • Shrink film compositions are used commercially as shrink film labels for food, beverage, personal care, household goods, etc. Often, these shrink films are used in combination with clear polyethylene terephthalate (PET) bottles or containers. The total package (bottle plus label) is then placed in the recycling process. In a typical recycling center, the PET and the shrink film material can end up together at the end of the process due to similarities in composition and density. Drying of the PET flake is required to remove residual water that remains with the PET through the recycling process. Typically, PET is dried at temperatures above 200 °C. At those temperatures, typical polyester shrink film resins will soften and become sticky, often creating clumps with PET flakes. These clumps must be removed before further processing.
  • PET polyethylene terephthalate
  • polyesters that contain certain combinations of glycol monomers in shrink film polyester resin blend compositions can produce films with good shrink film performance and also be crystallizable such that it does not impact the recycling of the PET flake during recycling. These crystallizable shrink film resin blends can be processed with the PET bottle and end up as a component in the recyclable PET flake leaving the recycling process. It has also been found that the choice and quantity of specific combinations of glycol monomers in each composition (the amorphous composition and the crystallizable composition) of the crystallizable polyester blend composition are important to produce films with good shrink film properties and to produce a film that is crystallizable.
  • polystyrene resin is intended to include “copolyesters” and is understood to mean a synthetic polymer prepared by the reaction of one or more difunctional carboxylic acids and/or multifunctional carboxylic acids with one or more difunctional hydroxyl compounds and/or multifunctional hydroxyl compounds, for example, branching agents.
  • the difunctional carboxylic acid can be a dicarboxylic acid and the difunctional hydroxyl compound can be a dihydric alcohol, for example, glycols and diols.
  • glycocol as used herein includes, but is not limited to, diols, glycols, and/or multifunctional hydroxyl compounds, for example, branching agents.
  • the difunctional carboxylic acid may be a hydroxy carboxylic acid, for example, p-hydroxybenzoic acid, and the difunctional hydroxyl compound may have an aromatic nucleus bearing 2 hydroxyl substituents, for example, hydroquinone.
  • reduce means any organic structure incorporated into a polymer through a polycondensation and/or an esterification reaction from the corresponding monomer.
  • relpeating unit means an organic structure having a dicarboxylic acid residue and a diol residue bonded through an ester group.
  • the dicarboxylic acid residues may be derived from a dicarboxylic acid monomer or its associated acid halides, esters, salts, anhydrides, and/or mixtures thereof.
  • the term “diacid” includes multifunctional acids, for example, branching agents.
  • the term“dicarboxylic acid” is intended to include dicarboxylic acids and any derivative of a dicarboxylic acid, including its associated acid halides, esters, half-esters, salts, half-salts, anhydrides, mixed anhydrides, and/or mixtures thereof, useful in a reaction process with a diol to make a polyester.
  • terephthalic acid is intended to include terephthalic acid itself and residues thereof as well as any derivative of terephthalic acid, including its associated acid halides, esters, half-esters, salts, half-salts, anhydrides, mixed anhydrides, and/or mixtures thereof or residues thereof useful in a reaction process with a diol to make a polyester.
  • the polyesters used in the present disclosure typically can be prepared from dicarboxylic acids and diols which react in substantially equal proportions and are incorporated into the polyester polymer as their corresponding residues.
  • the polyesters of the present disclosure therefore, can contain substantially equal molar proportions of acid residues (100 mole%) and diol (and/or multifunctional hydroxyl compound) residues (100 mole%) such that the total moles of repeating units is equal to 100 mole%.
  • the mole percentages provided in the present disclosure therefore, may be based on the total moles of acid residues, the total moles of diol residues, or the total moles of repeating units.
  • a polyester containing 10 mole% isophthalic acid means the polyester contains 10 mole% isophthalic acid residues out of a total of 100 mole% acid residues. Thus, there are 10 moles of isophthalic acid residues among every 100 moles of acid residues.
  • a polyester containing 25 mole% 1 ,4- cyclohexanedimethanol means the polyester contains 25 mole% 1 ,4-cyclohexanedimethanol residues out of a total of 100 mole% diol residues. Thus, there are 25 moles of 1 ,4-cyclohexanedimethanol residues among every 100 moles of diol residues.
  • terephthalic acid or an ester thereof for example, dimethyl terephthalate or a mixture of terephthalic acid residues and an ester thereof can make up a portion or all of the dicarboxylic acid component used to form the polyesters useful in the present disclosure.
  • terephthalic acid residues can make up a portion or all of the dicarboxylic acid component used to form the polyesters useful in this disclosure.
  • the terms“terephthalic acid” and “dimethyl terephthalate” are used interchangeably herein.
  • dimethyl terephthalate is part or all of the dicarboxylic acid component used to make the polyesters useful in the present disclosure.
  • ranges of from 70 to 100 mole%; or 80 to 100 mole%; or 90 to 100 mole%; or 99 to 100 mole%; or 100 mole% terephthalic acid and/or dimethyl terephthalate and/or mixtures thereof may be used.
  • the dicarboxylic acid component of the polyesters useful in the present disclosure can comprise up to 30 mole%, up to 20 mole%, up to 10 mole%, up to 5 mole%, or up to 1 mole% of one or more modifying aromatic dicarboxylic acids.
  • Yet another embodiment contains 0 mole% modifying aromatic dicarboxylic acids.
  • the amount of one or more modifying aromatic dicarboxylic acids can range from any of these preceding endpoint values including, for example, 0.01 to 10 mole%, from 0.01 to 5 mole% and from 0.01 to 1 mole%.
  • modifying aromatic dicarboxylic acids that may be used in the present disclosure include but are not limited to those having up to 20 carbon atoms, and which can be linear, para-oriented, or symmetrical.
  • Examples of modifying aromatic dicarboxylic acids which may be used in this disclosure include, but are not limited to, isophthalic acid, 4,4'- biphenyldicarboxylic acid, 1 ,4-, 1 ,5-, 2,6-, 2,7-naphthalenedicarboxylic acid, and trans-4,4'-stilbenedicarboxylic acid, and esters thereof.
  • the modifying aromatic dicarboxylic acid is isophthalic acid.
  • the carboxylic acid component of the polyesters useful in the present disclosure can be further modified with up to 10 mole%, such as up to 5 mole% or up to 1 mole% of one or more aliphatic dicarboxylic acids containing 2-16 carbon atoms, for example, cyclohexanedicarboxylic, malonic, succinic, glutaric, adipic, pimelic, suberic, azelaic and/or dodecanedioic dicarboxylic acids. Certain embodiments can also comprise 0.01 to 10 mole%, such as 0.1 to 10 mole%, 1 or 10 mole%, 5 to 10 mole% of one or more modifying aliphatic dicarboxylic acids.
  • Yet another embodiment contains 0 mole% modifying aliphatic dicarboxylic acids.
  • the total mole% of the dicarboxylic acid component is 100 mole%.
  • adipic acid and/or glutaric acid are provided in the modifying aliphatic dicarboxylic acid component of the polyesters and are useful in the present disclosure.
  • esters of terephthalic acid and the other modifying dicarboxylic acids or their corresponding esters and/or salts may be used instead of the dicarboxylic acids.
  • Suitable examples of dicarboxylic acid esters include, but are not limited to, the dimethyl, diethyl, dipropyl, diisopropyl, dibutyl, and diphenyl esters.
  • the esters are chosen from at least one of the following: methyl, ethyl, propyl, isopropyl, and phenyl esters.
  • the diol component of the polyester compositions and the polyester blend compositions useful in the present disclosure can comprise 1 ,4-cyclohexanedimethanol.
  • the diol component of the polyester compositions and the polyester blend compositions useful in the present disclosure comprise 1 ,4- cyclohexanedimethanol and 1 ,3-cyclohexanedimethanol.
  • the molar ratio of cis/trans 1 ,4-cyclohexandimethanol can vary within the range of 50/50 to 0/100, for example, between 40/60 to 20/80.
  • the diol component of the crystallizable polyester compositions and the crystallizable polyester blend compositions useful in the present disclosure can include, but is not limited to, compositions wherein the sum of the residues of 1 ,4-cyclohexanedimethanol and residues of neopentyl glycol in the final polyester composition is from 1 to 30 mole%, or from 1 to 25 mole%, 1 to 20 mole%, or from 1 to 15 mole%, or from 1 to 10 mole%, or from 2 to 30 mole%, or from 2 to 25 mole%, or from 2 to 20 mole%, or from 2 to 15 mole%, or from 2 to 10 mole%, or from 3 to 30 mole%, or from 3 to 25 mole%, or from 3 to 20 mole%, or from 3 to 15 mole%, or from 3 to 10 mole%, 4 to 30 mole%, or from 1 to 30 mole%, or from 1 to 25 mole%, 1 to 20 mole%, or from 1 to 15 mole%, or
  • 5 to 30 mole% or from 5 to 25 mole%, 5 to 20 mole%, or from 5 to 15 mole%, or from 5 to 10 mole%, 6 to 30 mole%, or from 6 to 25 mole%, 6 to 20 mole%, or from 6 to 15 mole%, or from 6 to 10 mole%, 7 to 30 mole%, or from 7 to 25 mole%, 7 to 20 mole%, or from 7 to 15 mole%, or from 7 to 10 mole%, 8 to 30 mole%, or from 8 to 25 mole%, 8 to 20 mole%, or from 8 to 15 mole%, or from
  • the sum of residues of 1 ,4-cyclohexanedimethanol and residues of neopentyl glycol in the final polyester composition can be from 4 to 15 mole%, or from 2 to 21 mole%, or from 2 to less than 20 mole%, or from 4 to 20 mole%, or from 5 to 18 mole%, or from 10 to 21 mole%, or from 12 to 21 mole%, wherein the total mole% of the diol component is 100 mole%.
  • the diol component of the crystallizable polyester compositions and crystallizable polyester blend compositions useful in this disclosure can contain 0 to 30 mole% of neopentyl glycol based on the total mole% of the diol component being 100 mole%. In one embodiment, the diol component of the polyester compositions and the polyester blend compositions useful in this disclosure can contain 0 to 25 mole% of neopentyl glycol based on the total mole% of the diol component being 100 mole%.
  • the diol component of the polyester compositions and polyester blend compositions useful in this disclosure can contain 0 to 17 mole% of neopentyl glycol based on the total mole% of the diol component being 100 mole%. In one embodiment, the diol component of the polyester compositions and polyester blend compositions useful in this disclosure can contain 5 to 20 mole% of neopentyl glycol based on the total mole% of the diol component being 100 mole%. In one embodiment, the diol component of the polyester compositions and polyester blend compositions useful in this disclosure can contain 10 to 20 mole% of neopentyl glycol based on the total mole% of the diol component being 100 mole%.
  • the diol component of the polyester compositions and polyester blend compositions useful in this disclosure can contain 10 to 15 mole% of neopentyl glycol based on the total mole% of the diol component being 100 mole%. In one embodiment, the diol component of the polyester compositions and polyester blend compositions useful in this disclosure can contain 15 to 25 mole% of neopentyl glycol based on the total mole% of the diol component being 100 mole%.
  • the diol component of the crystallizable polyester compositions and crystallizable polyester blend compositions useful in the present disclosure can contain from 0 to 30 mole%, or from 0.01 to 30 mole%, or from 0 to 20 mole%, or from 0.1 to 20 mole%, or from 2 to 20 mole%, or from 0.01 to 15 mole%, or from 0.01 to 14 mole%, or from 0.01 to 13 mole%, or from 0.01 to 12 mole%, or from 0.01 to 1 1 mole%, or 0.01 to 10 mole%, or from 0.01 to 9 mole%, or from 0.01 to 8 mole%, or from 0.01 to 7 mole%, or from 0.01 to 6 mole%, or from 0.01 to 5 mole%, 3 to 15 mole%, or from 3 to 14 mole%, or from 3 to 13 mole%, or from 3 to 12 mole%, or from 3 to 1 1 mole%, or 3 to 10 mole%, or from 3 to 9 mole%,
  • the diol component of the crystallizable polyester compositions and the crystallizable polyester compositions of the polyester blend compositions useful in the present disclosure can contain 0 to 15 mole% of 1 ,4-cyclohexanedimethanol based on the total mole% of the diol component being 100 mole%. In one embodiment, the diol component of the polyester compositions useful in this disclosure can contain 0.01 to less than 15 mole% of 1 ,4-cyclohexanedimethanol based on the total mole% of the diol component being 100 mole%.
  • the diol component of the polyester compositions useful in this disclosure can contain 0 to 10 mole% of 1 ,4- cyclohexanedimethanol based on the total mole% of the diol component being 100 mole%. In one embodiment, the diol component of the polyester compositions useful in this disclosure can contain 0.01 to less than 10 mole% of 1 ,4-cyclohexanedimethanol based on the total mole% of the diol component being 100 mole%. In one embodiment, the diol component of the polyester compositions useful in this disclosure can contain 0.01 to 5 mole% of 1 ,4- cyclohexanedimethanol based on the total mole% of the diol component being 100 mole%.
  • the diol component of the polyester compositions useful in this disclosure can contain 0 to less than 5 mole% of 1 ,4-cyclohexanedimethanol based on the total mole% of the diol component being 100 mole%.
  • diethylene glycol residues may be formed in situ during processing.
  • the total amount of diethylene glycol residues can be present in the crystallizable polyester blend compositions useful in the present disclosure, whether or not formed in situ during processing or intentionally added, or both, in any amount, for example, from 1 to 15 mole%, or from 2 to 12 mole%, or from 2 to 1 1 mole%, or 2 to 10 mole%, or from 2 to 9 mole%, or from 3 to 12 mole%, or from 3 to 1 1 mole%, or 3 to 10 mole%, or from 3 to 9 mole%, or from 4 to 12 mole%, or from 4 to 1 1 mole%, or 4 to 10 mole%, or from 4 to 9 mole%, or, from 5 to 12 mole%, or from 5 to 1 1 mole%, or 5 to 10 mole%, or from 5 to 9 mole%, of diethylene glycol residues, based on the total mole% of the diol component being 100 mole%.
  • the total amount of diethylene glycol residues can be present in the polyester useful in the present disclosure, whether or not formed in situ during processing or intentionally added or both, can be from 5 mole% or less, or 4 mole% or less, or from 3.5 mole% or less, or from 3.0 mole% or less, or from 2.5 mole% or less, or from 2.0 mole% or less, or from 1.5 mole% or less, or from 1.0 mole% or less, or from 1 to 4 mole%, or from 1 to 3 mole%, or from 1 to 2 mole% of diethylene glycol residues, or from 2 to 8 mole%, or from 2 to 7 mole%, or from 2 to 6 mole%, or from 2 to 5 mole%, or from 3 to 8 mole%, or from 3 to 7 mole%, or from 3 to 6 mole%, or from 3 to 5 mole%, or in some embodiments there is no intentionally added diethylene glycol residues, based on the total mole% of the diol
  • the diol component of the crystallizable polyester blend compositions useful in the present disclosure can contain up to 20 mole%, or up to 19 mole%, or up to 18 mole%, or up to 17 mole%, or up to 16 mole%, or up to 15 mole %, or up to 14 mole %, or up to 13 mole %, or up to 12 mole %, or up to 1 1 mole %, or up to 10 mole%, or up to 9 mole%, or up to 8 mole%, or up to 7 mole%, or up to 6 mole%, or up to 5 mole %, or up to 4 mole %, or up to 3 mole %, or up to 2 mole %, or up to 1 mole %, or less of one or more modifying diols (modifying diols are defined as diols which are not ethylene glycol, diethylene glycol, neopentyl glycol, or 1 ,4-
  • the polyesters useful in this disclosure can contain 10 mole% or less of one or more modifying diols. In certain embodiments, the polyesters useful in this disclosure can contain 5 mole% or less of one or more modifying diols. In certain embodiments, the polyesters useful in this disclosure can contain 3 mole% or less of one or more modifying diols. In another embodiment, the polyesters useful in this disclosure can contain 0 mole % modifying diols. It is contemplated, however, that some other diol residuals may form in situ so that residual amounts formed in situ are also an embodiment of this disclosure.
  • modifying diols for use in the crystallizable polyesters blend compositions contain 2 to 16 carbon atoms.
  • modifying diols include, but are not limited to, 1 ,2- propanediol, 1 ,3-propanediol, isosorbide, 1 ,4-butanediol, 1 ,5-pentanediol, 1 ,6- hexanediol, p-xylene glycol, polytetramethylene glycol, 2,2,4,4-tetramethyl-1 ,3- cyclobutanediol (TMCD) and mixtures thereof.
  • TMCD 2,2,4,4-tetramethyl-1 ,3- cyclobutanediol
  • isosorbide is a modifying diol.
  • the modifying diols include, but are not limited to, at least one of 1 ,3-propanediol and 1 ,4-butanediol. In one embodiment, 1 ,3-propanediol and/or 1 ,4-butanediol can be excluded. If 1 ,4- or 1 ,3-butanediol are used, greater than 4 mole% or greater than 5 mole % can be provided in one embodiment. In one embodiment, at least one modifying diol is 1 ,4-butanediol which present in the amount of 5 to 25 mole%.
  • the remainder of the diol component can comprise ethylene glycol residues in any amount based on the total mole% of the diol component being 100 mole%.
  • the crystallizable polyester blend compositions useful in the present disclosure can contain 50 mole% or greater, or 55 mole% or greater, or 60 mole% or greater, or 65 mole% or greater, or 70 mole% or greater, or 75 mole% or greater, or 80 mole% or greater, or 85 mole% or greater, or 90 mole% or greater, or 95 mole% or greater, or from 50 to 80 mole%, or from 55 to 80 mole%, or from 60 to 80 mole%, or from 50 to 75 mole%, or from 55 to 75 mole%, or from 60 to 75 mole%, or from 65 to 75 mole% of ethylene glycol residues, based on the total mole% of the diol component being 100 mole%.
  • a shrink film comprising a crystallizable polyester blend composition (i.e., components (1 ) and (2)) further comprising: 1 ,4-cyclohexanedimethanol residues are present in the amount of 0.01 to about 10 mole%, diethylene glycol residues are present in the amount of 2 to 9 mole%, neopentyl glycol residues in the amount of 5 to 30 mole%, and ethylene glycol residues are present in the amount of 60 mole % or greater, based on the total mole% of the diol component being 100 mole%.
  • a shrink film comprising a crystallizable polyester blend composition comprising: 1 ,4- cyclohexanedimethanol residues are present in the amount of 0.01 to about 5 mole%, diethylene glycol residues are present in the amount of 1 to 9 mole%, neopentyl glycol residues in the amount of 5 to 25 mole%, and ethylene glycol residues are present in the amount of 60 mole % or greater, based on the total mole% of the diol component being 100 mole%.
  • a shrink film comprising a crystallizable polyester blend composition comprising: 1 ,4- cyclohexanedimethanol residues are present in the amount of about 10 to about 20 mole%, diethylene glycol residues are present in the amount of 1 to 10 mole%, neopentyl glycol residues in the amount of up to about 1 mole%, and ethylene glycol residues are present in the amount of 60 mole % or greater, based on the total mole% of the diol component being 100 mole%.
  • a shrink film comprising a crystallizable polyester blend composition comprising: 1 ,4- cyclohexanedimethanol residues are present in the amount of 2 to 7 mole%, diethylene glycol residues are present in the amount of less than 10 mole%, neopentyl glycol residues in the amount of 5 to 20 mole%, and ethylene glycol residues are present in the amount of greater than 60 mole%, based on the total mole% of the diol component being 100 mole%.
  • a shrink film comprising a crystallizable polyester blend composition comprising: 1 ,4- cyclohexanedimethanol residues are present in the amount of less than 10 mole%, diethylene glycol residues are present in the amount of from 1 to 10 mole%, neopentyl glycol residues in the amount of greater than 5 mole%, and ethylene glycol residues are present in the amount of 60 mole% or greater, based on the total mole% of the diol component being 100 mole%.
  • a shrink film wherein the sum of one or more diol monomer components capable of forming an amorphous polyester composition in the polyester blend composition is from 20 to 45 mole%, or from 22 to 45 mole%, or from 20 to 40 mole%, or from 24 to 40 mole%, or from 30 to 45 mole%, or 25 to 45 mole%, or from 25 to 40 mole% or from 25 to 35 mole%, wherein the total mole % of the diol component content is 100 mole%.
  • a shrink film wherein the sum of the residues of 1 ,4-cyclohexanedimethanol and residues of neopentyl glycol in the amorphous polyester composition of the polyester blend is from 12 to 35 mole%, or from 15 to 40 mole%, or from 15 to 35 mole%, or from 20 to 40 mole%, or from 25 to 40 mole%, or from 20 to 45 mole%, or from 25 to 35 mole%, wherein the total mole% of the diol component is 100 mole%.
  • a crystallizable film comprising a blend of polyester compositions comprising: (1 ) at least one crystallizable polyester which comprises: residues of terephthalic acid, from 0 to about 20 mole%, or from 0 to about 17 mole %, or from about 1 to about 20 mole% or from about 1 to about 17 mole% or from about 5 to about 20 mole% of neopentyl glycol (NPG) residues, and from 0 to about 20 mole%, or from 0 to about 17 mole %, or from about 1 to about 20 mole% or from about 1 to about 17 mole% or from about 5 to about 20 mole% of 1 ,4- cyclohexanedimethanol (CHDM), and from about less than 5 mole% of diethylene glycol (DEG) residues, with the remainder as ethylene glycol (EG) residues, and (2) at least one amorphous polyester which comprises: residues of terephthalic acid, and
  • the polyester compositions according to the present disclosure can comprise from 0 to 10 mole%, for example, from 0.01 to 5 mole%, from 0.01 to 1 mole%, from 0.05 to 5 mole%, from 0.05 to 1 mole%, or from 0.1 to 0.7 mole%, based the total mole percentages of either the diol or diacid residues; respectively, of one or more residues of a branching monomer, also referred to herein as a branching agent, having 3 or more carboxyl substituents, hydroxyl substituents, or a combination thereof.
  • the branching monomer or agent may be added prior to and/or during and/or after the polymerization of the polyester.
  • the polyester(s) useful in the present disclosure can thus be linear or branched.
  • branching monomers include, but are not limited to, multifunctional acids or multifunctional alcohols such as trimellitic acid, trimellitic anhydride, pyromellitic dianhydride, trimethylolpropane, glycerol, pentaerythritol, citric acid, tartaric acid, 3-hydroxyglutaric acid and the like.
  • the branching monomer residues can comprise 0.1 to 0.7 mole% of one or more residues chosen from at least one of the following: trimellitic anhydride, pyromellitic dianhydride, glycerol, sorbitol, 1 ,2,6- hexanetriol, pentaerythritol, trimethylolethane, and/or trimesic acid.
  • the branching monomer may be added to the polyester reaction mixture or blended with the polyester in the form of a concentrate as described, for example, in U.S. Pat. Nos. 5,654,347 and 5,696,176, whose disclosure regarding branching monomers is incorporated herein by reference.
  • the polyesters useful in the present disclosure can comprise at least one chain extender.
  • Suitable chain extenders include, but are not limited to, multifunctional (including, but not limited to, bifunctional) isocyanates, multifunctional epoxides, including, for example, epoxylated novolacs, and phenoxy resins.
  • chain extenders may be added at the end of the polymerization process or after the polymerization process. If added after the polymerization process, chain extenders can be incorporated by compounding or by addition during conversion processes such as injection molding or extrusion.
  • the amount of chain extender used can vary depending on the specific monomer composition used and the physical properties desired but is generally about 0.1 percent by weight to about 10 percent by weight, such as about 0.1 to about 5 percent by weight, based on the total weight of the polyester.
  • polyester blend compositions useful in the present disclosure can possess at least one of the inherent viscosity ranges described herein and at least one of the monomer ranges for the polyester compositions described herein, unless otherwise stated. It is also contemplated that polyester blend compositions useful in the present disclosure can possess at least one of the Tg ranges described herein and at least one of the monomer ranges for the polyester compositions described herein, unless otherwise stated. It is also contemplated that polyester compositions useful in the present disclosure can possess at least one of the inherent viscosity ranges described herein, at least one of the Tg ranges described herein, and at least one of the monomer ranges for the polyester compositions described herein, unless otherwise stated.
  • the polyester compositions useful in this disclosure can exhibit at least one of the following inherent viscosities as determined in 60/40 (wt/wt) phenol/ tetrachloroethane at a concentration of 0.5 g/dL at 25 Q C: 0.50 to 1 .2 dL/g; 0.50 to 1 .0 dL/g; 0.50 to 0.90 dL/g; 0.50 to 0.80 dL/g; 0.55 to 0.80 dL/g; 0.60 to 0.80 dL/g; 0.65 to 0.80 dL/g; 0.70 to 0.80 dL/g; 0.50 to 0.75 dL/g; 0.55 to 0.75 dL/g; or 0.60 to 0.75 dL/g.
  • the glass transition temperature (Tg) of the polyesters of the polyester blend compositions is determined using a TA DSC 2920 from Thermal Analyst Instrument at a scan rate of 20 Q C/min. The value of the glass transition temperature is determined during the second heat.
  • the oriented films or shrink films of this disclosure comprise polyesters/polyester compositions wherein the polyester has a Tg of 60 to 80 °C; 70 to 80 °C; or 65 to 80 °C; or 65 to 75 °C. In certain embodiments, these Tg ranges can be met with or without at least one plasticizer being added during polymerization.
  • certain oriented films and/or shrinkable films comprising the polyesters and/or polyester compositions useful in this disclosure can have a unique combination of all of the following properties: good stretchability, controlled shrinkage properties, certain toughness, certain inherent viscosities, certain glass transition temperatures (Tg), certain strain induced crystalline melting points, certain flexural modulus, certain densities, certain tensile modulus, certain surface tension, good melt viscosity, good clarity, and good color.
  • polyester blend compositions useful in this disclosure can be visually clear.
  • the term“visually clear” is defined herein as an appreciable absence of cloudiness, haziness, and/or muddiness, when inspected visually.
  • the polyester portions (the amorphous compositions and the crystallizable compositions) of the polyester blend compositions useful in this disclosure can be made by processes known from the literature, for example, by processes in homogenous solution, by transesterification processes in the melt, and by two phase interfacial processes. Suitable methods include, but are not limited to, the steps of reacting one or more dicarboxylic acids with one or more diols at a temperature of 100 °C. to 315 °0. at a pressure of 0.1 to 760 mm Hg for a time sufficient to form a polyester. See U.S. Pat. No. 3,772,405 for methods of producing polyesters, the disclosure regarding such methods is hereby incorporated herein by reference.
  • the polyester in general may be prepared by condensing the dicarboxylic acid or dicarboxylic acid ester with the diol in the presence of a catalyst at elevated temperatures increased gradually during the course of the condensation up to a temperature of about 225 °C to 310 °C., in an inert atmosphere, and conducting the condensation at low pressure during the latter part of the condensation, as described in further detail in U.S. Pat. No. 2,720,507 incorporated herein by reference herein.
  • certain agents which colorize the polymer can be added to the melt including toners or dyes.
  • a bluing toner is added to the melt in order to reduce the b * of the resulting polyester polymer melt phase product.
  • bluing agents include blue inorganic and organic toner(s) and/or dyes.
  • red toner(s) and/or dyes can also be used to adjust the a * color.
  • the organic toner(s) can be fed as a premix composition.
  • the premix composition may be a neat blend of the red and blue compounds or the composition may be pre-dissolved or slurried in one of the polyester's raw materials, e.g., ethylene glycol.
  • the total amount of toner components added can depend on the amount of inherent yellow color in the base polyester and the efficacy of the toner. In one embodiment, a concentration of up to about 15 ppm of combined organic toner components and a minimum concentration of about 0.5 ppm can be used. In one embodiment, the total amount of bluing additive can range from 0.5 to 10 ppm.
  • the toner(s) can be added to the esterification zone or to the polycondensation zone.
  • the toner(s) are added to the esterification zone or to the early stages of the polycondensation zone, such as to a prepolymerization reactor, or the toner can be added during a compounding or extrusion step after polymerization.
  • the present disclosure further relates to polymers compounded with the crystallizable polyester compositions as part of the polyester blend composition.
  • the compounded compositions comprise: (a) from 5 to 80 weight % of the crystallizable polyester compositions of the disclosure described herein; and (b) from 20 to 95 weight % of at least one polymeric component(/.e., a component which is other than the blends of this disclosure).
  • Suitable examples of the polymeric components include, but are not limited to, nylon; polyesters different than those described herein; polyamides such as ZYTEL® from DuPont; polystyrene; polystyrene copolymers; styrene acrylonitrile copolymers; acrylonitrile butadiene styrene copolymers; poly(methyl methacrylate); acrylic copolymers; poly(ether-imides) such as ULTEM® (a poly(ether-imide) from SABIC); polyphenylene oxides such as poly(2,6-dimethylphenylene oxide) or poly(phenylene oxide)/polystyrene blends such as NORYL 1000® (a blend of poly(2,6-dimethylphenylene oxide) and polystyrene resins from SABIC); polyphenylene sulfides; polyphenylene sulfide/sulfones; poly(ester-carbonates); polycarbonates
  • aliphatic-aromatic polyesters can be excluded from the polyester compositions useful in this disclosure.
  • the following polyesters, which can be blended to make the polyester compositions of this disclosure, can be excluded as the polymeric components used in additional blending if such blending exceeds the compositional ranges of the disclosure: polyethylene terephthalate (PET), glycol modified PET (PETG), glycol modified poly(cyclohexylene dimethylene terephthalate) (PCTG), poly(cyclohexylene dimethylene terephthalate) (POT), acid modified poly(cyclohexylene dimethylene terephthalate) (PCTA), poly(butylene terephthalate) and/or diethylene glycol modified PET (EASTOBONDTM copolyester).
  • PET polyethylene terephthalate
  • PET glycol modified PET
  • PCTG glycol modified poly(cyclohexylene dimethylene terephthalate)
  • POT poly(cyclohexylene dimethylene terephthalate)
  • PCTA acid
  • the blends can be prepared by conventional processing techniques known in the art, such as melt blending or solution blending.
  • the polyester compositions and the polymer blend compositions can also contain from 0.01 to 25% by weight of the overall composition common additives such as colorants, toner(s), dyes, mold release agents, flame retardants, plasticizers, glass bubbles, nucleating agents, stabilizers, including but not limited to, UV stabilizers, thermal stabilizers, and/or reaction products thereof, fillers, and impact modifiers.
  • colorants such as colorants, toner(s), dyes, mold release agents, flame retardants, plasticizers, glass bubbles, nucleating agents, stabilizers, including but not limited to, UV stabilizers, thermal stabilizers, and/or reaction products thereof, fillers, and impact modifiers.
  • Examples of commercially available impact modifiers include, but are not limited to, ethylene/propylene terpolymers, functionalized polyolefins such as those containing methyl acrylate and/or glycidyl methacrylate, styrene-based block copolymeric impact modifiers, and various acrylic core/shell type impact modifiers. Residues of such additives are also contemplated as part of the polyester composition.
  • the reinforcing materials may include, but are not limited to, carbon filaments, silicates, mica, clay, talc, titanium dioxide, Wollastonite, glass flakes, glass beads and fibers, and polymeric fibers and combinations thereof.
  • the reinforcing materials include glass, such as, fibrous glass filaments, mixtures of glass and talc, glass and mica, and glass and polymeric fibers.
  • the films and the shrink films according to the present disclosure may contain from 0.01 to 10 weight percent of the polyester plasticizer. In one embodiment, the shrink films can contain from 0.1 to 5 weight percent of the polyester plasticizer. Generally, the shrink films can contain from 90 to 99.99 weight percent of the copolyester. In certain embodiments, the shrink films can contain from 95 to 99.9 weight percent of the copolyester.
  • the present disclosure relates to shrink film(s) and molded article(s) of this disclosure comprising the polyester compositions and/or polymer blends useful in this disclosure.
  • the methods of forming the polyesters and/or blends into film(s) and/or sheet(s) are well known in the art.
  • film(s) and/or sheet(s) useful the present disclosure include but not are limited to extruded film(s) and/or sheet(s), compression molded film(s), calendered film(s) and/or sheet(s), solution casted film(s) and/or sheet(s).
  • methods of making film and/or sheet useful to produce the shrink films of the present disclosure include but are not limited to extrusion, compression molding, calendering, and solution casting.
  • the polyester composition useful in this disclosure are made into film using any method known in the art to produce films from polyesters, for example, solution casting, extrusion, compression molding, or calendering.
  • the as-formed film is then oriented in one or more directions (e.g., monoaxially and/or biaxially oriented film).
  • This orientation of the film can be performed by any method known in the art using standard orientation conditions.
  • the oriented films of the disclosure can be made from films having a thickness of about 100 to 400 microns, for example, extruded, cast or calendered films, which can be oriented at a ratio of 5:1 to 3:1 at a temperature of from Tg to Tg +55 °C , for example, at a ratio of 5:1 or of 3:1 at a temperature from 70 °C to 125 °C, and which can be oriented to a thickness of 20 to 80 microns.
  • the orientation of the initial as-formed film can be performed on a tenter frame according to these orientation conditions.
  • the shrink films of the present disclosure can have an onset of shrinkage temperature of from about 55 to about 80 °C, or about 55 to about 75 °C, or about 55 to about 70 °C.
  • Onset of shrinkage temperature is the temperature at which the beginning of shrinking occurs.
  • the polyester compositions useful in the present disclosure can have densities of 1 .6 g/cc or less, or 1 .5 g/cc or less, or 1 .4 g/cc or less, or 1 .1 g/cc to 1 .5 g/cc, or 1 .2 g/cc to 1 .4 g/cc, or 1 .2 g/cc to 1 .35 g/cc.
  • the density of the films is reduced by introducing many small voids or holes into the film or shaped article.
  • This process is called “voiding” and may also be referred to as“cavitating” or“microvoiding”.
  • Voids are obtained by incorporating about 1 to about 50 weight% of small organic or inorganic particles (including glass microspheres) or "inclusions” (referred in the art as“voiding” or“cavitation” agents) into a matrix polymer and orienting the polymer by stretching in at least one direction. During stretching, small cavities or voids are formed around the voiding agent.
  • the resulting voided film When voids are introduced into polymer films, the resulting voided film not only has a lower density than the non-voided film, but also becomes opaque and develops a paper-like surface. This surface also has the advantage of increased printability; that is, the surface is capable of accepting many inks with a substantially greater capacity over a non-voided film. Typical examples of voided films are described in U.S.
  • Patent No. s 3,426,754; 3,944,699; 4,138,459; 4,582,752; 4,632,869; 4,770,931 ; 5,176,954; 5,435,955; 5,843,578; 6,004,664; 6,287,680; 6,500,533; 6,720,085; U.S. Patent Application Publication No.’s 2001 /0036545; 2003/0068453; 2003/0165671 ;
  • the as-formed or extruded films are oriented while they are stretched.
  • the oriented films or shrinkable films of the present disclosure can be made from films having any thickness depending on the desired end-use.
  • the desirable conditions are, in one embodiment, where the oriented films and/or shrinkable films can be printed with ink for applications including labels, photo films which can be adhered to substrates such as paper, and/or other applications that it may be useful in. It may be desirable to coextrude the polyesters useful in the present disclosure with another polymer, such as PET, to make the films useful in making the oriented films and/or shrink films of this disclosure.
  • One advantage of doing the latter is that a tie layer may not be needed in some embodiments.
  • the monoaxially and biaxially oriented films of the present disclosure can be made from films having a thickness of about 100 to 400 microns, for example, extruded, cast or calendered films, which can be stretched at a ratio of 6.5:1 to 3:1 at a temperature of from the Tg of the film to the Tg + 55 deg C. in one or more directions, and which can be stretched to a thickness of 20 to 80 microns.
  • the orientation of the initial as extruded film can be performed on a tenter frame according to these orientation conditions.
  • the shrink films of the present disclosure can be made from the oriented films of this disclosure.
  • the shrink films of the present disclosure have gradual shrinkage with little to no wrinkling. In certain embodiments, the shrink films of the present disclosure have no more than 40% shrinkage in the main shrinkage direction per 5 °C temperature increase increment.
  • the shrink films of this disclosure have shrinkage in the machine direction (i.e. the direction orthogonal to the main shrinkage direction) of from 10% or less, or 5% or less, or 3% or less, or 2% or less, or no shrinkage when immersed in water at 65 °C for 10 seconds.
  • the shrink films of this disclosure have shrinkage in the machine direction of from -5% to 10%, -5% to 5%, or -5% to 3%, or -5% to 2%, or -4% to 5%, or -3% to 5% or - 2% to 5%, or -2% to 3%, or -2% to 2%, or 0 to 2%, or no shrinkage, when immersed in water at 65 °C for 10 seconds.
  • Negative machine direction shrinkage percentages here indicate machine direction growth.
  • Positive machine direction shrinkages indicate shrinkage in the machine direction.
  • the shrink films of this disclosure have shrinkage in the main shrinkage direction of from 50% or greater, or 60% or greater, or 70% or greater, when immersed in water at 95 °C for 10 seconds.
  • the shrink films of this disclosure have shrinkage in the main shrinkage direction in the amount of 50 to 90% and shrinkage in the machine direction of 10% or less, or from -10% to 10%, when immersed in water at 95 °C for 10 seconds.
  • the polyesters useful in the present disclosure are made into films using any method known in the art to produce films from polyesters, for example, solution casting, extrusion, compression molding, or calendering.
  • the as-extruded (or as-formed) film is then oriented in one or more directions (e.g., monoaxially and/or biaxially oriented film). This orientation of the films can be performed by any method known in the art using standard orientation conditions.
  • the monoaxially oriented films of the present disclosure can be made from films having a thickness of about 100 to 400 microns, such as, extruded, cast or calendered films, which can be stretched at a ratio of 6.5:1 to 3:1 at a temperature of from the Tg of the film to the Tg + 55 deg C., and which can be stretched to a thickness of 20 to 80 microns.
  • the orientation of the initial as extruded film can be performed on a tenter frame according to these orientation conditions.
  • the shrink films of this disclosure can have an onset of shrinkage temperature of from about 55 to about 80 °C, or about 55 to about 75 °C, or 55 to about 70 °C.
  • Onset of shrinkage temperature is the temperature at which onset of shrinking occurs.
  • the shrink films of this disclosure can have an onset of shrinkage temperature of between 55 °C and 70 °C.
  • the shrink films of this disclosure can have a break strain percentage greater than 200% at a stretching speed of 500 mm/minute in the direction orthogonal to the main shrinkage direction according to ASTM Method D882.
  • the shrink films of this disclosure can have a break strain percentage of greater than 300% at a stretching speed of 500 mm/minute in the direction orthogonal to the main shrinkage direction according to ASTM Method D882.
  • the shrink films of this disclosure can have a tensile stress at break (break stress) of from 20 to 400 MPa; or 40 to 260 MPa; or 42 to 260 MPa; 20 to 100 MPa as measured according to ASTM Method D882.
  • the shrink films of this disclosure can have a shrink force of from 4 to 18 MPa, or from 4 to 15 MPa, as measured by ISO Method 14616 depending on the stretching conditions and the end-use application desired.
  • certain labels made for plastic bottles can have an MPa of from 4 to 8 and certain labels made for glass bottles can have a shrink force of from 10 to 14 Mpa as measured by ISO Method 14616 using a Shrink Force Tester made by LabThink @ 80 °C.
  • the polyester compositions can be formed by reacting the monomers by known methods for making polyesters in what is typically referred to as reactor grade compositions.
  • the polyester compositions of this disclosure can be formed by blending polyesters, such as polyethylene terephthalate (PET), glycol modified PET (PETG), glycol modified poly(cyclohexylene dimethylene terephthalate) (PCTG), poly(cyclohexylene dimethylene terephthalate) (POT), acid modified poly(cyclohexylene dimethylene terephthalate) (PCTA), poly(butylene terephthalate) and/or diethylene glycol modified PET (EASTOBONDTM copolyester) to achieve the monomer ranges of these compositions.
  • PET polyethylene terephthalate
  • PET glycol modified PET
  • PCTG glycol modified poly(cyclohexylene dimethylene terephthalate)
  • POT poly(cyclohexylene dimethylene terephthalate)
  • PCTA acid modified poly(cyclohexylene dimethylene terephthalate)
  • PCTA acid modified poly(cyclohexylene dimethylene terephthalate)
  • PET di
  • the polyester compositions and the polymer blend compositions can also contain from 0.01 to 25% by weight of the overall composition common additives such as colorants, toner(s), dyes, mold release agents, flame retardants, plasticizers, glass bubbles, nucleating agents, stabilizers, including but not limited to, UV stabilizers, thermal stabilizers and/or reaction products thereof, fillers, and impact modifiers.
  • colorants such as colorants, toner(s), dyes, mold release agents, flame retardants, plasticizers, glass bubbles, nucleating agents, stabilizers, including but not limited to, UV stabilizers, thermal stabilizers and/or reaction products thereof, fillers, and impact modifiers.
  • Examples of commercially available impact modifiers include, but are not limited to, ethylene/propylene terpolymers, functionalized polyolefins such as those containing methyl acrylate and/or glycidyl methacrylate, styrene-based block copolymeric impact modifiers, and various acrylic core/shell type impact modifiers. Residues of such additives are also contemplated as part of the polyester composition.
  • the reinforcing materials can be added to the polyester compositions useful in this disclosure.
  • the reinforcing materials may include, but are not limited to, carbon filaments, silicates, mica, clay, talc, titanium dioxide, Wollastonite, glass flakes, glass beads and fibers, and polymeric fibers and combinations thereof.
  • the reinforcing materials include glass, such as, fibrous glass filaments, mixtures of glass and talc, glass and mica, and glass and polymeric fibers.
  • Molded articles can also be manufactured from any of the polyester compositions disclosed herein which may or may not consist of or contain shrink films and are included within the scope of the present disclosure.
  • the shrink films according to the present disclosure may contain from 0.01 to 10 weight percent of the polyester plasticizer. In one embodiment, the shrink films can contain from 0.1 to 5 weight percent of the polyester plasticizer. Generally, the shrink films can contain from 90 to 99.99 weight percent of the copolyester. In certain embodiments, the shrink films can contain from 95 to 99.9 weight percent of the copolyester.
  • the shrink films of the present disclosure can have one or more of the following properties: (1 ) shrinkage in the main shrinkage direction or transverse direction in the amount of greater than 50% (or greater than 60%), and 10% or less (or from -10% to 10%) shrinkage in the machine direction when immersed in water at 95 °C for 10 seconds; (2) an onset of shrinkage temperature of from about 55 °C to about 70 °C; (3) a break strain percentage of greater than 200% at stretching speeds of 500 mm/minute, or 200 to 600%, or 200 to 500%, or 226 to 449%, or 250 to 455% in the transverse direction or in the machine direction or in both directions according to ASTM Method D882; (4) no more than 40% shrinkage per each
  • the shrink films of the present disclosure can have a combination of two or more of the above described shrink film properties.
  • the shrink films of the present disclosure can have a combination of three or more of the above described shrink film properties.
  • the shrink films of the present disclosure can have a combination of four or more of the above described shrink film properties.
  • properties (1 ) - (2) are present.
  • properties (1 ) - (5) are present.
  • properties (1 ) - (3) are present, etc.
  • the shrinkage percentages herein are based on initial stretched films having a thickness of about 20 to 80 microns that have been oriented at a ratio of from 6.5:1 to 3:1 at a temperature of Tg to Tg + 55 °C on a tenter frame, for example, at a ratio of 5:1 at a temperature from 70 °C to 85 °C.
  • the shrinkage properties of the oriented films used to make the shrink films of this disclosure were not adjusted by annealing the films at a temperature higher than the temperature in which it was oriented.
  • the shrinkage properties can be adjusted by annealing.
  • the shape of the films useful in making the oriented films or shrink films of the present disclosure is not restricted in any way.
  • it may be a flat film or a film that has been formed into a tube.
  • the polyester is first formed into a flat film and then is“uniaxially stretched”, meaning the polyester film is oriented in one direction. The edges of the stretched film are then bonded using a seaming solvent or seaming adhesives to form a shrinkable tube.
  • the films could also be "biaxially oriented,” meaning the polyester films are oriented in two different directions; for example, the films are stretched in both the machine direction and a direction different from the machine direction. Typically, but not always, the two directions are substantially perpendicular.
  • the two directions are in the longitudinal or machine direction (“MD") of the film (the direction in which the film is produced on a film-making machine) and the transverse direction ("TD") of the film (the direction perpendicular to the MD of the film).
  • MD longitudinal or machine direction
  • TD transverse direction
  • Biaxially oriented films may be sequentially oriented, simultaneously oriented, or oriented by some combination of simultaneous and sequential stretching.
  • the films may be oriented by any usual method, such as the roll stretching method, the long-gap stretching method, the tenter-stretching method, and the tubular stretching method. With use of any of these methods, it is possible to conduct biaxial stretching in succession, simultaneous biaxial stretching, uni-axial stretching, or a combination of these. With the biaxial stretching mentioned above, stretching in the machine direction and transverse direction may be done at the same time. Also, the stretching may be done first in one direction and then in the other direction to result in effective biaxial stretching. In one embodiment, stretching of the films is done by preliminarily heating the films 5 Q C to 80 Q C above their glass transition temperature (Tg).
  • Tg glass transition temperature
  • the films can be preliminarily heated from 10 Q C to 30 Q C above their Tg.
  • the stretch rate is from 5 to 20 inches (12.7 to 50.8 cm) per second.
  • the films can be oriented, for example, in either the machine direction, the transverse direction, or both directions from 2 to 6 times the original measurements.
  • the films can be oriented as a single film layer or can be coextruded with another polymeric material or polyester such as PET (polyethylene terephthalate) as a multilayer film and then oriented.
  • the present disclosure includes an article of manufacture or a shaped article comprising the shrink films of any of the shrink film embodiments of this disclosure. In another embodiment, the present disclosure includes an article of manufacture or a shaped article comprising the oriented films of any of the oriented film embodiments of this disclosure.
  • the present disclosure includes but is not limited to shrink films applied to containers, plastic bottles, glass bottles, packaging, batteries, hot fill containers, and/or industrial articles or other applications.
  • the present disclosure includes but is not limited to oriented films applied to containers, packaging, plastic bottles, glass bottles, photo substrates such as paper, batteries, hot fill containers, and/or industrial articles or other applications.
  • the shrink films of this disclosure can be formed into a label or sleeve. The label or sleeve can then be applied to an article of manufacture, such as, the wall of a container, battery, or onto a sheet or film.
  • the oriented films or shrink films of the present disclosure can be applied to shaped articles, such as, sheets, films, tubes, bottles and are commonly used in various packaging applications.
  • films and sheets produced from polymers such as polyolefins, polystyrene, poly(vinyl chloride), polyesters, polylactic acid (PLA) and the like are used frequently for the manufacture of shrinkable labels for plastic beverage or food containers.
  • the shrinkable films of the present disclosure can be used in many packaging applications where the shaped article would exhibit properties, such as, good printability, high opacity, higher shrink force, good texture, and good stiffness after application of the shrink film.
  • the combination of the improved shrink properties as well as the improved toughness should offer new commercial options, including but not limited to, shrink films applied to containers, plastic bottles, glass bottles, packaging, batteries, hot fill containers, and/or industrial articles or other applications.
  • the disclosed polyester blend compositions are useful as thermoformed and/or thermoformable film(s) or sheet(s).
  • the present disclosure is also directed to articles of manufacture which incorporate the thermoformed film(s) and/or sheet(s) of this disclosure.
  • the polyester blend compositions of the present disclosure are useful as films and sheets which are easily formed into shaped or molded articles.
  • the film(s) and/or sheet(s) of the present disclosure may be processed into molded articles or parts by thermoforming.
  • the polyester compositions of the present disclosure may be used in a variety of molding and extrusion applications.
  • the polyester compositions and the polyester blend compositions useful in the thermoformed sheet(s) of this disclosure may also contain from 0.1 to 25% by weight of the overall composition common additives such as colorants, slip agents, anti-block agents, mold release agents, flame retardants, plasticizers, nucleating agents, stabilizers, including but not limited to, UV stabilizers, thermal stabilizers, fillers, and impact modifiers.
  • the overall composition common additives such as colorants, slip agents, anti-block agents, mold release agents, flame retardants, plasticizers, nucleating agents, stabilizers, including but not limited to, UV stabilizers, thermal stabilizers, fillers, and impact modifiers.
  • reinforcing materials may be included in the thermoformed film(s) or sheet(s) comprising the polyester compositions of this disclosure.
  • suitable the reinforcing materials may include carbon filaments, silicates, mica, clay, talc, titanium dioxide, Wollastonite, glass flakes, glass beads and fibers, and polymeric fibers and combinations thereof.
  • thermoformed films or sheets are multilayered films or sheets.
  • at least one layer of the multilayer film or sheet is a foam or foamed polymer or polyester layer.
  • One aspect of the present disclosure is a method of making molded or shaped parts and articles using thermoforming. Any thermoforming techniques or processes known to those skilled in the art may be used to produce the molded or shaped articles of this disclosure.
  • thermoforming processes can be done in several ways, for example as taught in "Technology of Thermoforming”; Throne, James; Hanser Publishers; 1996; pp. 16-29, which is incorporated herein by reference.
  • it is a positive thermoforming process where gas or air pressure is applied to the softened sheet, the sheet is then stretched and drawn out like a bubble and a male mold is brought into the bubble from the inside. Then vacuum is applied to further draw and conform the part to the male mold surface.
  • biaxial stretching/orientation is done primarily in one step when there is a gas or air pressure applied to the softened sheet.
  • the molding step is then completed with the vacuum and male mold to freeze the orientation into the sheet after cooling for a good balance of physical and appearance properties.
  • it is a negative thermoforming process where a vacuum or a physical plug is applied to the heat softened sheet and stretches and draws the sheet to nearly the final part size, and then, positive air pressure from the inside or further external vacuum from the outside draws and conforms the sheet against an outer, female mold, the orientation is frozen into the polymer after cooling and the sheet is formed into the article.
  • the produced bubble is sometimes further formed by making use of a plug assist, and this is followed by draping and shaping the sheet over the rising positive mold and then the corners and shelves guides, etc. are pulled into the mold by applying a vacuum.
  • the molded parts or articles can be trimmed, holes punched, and corners cut out as needed.
  • thermoforming is a process where a film or sheet of the polyester compositions of the present disclosure are heated to a temperature sufficient to allow the deformation thereof, and the heated film or sheet is then made to conform to the contours of a mold by such means as vacuum assist, air pressure assist and matched mold assist.
  • the heated film or sheet is placed in a mold and forced to conform to the contours of the mold by, for example, application of air pressure, application of a vacuum, plug assist or application of a matching mold.
  • thermoforming produces thin wall articles.
  • thermoforming molds the films or sheets into the desired shapes through the pressing of positive molds into the heated films or sheets.
  • thermoforming involves having a positive mold of an article supported between a vacuum-equipped surface or table.
  • heat from an external heat source such as a hot air blower, heat lamp or other radiant heat source is directed at the film or sheet.
  • the film or sheet is heated to the point of softening.
  • a vacuum is then applied to and below the table and around the mold, and the heat softened film or sheet is drawn toward the table, thus placing the softened film or sheet in contact with the mold surface.
  • the vacuum draws the softened film or sheet into tight contact with, and conformance to, the contours of the mold surface. As such, the film or sheet then assumes the shape of the mold. In this embodiment, after the film or sheet cools, it hardens, and the resulting article or part may be removed from the mold.
  • the thermoforming process comprises: forming a film or sheet from the polyester blend compositions of the present disclosure; heating the film or sheet until it softens and positioning it over a mold; drawing the preheated film or sheet onto the heated mold surface; cooling the film or sheet; and then removing the molded article or part from the mold cavity, or optionally, heatsetting the formed film or sheet by maintaining the film or sheet in contact against the heated mold for a sufficient time period to partially crystallize the film or sheet.
  • thermoforming process comprising: forming a film or sheet from the polyester blend compositions of the present disclosure; heating a film or sheet to a temperature at or above the Tg of the polyester; applying gas, vacuum and/or physical pressure to the heat softened film or sheet and stretching the film or sheet to nearly the final part size; conforming the sheet by vacuum or pressure to a mold shape; cooling the film or sheet to a temperature below the Tg of the polyester; and then removing the thermoformed article or part from the mold.
  • the film and sheet used in the thermoforming process can be made by any conventional method known to those skilled in the art.
  • the sheet or film is formed by extrusion.
  • the sheet or film is formed by calendering.
  • the film or sheet is heated to a temperature at or above the Tg of the polyester. In one embodiment, this temperature is about 10 to about 60° C above the Tg of the polyester. In one embodiment, the heating of the film or sheet prior to positioning over the thermoforming mold is necessary in order to achieve a shorter molding time. In one embodiment, the sheet must be heated above its Tg and below the point at which it sags excessively during positioning over the mold cavity.
  • thermoforming methods may include vacuum assist, air assist, mechanical plug assist or matched mold.
  • the mold is heated to a temperature at or above the Tg of the film or sheet. Selection of optimum mold temperature is dependent upon type of thermoforming equipment, configuration and wall thickness of article being molded and other factors.
  • the heated film or sheet is stretched by creating and pulling a vacuum.
  • heatsetting is the process of thermally inducing partial crystallization of a polyester film or sheet without appreciable orientation being present. In one embodiment, heatsetting is achieved by maintaining contact of the film or sheet with the heated mold surface for a sufficient time to achieve a level of crystallinity which gives adequate physical properties to the finished part. In one embodiment, the levels of crystallinity should be about 10 to about 30 percent.
  • the heatset part can be removed from the mold cavity by known means for removal.
  • blowback is used and it involves breaking the vacuum established between the mold and the formed film or sheet by the introduction of compressed air.
  • the molded article or part is subsequently trimmed and the scrap ground and recycled.
  • nucleating agents provide faster crystallization during thermoforming and thus provide for faster molding.
  • nucleating agents such as fine particle size inorganic or organic materials may be used.
  • suitable nucleating agents include talc, titanium dioxide, calcium carbonate, and immiscible or cross-linked polymers.
  • the nucleating agents are used in amounts varying from about 0.01 % to about 20%, based on the weight of the article.
  • other conventional additives such as pigments, dyes, plasticizers, anti-cracking agent and stabilizers may be used as needed for thermoforming.
  • the anti-cracking agent improves impact strength, and the nucleating agent provides faster crystallization.
  • crystallization is necessary to achieve high temperature stability.
  • a foamed polyester film or sheet is made by foaming a polyester composition of the present disclosure with chemical and/or physical blow agents, extruding the foamed polyester into sheet or film, and thermoforming the foamed polyester film or sheet.
  • Additives for providing enhanced properties to the foamed polyester film may be added to the polyester prior to foaming.
  • Some examples of additives include slip agents, antiblocking agents, plasticizers, optical brightener and ultra violet inhibitor.
  • the foamed polyester films can be extrusion or lamination coated on one side or on both sides using conventional techniques in order to enhance its properties.
  • the coating materials may be applied to the printed surface, rather than the foam film itself, that provides for product labelling.
  • the blend compositions of this disclosure are useful as molded or shaped plastic parts or as solid plastic objects.
  • the blend compositions of this disclosure are useful as thermoformed parts or articles.
  • the blend compositions are suitable for use in any applications where clear, hard plastics are required. Examples of such parts include disposable knives, forks, spoons, plates, cups, straws as well as eyeglass frames, toothbrush handles, toys, automotive trim, tool handles, camera parts, parts of electronic devices, razor parts, ink pen barrels, disposable syringes, bottles, and the like.
  • the blend compositions of the present disclosure are useful as plastics, films, fibers, and sheets.
  • compositions are useful as plastics to make bottles, bottle caps, eyeglass frames, cutlery, disposable cutlery, cutlery handles, shelving, shelving dividers, electronics housing, electronic equipment cases, computer monitors, printers, keyboards, pipes, automotive parts, automotive interior parts, automotive trim, signs, thermoformed letters, siding, toys, thermally conductive plastics, ophthalmic lenses, tools, tool handles, and utensils.
  • the blend compositions of the present disclosure are suitable for use as films, sheeting, fibers, molded articles, shaped articles, molded parts, shaped parts, medical devices, dental trays, dental appliances, containers, food containers, shipping containers, packaging, bottles, bottle caps, eyeglass frames, cutlery, disposable cutlery, cutlery handles, shelving, shelving dividers, furniture components, electronics housing, electronic equipment cases, computer monitors, printers, keyboards, pipes, toothbrush handles, automotive parts, automotive interior parts, automotive trim, signs, outdoor signs, skylights, multiwall film, multilayer film, insulated parts, insulated articles, insulated containers, thermoformed letters, siding, toys, toy parts, trays, food trays, dental trays, thermally conductive plastics, ophthalmic lenses and frames, tools, tool handles, and utensils, healthcare supplies, commercial foodservice products, boxes, film for graphic arts applications, plastic film for plastic glass laminates, point of purchase displays, skylights, smoke vents, laminated cards, fenestration, glazing, partition
  • thermoformed or thermoformable blend compositions are useful in forming films, molded articles, molded parts, shaped articles, shaped parts and sheeting.
  • the methods of making the thermoformed or thermoformable blend compositions into films, molded articles, molded parts, shaped articles, shaped parts and sheeting can be according to any methods known in the art.
  • molded articles include without limitation: medical device packaging, medical packaging, healthcare supply packaging, commercial foodservice products such as trays, containers, food pans, tumblers, storage boxes, bottles, food processors, blender and mixer bowls, utensils, water bottles, crisper trays, washing machine parts, refrigerator parts, vacuum cleaner parts, ophthalmic lenses and frames, and toys.
  • This disclosure further relates to articles of manufacture comprising the film(s) and/or sheet(s) containing polyester compositions described herein.
  • the films and/or sheets of the present disclosure can be of any thickness as required for the intended application.
  • This disclosure further relates to the film(s) and/or sheet(s) described herein.
  • the methods of forming the polyester blend compositions into film(s) and/or sheet(s) includes any methods known in the art.
  • Examples of film(s) and/or sheet(s) of the disclosure including but not limited to extruded film(s) and/or sheet(s), calendered film(s) and/or sheet(s), compression molded film(s) and/or sheet(s), solution casted film(s) and/or sheet(s).
  • Methods of making film and/or sheet include but are not limited to extrusion, calendering, compression molding, wet block processing, dry block processing and solution casting.
  • This disclosure further relates to the molded or shaped articles described herein.
  • the methods of forming the polyester compositions into molded or shaped articles includes any known methods in the art. Examples of molded or shaped articles of this disclosure including but not limited to thermoformed or thermoformable articles, injection molded articles, extrusion molded articles, injection blow molded articles, injection stretch blow molded articles and extrusion blow molded articles. Methods of making molded articles include but are not limited to thermoforming, injection molding, extrusion, injection blow molding, injection stretch blow molding, and extrusion blow molding.
  • the processes of this disclosure can include any thermoforming processes known in the art.
  • the processes of this disclosure can include any blow molding processes known in the art including, but not limited to, extrusion blow molding, extrusion stretch blow molding, injection blow molding, and injection stretch blow molding.
  • This disclosure includes any injection blow molding manufacturing process known in the art.
  • a typical description of injection blow molding (IBM) manufacturing process involves: 1 ) melting the composition in a reciprocating screw extruder; 2) injecting the molten composition into an injection mold to form a partially cooled tube closed at one end (i.e. a preform); 3) moving the preform into a blow mold having the desired finished shape around the preform and closing the blow mold around the preform; 4) blowing air into the preform, causing the preform to stretch and expand to fill the mold; 5) cooling the molded article; 6) ejecting the article from the mold.
  • IBM injection blow molding
  • This disclosure includes any injection stretch blow molding manufacturing process known in the art.
  • a typical description of injection stretch blow molding (ISBM) manufacturing process involves: 1 ) melting the composition in a reciprocating screw extruder; 2) injecting the molten composition into an injection mold to form a partially cooled tube closed at one end (i.e. a preform); 3) moving the preform into a blow mold having the desired finished shape around the preform and closing the blow mold around the preform; 4) stretching the preform using an interior stretch rod, and blowing air into the preform causing the preform to stretch and expand to fill the mold; 5) cooling the molded article; 6) ejecting the article from the mold.
  • ISBM injection stretch blow molding
  • extrusion blow molding manufacturing process includes: 1 ) melting the composition in an extruder; 2) extruding the molten composition through a die to form a tube of molten polymer (i.e. a parison); 3) clamping a mold having the desired finished shape around the parison; 4) blowing air into the parison, causing the extrudate to stretch and expand to fill the mold; 5) cooling the molded article; 6) ejecting the article of the mold; and 7) removing excess plastic (commonly referred to as flash) from the article.
  • a typical description of extrusion blow molding manufacturing process involves: 1 ) melting the composition in an extruder; 2) extruding the molten composition through a die to form a tube of molten polymer (i.e. a parison); 3) clamping a mold having the desired finished shape around the parison; 4) blowing air into the parison, causing the extrudate to stretch and expand to fill the mold; 5) cooling the
  • polyesters of the present disclosure can be made and evaluated, and they are intended to be purely exemplary and are not intended to limit the scope thereof. Unless indicated otherwise, parts are parts by weight, temperature is in degrees C (Celsius) or is at room temperature, and pressure is at or near atmospheric.
  • Copolyester resin samples were made using procedures described elsewhere. In all cases, resin samples are dried prior to extrusion.
  • Tenter frame film samples were made by extruding and stretching resins samples on a commercial tenter frame (located at Marshall and Williams, a division of Parkinson Technologies) where the film is extruded using a 3 layer, A-B-C die where the B-layer is extruded from a 2.5 inch single screw extruder and the A and C layers are extruded from separate, 1 .25 inch single screw satellite extruders.
  • the film is cast at a thickness of roughly 10mil (250microns) and then stretched with a 5:1 stretch ratio and to a thickness of 50 microns. In general, the cast thickness is 250microns and the final film thickness is 50 microns.
  • the line speed was 45fpm.
  • the glycol content of the extruded film compositions was determined via NMR. All NMR spectra were recorded on a JEOL Eclipse Plus 600 MHz nuclear magnetic resonance spectrometer using either chloroform- trifluoroacetic acid (70-30 volume/volume) for polymers with deuterated chloroform added for lock.
  • the acid component of the blended polymers used in the examples herein was 100 mole% terephthalic acid. The total mole percentages of the glycol component equaled 100 mole% and the total mole percentages of the acid component equaled 100 mole%.
  • polyesters herein The inherent viscosity of the polyesters herein was determined in 60/40 (wt/wt) phenol/tetrachloroethane at a concentration of 0.5 g/dL at 25 ° C., and is reported in dL/g.
  • Shrinkage is measured herein by placing a 50mm by 50mm square film sample in water at a temperature in 5 degree increments between and including 65 °C to 95 °C. The film is immersed in the water for 10 seconds without restricting shrinkage in any direction and the shrinkage (or growth) of the film sample is measured. The percent shrinkage is calculated by the following equation:
  • % shrinkage [(50mm-length after shrinkage)/50mm]x100%.
  • Shrinkage was measured in the direction orthogonal to the main shrinkage direction (machine direction, MD) and was also measured in the main shrinkage direction (transverse direction, TD).
  • Shrink force is measured for the examples herein with a LabThink FST-02 Thermal Shrinkage Tester in MPa at the same temperature used to stretch the film.
  • PET flake is combined 18g shrink flaked film (3% film with PET flake) in its shrunk state (film was previously shrunk by immersing in water at 85 °C for 10 seconds)
  • PET flake + film was placed in an aluminum pan to achieve a depth of 1 .5 inches.
  • the pan containing the flake is placed in a circulating oven at 208 °C for 1 -1 /2 hours.
  • Modulated Differential Scanning Calorimetry is a technique which measures the difference in heat flow between a sample and an inert reference as a function of time and temperature.
  • the same heat flux cell design is used as is used in traditional DSC.
  • a different heating profile temperature regime
  • oscillation is overlaid on the conventional linear heating or cooling ramp to yield a profile in which the average sample temperature continuously changes with time but not in a linear fashion.
  • Reversing heat flow was used to analyze the glass transition temperature and the area of the melt peak.
  • the heat of fusion (Hf) upon heating was measured as the integrated reversing Heat Flow signal.
  • the heat of crystallization (He) upon heating was integrated from the Total Heat Flow signal.
  • the sample’s relative crystallinity (C) was measured by subtracting the heat of fusion (Hf) from the heat of crystallization (He) upon heating.
  • blends 1 , 2, and 3 were made by combining resin #1 and resin #2 and resin #2 and #3 in the combinations shown in Table 2. These blends along with their unblended starting materials were converted into shrinkable films using a lab scale process and the properties of those films were measured and are summarized in Table 3. The films made exclusively with resin #1 or resin #3 are not compatible with the PET recycling process and create >1 % clumps of PET. The properties of shrinkable film made with these blends are shown in Tables 4 and 5.
  • crystallization is calculated as the heat of fusion minus the heat of crystallization; in those cases where this value is greater than 8; this value corresponds to a composition which is sufficiently crystalline so as to be recyclable in the context of the present disclosure.
  • the strain induced crystalline melting point must be >200 °C to withstand the drying temperature for PET and remain free-flowing.
  • the strain induced crystalline melting points of these resin blends are much higher than is possible from reactor grade materials made with the same compositions. This high strain induced crystalline melting point would be advantageous in applications where higher melting points are required. For example, if the PET flake is dried at a temperature higher than the APR test temperature (420F or

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
PCT/US2019/055092 2018-10-08 2019-10-08 Crystallizable shrinkable films and thermoformable sheets made from resin blends Ceased WO2020076749A1 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
CN201980066310.4A CN112789156A (zh) 2018-10-08 2019-10-08 由树脂共混物制成的可结晶可收缩膜和可热成形片材
EP19794356.6A EP3863832A1 (en) 2018-10-08 2019-10-08 Crystallizable shrinkable films and thermoformable sheets made from resin blends
CN202410235347.8A CN117986819A (zh) 2018-10-08 2019-10-08 由树脂共混物制成的可结晶可收缩膜和可热成形片材
US17/250,975 US12116452B2 (en) 2018-10-08 2019-10-08 Crystallizable shrinkable films and thermoformable sheets made from resins blends
KR1020217013768A KR102886788B1 (ko) 2018-10-08 2019-10-08 수지 배합물로부터 제조된 결정화가능한 수축성 필름 및 열성형성 시트
JP2021544108A JP7530370B2 (ja) 2018-10-08 2019-10-08 樹脂混合物製の結晶化可能な収縮性フィルムおよび熱成形性シート
MX2021003703A MX2021003703A (es) 2018-10-08 2019-10-08 Peliculas contraibles cristalizables y laminas termoformables hechas de mezclas de resina.
JP2024121143A JP2024153767A (ja) 2018-10-08 2024-07-26 樹脂混合物製の結晶化可能な収縮性フィルムおよび熱成形性シート
US18/884,597 US20250011534A1 (en) 2018-10-08 2024-09-13 Crystallizable shrinkable films and thermoformable sheets made from reactor grade resins

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US201862742726P 2018-10-08 2018-10-08
US62/742,726 2018-10-08
US201862782626P 2018-12-20 2018-12-20
US62/782,626 2018-12-20

Related Child Applications (2)

Application Number Title Priority Date Filing Date
US17/250,975 A-371-Of-International US12116452B2 (en) 2018-10-08 2019-10-08 Crystallizable shrinkable films and thermoformable sheets made from resins blends
US18/884,597 Division US20250011534A1 (en) 2018-10-08 2024-09-13 Crystallizable shrinkable films and thermoformable sheets made from reactor grade resins

Publications (1)

Publication Number Publication Date
WO2020076749A1 true WO2020076749A1 (en) 2020-04-16

Family

ID=68343509

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2019/055092 Ceased WO2020076749A1 (en) 2018-10-08 2019-10-08 Crystallizable shrinkable films and thermoformable sheets made from resin blends

Country Status (7)

Country Link
US (2) US12116452B2 (enExample)
EP (1) EP3863832A1 (enExample)
JP (2) JP7530370B2 (enExample)
KR (1) KR102886788B1 (enExample)
CN (2) CN112789156A (enExample)
MX (1) MX2021003703A (enExample)
WO (1) WO2020076749A1 (enExample)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022072477A1 (en) * 2020-09-30 2022-04-07 Klöckner Pentaplast Of America, Inc. Heat shrinkable films, and method of manufacturing the same
WO2022076765A1 (en) * 2020-10-08 2022-04-14 Eastman Chemical Company Shrinkable polyester films
WO2022109025A1 (en) * 2020-11-18 2022-05-27 Klöckner Pentaplast Of America, Inc. Thermoformed packaging and methods of forming the same
KR20230054723A (ko) 2020-11-19 2023-04-25 본셋 아메리카 코포레이션 폴리에스테르계 열 수축 필름
CN116096551A (zh) * 2020-08-27 2023-05-09 东洋纺株式会社 热收缩性聚酯系薄膜、热收缩性标签、及包装体
WO2023091540A1 (en) 2021-11-22 2023-05-25 Eastman Chemical Company Recyclable copolyesters articles with living hinges
WO2023091544A1 (en) 2021-11-22 2023-05-25 Eastman Chemical Company Process for making recyclable copolyesters articles with living hinges
WO2023163974A1 (en) * 2022-02-22 2023-08-31 Klöckner Pentaplast Of America, Inc. Bio-based thermoformed packaging and methods of forming the same
WO2023196829A1 (en) * 2022-04-06 2023-10-12 Eastman Chemical Company Multilayer shrinkable polyester films with improved toughness
US11858241B2 (en) 2018-05-29 2024-01-02 Klöckner Pentaplast Gmbh Transparent polymer film with discolouration compensation
KR20240004952A (ko) 2021-08-31 2024-01-11 다키론 씨아이 가부시키가이샤 폴리에스테르계 열 수축 필름
WO2024152231A1 (en) * 2023-01-18 2024-07-25 Klöckner Pentaplast Of America, Inc. Heat-shrinkable films and related systems and methods
US12116452B2 (en) 2018-10-08 2024-10-15 Eastman Chemical Company Crystallizable shrinkable films and thermoformable sheets made from resins blends
US12162250B2 (en) 2016-08-15 2024-12-10 Klöckner Pentaplast Of America, Inc. Hot fill laminate
US12410288B2 (en) 2022-11-30 2025-09-09 Klöckner Pentaplast Of America, Inc. Heat-shrinkable films and related systems and methods

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI790692B (zh) * 2021-07-22 2023-01-21 遠東新世紀股份有限公司 熱收縮聚酯標籤膜及其製備方法、容器
WO2023091542A1 (en) 2021-11-22 2023-05-25 Eastman Chemical Company Process for making recyclable copolyesters articles with living hinges
CN118922305A (zh) * 2022-03-18 2024-11-08 伊士曼化工公司 多层可结晶可收缩膜和片材
CN118922467A (zh) * 2022-03-23 2024-11-08 Sk化学株式会社 用于热收缩标签的聚酯共聚物、包含其的组合物和包含其的产品
CN115895202B (zh) * 2022-10-21 2025-04-01 无锡崇华新材料科技有限公司 一种聚酯热收缩薄膜
WO2024246768A1 (en) * 2023-06-01 2024-12-05 Enel Green Power Italia S.r.l. New polyester material for a high-performance polymer applications

Citations (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2720507A (en) 1952-10-03 1955-10-11 Eastman Kodak Co Organo-metallic tin catalysts for preparation of polyesters
US3426754A (en) 1964-06-12 1969-02-11 Celanese Corp Breathable medical dressing
US3772405A (en) 1972-02-02 1973-11-13 Eastman Kodak Co Process for preparing aromatic diester containing copolyesters and products obtained thereby
US3944699A (en) 1972-10-24 1976-03-16 Imperial Chemical Industries Limited Opaque molecularly oriented and heat set linear polyester film and process for making same
US4138459A (en) 1975-09-08 1979-02-06 Celanese Corporation Process for preparing a microporous polymer film
JPS6137827A (ja) 1984-07-31 1986-02-22 Asahi Chem Ind Co Ltd 印刷用合成樹脂フイルム
US4582752A (en) 1985-07-11 1986-04-15 Mobil Oil Corporation Heat shrinkable, lustrous satin appearing, opaque film compositions
US4632869A (en) 1985-09-03 1986-12-30 Mobil Oil Corporation Resin composition, opaque film and method of preparing same
EP0214859A2 (en) 1985-09-09 1987-03-18 E.I. Du Pont De Nemours And Company Microporous polymeric films and process for their manufacture
JPS63193822A (ja) 1987-02-05 1988-08-11 Diafoil Co Ltd 収縮フイルム
US4770931A (en) 1987-05-05 1988-09-13 Eastman Kodak Company Shaped articles from polyester and cellulose ester compositions
US5176954A (en) 1989-03-16 1993-01-05 Mobil Oil Corporation High opacity film and method thereof
US5372864A (en) 1993-09-03 1994-12-13 Eastman Chemical Company Toners for polyesters
US5435955A (en) 1984-12-21 1995-07-25 Ube Industries, Ltd. Process of producing porous polypropylene hollow fiber and film
US5654347A (en) 1993-10-04 1997-08-05 Eastman Chemical Company Concentrates for improving polyester compositions and method of making same
US5696176A (en) 1995-09-22 1997-12-09 Eastman Chemical Company Foamable polyester compositions having a low level of unreacted branching agent
EP0581970B1 (en) 1992-02-25 1998-08-26 Toray Industries, Inc. Biaxially oriented, laminated polyester film
US5843578A (en) 1994-11-02 1998-12-01 Toyo Boseki Kabushiki Kaisha Film having fine voids and manufacture thereof
US6004664A (en) 1994-11-02 1999-12-21 Toyo Boseki Kabushiki Kaisha Film having fine voids and manufacture thereof
US6287680B1 (en) 1998-12-08 2001-09-11 Toyo Boseki Kabushiki Kaisha Porous polyester film
US20010036545A1 (en) 2000-04-03 2001-11-01 Toyo Boseki Kabushiki Kaisha Porous polyester film
US6500533B1 (en) 2000-02-09 2002-12-31 Exxonmobil Oil Corporation Opaque polymeric films cavitated with PBT and polycarbonate
US20030068453A1 (en) 2001-10-02 2003-04-10 Dan-Cheng Kong Multilayer sleeve labels
US20030165671A1 (en) 2002-02-14 2003-09-04 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester films
US20030170427A1 (en) 2002-02-14 2003-09-11 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester films and labels
US6720085B2 (en) 2000-07-28 2004-04-13 Toyo Boseki Kabushiki Kaisha Heat shrinkable polyester film
EP1418042A1 (en) * 2001-07-11 2004-05-12 Toyo Boseki Kabushiki Kaisha Heat shrinkable polyester films and process for production thereof
JP2004181863A (ja) 2002-12-05 2004-07-02 Toyobo Co Ltd 熱収縮性ポリエステル系フィルムロールおよびその製造方法
US20090227735A1 (en) * 2008-03-07 2009-09-10 Eastman Chemical Company Miscible polyester blends and shrinkable films prepared therefrom
US20110091705A1 (en) * 2009-10-19 2011-04-21 Eastman Chemical Company Radio-frequency sealable polymer and articles thereof
EP2365025A1 (en) * 2010-03-09 2011-09-14 SKC Co., Ltd. Heat-shrinkable polyester film

Family Cites Families (211)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5825331B2 (ja) * 1977-07-13 1983-05-26 東レ株式会社 ポリエステルフイルム
GB2007685B (en) 1977-10-11 1982-05-12 Asahi Dow Ltd Composition for drawn film cold drawn film made of said composition and process for manufacture of said film
US4578437A (en) 1983-08-01 1986-03-25 Eastman Kodak Company Copolyester/polyester blends having reduced carbon dioxide permeability
US4705707A (en) 1985-12-17 1987-11-10 Presto Products, Incorporated Polyethylene/polyester nonoriented heat sealable moisture barrier film and bag
DE3751722T2 (de) 1986-11-12 1996-07-11 Diafoil Hoechst Co Ltd Polyester-Schrumpffolie
DE3752051T2 (de) 1986-12-19 1997-07-24 Toyo Boseki Wärmeschrumpfbarer Polyesterfilm
JPH0216032A (ja) 1988-07-05 1990-01-19 Diafoil Co Ltd ポリエステル系収縮フィルム
US5023143A (en) 1989-03-14 1991-06-11 W. R. Grace & Co.-Conn. Low shrink force shrink film
JP2781598B2 (ja) 1989-04-28 1998-07-30 鐘紡株式会社 ポリエステル系シュリンクフィルム
JPH0368634A (ja) 1989-08-08 1991-03-25 Mitsubishi Rayon Co Ltd 熱収縮性ポリエステルフィルム
JP2629370B2 (ja) 1989-08-29 1997-07-09 東洋紡績株式会社 熱収縮性ポリエステルフィルム
JP2793713B2 (ja) 1990-10-27 1998-09-03 鐘紡株式会社 表面特性の改善されたポリエステル系シュリンクフィルム
JP3351473B2 (ja) 1992-05-21 2002-11-25 東洋紡績株式会社 熱収縮性ポリエステル系フイルム
JP2596287B2 (ja) 1992-07-16 1997-04-02 東洋紡績株式会社 熱収縮性ポリエステル系フィルム
US5336552A (en) 1992-08-26 1994-08-09 Kimberly-Clark Corporation Nonwoven fabric made with multicomponent polymeric strands including a blend of polyolefin and ethylene alkyl acrylate copolymer
WO1994013732A1 (fr) 1992-12-04 1994-06-23 Toray Industries, Inc. Film de polyester a stratification thermique
US5385773A (en) 1993-04-27 1995-01-31 Eastman Chemical Company Copolyester of cyclohexanenedimethanol and process for producing such polyester
JP2693358B2 (ja) 1993-07-23 1997-12-24 吉貝機械金属株式会社 操作レバー装置
TW300241B (enExample) 1993-08-10 1997-03-11 Toyo Boseki
US5340624A (en) 1993-08-16 1994-08-23 Eastman Chemical Company Shrinkable copolyester film
JPH0753737A (ja) 1993-08-18 1995-02-28 Kanebo Ltd ポリエステル系シュリンクフィルム
KR950008582A (ko) 1993-09-10 1995-04-19 하기주 라벨용 수축필름 및 그의 제조 방법
JPH07138388A (ja) 1993-11-17 1995-05-30 Sekisui Chem Co Ltd ポリエステル系熱収縮性フイルムの製造方法
CA2177620A1 (en) 1993-11-26 1995-06-01 Wayne Keng Shih Plasticized polyester for shrink film applications
JP3187228B2 (ja) 1993-12-27 2001-07-11 株式会社クラレ 共重合ポリエステルおよびそれからなる熱収縮フィルム
CA2139061C (en) 1993-12-28 1998-12-08 Mitsui Chemicals, Inc. Process for preparing polyester
US5567758A (en) 1994-08-26 1996-10-22 Toyo Boseki Kabushiki Kaisha Thermoplastic polyester resin composition
EP0724947B1 (en) 1994-08-30 2002-05-08 Toray Industries, Inc. Biaxially oriented polyester film and process for production thereof
TW354305B (en) 1994-12-22 1999-03-11 Eastman Chem Co Production of particular polyesters using a novel catalyst system
US5608031A (en) 1995-11-30 1997-03-04 Eastman Chemical Company Polyesters modified with 1,4-cyclohexaned imethanol having high clarity prepared utilizing an antimony containing catalyst/stabilizer system
US6287667B1 (en) 1995-12-22 2001-09-11 Mitsubishi Polyester Film Corporation Polyester film and capacitor using the same
US5972445A (en) 1996-01-17 1999-10-26 Mitsubishi Chemical Corporation Multilayer polyester sheet
JP3896604B2 (ja) 1996-03-22 2007-03-22 東洋紡績株式会社 熱収縮性ポリエステル系フィルム
US5852164A (en) 1996-04-16 1998-12-22 Mitsubishi Chemical Corporation Polyester, process for producing the same and molding product therefrom
US5668899A (en) 1996-04-24 1997-09-16 Eastman Kodak Company Optical radiation coupler for an optical fiber
US5824398A (en) 1996-06-24 1998-10-20 Eastman Chemical Company Plasticized polyester for shrink film applications
US5932685A (en) 1996-08-30 1999-08-03 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester films
CA2199334C (en) 1996-09-09 2006-04-18 Kohzo Takahashi A biaxially oriented polyester film for laminating metallic sheets
KR100386147B1 (ko) 1996-10-11 2004-03-24 데이진 가부시키가이샤 금속판첩합성형가공용이축배향폴리에스테르필름
US5859116A (en) 1997-01-21 1999-01-12 Eastman Chemical Company Clarity and adjustable shrinkage of shrink films using miscible polyester blends
CN1146679C (zh) 1997-08-28 2004-04-21 伊斯曼化学公司 改良的共聚物粘合纤维
DE69807423T2 (de) 1997-10-06 2003-04-10 Toyo Boseki K.K., Osaka Themoplastisches Polyester-Elastomer und dieses enthaltende Zusammensetzung
CA2249766A1 (en) 1997-10-14 1999-04-14 Kenichi Etou Biaxially oriented polyester films and their production methods
EP0979722B8 (en) 1997-12-05 2005-03-02 Gunze Limited Low temperature heat shrinkable film for labels
WO1999029489A1 (en) 1997-12-11 1999-06-17 Teijin Limited Biaxially oriented polyester film
DE69924421T2 (de) 1998-01-30 2006-03-09 Toyo Boseki K.K. Wärmeschrumpfbarer Polyesterfilm
US6846440B2 (en) 1998-03-17 2005-01-25 Eastman Chemical Company Polyester resin compositions for calendering
US6068910A (en) 1998-03-17 2000-05-30 Eastman Chemical Company Polyester resin compositions for calendering
US6925040B1 (en) 1998-08-04 2005-08-02 Hitachi, Ltd. Information recording method, information recording medium and information recording apparatus
US6485810B1 (en) 1998-10-09 2002-11-26 Teijin Limited Biaxially oriented polyester film and flexible disk
WO2000024804A1 (fr) 1998-10-23 2000-05-04 Toyo Boseki Kabushiki Kaisha Catalyseur de polymerisation destine a la production de polyester, polyester et procede de production associe
KR100497872B1 (ko) * 1999-01-28 2005-06-29 도요 보세키 가부시키가이샤 열수축성 폴리에스테르계 필름
US6616998B2 (en) 1999-02-02 2003-09-09 Eastman Chemical Company Polyester packaging films producing a peelable seal
JP2000229357A (ja) 1999-02-09 2000-08-22 Gunze Ltd 熱収縮性フィルム及びそれが熱収縮装着された容器
JP3642229B2 (ja) 1999-05-21 2005-04-27 東洋紡績株式会社 熱収縮性ポリエステル系フィルム
US6287656B1 (en) 1999-06-03 2001-09-11 Eastman Chemical Corporation Low melt viscosity amorphous copolyesters having improved resistance to lipids
US6120889A (en) 1999-06-03 2000-09-19 Eastman Chemical Company Low melt viscosity amorphous copolyesters with enhanced glass transition temperatures
DE60030635T2 (de) 1999-07-12 2007-09-06 Teijin Ltd. Magnetisches Aufzeichnungsmittel und Polyesterfilm dafür
DE60014530T2 (de) 1999-07-27 2006-03-09 SKC Co., Ltd., Suwon Wärmeschrumpfbarer Polyesterfilm und Verfahren zu seiner Herstellung
JP4488126B2 (ja) 1999-08-03 2010-06-23 東洋紡績株式会社 ラベル並びにそのラベルを装着したボトル及びその再生方法
US6362306B1 (en) 1999-08-17 2002-03-26 Eastman Chemical Company Reactor grade copolyesters for shrink film applications
AUPQ294699A0 (en) 1999-09-17 1999-10-14 Visy Plastics Pty Ltd Process for preparing food contact grade polyethylene terephthalate resin from waste pet containers
JP4356153B2 (ja) 1999-10-04 2009-11-04 東洋紡績株式会社 熱収縮性ポリエステル系フィルム
EP1120352B1 (en) 2000-01-28 2007-05-23 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester films
EP1661936B1 (en) 2000-04-11 2016-08-03 Toyobo Co., Ltd. Heat-shrinkable polyester films
JP4552097B2 (ja) 2000-04-27 2010-09-29 東洋紡績株式会社 熱収縮性熱可塑性樹脂系フィルム
JP4304243B2 (ja) 2000-08-02 2009-07-29 東洋紡績株式会社 熱収縮性ポリエステル系フィルム
EP1186633B1 (en) 2000-09-05 2005-06-08 Toyo Boseki Kabushiki Kaisha Polyester film, use thereof and metal laminated sheet made of said film, and metal can and metal lid made of the sheet
JP3890972B2 (ja) 2000-12-26 2007-03-07 コニカミノルタホールディングス株式会社 セルロースエステルフィルム、それを用いる偏光板用保護フィルム及び偏光板
KR100785251B1 (ko) 2001-01-25 2007-12-12 도요 보세키 가부시키가이샤 열수축성 폴리에스테르계 필름 및 라벨
US6551688B2 (en) 2001-02-28 2003-04-22 Eastman Chemical Company Calendered polyester films or sheets having a haze value of less than five percent
JP3767511B2 (ja) 2001-04-26 2006-04-19 東洋紡績株式会社 熱収縮性ポリエステル系フィルムロール
US6765070B2 (en) 2001-05-18 2004-07-20 Mitsubishi Chemical Corporation Copolymerized polyester resin composition and stretched film
JP2002363312A (ja) 2001-06-05 2002-12-18 Toyobo Co Ltd 熱収縮性ポリエステル系フィルム
US6599994B2 (en) 2001-07-18 2003-07-29 Eastman Chemical Company Polyester blends and heat shrinkable films made therefrom
FR2828129A1 (fr) 2001-07-31 2003-02-07 Perrier Vittel Man Technologie Procedes de fabrication de preformes et de contenants en pet tels que bouteilles alimentaires, contenants et preformes intermediaires obtenus
GB0118796D0 (en) 2001-08-01 2001-09-26 Dupont Teijin Films Us Ltd Par Copolyester film
JP3678186B2 (ja) 2001-08-01 2005-08-03 東洋紡績株式会社 熱収縮性ポリエステル系フィルムロール
US7001651B2 (en) 2001-09-26 2006-02-21 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester film
US6465063B1 (en) 2001-10-02 2002-10-15 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester films
CN1263782C (zh) 2001-10-22 2006-07-12 Sk化学株式会社 用于溶剂基涂料的共聚聚酯树脂和含有该树脂的涂料组合物
DE60219512T2 (de) 2001-11-02 2007-12-27 Skc Ltd. Wärmeschrumfbare polyesterfolie
US6653440B2 (en) 2001-11-13 2003-11-25 Mitsubishi Gas Chemical Company Process for producing copolyester resin
KR100541230B1 (ko) 2001-12-11 2006-01-10 에스케이씨 주식회사 이축연신 폴리에스테르 필름
ATE389685T1 (de) 2001-12-27 2008-04-15 Toyo Boseki Use of a heat-shrinkable resin film for labels
US7037576B2 (en) 2002-02-06 2006-05-02 Eastman Chemical Company Polyester or copolyester/polyolefin laminate structures and methods of making the same
DE60312640T2 (de) 2002-04-11 2007-12-06 Toyo Boseki K.K. Granulat aus amorphem polyester und herstellungsverfahren dafür sowie verfahren zur lagerung von granulat aus amorphem polyester
EP1500489B1 (en) 2002-04-24 2008-02-13 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester film and label
JP2004051888A (ja) 2002-07-23 2004-02-19 Toyobo Co Ltd 熱収縮性ポリエステル系フィルム
JP4250383B2 (ja) 2002-07-26 2009-04-08 三菱樹脂株式会社 熱収縮性ポリエステル系フィルム
ES2391767T3 (es) 2002-12-20 2012-11-29 Mitsubishi Rayon Co., Ltd. Composición de resina de poliéster para tóner y tóner
US6863939B2 (en) 2002-12-20 2005-03-08 Eastman Kodak Company Microbead and immiscible polymer voided polyester for inkjet imaging medias
WO2004069896A1 (en) 2003-02-06 2004-08-19 Surface Specialties, S.A. Process for producing neopentyl-glycol based polyesters
CN100594220C (zh) 2003-03-05 2010-03-17 伊士曼化工公司 聚合物共混物
US20070059465A1 (en) 2004-05-20 2007-03-15 Thompson David E Polyester Resins for High-Strength Articles
WO2004104080A1 (en) 2003-05-21 2004-12-02 Wellman, Inc. Slow-crystallizing polyester resins
US7008698B2 (en) * 2003-06-17 2006-03-07 Mitsubishi Polyester Film, Llc Propane diol-based polyester resin and shrink film
KR100549111B1 (ko) * 2003-06-23 2006-02-02 도레이새한 주식회사 결정성이 우수한 열수축성 폴리에스테르 필름
KR100549112B1 (ko) 2003-06-25 2006-02-02 도레이새한 주식회사 결정성이 우수한 열수축성 폴리에스테르 필름
WO2005017007A1 (ja) 2003-08-19 2005-02-24 Toyo Boseki Kabushiki Kaisya ポリエステルフィルム
WO2005023910A1 (ja) 2003-09-02 2005-03-17 Toyo Boseki Kabushiki Kaisha 成型用ポリエステルフィルム
EP1666521B1 (en) 2003-09-11 2014-03-26 Teijin Dupont Films Japan Limited Polyester film
US7235623B2 (en) * 2003-11-26 2007-06-26 Eastman Chemical Company Polyester compositions for calendering
US20050119359A1 (en) 2003-12-02 2005-06-02 Shelby Marcus D. Void-containing polyester shrink film
JP2005206730A (ja) 2004-01-23 2005-08-04 Toyobo Co Ltd 熱収縮性ポリエステル系フィルム
US7582369B2 (en) 2004-02-17 2009-09-01 Toray Industries, Inc. Biaxially oriented polyester film
KR100874131B1 (ko) 2004-06-10 2008-12-15 주식회사 코오롱 폴리에스터 수축 필름
US20090240024A1 (en) 2004-09-02 2009-09-24 Skc Co., Ltd. Biaxially oriented polyester film and preparation thereof
US20070004813A1 (en) 2004-09-16 2007-01-04 Eastman Chemical Company Compositions for the preparation of void-containing articles
TWI393637B (zh) 2004-11-11 2013-04-21 Mitsubishi Plastics Inc 熱收縮性積層薄膜，使用該薄膜之成形品，熱收縮性標籤及容器
US20060121219A1 (en) 2004-12-07 2006-06-08 Eastman Chemical Co. Void-containing polyester shrink film with improved density retention
CN101084116A (zh) 2004-12-23 2007-12-05 艾利丹尼森公司 热收缩膜及其中包封的制品
JP2006233092A (ja) * 2005-02-25 2006-09-07 Mitsubishi Plastics Ind Ltd ポリエステル系樹脂組成物、並びに該組成物を用いた熱収縮性フィルム、熱収縮性ラベル及び該ラベルを装着した容器
US20060249715A1 (en) 2005-04-12 2006-11-09 Salyer David G Method for reducing flame spread
CA2630607C (en) 2005-11-22 2015-04-07 Wellman, Inc. Polyester resins for high-efficiency injection molding
EP1984434A4 (en) 2006-01-27 2014-01-15 Kolon Inc HEAT SHRINKABLE POLYESTER FOIL
JP5036706B2 (ja) 2006-03-31 2012-09-26 株式会社フジシールインターナショナル シュリンクフィルム
EP1852255B1 (de) 2006-04-08 2009-12-09 Mitsubishi Polyester Film GmbH Polyesterfolie mit geringer mechanischer Festigkeit
JP4411556B2 (ja) 2006-06-14 2010-02-10 東洋紡績株式会社 熱収縮性ポリエステル系フィルム、およびその製造方法
JP4882919B2 (ja) 2006-08-30 2012-02-22 東洋紡績株式会社 熱収縮性ポリエステル系フィルム、およびその製造方法、包装体
US8088474B2 (en) 2007-03-27 2012-01-03 Agfa-Gevaert N.V. Non-transparent microvoided biaxially stretched film, its use in synthetic paper and an image recording element comprising same
US8476364B2 (en) 2007-03-29 2013-07-02 Beaulieu Group, Llc Polymer manufacturing process
KR101467009B1 (ko) 2007-05-30 2014-12-01 데이진 듀폰 필름 가부시키가이샤 자동차 구동 모터용 2 축 배향 폴리에스테르 필름 및 그것으로 이루어지는 전기 절연 부재
JP4560740B2 (ja) 2007-09-25 2010-10-13 東洋紡績株式会社 熱収縮性ポリエステル系フィルムの製造方法、熱収縮性ポリエステル系フィルム及び包装体
WO2009066928A2 (en) 2007-11-19 2009-05-28 Kolon Industries, Inc. Thermo-shrinkable polyester film
US7687594B2 (en) 2007-11-27 2010-03-30 Industrial Technology Research Institute Random amorphous copolymer and manufacturing method thereof
KR101190348B1 (ko) 2007-12-11 2012-10-11 코오롱인더스트리 주식회사 열수축성 폴리에스테르계 필름
US8318893B2 (en) 2007-12-12 2012-11-27 Mitsubishi Chemical Corporation Aliphatic polyester resin and its production method
JP5286829B2 (ja) 2007-12-13 2013-09-11 東洋紡株式会社 ラベル
JP4809419B2 (ja) 2007-12-13 2011-11-09 東洋紡績株式会社 熱収縮性ポリエステル系フィルム、およびその製造方法
US8012571B2 (en) 2008-05-02 2011-09-06 3M Innovative Properties Company Optical film comprising birefringent naphthalate copolyester having branched or cyclic C4-C10 alkyl units
KR101219525B1 (ko) 2008-05-16 2013-01-11 에스케이씨 주식회사 열수축성 폴리에스테르 필름
US8383246B2 (en) 2008-05-22 2013-02-26 Exxonmobil Oil Corporation Polypropylene-based shrink films
KR100987065B1 (ko) 2008-06-11 2010-10-11 에스케이씨 주식회사 열수축성 폴리에스터계 필름 및 그의 제조 방법
US9375902B2 (en) 2008-09-30 2016-06-28 Toray Industries, Inc. Polyester film
KR101447756B1 (ko) 2008-11-28 2014-10-06 에스케이케미칼주식회사 공중합 폴리에스테르 수지 및 이를 이용한 성형제품
KR20100060848A (ko) 2008-11-28 2010-06-07 에스케이케미칼주식회사 공중합 폴리에스테르 및 이를 이용한 성형 제품
KR101066517B1 (ko) 2008-12-01 2011-09-21 에스케이씨 주식회사 열수축성 폴리에스터계 필름
CN102272205B (zh) 2009-03-19 2015-03-04 Skc株式会社 热收缩聚酯薄膜及其制备方法
US9062197B2 (en) 2009-03-27 2015-06-23 Eastman Chemical Company Polyester blends
ES2461849T3 (es) 2009-05-26 2014-05-21 Toyobo Co., Ltd Película de poliéster termocontraíble, método de fabricación de la misma y producto envasado usando la misma
WO2010143318A1 (ja) 2009-06-12 2010-12-16 東洋紡績株式会社 空洞含有熱収縮性ポリエステル系フィルム及びその製造方法
JP4947194B2 (ja) 2009-09-30 2012-06-06 東洋紡績株式会社 太陽電池裏面保護膜用ポリエステルフィルム
US20110081510A1 (en) 2009-10-07 2011-04-07 Eastman Chemical Company Melt strength enhanced copolyester with improved stability and profile in blown film
EP2548913B1 (en) 2010-03-15 2016-03-02 Toyobo Co., Ltd. Heat-shrinkable polyester film, packaging body thereof, the method for producing heat-shrinkable polyester film
KR101268217B1 (ko) 2010-03-31 2013-06-10 코오롱인더스트리 주식회사 열수축성 폴리에스테르계 단층 필름
WO2011125435A1 (ja) 2010-04-08 2011-10-13 東洋紡績株式会社 熱収縮性ポリエステル系フィルム、およびその製造方法、包装体
JP2012017456A (ja) 2010-06-11 2012-01-26 Fujifilm Corp ポリエステルフィルム及びその製造方法、太陽電池用バックシート、並びに太陽電池モジュール
WO2012023571A1 (ja) 2010-08-18 2012-02-23 東洋紡績株式会社 耐加水分解性ポリエステルフィルム
KR101526623B1 (ko) 2010-08-26 2015-06-08 코오롱인더스트리 주식회사 열수축성 폴리에스테르계 필름
CN103189415B (zh) 2010-09-08 2015-04-15 东丽株式会社 聚酯组合物的制造方法
US8742058B2 (en) 2010-09-27 2014-06-03 Toray Industries, Inc. Biaxially oriented polyester film and linear magnetic recording medium
KR101220226B1 (ko) 2010-10-20 2013-01-09 에스케이씨 주식회사 열수축성 폴리에스터 필름
KR101879609B1 (ko) 2010-12-24 2018-07-18 도레이 카부시키가이샤 폴리에스테르 필름 및 그것을 사용한 적층체
US9150006B2 (en) 2011-06-23 2015-10-06 Eastman Chemical Company Lamination process optimization utilizing neopentyl glycol-modified polyesters
US10525678B2 (en) 2011-10-14 2020-01-07 Avery Dennison Corporation Shrink film for label
SG11201401541PA (en) 2012-01-11 2014-08-28 Avery Dennison Corp Multi-layered shrink film with polyolefin core
US8889820B2 (en) 2012-02-15 2014-11-18 Saudi Basic Industries Corporation Amorphous, high glass transition temperature copolyester compositions, methods of manufacture, and articles thereof
US8969506B2 (en) 2012-02-15 2015-03-03 Saudi Basic Industries Corporation Amorphous, high glass transition temperature copolyester compositions, methods of manufacture, and articles thereof
US8901273B2 (en) 2012-02-15 2014-12-02 Saudi Basic Industries Corporation Amorphous, high glass transition temperature copolyester compositions, methods of manufacture, and articles thereof
US20130217830A1 (en) * 2012-02-16 2013-08-22 Eastman Chemical Company Clear Semi-Crystalline Articles with Improved Heat Resistance
JP6083378B2 (ja) 2012-03-29 2017-02-22 東洋紡株式会社 ポリエステル組成物およびポリエステルフィルム
JP5993635B2 (ja) * 2012-07-05 2016-09-14 シーアイ化成株式会社 熱収縮性ポリエステル系フィルムおよびその製造方法
JP5240387B1 (ja) 2012-07-26 2013-07-17 東洋紡株式会社 熱収縮性ポリエステル系フィルムおよび包装体
US9145470B2 (en) 2012-07-30 2015-09-29 Sabic Global Technologies B.V. Method for the preparation of polyalkylene terephthalate resin compositions employing titanium-containing catalyst complex
EP2862892B1 (en) 2012-08-03 2020-09-09 Toyobo Co., Ltd. Heat-shrinkable polyester-based film
TWI576367B (zh) 2012-08-29 2017-04-01 東洋紡股份有限公司 熱收縮性聚酯系薄膜
FR2997342B1 (fr) 2012-10-26 2014-12-05 Sleever Int Film en matiere plastique thermoretractable multicouche
KR102128297B1 (ko) 2012-10-31 2020-06-30 도레이 카부시키가이샤 폴리에스테르 필름, 상기 필름을 사용한 적층체, 및 상기 적층체와 실란트층을 포함하는 구성체
US10329393B2 (en) 2012-12-12 2019-06-25 Eastman Chemical Company Copolysters plasticized with polymeric plasticizer for shrink film applications
KR102082304B1 (ko) 2013-05-02 2020-02-27 에스케이케미칼 주식회사 공중합 폴리에스테르 수지 및 이를 이용한 성형제품
EP2998341B1 (en) 2013-05-16 2016-12-28 Toyobo Co., Ltd. Heat-shrinkable polyester film and package
US10287433B2 (en) 2013-06-11 2019-05-14 Toyobo Co., Ltd. Heat-shrinkable polyester film and packages
WO2014204157A1 (ko) 2013-06-17 2014-12-24 에스케이케미칼주식회사 폴리에틸렌테레프탈레이트 수지와 공중합 폴리에스테르 수지를 포함하는 열수축 필름 형성용 조성물, 및 열수축 필름
KR101582462B1 (ko) 2013-08-23 2016-01-06 (주)디엔에프 신규한 중합체 및 이를 포함하는 조성물
JP6500440B2 (ja) 2013-10-24 2019-04-17 東洋紡株式会社 共重合ポリエステル樹脂
JP6442828B2 (ja) 2014-01-20 2018-12-26 三菱ケミカル株式会社 熱収縮性フィルム、並びに該フィルムを用いた成形品、熱収縮性ラベル、および該成形品、または該ラベルを装着した容器
JP6269399B2 (ja) 2014-02-04 2018-01-31 東洋紡株式会社 熱収縮性ポリエステル系フィルム
KR101561286B1 (ko) 2014-02-11 2015-10-16 도레이첨단소재 주식회사 저비중 열수축성 폴리에스테르 필름
JP6459533B2 (ja) 2014-04-01 2019-01-30 東洋紡株式会社 熱収縮性ポリエステル系フィルムおよび包装体
JP6519189B2 (ja) * 2014-04-01 2019-05-29 東洋紡株式会社 熱収縮性ポリエステル系フィルムおよび包装体
GB201412153D0 (en) * 2014-07-08 2014-08-20 Dupont Teijin Films Us Ltd Polyester film
KR102193168B1 (ko) 2014-08-26 2020-12-18 에스케이케미칼 주식회사 폴리에스테르 수지 조성물 및 이의 제조 방법
US10005890B2 (en) 2014-10-15 2018-06-26 Skc Inc. Polyester film and envelope
CN107000909B (zh) 2014-12-02 2020-03-17 东洋纺株式会社 包装用薄膜以及包装袋
US10392485B2 (en) 2015-03-20 2019-08-27 Toyobo Co., Ltd. Heat-shrinkable polyester-based film and package
CN107405825B (zh) 2015-03-25 2019-10-08 东洋纺株式会社 热收缩性聚酯系薄膜及包装体
JP6519331B2 (ja) 2015-06-11 2019-05-29 東洋紡株式会社 熱収縮性ポリエステル系フィルムおよび包装体
JP6572907B2 (ja) 2015-07-24 2019-09-11 東洋紡株式会社 熱収縮性ポリエステル系フィルム、およびその製造方法、包装体
KR102500312B1 (ko) 2015-08-05 2023-02-14 도요보 가부시키가이샤 열수축성 폴리에스테르계 필름 및 포장체
ES2828040T3 (es) 2015-08-19 2021-05-25 Toyo Boseki Película de poliéster termocontráctil y envase
TWI731872B (zh) 2015-09-02 2021-07-01 日商東洋紡股份有限公司 含有呋喃二甲酸酯單元之聚酯膜及其生產方法
JP6504010B2 (ja) * 2015-09-30 2019-04-24 東洋紡株式会社 ポリエステル系ラベルおよび包装容器
KR102396755B1 (ko) 2016-08-01 2022-05-12 도요보 가부시키가이샤 열수축성 폴리에스테르계 필름 및 포장체
KR102409406B1 (ko) 2016-09-28 2022-06-15 도요보 가부시키가이샤 백색 열수축성 폴리에스테르계 필름 롤
KR102654778B1 (ko) 2016-11-24 2024-04-03 에스케이케미칼 주식회사 내열성 mdo 열수축 필름
WO2018110493A1 (ja) 2016-12-12 2018-06-21 東洋紡株式会社 熱収縮性ポリエステル系ラベル、包装体、および熱収縮性ポリエステル系ラベルの製造方法
WO2018124585A1 (ko) 2016-12-28 2018-07-05 에스케이씨 주식회사 폴리에스테르 수지, 및 이의 제조방법 및 이를 이용한 공중합 폴리에스테르 필름의 제조방법
US11167887B2 (en) 2017-02-13 2021-11-09 Toyobo Co., Ltd. Amorphous copolymerized polyester raw material for film, heat-shrinkable polyester-based film, heat-shrinkable label, and packaged product
EP3617247A4 (en) 2017-04-27 2020-12-30 Toyobo Co., Ltd. POLYESTER RESIN FOR HEAT SHRINK FILM, HEAT SHRINK FILM, HEAT SHRINK LABEL AND PACKAGING
US11668863B2 (en) 2017-05-26 2023-06-06 Sk Microworks Co., Ltd. Optical polyester film, and prism sheet or polarized reflection sheet comprising same
WO2019103370A1 (ko) 2017-11-22 2019-05-31 에스케이케미칼주식회사 폴리에스테르 수지 조성물 및 이를 포함하는 이축 연신 폴리에스테르 필름
CN111655806B (zh) 2018-01-23 2023-12-05 伊士曼化工公司 聚酯酰胺、其制备方法以及聚酯酰胺组合物
WO2019147676A1 (en) 2018-01-23 2019-08-01 Solutia Inc. Interlayers comprising polyesteramide compositions
US10800898B2 (en) 2018-04-30 2020-10-13 Skc Inc. Method for reproducing polyester container and reproduced polyester chip prepared therefrom
KR102153670B1 (ko) 2018-05-21 2020-09-08 에스케이씨 주식회사 열수축성 필름 및 이의 제조방법
JP7363788B2 (ja) 2018-08-03 2023-10-18 東洋紡株式会社 非晶性のフィルム用共重合ポリエステル原料、熱収縮性ポリエステル系フィルム、熱収縮性ラベル、及び包装体
MX2021003703A (es) 2018-10-08 2021-06-04 Eastman Chem Co Peliculas contraibles cristalizables y laminas termoformables hechas de mezclas de resina.
EP3863831B1 (en) 2018-10-08 2025-02-19 Eastman Chemical Company Crystallizable shrinkable and thermoformable sheets made from reactor grade resins
KR102281770B1 (ko) 2019-10-29 2021-07-26 에스케이씨 주식회사 폴리에스테르 필름 및 이를 이용한 폴리에스테르 용기의 재생 방법
KR102226711B1 (ko) 2019-10-29 2021-03-11 에스케이씨 주식회사 폴리에스테르 용기의 재생 방법 및 이를 위한 폴리에스테르 필름

Patent Citations (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2720507A (en) 1952-10-03 1955-10-11 Eastman Kodak Co Organo-metallic tin catalysts for preparation of polyesters
US3426754A (en) 1964-06-12 1969-02-11 Celanese Corp Breathable medical dressing
US3772405A (en) 1972-02-02 1973-11-13 Eastman Kodak Co Process for preparing aromatic diester containing copolyesters and products obtained thereby
US3944699A (en) 1972-10-24 1976-03-16 Imperial Chemical Industries Limited Opaque molecularly oriented and heat set linear polyester film and process for making same
US4138459A (en) 1975-09-08 1979-02-06 Celanese Corporation Process for preparing a microporous polymer film
JPS6137827A (ja) 1984-07-31 1986-02-22 Asahi Chem Ind Co Ltd 印刷用合成樹脂フイルム
US5435955A (en) 1984-12-21 1995-07-25 Ube Industries, Ltd. Process of producing porous polypropylene hollow fiber and film
US4582752A (en) 1985-07-11 1986-04-15 Mobil Oil Corporation Heat shrinkable, lustrous satin appearing, opaque film compositions
US4632869A (en) 1985-09-03 1986-12-30 Mobil Oil Corporation Resin composition, opaque film and method of preparing same
EP0214859A2 (en) 1985-09-09 1987-03-18 E.I. Du Pont De Nemours And Company Microporous polymeric films and process for their manufacture
JPS63193822A (ja) 1987-02-05 1988-08-11 Diafoil Co Ltd 収縮フイルム
US4770931A (en) 1987-05-05 1988-09-13 Eastman Kodak Company Shaped articles from polyester and cellulose ester compositions
US5176954A (en) 1989-03-16 1993-01-05 Mobil Oil Corporation High opacity film and method thereof
EP0581970B1 (en) 1992-02-25 1998-08-26 Toray Industries, Inc. Biaxially oriented, laminated polyester film
US5372864A (en) 1993-09-03 1994-12-13 Eastman Chemical Company Toners for polyesters
US5384377A (en) 1993-09-03 1995-01-24 Eastman Chemical Company Toners for polyesters
US5654347A (en) 1993-10-04 1997-08-05 Eastman Chemical Company Concentrates for improving polyester compositions and method of making same
US6004664A (en) 1994-11-02 1999-12-21 Toyo Boseki Kabushiki Kaisha Film having fine voids and manufacture thereof
US5843578A (en) 1994-11-02 1998-12-01 Toyo Boseki Kabushiki Kaisha Film having fine voids and manufacture thereof
US5696176A (en) 1995-09-22 1997-12-09 Eastman Chemical Company Foamable polyester compositions having a low level of unreacted branching agent
US6287680B1 (en) 1998-12-08 2001-09-11 Toyo Boseki Kabushiki Kaisha Porous polyester film
US6500533B1 (en) 2000-02-09 2002-12-31 Exxonmobil Oil Corporation Opaque polymeric films cavitated with PBT and polycarbonate
US20010036545A1 (en) 2000-04-03 2001-11-01 Toyo Boseki Kabushiki Kaisha Porous polyester film
US6720085B2 (en) 2000-07-28 2004-04-13 Toyo Boseki Kabushiki Kaisha Heat shrinkable polyester film
EP1418042A1 (en) * 2001-07-11 2004-05-12 Toyo Boseki Kabushiki Kaisha Heat shrinkable polyester films and process for production thereof
US20030068453A1 (en) 2001-10-02 2003-04-10 Dan-Cheng Kong Multilayer sleeve labels
US20030165671A1 (en) 2002-02-14 2003-09-04 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester films
US20030170427A1 (en) 2002-02-14 2003-09-11 Toyo Boseki Kabushiki Kaisha Heat-shrinkable polyester films and labels
JP2004181863A (ja) 2002-12-05 2004-07-02 Toyobo Co Ltd 熱収縮性ポリエステル系フィルムロールおよびその製造方法
US20090227735A1 (en) * 2008-03-07 2009-09-10 Eastman Chemical Company Miscible polyester blends and shrinkable films prepared therefrom
US20110091705A1 (en) * 2009-10-19 2011-04-21 Eastman Chemical Company Radio-frequency sealable polymer and articles thereof
EP2365025A1 (en) * 2010-03-09 2011-09-14 SKC Co., Ltd. Heat-shrinkable polyester film

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
CRITICAL GUIDANCE PROTOCOL FOR CLEAR PET ARTICLES WITH LABELS AND CLOSURES, 11 April 2019 (2019-04-11)
THRONE, JAMES: "Technology of Thermoforming", 1996, HANSER PUBLISHERS, pages: 16 - 29

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12162250B2 (en) 2016-08-15 2024-12-10 Klöckner Pentaplast Of America, Inc. Hot fill laminate
US11858241B2 (en) 2018-05-29 2024-01-02 Klöckner Pentaplast Gmbh Transparent polymer film with discolouration compensation
US12319037B2 (en) 2018-05-29 2025-06-03 Klöckner Pentaplast Gmbh Transparent polymer film with discoloration compensation
US12116452B2 (en) 2018-10-08 2024-10-15 Eastman Chemical Company Crystallizable shrinkable films and thermoformable sheets made from resins blends
EP4205948A4 (en) * 2020-08-27 2024-09-04 Toyobo Co., Ltd. HEAT SHRINKABLE POLYESTER FILM, HEAT SHRINKABLE LABEL AND PACKAGING
CN116096551A (zh) * 2020-08-27 2023-05-09 东洋纺株式会社 热收缩性聚酯系薄膜、热收缩性标签、及包装体
JP2024149713A (ja) * 2020-08-27 2024-10-18 東洋紡株式会社 熱収縮性ポリエステル系フィルム、熱収縮性ラベル、及び包装体
CN114316523A (zh) * 2020-09-30 2022-04-12 美国克罗克纳潘塔普拉斯特有限公司 热收缩膜及其制造方法
WO2022072477A1 (en) * 2020-09-30 2022-04-07 Klöckner Pentaplast Of America, Inc. Heat shrinkable films, and method of manufacturing the same
WO2022076765A1 (en) * 2020-10-08 2022-04-14 Eastman Chemical Company Shrinkable polyester films
US11891479B2 (en) 2020-11-18 2024-02-06 Klöckner Pentaplast Of America, Inc. Thermoformed packaging and methods of forming the same
US11603432B2 (en) 2020-11-18 2023-03-14 Klöckner Pentaplast Of America, Inc. Thermoformed packaging and methods of forming the same
WO2022109025A1 (en) * 2020-11-18 2022-05-27 Klöckner Pentaplast Of America, Inc. Thermoformed packaging and methods of forming the same
US12312441B2 (en) 2020-11-18 2025-05-27 Klöckner Pentaplast Of America, Inc. Thermoformed packaging and methods of forming the same
DE112021003920T5 (de) 2020-11-19 2023-05-11 Bonset America Corporation Wärmeschrumpfbare polyesterfolie
KR20230054723A (ko) 2020-11-19 2023-04-25 본셋 아메리카 코포레이션 폴리에스테르계 열 수축 필름
DE112022002485T5 (de) 2021-08-31 2024-03-07 C.I. Takiron Corporation Wärmeschrumpfbare polyesterfolie
KR20240004952A (ko) 2021-08-31 2024-01-11 다키론 씨아이 가부시키가이샤 폴리에스테르계 열 수축 필름
WO2023091544A1 (en) 2021-11-22 2023-05-25 Eastman Chemical Company Process for making recyclable copolyesters articles with living hinges
WO2023091540A1 (en) 2021-11-22 2023-05-25 Eastman Chemical Company Recyclable copolyesters articles with living hinges
WO2023163974A1 (en) * 2022-02-22 2023-08-31 Klöckner Pentaplast Of America, Inc. Bio-based thermoformed packaging and methods of forming the same
WO2023196829A1 (en) * 2022-04-06 2023-10-12 Eastman Chemical Company Multilayer shrinkable polyester films with improved toughness
US12410288B2 (en) 2022-11-30 2025-09-09 Klöckner Pentaplast Of America, Inc. Heat-shrinkable films and related systems and methods
WO2024152231A1 (en) * 2023-01-18 2024-07-25 Klöckner Pentaplast Of America, Inc. Heat-shrinkable films and related systems and methods

Also Published As

Publication number Publication date
MX2021003703A (es) 2021-06-04
US20210395446A1 (en) 2021-12-23
JP2024153767A (ja) 2024-10-29
KR20210072065A (ko) 2021-06-16
US20250011534A1 (en) 2025-01-09
JP7530370B2 (ja) 2024-08-07
EP3863832A1 (en) 2021-08-18
KR102886788B1 (ko) 2025-11-19
CN112789156A (zh) 2021-05-11
US12116452B2 (en) 2024-10-15
JP2022508653A (ja) 2022-01-19
CN117986819A (zh) 2024-05-07

Similar Documents

Publication Publication Date Title
US20250011534A1 (en) Crystallizable shrinkable films and thermoformable sheets made from reactor grade resins
EP3863831B1 (en) Crystallizable shrinkable and thermoformable sheets made from reactor grade resins
JP7698637B2 (ja) 再資源化物を有する反応器級樹脂から製造される結晶化可能な収縮性フィルムならびに熱成形性フィルムおよびシート
JP2022552207A (ja) 再資源化含量を有する結晶化可能な反応器級樹脂のための触媒システム
US20230128818A1 (en) Crystallizable shrinkable films and thermoformable sheets made from resin blends
KR20220166822A (ko) 다층 열성형성 필름 및 시트로 제조된 고온 충전 가능 물품
EP4493406A1 (en) Multilayer crystallizable shrinkable film and sheet
US20220372216A1 (en) Catalyst systems for crystallizable reactor grade resins

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 19794356

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2021544108

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 20217013768

Country of ref document: KR

Kind code of ref document: A

ENP Entry into the national phase

Ref document number: 2019794356

Country of ref document: EP

Effective date: 20210510