CA2525551A1 - Longitudinal shrink films - Google Patents
Longitudinal shrink films Download PDFInfo
- Publication number
- CA2525551A1 CA2525551A1 CA002525551A CA2525551A CA2525551A1 CA 2525551 A1 CA2525551 A1 CA 2525551A1 CA 002525551 A CA002525551 A CA 002525551A CA 2525551 A CA2525551 A CA 2525551A CA 2525551 A1 CA2525551 A1 CA 2525551A1
- Authority
- CA
- Canada
- Prior art keywords
- film
- polystyrene
- viscosity value
- polymer blend
- heat
- 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.)
- Granted
Links
Classifications
-
- 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
-
- 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
- B29C61/00—Shaping by liberation of internal stresses; Making preforms having internal stresses; Apparatus therefor
- B29C61/003—Shaping by liberation of internal stresses; Making preforms having internal stresses; Apparatus therefor characterised by the choice of material
-
- 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
-
- 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
- B29C55/28—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of blown tubular films, e.g. by inflation
-
- 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
- B29K2025/00—Use of polymers of vinyl-aromatic compounds 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
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/0088—Blends of polymers
-
- 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
- C08J2325/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Derivatives of such polymers
- C08J2325/02—Homopolymers or copolymers of hydrocarbons
- C08J2325/04—Homopolymers or copolymers of styrene
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
- Y10T428/1328—Shrinkable or shrunk [e.g., due to heat, solvent, volatile agent, restraint removal, etc.]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
- Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
Abstract
A heat-shrinkable film and a method of its manufacture are provided. In an exemplary embodiment, a polystyrene film exhibits heat-induced growth in the cross direction of great than or equal to 5% with greater than or equal to 30%
concomitant shrinkage in the machine direction. The films may comprise crystal polystyrene, high impact polystyrene, and/or elastomers. A method of manufacture is disclosed which includes a post~extrusion temperature conditioning step.
concomitant shrinkage in the machine direction. The films may comprise crystal polystyrene, high impact polystyrene, and/or elastomers. A method of manufacture is disclosed which includes a post~extrusion temperature conditioning step.
Claims (41)
1. A shrink film comprised of a polystyrene polymer blend which, upon exposure to heat, exhibits shrinkage in the length direction and controlled growth in the cross direction, thus allowing the film to exhibit reduced curling of its outer edges as the film shrinks upon exposure to heat.
2. The shrink film of claim 1 in which the film exhibits shrinkage in the length direction in the range of about 10% to about 90% and exhibits a shrinkage in the cross direction in the range of about 30% to about -30% (a negative value indicates growth) When subjected to heat in a hot air oven at 120 °C after about five minutes.
3. The shrink film of claim 2 in which the film exhibits shrinkage in the length direction of about 50% and exhibits a shrinkage in the cross direction of about -10% (a negative value indicates growth) when subjected to heat in a hot air oven at 120 °C
after about five minutes.
after about five minutes.
4. The shrink film of claim 2 in which the film exhibits shrinkage in the length direction of about 30% and exhibits a shrinkage in the cross direction of about -5% (a negative value indicates growth) when subjected to heat in a hot air oven at 120 °C
after about five minutes.
after about five minutes.
5. The shrink film of claim 2 in which the film exhibits shrinkage in the length direction of up to about 50% or greater and exhibits a shrinkage in the cross direction of up to about -10% (a negative value indicates growth) when subjected to heat in a hot air oven over a temperature range of about 220°F to about 250 °F after about five minutes.
6. The shrink film of claim 1 in which the polystyrene polymer blend includes crystal polystyrene and elastomers.
7. The shrink film of claim 1 in which the polystyrene polymer blend includes high impact polystyrene and elastomers.
8. The shrink film of claim 1 in which the polystyrene polymer blend includes crystal polystyrene, high impact polystyrene and elastomers.
9. The shrink film of claim 8 in which the polystyrene polymer blend includes 48 parts crystal polystyrene, 2 parts high impact polystyrene and 50 parts elastomers.
10. The shrink film of claim 8 in which the polystyrene polymer blend includes 33 parts crystal polystyrene, 2 parts high impact polystyrene and 65 parts elastomers.
11. The shrink film of claim 8 in which the polystyrene polymer blend includes 68 parts crystal polystyrene, 2 parts high impact polystyrene and 30 parts elastomers.
12. The shrink film of claim 8 in which the polystyrene polymer blend includes 58 parts crystal polystyrene, 2 parts high impact polystyrene and 40 parts elastomers.
13. A packaged good comprising a consumable item and a heat treated film wrapped around at least a portion of the consumable item, which heat treated film is obtained by exposing to heat a shrink film comprised of a polystyrene polymer blend which exhibits shrinkage in the length direction and controlled growth in the cross direction upon exposure to heat.
14. The packaged good of claim 13 in which the consumable item includes batteries, cans, bottles, disposable lighters, pens and decorative items.
15. The packaged good of claim 13 in which the consumable item is a battery.
16. The packaged good of claim 13 in which the heat treated film forms a perforated or non-perforated neck band around the consumable item.
17. The packaged good of claim 13 in which the heat treated film is clear, matte, translucent, or opaque.
18. The packaged good of claim 13 in which the heat treated film includes a packaging label.
19. The packaged good of claim 18 in which the packaging label is printed onto the film.
20. A method of making a shrink film comprising (a) providing pellets of a polystyrene polymer blend, (b) drying the pellets, (c) melting the pellets to form a molten mass at a first desired viscosity value or range of values, (d) increasing the viscosity of the molten mass to a second desired viscosity value or range of values, (e) stretching the resulting molten mass to form a film, and (f) annealing the resulting film.
21. The method of claim 20 in which the drying step is carried out in an air dryer.
22. The method of claim 20 in which the melting step is carried out at a temperature range of about 150 °C to about 300 °C.
23. The method of claim 22 in which the melting step is carried out at a temperature range of about 180 °C to about 270 °C.
24. The method of claim 23 in which the melting step is carried out as a temper store of about 200 °C.
25. The method of claim 20 in which the first viscosity value ranges from about 3,000 P to about 6,000 P at about 240 °C and an apparent shear rate of about 55 seconds-1.
26. The method of claim 25 in which the first viscosity value ranges from about 4,000 P to about 5,000 P at about 240 °C and about 55 seconds 1.
27. The method of claim 26 in which the first viscosity value is about 4,500 P
at about 240 °C
and about 55 seconds-1.
at about 240 °C
and about 55 seconds-1.
28. The method of claim 20 in which the second viscosity value ranges from about 16,000 P
to about 19,500 P at about 180 °C and an apparent shear rate of about 55 seconds-1.
to about 19,500 P at about 180 °C and an apparent shear rate of about 55 seconds-1.
29. The method of claim 28 in which the second viscosity value ranges from about 16,500 P
to about 18,000 P at about 180 °C and about 55 seconds-1.
to about 18,000 P at about 180 °C and about 55 seconds-1.
30. The method of claim 29 in which the second viscosity value is about 17,500 P at about 180 °C and about 55 seconds-1.
31. The method of claim 20 in which the viscosity increasing step is carried out in a polymer cooling unit.
32. The method of claim 20 in which the stretching step orients the film.
33. The method of claim 32 in which the stretching step is carried out using a blown film orientation process.
34. The method of claim 20 in which the annealing step is carried out at a temperature ranging from about 25 °C to about 200 °C.
35. The method of claim 34 in which the annealing step is carried out at a temperature ranging from about 30 °C to about 175 °C.
36. The method of claim 35 in which the annealing step is carried out at a temperature ranging from about 50 °C to about 100 °C.
37. The method of claim 36 in which the annealing step temperature is about 90 °C.
38. A method of increasing the viscosity of a polystyrene polymer blend suitable for shrink films, comprising (a) providing pellets of a polystyrene polymer blend, (b) melting the pellets to form a molten mass at a first desired viscosity value or range of values, and (c) cooling the molten mass to a second desired viscosity value or range of values in a polymer cooling unit.
39. The method of claim 38 in which the second desired viscosity value falls in the range of about two times to about ten times the first desired viscosity value.
40. The method of claim 38 in which the second desired viscosity value falls in the range of about four times to about eight times the first desired viscosity value.
41. The method of claim 38 in which the second desired viscosity value falls about six times the first desired viscosity value.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US44527203P | 2003-02-06 | 2003-02-06 | |
US60/445,272 | 2003-02-06 | ||
PCT/US2004/003200 WO2004072155A2 (en) | 2003-02-06 | 2004-02-05 | Longitudinal shrink films |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2525551A1 true CA2525551A1 (en) | 2004-08-26 |
CA2525551C CA2525551C (en) | 2012-03-27 |
Family
ID=32869329
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2525551A Expired - Fee Related CA2525551C (en) | 2003-02-06 | 2004-02-05 | Longitudinal shrink films |
Country Status (4)
Country | Link |
---|---|
US (3) | US6897260B2 (en) |
EP (1) | EP1644260A4 (en) |
CA (1) | CA2525551C (en) |
WO (1) | WO2004072155A2 (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040185235A1 (en) * | 2003-02-06 | 2004-09-23 | Philip Emery | Shrinkable battery label |
US8133558B2 (en) | 2004-08-30 | 2012-03-13 | Plastics Suppliers, Inc. | Polylactic acid blown film and method of manufacturing same |
US7846517B2 (en) * | 2005-04-19 | 2010-12-07 | Plastic Suppliers, Inc. | Polylactic acid shrink films and methods of manufacturing same |
EP1913079A1 (en) * | 2005-07-28 | 2008-04-23 | Dow Gloval Technologies Inc. | Biaxially oriented polystyrene film containing small rubber particles and low rubber particle gel content |
WO2007015245A2 (en) * | 2005-08-04 | 2007-02-08 | Polysack Plastic Industries Ltd | Thermoplastic shrinkable polymeric film |
WO2007058783A1 (en) * | 2005-11-15 | 2007-05-24 | Dow Global Technologies Inc. | Oriented multi-layer shrink labels |
ES2615341T3 (en) * | 2005-11-21 | 2017-06-06 | Plastic Suppliers, Inc. | Methods of molding shrinkable films of polylactic acid |
WO2008013542A2 (en) * | 2006-07-27 | 2008-01-31 | Dow Global Technologies Inc. | Shrink labels of oriented polystyrene film containing small rubber particles and low rubber particle gel content and block copolymers |
WO2008024170A2 (en) * | 2006-08-24 | 2008-02-28 | Dow Global Technologies Inc. | Window envelopes with scratch resistant window film patches |
JP5286763B2 (en) * | 2006-12-20 | 2013-09-11 | 東洋紡株式会社 | Heat-shrinkable polystyrene film and method for producing the same |
US8431198B2 (en) | 2007-10-02 | 2013-04-30 | Dow Global Technologies Inc. | Multilayer coextruded shrink labels of oriented polystyrene film containing small rubber particles and low rubber particle gel content and block copolymers |
US20100170618A1 (en) * | 2008-06-09 | 2010-07-08 | Keeney Sean M | Cut-and-stack label made from shrink film and related methods |
US20090301636A1 (en) * | 2008-06-09 | 2009-12-10 | Keeney Sean M | Cut-and-stack label made from shrink film and related methods |
US20090325440A1 (en) * | 2008-06-30 | 2009-12-31 | Thomas Oomman P | Films and film laminates with relatively high machine direction modulus |
EP2311734A1 (en) * | 2009-10-16 | 2011-04-20 | Ulma Packaging Technological Center, S. Coop. | Packaging machine for wrapping products or batches of products, and packaging process |
CN102120361A (en) * | 2010-01-07 | 2011-07-13 | 上海通冷挤出机有限公司 | Upwards-rotating PVC (Polyvinyl Chloride) heat shrinkable film set |
US9517611B2 (en) | 2010-02-26 | 2016-12-13 | Coveris Flexibles Us Llc | Multi-layer low temperature shrink film |
US10099435B2 (en) * | 2015-06-04 | 2018-10-16 | Ford Global Technologies, Llc | Method of splitting fiber tows |
CN114163939B (en) * | 2021-11-12 | 2023-06-30 | 东莞澳中新材料科技股份有限公司 | High-temperature-resistant high-swelling-rate oriented polystyrene swelling adhesive tape and preparation method thereof |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3557947A (en) * | 1968-04-19 | 1971-01-26 | Du Pont | Multiple container package |
US3910013A (en) * | 1974-02-13 | 1975-10-07 | Pfizer | Apparatus for applying tubular neckbands to containers |
US4333570A (en) * | 1976-06-09 | 1982-06-08 | Owens-Illinois, Inc. | Merchandising package for containers |
US4255315A (en) * | 1979-03-23 | 1981-03-10 | United States Steel Corporation | Method of making a high impact polystyrene |
US4403695A (en) * | 1982-01-06 | 1983-09-13 | Hallmark Cards, Inc. | Heat-shrinkable film wrapped packaging |
CA1191006A (en) * | 1982-01-14 | 1985-07-30 | Sekisui Kaseihin Kogyo Kabushiki Kaisha | Sheet for forming sleeve and process for producing the same |
ZA874989B (en) * | 1986-07-11 | 1988-02-24 | Sekisui Plastics | Heat-shrinkable sheet |
US5230906A (en) * | 1986-11-24 | 1993-07-27 | Polytex Plastic Sa | Method of and apparatus for manufacturing fiber-reinforced plastics articles |
US5078289A (en) * | 1990-03-15 | 1992-01-07 | Kraft General Foods, Inc. | Container with measuring cup closure |
US5851610A (en) * | 1991-02-07 | 1998-12-22 | Applied Extrusion Technologies, Inc. | Shrink films and articles including the same |
US5460878A (en) * | 1992-10-26 | 1995-10-24 | Applied Extrusion Technologies, Inc. | Heat sealable shrink laminate |
US5322664A (en) * | 1993-02-02 | 1994-06-21 | Owens-Illinois Labels Inc. | Clear film extrusion from an annular die |
JP3522791B2 (en) * | 1993-06-11 | 2004-04-26 | 三菱樹脂株式会社 | Heat-shrinkable polystyrene tube |
GB9412849D0 (en) * | 1993-08-02 | 1994-08-17 | Marketing Store Ltd | Package |
US5756577A (en) * | 1995-03-27 | 1998-05-26 | Grupo Cydsa, S.A. De C.V. | Styrene butadiene copolymer and polyolefin resins based shrink films |
CA2272081C (en) * | 1996-11-13 | 2007-12-18 | The Dow Chemical Company | Shrink film having balanced properties or improved toughness and methods of making the same |
WO1999029490A1 (en) * | 1997-12-05 | 1999-06-17 | Gunze Limited | Low temperature heat shrinkable film for labels |
JP2001315260A (en) * | 2000-03-02 | 2001-11-13 | C I Kasei Co Ltd | Heat shrinkable polyolefin film |
US7875678B2 (en) * | 2005-04-15 | 2011-01-25 | Chevron Phillips Cheimcal Company, LP | Process for making high impact strength polystyrene and related compositions |
-
2004
- 2004-02-05 CA CA2525551A patent/CA2525551C/en not_active Expired - Fee Related
- 2004-02-05 EP EP04708582A patent/EP1644260A4/en not_active Withdrawn
- 2004-02-05 US US10/771,346 patent/US6897260B2/en not_active Expired - Fee Related
- 2004-02-05 WO PCT/US2004/003200 patent/WO2004072155A2/en active Application Filing
- 2004-12-13 US US11/009,018 patent/US7101935B2/en not_active Expired - Fee Related
-
2005
- 2005-03-18 US US11/083,222 patent/US20050158492A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
WO2004072155A2 (en) | 2004-08-26 |
EP1644260A4 (en) | 2007-10-10 |
CA2525551C (en) | 2012-03-27 |
US6897260B2 (en) | 2005-05-24 |
US20050100698A1 (en) | 2005-05-12 |
US7101935B2 (en) | 2006-09-05 |
US20040242786A1 (en) | 2004-12-02 |
WO2004072155A3 (en) | 2004-11-25 |
US20050158492A1 (en) | 2005-07-21 |
EP1644260A2 (en) | 2006-04-12 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |
Effective date: 20150205 |