NO830892L - PROCEDURE FOR PREPARING A CLOSELY WRAPPING PACKAGING - Google Patents
PROCEDURE FOR PREPARING A CLOSELY WRAPPING PACKAGINGInfo
- Publication number
- NO830892L NO830892L NO830892A NO830892A NO830892L NO 830892 L NO830892 L NO 830892L NO 830892 A NO830892 A NO 830892A NO 830892 A NO830892 A NO 830892A NO 830892 L NO830892 L NO 830892L
- Authority
- NO
- Norway
- Prior art keywords
- nylon layer
- packaging
- laminate
- tubular
- layer
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 17
- 238000004806 packaging method and process Methods 0.000 title description 94
- 239000004677 Nylon Substances 0.000 claims description 67
- 229920001778 nylon Polymers 0.000 claims description 67
- 238000010438 heat treatment Methods 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 238000001816 cooling Methods 0.000 claims description 13
- 239000000853 adhesive Substances 0.000 claims description 10
- 230000001070 adhesive effect Effects 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 229920000642 polymer Polymers 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 235000013305 food Nutrition 0.000 description 18
- 238000011049 filling Methods 0.000 description 17
- 239000004698 Polyethylene Substances 0.000 description 10
- 238000001035 drying Methods 0.000 description 10
- 229920003023 plastic Polymers 0.000 description 10
- 239000004033 plastic Substances 0.000 description 10
- 235000013351 cheese Nutrition 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- 230000008602 contraction Effects 0.000 description 7
- 238000002425 crystallisation Methods 0.000 description 6
- 230000008025 crystallization Effects 0.000 description 6
- -1 polyethylene Polymers 0.000 description 6
- 229920000573 polyethylene Polymers 0.000 description 6
- 238000003860 storage Methods 0.000 description 6
- 229920003300 Plexar® Polymers 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 4
- 230000004888 barrier function Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 4
- 238000011282 treatment Methods 0.000 description 4
- 239000005977 Ethylene Substances 0.000 description 3
- 229920002292 Nylon 6 Polymers 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000002427 irreversible effect Effects 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 229920000098 polyolefin Polymers 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 229920002302 Nylon 6,6 Polymers 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 150000001244 carboxylic acid anhydrides Chemical class 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 239000005038 ethylene vinyl acetate Substances 0.000 description 2
- 229920000578 graft copolymer Polymers 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229920003189 Nylon 4,6 Polymers 0.000 description 1
- 229920003182 Surlyn® Polymers 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 1
- 235000014121 butter Nutrition 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920013716 polyethylene resin Polymers 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
-
- 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
- B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
- B29C48/10—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
-
- 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
- B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
-
- 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
- B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
- B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
- B29C48/21—Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
-
- 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
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/30—Extrusion nozzles or dies
- B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
- B29C48/335—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles
-
- 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
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
- B29C48/901—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies
- B29C48/902—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies internally
-
- 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
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
- B29C48/901—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies
- B29C48/903—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies externally
-
- 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
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/90—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
- B29C48/908—Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article characterised by calibrator surface, e.g. structure or holes for lubrication, cooling or venting
-
- 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
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/91—Heating, e.g. for cross linking
-
- 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
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/911—Cooling
- B29C48/9115—Cooling of hollow articles
- B29C48/912—Cooling of hollow articles of tubular 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
- B29C71/00—After-treatment of articles without altering their shape; Apparatus therefor
- B29C71/0009—After-treatment of articles without altering their shape; Apparatus therefor using liquids, e.g. solvents, swelling agents
-
- 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
- B29C71/00—After-treatment of articles without altering their shape; Apparatus therefor
- B29C71/02—Thermal after-treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B1/00—Layered products having a non-planar shape
- B32B1/08—Tubular products
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/34—Layered products comprising a layer of synthetic resin comprising polyamides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/06—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the heating method
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/08—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the cooling method
- B32B37/085—Quenching
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B7/00—Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
- B32B7/04—Interconnection of layers
- B32B7/12—Interconnection of layers using interposed adhesives or interposed materials with bonding properties
-
- 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
- B29C48/0019—Combinations of extrusion moulding with other shaping operations combined with shaping by flattening, folding or bending
-
- 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
- B29K2023/00—Use of polyalkenes 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
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/04—Polymers of ethylene
- B29K2023/08—Copolymers of ethylene
- B29K2023/083—EVA, i.e. ethylene vinyl acetate copolymer
-
- 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
- B29K2077/00—Use of PA, i.e. polyamides, e.g. polyesteramides 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
- B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
- B29K2995/0037—Other properties
- B29K2995/0041—Crystalline
-
- 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
- B29L2023/00—Tubular articles
- B29L2023/001—Tubular films, sleeves
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/704—Crystalline
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/70—Food packaging
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Laminated Bodies (AREA)
- Packages (AREA)
- Wrappers (AREA)
- Containers And Plastic Fillers For Packaging (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Bag Frames (AREA)
- Processing Of Meat And Fish (AREA)
Description
:Foreliggende oppfinnelse vedrører generelt rørformede nærings-jmiddelomhylninger av laminert film og mere spesielt til eri^ jomhylning som tett omslutter et næringsmiddel ekstrudert Jinh i eller stappet inn i omhylningen. The present invention generally relates to tubular food casings made of laminated film and more particularly to casings which tightly enclose a foodstuff extruded into or stuffed into the casing.
Mange næringsmidler presses inn i en omhylning under dereis I ibejarbeiding, eksempelvis kan næringsmiddelet i flytende Many foodstuffs are pressed into a casing during their processing, for example the foodstuffs can be liquid
.tilstand strømme inn under trykk i den rørformede omhylning. j(iNvrlæuéernt ltilae nev gr asmv otmyipdyhdytietslnk elreit nlfogigrekmn aen ret ee ylvbtleeetr ad errdbtlreeigyt idkerkkiae nfg yn bleellaailrgnlg rber eeis i dsdaei els gon mm. ehryFønrls .nefdokinersmgt . eedn eer r e i oonmpæshråtye-ini-g-s-middelomhylning med varm smeltet ost eller fast surmyss smør. ;Dén omhyllede ost får deretter størkne eller avbindes og under jideelle betingelser vil omhylningen være jevnt fylt med en losterull med jevn diameter. Ideelt bør disse rørformede |bmhylninger besitte materialegenskaper s^lik at de kan sies å danne "en eksakt pasning". Dette betyr at omhylningen ;evn. deformeres radielt under trykkfyllingen slik at nærings-middelrullen som dannes deri utviser en i det vesentlige 'lik diameter langs dens lengde. Ytterligere forhindres ikke jévn radiell deformasjon, som svekker omhylningen og fremmer oppsprekking og spill av matvareproduktet. Ytterligere vil .betegnelsen "eksakt pasning" innebefatte at den ideelle omhylning har dimensjonshukommelse slik at når det innførte måtvareprodukt avkjøler eller setter seg vil kontraksjon av .omhylningen være tilstrekkelig til å holde omhylningen sikkert og jevnt strukket over den krympede matvarerull i omhylningen. .state flow under pressure into the tubular casing. j(iNvrlæuéernt ltilae nev gr asmv otmyipdyhydtietslnk elreit nlfogigrekmn aen ret ee ylvbtleeetr ad errdbtlreeigyt idkerkkiae nfg yn bleellaailrgnlg rber eeis i dsdaei els gon etc. ehryFønrls .nefdokinersmgt . eedn eer melts r e in oonmpæshråtye warm-ini-g-s-medium cheese cover with butter or solid cheese .The encased cheese is then allowed to solidify or set off and under ideal conditions the encasement will be uniformly filled with a loosing roll of uniform diameter. Ideally, these tubular |bm encasements should possess material properties such that they can be said to form "an exact fit". This means that the wrapping is possibly deformed radially during pressure filling so that the food roll formed therein exhibits a substantially equal diameter along its length. Furthermore, even radial deformation is not prevented, which weakens the wrapping and promotes cracking and spillage of the food product. .the term "exact fit" implies that the ideal casing has dimensional memory sl ik that when the introduced custom food product cools or sets, contraction of the wrapping will be sufficient to keep the wrapping securely and evenly stretched over the shrunk food roll in the wrapping.
Konvensjonelt består slike omhylninger av en fibrøs omhylnj.ng bygget opp av en fibrøs bane av ikke-vevet papir, eventuelt impregnert med forskjellige syntetiske polymerer eller som er laminert for å oppnå ønskede kombinerte egenskaper for en spesiell anvendelse, såsom lav transmisjon av oksygen og vanndamp slik som eksempelvis vist i US patent nr. 4.026. 985. Ved anvendelse må disse cellulosebaserte omhylninger bløtes i varmt vann umiddelbart før fylling for å gjøre oIra-ihylningen tilstrekkelig fleksibel og elastisk for en jevn I ■if' ylling, idet omhylningen før vannbehandl.ing_en__f_o.r_el_igg.eI<r>;i|en krympet og sammenfallen konfigurasjon. Ytterligere I .jtjener vannbehandlingen til å vaske bort preserveringsmicler, jDenne type omhylninger er beheftet med en rekke ulemper'ved jat det er nødvendig med bløtning i varmt vann, idet hvis en Jiiyllingsoperasjon blir avbrutt kan de allerede oppbløttejomhylninger ikke anvendes. Conventionally, such wraps consist of a fibrous wrap built up from a fibrous web of non-woven paper, possibly impregnated with various synthetic polymers or laminated to achieve desired combined properties for a particular application, such as low transmission of oxygen and water vapour. such as, for example, shown in US patent no. 4,026. 985. When used, these cellulose-based wraps must be soaked in hot water immediately before filling to make the oIra wrap sufficiently flexible and elastic for a uniform I ■if' woolling, as the wrap before water treatment_en__f_o.r_el_igg.eI<r>;i| a shrunken and collapsed configuration. Furthermore, the water treatment serves to wash away preservation micelles, this type of wrapping is burdened with a number of disadvantages in that soaking in hot water is necessary, since if a curing operation is interrupted the already soaked wrappings cannot be used.
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'Ytterligere vil bløtevannet være en forurensningskilde oc isom følge av den høye fuktighetspermeabilitet må lagrings.-.tiden for de fylte omhylninger være relativt korte for å forhindre uttørkning av næringsmiddelet. Det er jo også vik-<i>tig å bemerke at de fylte omhylninger lett kan briste. Furthermore, the soaking water will be a source of contamination and, as a result of the high moisture permeability, the storage time for the filled casings must be relatively short in order to prevent the food from drying out. It is also important to note that the filled casings can easily burst.
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I jl^imotsetning til dette,tilveiebringer foreliggende oppfinnelse jen omhylning som ikke har noen tendens til sprøhetsbrudd men i<In contrast to this, the present invention provides a coating that has no tendency to brittleness but
|i;steden vil undergå en betydelig jevn plastisk deformas;on juten tap av det innførte næringsmiddel, hvis omhylningen jutilsiktet ifylles utover den elastiske "grense, og samtidig 'tilveiebringe en forsterket tilsynelatende elastisitet oc derved fremme en tettere og mere jevn tilpasning. Ytterligere .kan omhylningene oppfuktes i god tid før fylling men,vil ilikevel synes tørre i fuktig tilstand og skulle imidlertid omhylningene tørke ut kan de oppbløtes på ny og en eventuelt .avbrutt pakkesyklus gjentas. Instead, it will undergo a significant uniform plastic deformation due to the loss of the introduced nutrient, if the casing is intentionally filled beyond the elastic limit, and at the same time provide an enhanced apparent elasticity and thereby promote a tighter and more even fit. Furthermore. the wrappings can be moistened in good time before filling, but will still appear dry in a moist state and should the wrappings dry out, they can be re-soaked and any interrupted packaging cycle repeated.
II!henhold til oppfinnelsen vil omhylningen, som i det etter-følgende for enkelthets skyld vil bli betegnet som emballasjen omfatte et ikke fibrøst, polymert rørformet laminat med et ytre lag av krystallisert og fuktet nylon, hvorved maksimaleres det elastiske området og den elastiske grense for emballasjen samtidig holde denne i en plastisk ettergiv-ende tilstand. Ved en anvendelsesmåte lagres emballasjen i fuktige omgivelser for å forhindre uttørkning av det ytre lag av nylon. I en alternativ måte hvor emballasjen tillates |å tørke ut under lagring vil nylonlaget gjenoppfuktes før fylling. Eventuelt kan emballasjen fylles og vil derved utsettes for en fylningsbelastning som er mindre enn den i tilsynelatende elastiske grense slik at radiell deformas;on I vil være jevn langs lengden av den rørformede emballasjej According to the invention, the wrapping, which in the following for the sake of simplicity will be referred to as the packaging, comprises a non-fibrous, polymeric tubular laminate with an outer layer of crystallized and moistened nylon, thereby maximizing the elastic area and the elastic limit of the packaging at the same time keeping it in a plastic yielding state. In one application, the packaging is stored in a humid environment to prevent the outer layer of nylon from drying out. In an alternative way where the packaging is allowed to dry out during storage, the nylon layer will be re-moistened before filling. Optionally, the packaging can be filled and will thereby be subjected to a filling load that is less than that in the apparent elastic limit so that the radial deformation I will be uniform along the length of the tubular packagingj
Når det eksponerte, ytre nylonlag tørker ut vil flerlags-- emballasjen overraskende krympe jevnt hvilket ytterligere: vil føre til en elastisk fast sammentrekning over den innførte il As the exposed, outer nylon layer dries out, the multi-layer packaging will surprisingly shrink uniformly which further: will cause an elastically firm contraction over the introduced il
jmatvarerull i emballasjen. Denne kontraksjon ved uttørkning 'vi!l tilveiebringe en tilsynelatende forøkelse i emballasjens i ■ jfood rolls in the packaging. This contraction on drying will provide an apparent increase in the packaging's i ■
jelastisitet. I det tilfelle hvor det ifylte næringsmiddel jer varmt vil denne forsinkede krympning motvirke termisk jkonsentrasjon ved avkjøling a<y>det ifylte næringsmiddel og iderved tilveiebringe en rynkefri, tett emballasje. I henhold jtil et fremgangsmåtetrekk ved oppfinnelsen er det tilveie-jbragt en fremgangsmåte for fremstilling av en emballasje^med eksakt tilpasning og omfatter fremstilling av et rørformet :polymert laminat med et ytre lag av krystallisert nylon og i gel elasticity. In the case where the filled foodstuff is hot, this delayed shrinkage will counteract thermal concentration when cooling the filled foodstuff and thereby provide a wrinkle-free, tight packaging. According to a method feature of the invention, a method is provided for the production of a packaging with exact adaptation and comprises the production of a tubular polymeric laminate with an outer layer of crystallized nylon and in
joppfukte dette nylonlag. I en fordelaktig utførelsesform ,omfatter fremgangsmåten smelteformning av et blivende rør-formet polymert laminat med et ytre nylonlag, deretter brå-;kjøle og størkne det blivende rørformede laminat slik at jnylonlaget i det vesentlige gjøres amorft, samtidig med at !diameteren innstilles til ca. den forhåndsbestemte bruks--;diameter og deretter varmebehandle det rørformede laminat ifor å krystallisere nylonlaget og samtidig fukte nylonlaget !til metning. moisten this nylon layer. In an advantageous embodiment, the method includes melt forming a tubular polymer laminate with an outer nylon layer, then quenching and solidifying the tubular laminate so that the nylon layer is essentially amorphous, while the diameter is set to approx. the predetermined working diameter and then heat treat the tubular laminate to crystallize the nylon layer while simultaneously wetting the nylon layer to saturation.
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j I !henhold til oppfinnelsen er det også tilveiebragt en eksakt ^ntait lpmaesd set et emybtare llalasg jea, v omkrfyatsttaenldle iseert t røorg fofrumkettet ,ponylylmoen rot g laemti- According to the invention, an exact ^ntait lpmaesd set et emybtare llalasg jea, v omkrfyatsttaenldle iseert t røorg fofrumkettet,ponylylmoen rot g laemti-
indre fuktighetsbarrierelag. I en'fordelaktig utførelsesform ier emballasjen ytterligere særpreget ved at nylonlaget er varmekrystallisert fra en i det vesentlige amorf tilstand og samtidig mettet med vann, forutsatt av at nylonlaget ble gjort i det vesentlige amorft under en samtidig størrels^s-tilpasning av det rørformede laminat til den forhåndsbestemta ibruksdiameter, tykkelsen av nylonlaget er valgt slik at det lelastiske området for kraft-forlengelsesprofilen av emba..-jlasjen i det minste dekker området for bruksbelastningen, internal moisture barrier layer. In an advantageous embodiment, the packaging is further characterized by the fact that the nylon layer is heat crystallized from a substantially amorphous state and simultaneously saturated with water, provided that the nylon layer was made substantially amorphous during a simultaneous sizing of the tubular laminate to the predetermined in-use diameter, the thickness of the nylon layer is chosen so that the elastic range of the force-extension profile of the emba..jlass at least covers the range of the in-use load,
'i henhold til oppfinnelsen er det også tilveiebragt et abpa-råt for fremstilling av en eksakt passende matvareemballasje I !mometfa, tptoenldyme emrt idllaemr infaor t msmed eltet efoyrtmrne innyg loav nlaegt , bmliivdelnedr e froør rfo|r- According to the invention, there is also a device for the production of an exactly suitable food packaging.
Jbfåkjøling og størkning av det blivende rørformede laminat, 'Jbcooling and solidification of the resulting tubular laminate, '
. jslik at nylonlaget i det vesentlige gjøres amorft, midler. js such that the nylon layer is essentially made amorphous, means
for varmebehandling av det rørformede laminat for å krystal-i I lisere nylonlaget, samt midler for oppfuktning av nylonlaget. I en fordelaktig utførelsesform omfatter apparatet ytterligere midler for rask avkjøling av det blivende rørformede laminat samtidig som laminatets diameter innstilles til å bli tilnærmet lik den forhåndsbestemte bruksdiameter, samt midler for samtidig varmebehandling og oppfuktning av nylonlaget. for heat treatment of the tubular laminate to crystallize the nylon layer, as well as agents for moistening the nylon layer. In an advantageous embodiment, the apparatus comprises further means for rapid cooling of the becoming tubular laminate at the same time as the diameter of the laminate is set to be approximately equal to the predetermined use diameter, as well as means for simultaneous heat treatment and moistening of the nylon layer.
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Ytterligere detaljer ved oppfinnelsen vil fremgå av de ved-, ilagte tegninger hvori Further details of the invention will appear from the attached drawings in which
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[Fig. 1 viser skjematisk et flytskjema for en foretrukket [Fig. 1 schematically shows a flowchart for a preferred
■utførelsesform ved fremstilling av emballasjen ifølge opp-|finnelsen. ■embodiment when manufacturing the packaging according to the invention.
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Tig. 2 er et spennings-forlengelsesdiagram hvori er sammen-jlignet emballasjen ifølge oppfinnelsen med en konvensjonell i jfiibrøs omhylning i tørr og bløtet tilstand. Shut up. 2 is a stress-elongation diagram in which the packaging according to the invention is compared with a conventional fibrous wrapping in a dry and wet state.
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.Laminatstrukturen ifølge foreliggende oppfinnelse er rettet på en flerlags, rørformet emballasje med et ytre nylonlag ;s6m hefter til en eller flere indre lag innebefattende en •eller flere fuktighetsbarrierelag, eksempelvis er strukturen 'nylon (ytterst]./klebemiddel/barriere (innerlagl. Konvensjonelt er nylon tilstede i matemballasjelaminater for å tj^ne som en oksygenbarriere for å hindre indiffusjon av oksygen og for å tilveiebringe høy styrke til laminatet, mens et polyolefin, såsom polyetylen, EVA, såran eller surlyn, innebefattende kopolymerer og terpolymerer derav anvendes som en indre overflate som er relativt fuktighetsugjennom-itrengelig og kjemisk inert i forhold til matvarene. Det må iimidlertid understrekes at den nevnte sammensetning kun er •et eksempel og at emballasjen i henhold til oppfinnelsen jkan omfatte flere indre lag som kan velges for å oppnå ønskede sammensatte egenskaper som kan være nødvendige for en git_ The laminate structure according to the present invention is directed to a multilayer, tubular packaging with an outer nylon layer; s6m adheres to one or more inner layers including one or more moisture barrier layers, for example the structure is 'nylon (outer)/adhesive/barrier (inner layer. Conventionally nylon is present in food packaging laminates to serve as an oxygen barrier to prevent indiffusion of oxygen and to provide high strength to the laminate, while a polyolefin, such as polyethylene, EVA, wound or surlyn, including copolymers and terpolymers thereof, is used as an inner surface which is relatively impermeable to moisture and chemically inert in relation to the food. It must, however, be emphasized that the aforementioned composition is only an example and that the packaging according to the invention may comprise several inner layers which can be selected to achieve desired composite properties which may be necessary for a git_
[anvendelse, forutsatt at emballasjen er i overensstemmelse [use, provided that the packaging is in compliance
■méd oppfinnelsen. Som omtalt ovenfor er det vesentlig atj■with the invention. As discussed above, it is essential that
i il nylonlaget formes som det ytre lag av emballasjen og umiddelbart bring.e nylonlaget i en tilstand for en utvalgt varme;-^behandling, oppfuktning og tørkebetingelser. I henhold t:.l eh spesiell fordelaktig utførelsesform av oppfinnelsen sa er nylonlaget særpreget med en utvalgt krystallinsk mikro-i stiruktur, fremkalt ved et spesielt fremstillingstrinn. Dénne utvalgte mikrostruktur viser seg i en spesiell spennings-forlengelsesprofil, som vil bli omtalt i det etterfølgende og som utviser et særpreget flytepunkt og elastisk forlengelse, samt fuktighetsabsorberende egenskaper i forhold til jtidligere kjente rørformede matvareemballasjer og som i I fuktet tilstand bibeholder en plastisk, ikke-sprø egenskaper jmed betydelig plastisk forlengelse. i il the nylon layer is formed as the outer layer of the packaging and immediately bring.e the nylon layer into a condition for a selected heat;-^ treatment, moistening and drying conditions. According to a particularly advantageous embodiment of the invention, the nylon layer is characterized by a selected crystalline micro-structure, produced by a special manufacturing step. This selected microstructure manifests itself in a special stress-elongation profile, which will be discussed in the following and which exhibits a distinctive yield point and elastic elongation, as well as moisture-absorbing properties compared to previously known tubular food packaging and which in the wetted state retains a plastic, not -brittle properties with considerable plastic elongation.
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jMed hensyn til å utvikle foretrukne spennings-forlengelses-profiler i rørformede matemballasjer kan det henvises ti!. With regard to developing preferred tension-elongation profiles in tubular food packaging, reference can be made to!.
US patent nr. 4.303.711 hvori er angitt^at det elektriske ;området for en omhylning utvides til nær den ultimate ding ved valg av behandlingstrinn som innebefatter biaksjal i orientering og derved minske emballasjens evne til irrever-isibel plastisk deformasjon under trykkfylling av emballasjen. US patent no. 4,303,711 in which it is stated that the electrical range of an envelope is extended to close to the ultimate thing by choosing a treatment step that includes biaxial orientation and thereby reducing the ability of the packaging to undergo irreversible plastic deformation during pressure filling of the packaging.
(Fordelaktig består nylonlaget i emballasjen ifølge oppfinn-I eisen av en varmekrystalliserbar nylon med en fuktighetsj-'absorpsjon på minst 8%, såsom nylon 4,6 eller 66 eller mere (Advantageously, the nylon layer in the packaging according to the invention consists of a heat-crystallisable nylon with a moisture absorption of at least 8%, such as nylon 4,6 or 66 or more
'foretrukket en fuktighetsabsorpsjon på 15%. En foretrukket 1låminatstruktur for emballasjen er nylon 6 eller 6 6/Plexar/ ,polyetylen. Klebemiddelet Plexar (TM), (the-Chemplex Company) og varianter derav er beskrevet i US patentene nr. 4.087.587, ,4.087.588 og 4.303.711. Plexar 2 klebemiddel kan generell 'preferred a moisture absorption of 15%. A preferred laminate structure for the packaging is nylon 6 or 6 6/Plexar/ polyethylene. The adhesive Plexar (TM), (the-Chemplex Company) and variants thereof are described in US patents nos. 4,087,587, 4,087,588 and 4,303,711. Plexar 2 adhesive can general
karakteriseres som et klebemiddel av en type omfattende i blandinger av en podekopolymer av HD polyetylen og minst et'umettet, ringkondensert karboksylsyreanhydrid og denne is characterized as an adhesive of a type comprising mixtures of a graft copolymer of HD polyethylene and at least one unsaturated, ring-condensed carboxylic anhydride and this
i blanding med en eller flere harpikskopolymere av etylen og jetylenisk umettet ester. Plexar 3 er foretrukket i den foregående utførelsesform og omfatter blandinger av en podekopolymer av HD- polyetylen og minst et umettet, ringkondensert jkarboksylsyreanhydrid blandet med en polyetylenharpiks med<1>eh eller flere homopolymere, av. etylen,..ko.pjolyjBere__ay..._etylen in mixture with one or more resin copolymers of ethylene and ethylenic unsaturated ester. Plexar 3 is preferred in the preceding embodiment and comprises mixtures of a graft copolymer of HD polyethylene and at least one unsaturated, ring-condensed carboxylic acid anhydride mixed with a polyethylene resin with <1>eh or more homopolymers, of. ethylene,..ko.pjolyjBere__ay..._ethylene
, og et alfaolefin eller en blanding av alle disse. Mere g<;ne-- reit omfatter klebemidlene som er egnet for foreliggende oppfinnelse et kjemisk modifisert, polyolefin såsom etylen-vinylacetatpolymer, HD polyetylen og gummimodifisert med HD polyetylen, som hver er kjemisk modifisert ved tilveiebring-else av funksjonelle grupper til polymeren og som utvise]: en sterk affinitet for nylon og som vil danne en sterk bind-ing til nylon under varme og trykk ved koekstrudering, s!.ik , and an alpha olefin or a mixture of all of these. More generally, the adhesives which are suitable for the present invention comprise a chemically modified polyolefin such as ethylene-vinyl acetate polymer, HD polyethylene and rubber modified with HD polyethylene, each of which is chemically modified by providing functional groups to the polymer and which exhibit]: a strong affinity for nylon and which will form a strong bond to nylon under heat and pressure in coextrusion, s!.ik
som angitt i US patent nr. 4.233.367. En alternativ men nindre foretrukket struktur utnytter delvis teknologien beskrevet i; US patent nr. 4 .104 . 404 for "Cross-Linked Amide/ OlefinIPolymeric Tubular Film CoextrudedLaminates", hvori amid/ole-'finfilmer er angitt og som er relativt resistente mot lami-nering når de anvendes- i oppvarmet tilstand. Det anvendte klebemiddel er av den type som inneholder ved bestråling fornettbare monomere enheter, hovedbestanddelen er olefi:i-enheter med det forbehold at olefinene i klebemidlet ; er den samme som i polyolefinlaget. as set forth in US Patent No. 4,233,367. An alternative but less preferred structure partially utilizes the technology described in; US Patent No. 4,104. 404 for "Cross-Linked Amide/OlefinIPolymeric Tubular Film CoextrudedLaminates", in which amide/olefin films are indicated and which are relatively resistant to lamination when used in a heated state. The adhesive used is of the type that contains monomeric units that can be cross-linked by irradiation, the main component being olefinic units with the proviso that the olefins in the adhesive; is the same as in the polyolefin layer.
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I i !iUs' ntdi•elr linhgensmvåitsne infg or teiml bafligla. s1 jen so.m i vheinsehr old en tfiol roeptprufkiknnet elfsreneijn.-I i !iUs' ntdi•elr linhgensmvåitsne infg or teiml bafligla. s1 jen so.m i vheinsehr old en tfiol roeptprufkiknnet elfsreneijn.-
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I En flerlagsomhylning ekstruderes rørformet gjennom .en kon-Ijv-e2n4 smjo/ns emll ends ydse et 1u1t, geåeknsdeme preølvr i1s 2 meld ett en trhaekskteigs hefrt a pdå y7se,n 6<m>so</>m<s>I A multi-layer coating is extruded tubularly through a cone-Ijv-e2n4 smjo/ns emll ends ydse a 1u1t, geåeknsdeme preølvr i1s 2 meld et a trhaekskteigs hefrt a pdå y7se,n 6<m>so</>m<s>
jindikert ved 13. Det blivende rør trekkes forsiktig med press-jvalser 14 over en kalibreringsspindel 15 og gjennom en kjøle-'anordning 16 som tilveiebringer en vannkaskade fra en konvensjonell vannring, eller ved vann-nedsenkning eller sprøyting, j Ekstruderingshastigheten er tilstrekkelig slik at når det ,dannede rør føres inn i kjølesonen vil det ytre nylonlag ;forbli i en i det vesentlige amorf tilstand. Kjøléanordningen ;16 har en tilstrekkelig kapasitet til å kjøle nylonlaget:slik at dette bibeholder en ekstrudert amorf tilstand ime indicated at 13. The remaining pipe is drawn carefully with pressure rollers 14 over a calibration spindle 15 and through a cooling device 16 which provides a water cascade from a conventional water ring, or by water immersion or spraying, j The extrusion speed is sufficient so that when the formed tube is fed into the cooling zone, the outer nylon layer will remain in an essentially amorphous state. The cooling device ;16 has a sufficient capacity to cool the nylon layer: so that it maintains an extruded amorphous state ime
li nylonlaget til under dets glassovergangstemperatur. For-'trinnsvis er kalibreringsspindelen 15 avkjølt innvendig for å fremme kjøl.ehastigheten, slik som indikert med kjølemiddel-rørledningene 17. Som diskutert i det etterfølgende er d^t funnet at diameteren av spindelen 15 bør velges til tiln^_r^_ li the nylon layer to below its glass transition temperature. Preferably, the calibration spindle 15 is internally cooled to promote the cooling rate, as indicated by the coolant piping 17. As discussed below, it has been found that the diameter of the spindle 15 should be selected to
met å være lik den ønskede anvendelsesdiameter for emballasjen, dvs. lik den ønskede diameter for matvarerullen som skal inneholdes i emballasjen. Etter avkjøling faller den fremadgående omhylning sammen og trekkes gjennom pressvaL-sene 14 og føres til en etterfølgende opprullingsvalse 13. Ruller med omhylningen blir deretter varmebehandlet i nærvær av fuktighet ved en temperatur og en tid tilstrekkelig til j å krystallisere det amorfe nylonlag i emballasjen. Fortrinns-i vis utføres varmebehandlingen ved neddykning av valsen i et i met to be equal to the desired application diameter for the packaging, i.e. equal to the desired diameter for the food roll to be contained in the packaging. After cooling, the advancing wrap collapses and is pulled through the press rollers 14 and fed to a subsequent take-up roller 13. Rolls with the wrap are then heat-treated in the presence of moisture at a temperature and time sufficient to crystallize the amorphous nylon layer in the packaging. The heat treatment is preferably carried out by immersing the roll in a i
I yarmtvannsbad (ikke vist}. En slik varmebehandling utføres I fortrinnsvis i 1-12 timer, fortrinnsvis 1-4 timer avhengig In a warm water bath (not shown). Such a heat treatment is preferably carried out for 1-12 hours, preferably 1-4 hours depending
av den ønskede grad av krystallisering, vannbadets tempera-jtur er i området 80-100°C. Alternativt kan varmebehandlinger j utføres ved kontinuerlig å føre det fremførte rør direkte j gjennom et varmebehandlingsmedium før oppvikling på opptaks-I rullen slik at en kortere behandlingstid kan være passende, I representativt 1-60 min., p.g.a. den relativt raske respons of the desired degree of crystallization, the temperature of the water bath is in the range 80-100°C. Alternatively, heat treatments j can be carried out by continuously passing the advanced tube directly j through a heat treatment medium before winding on the take-up I roll so that a shorter treatment time may be appropriate, I representative 1-60 min., due to the relatively quick response
jav det eksponerte nylon til varmebehandling. Den nevnte i i fremgangsmåte er spesielt egnet for enhetsfremstilling av : emballasjen ifølge oppfinnelsen. I en alternativ fremgangs-i måte som er mindre foretrukket blir nylonlaget smeltefornet I som et enkelt ark, krystallisert og fuktet og deretter lami-! nert med det ønskede substrat og deretter formet til et 'rør eller en slange. jav the exposed nylon for heat treatment. The method mentioned in i is particularly suitable for unit production of: the packaging according to the invention. In an alternative process which is less preferred, the nylon layer is melt formed as a single sheet, crystallized and wetted and then laminated. nerted with the desired substrate and then formed into a tube or tube.
Betegnelsen "krystallinsk" er anvendt i den konvensjonelle j betydning til å angi eksistensen av et bredt område av tre-I dimensjonalt ordnede atomer eller gjentagelser i atomskalaen inne i materialet. Betegnelsen "amorf" er også anvendt i der j konvensjonelle betydning og som synonymt med betegnelsen j "ikke-krystallinsk" til å angi fravær av et bredt område av ; atomperiodisitet inne i materialet. Graden av ordnede atsmer I kan bestemmes med konvensjonelle teknikker , såsom røntgpn-i strålediffraksjonsteknikker for å bestemme sannsynlighets-itettheten for sentrale atomer. Som en første tilnærmelse kan ! et materiale karakteriseres som i det vesentlige krysta 1-' linsk hvis materiale utviser et definert smeltepunkt eller smeltepunktområde, mens et materiale kan karakteriseres bom i! det alt vesentlige hvis materialet blir mindre viskøst] vec oppvarming uten å utvise et definert smeltepunkt eller smeltepunktområde. The term "crystalline" is used in the conventional sense to denote the existence of a wide range of three-dimensionally ordered atoms or repetitions at the atomic scale within the material. The term "amorphous" is also used in its conventional sense and as synonymous with the term "non-crystalline" to denote the absence of a wide range of ; atomic periodicity inside the material. The degree of ordered atoms I can be determined by conventional techniques, such as X-ray diffraction techniques to determine the probability density of central atoms. As a first approximation can ! a material is characterized as essentially crystalline if the material exhibits a defined melting point or melting point range, while a material can be characterized as bom i! the all-important if the material becomes less viscous] vec heating without exhibiting a defined melting point or melting point range.
Emballasjene som til slutt anvendes ved fremstilling avlær-iing smiddelruller hvor et næringsmiddel av pastatypen, såsom en varm ostesmelte, fylles under trykk i emballasjen som er j oppkuttet og lukket til ønskede lengder. Emballasjen blir typisk fylt fra en rynket tilstand i et konvensjonelt rna t-varefylleapparat, eksempelvis slik som vist i US patent nr. I 4j. 3 07.48 9 som vedrører forbehandling av "gathered" embalLasje. Emballasjens fleksibilitet er av viktighet for en jevn fyl-; ling av emballasjen. I henhold til foreliggende oppfinnelse j har den nyfremstilte emballasje etter den ovenfor nevnte varmebehandling blitt omhyggelig fuktet og er således i an relativt fleksibel tilstand. Fortrinnsvis pakkes emballasjer, I kuttes og påføres kutteklips i en flattliggende stabel og The packaging that is ultimately used in the production of learning agent rolls where a pasta-type foodstuff, such as a hot melted cheese, is filled under pressure in the packaging which is j cut up and closed to desired lengths. The packaging is typically filled from a wrinkled state in a conventional rna t product filling apparatus, for example as shown in US patent no. I 4j. 3 07.48 9 which relates to pre-treatment of "gathered" packaging. The flexibility of the packaging is important for an even filling; ling of the packaging. According to the present invention j, the newly produced packaging has, after the above-mentioned heat treatment, been carefully moistened and is thus in a relatively flexible state. Preferably packaging is packed, I is cut and cutting clips are applied in a flat stack and
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lagres i omgivelser mettet med fuktighet for å forhindre ut-tørkning. Alternativt kan emballasjen hvis den får tørke ut i stored in an environment saturated with moisture to prevent drying out. Alternatively, the packaging can if it is allowed to dry out in
I under lagringstider på ny oppfuktes før den fylles for å j gjenvinne fleksibiliteten. Under ifylling vil ostesmelten J ekstruderes i den rynkede emballasje under trykk slik at I emballasjen strekkes innen sitt elastiske område og derved I during storage times is re-moisturized before filling to j regain flexibility. During filling, the cheese melt J will be extruded into the wrinkled packaging under pressure so that the packaging I is stretched within its elastic range and thereby
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! forhindre ikke-jevn plastisk deformasjon av emballasjen, !i hvilket ville føre til ujevn ifylling og ujevn form av oste-lI rullen. Fordelaktig velges tykkelsene av nylonlaget slik at i det elastiske området for spenning-forlengelsesprofilen av emballasjen i det minste dekker området for sluttanvendelses-i belastningen. ! prevent non-uniform plastic deformation of the packaging, which would lead to uneven filling and uneven shape of the cheese roll. Advantageously, the thicknesses of the nylon layer are chosen so that in the elastic range of the stress-elongation profile of the packaging at least covers the range of the end-use load.
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ben fylte emballasje blir deretter lukket med klips og får avkjøle og tørke. Sammentrekning av matvareprodukter ved ! avkjøling og setting har en tendens til å gi en mindre til-! pasning av emballasjen for rnatvareproduktet, imidlertid, vec , uttørkning av nylonlaget i emballasjen som normalt skjer i I løpet av ca. 3 0 min. vil emballasjen trekke seg sammen som bone-filled packaging is then closed with clips and allowed to cool and dry. Contraction of food products by ! cooling and setting tend to give a smaller to-! fitment of the packaging for the raw material product, however, drying out of the nylon layer in the packaging which normally occurs in the course of approx. 30 min. the packaging will contract as
i følge av gjenværende elastisitet og tørke ut og derved eliminere effekten av den termiske sammentrekning av osteruller og således oppnås en stram, rynkefri tilpasning. Det kan således sies at den nye emballasjen har en tilsynelatendje due to remaining elasticity and drying out thereby eliminating the effect of the thermal contraction of cheese rolls and thus achieving a tight, wrinkle-free fit. It can thus be said that the new packaging has a supervisory tendency
I, oemlaråsdteis. itSoem t uttiodvleir gedree t ankognivtetn, shjoovneedlt redsuefltinaetrett e av elaopsptifsiintneetlss-en I, oemlaråsdteis. itSoem t uttiodvleir gedree t ankognivtetn, shjoovneedlt redsuefltinaetrett e of elaopsptifsiintneetlss-en
innebefatter forholdet mellom diameteren for spindelen 15 oc den endelige diameter for den fylte emballasje, nemlig at diameteren for den fylte og tørkede emballasje vil være tilnærmet lik den valgte diameter for spindelen 15. Eksempelvis; includes the ratio between the diameter of the spindle 15 and the final diameter of the filled packaging, namely that the diameter of the filled and dried packaging will be approximately equal to the selected diameter of the spindle 15. For example;
emballasje fremstilt i henhold til ovenfor nevnte fremgangs--måte under anvendelse av en spindeldiameter på 82 mm og be-stående av 0,05 mm nylon g/0,01 "Plexar 3"/0,04 mm eller packaging produced according to the above-mentioned method using a spindle diameter of 82 mm and consisting of 0.05 mm nylon g/0.01 "Plexar 3"/0.04 mm or
LDPE (innerst). Den nyfremstilte emballasje etter varmete-handlingen og holdt i mettet tilstand hadde en diameter på LDPE (inside). The newly produced packaging after the heating process and kept in a saturated state had a diameter of
I 78,84 mm og etter tørkingen var diameteren 76,81 mm. Den fuktige emballasje ble fylt med en ostesmelte ved ca. 71°C til en diameter på 419 mm: Etter avkjøling og uttørkning hadde den fylte emballasje en diameter på 416 mm. Diameteren for den ferdige fylte emballasje var således meget nær lik d,en "for kalibreringsspindelen 15. Ytterligere bør det bemerkes åt emballasjen utviste en kontraksjon ved uttørkning på ca. In 78.84 mm and after drying the diameter was 76.81 mm. The moist packaging was filled with a cheese melt at approx. 71°C to a diameter of 419 mm: After cooling and drying, the filled package had a diameter of 416 mm. The diameter of the finished filled packaging was thus very close to the d,en of the calibration spindle 15. Furthermore, it should be noted that the packaging exhibited a contraction upon drying of approx.
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3%, hvilket er en betydelig andel i forhold til emballasjens elastiske område. 3%, which is a significant proportion in relation to the packaging's elastic area.
Ytterligere ble det for en flerlagsemballasje observert atFurthermore, for a multi-layer packaging it was observed that
i den undergikk kontraksjon på en enhetsmåte, dvs. hele eirbal-lasjen fulgte det ytre nylonlag uten krympedannelse eller separasjon av de enkelte lag. in it underwent contraction in a unitary manner, i.e. the entire airbal layer followed the outer nylon layer without shrinkage or separation of the individual layers.
I Sammenlignet med konvensjonelle fibrøse emballasjer har foreliggende emballasje blitt funnet å utvise betydelige ' fordeler på andre måter. Vannløsning umiddelbart før fylling elimineres hvorved det elimineres overflatevann på embal- Compared to conventional fibrous packaging, the present packaging has been found to exhibit significant advantages in other ways. Water solution immediately before filling is eliminated, thereby eliminating surface water on packaging
j lasjen. Selv om nylonlaget kan være i en mettet tilstand I vil den tilsynelatende ikke være våt, og derved eliminere j the load. Although the nylon layer may be in a saturated state I, it will apparently not be wet, thereby eliminating
! fuktige tilstander ved og rundt fyllemaskinområdet. Embal-! damp conditions at and around the filling machine area. Packaging
i! lasjen er funnet å utvise dimensjonsstabilitet langs der.s ii lengde, eksempelvis er det funnet at diameteren i fylt til- in! the load has been found to exhibit dimensional stability along its length, for example it has been found that the diameter i filled to-
<i>j stand var innen 0,5 mm toleransen og derved ga en osterull med en i det.vesentlige jevn form. I det tilfelle det elastiske området for emballasjen overskrides under ifylling vil emballasjen forlenges plastisk og ikke u ndergå sprøjjets-- <i>j stand was within the 0.5 mm tolerance and thereby produced a cheese roll with a substantially uniform shape. In the event that the elastic area of the packaging is exceeded during filling, the packaging will be plastically extended and will not undergo spraying--
brudd og derved forhindres uttrengning av matevareproduktet - og spill. Det er eksempelvis funnet at emballasjen ifølge oppfinnelsen har en typisk plastisk forlengelse på ca. 500%, breakage and thereby preventing leakage of the food product - and spillage. It has been found, for example, that the packaging according to the invention has a typical plastic extension of approx. 500%,
sammenlignet med en forlengelse på 20% for den ovenfor nevnte konvensjonelle emballasje. Ved lagring vil matevare-innholdet ikke uttørke vesentlig fordi emballasjen ifølge oppfinnelsen er ikke-porøst og muliggjør således en betydelig lagringstid. Den fuktige tilstand for emballasjen ifølge oppfinnelsen er reversibel slik at emballasjen kan gjenfuktes før fylling i det tilfellet emballasjen har tørket ut under l lagring. Da denne prosess er reversibel for emballasjen ifølge<1>oppfinnelsen vil tap av emballasje forhindres i det tilfellet hvor matvareifyllingsprosessen avbrytes over■et lengre tids-rom. Ytterligere som følge av den fremhevede, tilsynelatende elastisitet for emballasje så gir denne et tett "secone skin fit" og matvareproduktet inneholdt i emballasjen vil oppnå en tiltalende, halvbland overflate etter at emballasje- compared to an extension of 20% for the above-mentioned conventional packaging. During storage, the food content will not dry out significantly because the packaging according to the invention is non-porous and thus enables a considerable storage time. The moist state of the packaging according to the invention is reversible so that the packaging can be remoistened before filling in the event that the packaging has dried out during storage. As this process is reversible for the packaging according to the <1>invention, loss of packaging will be prevented in the case where the food filling process is interrupted over a longer period of time. Furthermore, as a result of the highlighted, apparent elasticity of the packaging, this provides a tight "secone skin fit" and the food product contained in the packaging will achieve an appealing, semi-mixed surface after the packaging
materialet er fjernet fra matvarerullen.the material has been removed from the food roll.
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I I fig. 2 er vist kraft-forlengelsesprofliler i tverr-ret-ningen innen det elektriske området hvori sammenlignes en emballasje i henhold til oppfinnelsen med en konvensjonell j ikke-vevet fibrøs emballasje. Kurvene A og B viser, den ! elastiske forlengelse av en konvensjonell emballasje i hen- I I fig. 2 shows force-elongation profiles in the transverse direction within the electrical range in which a packaging according to the invention is compared with a conventional j non-woven fibrous packaging. Curves A and B show, the ! elastic extension of a conventional packaging in
i holdsvis tørr og våt tilstand. Den konvensjonelle embal-in dry and wet conditions respectively. The conventional packaging
j i lasje må fylles i våt tilstand og er relativt utsatt for over-i belastning og sprekking fordi kurven B ligger vesentlig under i j i lage must be filled in a wet state and is relatively exposed to over-i loading and cracking because the curve B lies significantly below i
!kurven A. Kurven C er typisk for den fuktede emballasje ifølge oppfinnelsen og kan sees å være sammenlignbar med den vesentlige sterkere konvensjonelle emballasje i tørr j tilstand. Curve A. Curve C is typical for the moistened packaging according to the invention and can be seen to be comparable to the substantially stronger conventional packaging in a dry state.
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i Det er flere trekk ved oppfinnelsen som er av betydning,i There are several features of the invention that are important,
j Som ovenfor angitt har emballasjen ifølge oppfinnelsen et iI forsterket tilsynelatende elastisitetsområde som manifesterer S seg ved at det oppfuktede ytre nylonlag av den fylte embal- j As stated above, the packaging according to the invention has an iI reinforced apparent elasticity area which manifests itself in that the moistened outer nylon layer of the filled packaging
ii lasje tørker.ut og krymper og derved fremmer en tett, jevn j tilpasning. Et annet trekk vedrører den forbedrede flytej-!. grense og forsterkede • elastiske området som tilskrives} The layer dries out and shrinks, thereby promoting a tight, even fit. Another feature relates to the improved flow rate. limit and reinforced • elastic area attributed}
iden krystalliserende varmebehandling som ovenfor omtalt.during crystallizing heat treatment as discussed above.
Hver av disse forbedringer tjener til å utstrekke det ,elastiske området av emballasjen og--derved fremme dimensjor.s-stabilitet under fylling, dvs. mindre mulighet for ikke-jevn, plastisk irreversibel deformering eller utbuling av den fylte emballasje. Det er en fordel at dette fremhevede ei lastiske området ikke skjer på bekostning av plastisk fJor-lengelse i det tilfellet hvor emballasjen utilsiktet blir overbelastet, i hvilket tilfelle emballasjen vil gi seg plastisk og ikke sprøtt. Det er antatt at de fordelaktige I mekaniske egenskaper for emballasjen ifølge oppfinnelser, Each of these improvements serves to extend the elastic range of the packaging and thereby promote dimensional stability during filling, i.e. less possibility of non-uniform, plastically irreversible deformation or bulging of the filled packaging. It is an advantage that this highlighted elastic area does not occur at the expense of plastic elongation in the case where the packaging is inadvertently overloaded, in which case the packaging will yield plastic and not brittle. It is believed that the advantageous I mechanical properties of the packaging according to inventions,
ytterligere kan forsterkes av den måten krystalliseringe:ncan be further enhanced by the manner of crystallization
av det ytre nylonlag utføres på. For det første i en foretrukket utf ørelsesf orm krystalliseres nylonlaget ved gjein-oppvarmning fra den i det vesentlige faste amorfe, avkjølte tilstand i motsetning til krystallisering fra en smelte. of the outer nylon layer is performed on. Firstly, in a preferred embodiment, the nylon layer is crystallized by reheating from the essentially solid amorphous, cooled state as opposed to crystallization from a melt.
Og ikke minst så er det tilveiebragt en meget reproduserbar fremgangsmåte for fremstilling av emballasjen ved at beting- And not least, a highly reproducible method for producing the packaging has been provided by conditionally
i eisene for nylonlaget like før varmebehandlingen er velc.ef i - ! i hiert. For det andre utføres krystalliseringsvarmebehandl.ingen 1 i nærvær av fuktighet noe som er antatt a ha en innvirkning på krystalliseringsprosessen såvel som å fremme en høy fuk- in the ices for the nylon layer just before the heat treatment is velc.ef i - ! in here. Secondly, the crystallization heat treatment 1 is carried out in the presence of moisture, which is believed to have an impact on the crystallization process as well as to promote a high moisture
j tighetsabsorpsjon og plastisitet til nylonlaget. Mere generelt omfatter oppfinnelsen i sitt bredeste omfang krystallisering av det ytre nylonlag for å fremme de mekaniske i egenskaper i det elastiske området og oppfuktning av nylonlaget for å fremme den elastiske fleksibilitet og.plastiske ! forlengbarhet for å tilveiebringe en ytterligere tilsynelatende elastisitet ved uttørkning, med det overraskende totale j resultat at flerlagsemballasjen utviser disse egenskaper for det ytre nylonlag på en i det vesentlige enhetlig måte. j density absorption and plasticity of the nylon layer. More generally, the invention encompasses in its broadest scope crystallization of the outer nylon layer to promote the mechanical properties in the elastic range and moistening of the nylon layer to promote the elastic flexibility and.plastic ! extensibility to provide additional apparent elasticity upon desiccation, with the surprising overall j result that the multi-layer packaging exhibits these properties for the outer nylon layer in a substantially uniform manner.
<1>I tabell I er vist en sammenligning av de mekaniske egen-<1>Table I shows a comparison of the mechanical properties
i skaper mellom en prøve av emballasjen med et ytre nylonlag , i forhold til en prøve med et nylonlag inne i et emballåsje- between a sample of the packaging with an outer nylon layer, in relation to a sample with a nylon layer inside a packaging lock-
' laminat. Emballasjeprøvene ble fremstilt i det vesentlige' laminate. The packaging samples were essentially produced
i henhold tii den ovenfor beskrevne foretrukne metode slik at de respektive nylonlag opprinnelig var i en i det velent-lige amorf tilstand....Sanmienligningen._bl.e_.gjori^jed_7_l°cJ according to the above-described preferred method so that the respective nylon layers were originally in an essentially amorphous state...
I som er en typisk temperatur ved varm fylling. Emballasjen merket SDX244 bestod av et laminat med strukturen:"nylon 6 I which is a typical temperature for hot filling. The packaging marked SDX244 consisted of a laminate with the structure: "nylon 6
(ytterstl/bindemiddel/PE/bindemiddel/PE, og hvor nylonle.get var 0,05 mm tykt og den totale tykkelse av laminatet vai' 6,10 mm. Prøven merket SDX246 hadde en totaltykkelse på (external/binder/PE/binder/PE, and where the nylon layer was 0.05 mm thick and the total thickness of the laminate was 6.10 mm. The sample labeled SDX246 had a total thickness of
0,10 mm og nylonlaget en tykkelse på 0,05 mm, som for den foregående prøve, men hadde strukturen: PE/klebemiddel/ 0.10 mm and the nylon layer a thickness of 0.05 mm, as for the previous sample, but had the structure: PE/adhesive/
nylon 6/klebemiddel/PE. I tabellen er vist data for flyte-sjtyrke.og forlengelse ved flytning for betingelse A som er ikke varmebehandlet, tørr tilstand, for tilstand B som ii ndikerer varmebehandling i et varmt vannbad ved 82 oC i 1 min. og for tilstand C som indikerer varmebehandling i varm _ vann ved 82°C i 1 time. Betegnelsen "flytestyrke" må forstås i den konvensjonelle betydning som angir spenningsverdien som danner en liten, irreversibel deformasjon eller setning i materialet. Flytestyrken ble bestemt under anvendelse av nylon 6/adhesive/PE. The table shows data for yield strength and elongation at yield for condition A which is not heat treated, dry condition, for condition B which indicates heat treatment in a hot water bath at 82 oC for 1 min. and for condition C indicating heat treatment in hot _ water at 82°C for 1 hour. The term "yield strength" must be understood in the conventional sense that indicates the stress value that produces a small, irreversible deformation or settlement in the material. The yield strength was determined using
I i en konvensjonell kraft-forlengelse bruddlastmaskin "Instron"<1>hvor en prøve strekkes under konstant forlengelseshastighet j og hvor kraft og forlengelse måles. Prøvene var strimler j med en bredde på 2,5 cm og 10 cm lange og ble trukket med ei i konstant klemmehastighet på ca. 5 cm/min. Prøven merket SDX244 med et ytre nylonlag kan sees å reagere raskt på varmebehana-ljingen, dvs. innen et minutt slik det fremgår ved å sammen-ligne kolonnene A og B. Ved ytterligere fortsatt varmebehandling kan det sees at etter en time oppnås en vesentlig forøkning i ytterligere flytestyrke såvel som forlengelse : ved flytning. I motsetning til dette kan det for prøven ! merket SDX24 6 som har et indre nylonlag som ikke er direkte i eksponert til varmt vann under varmebehandlingen så oppnås ! det i det vesentlige ingen effekt i løpet av 1 min. Etter , 1 time kan det sees at en viss effekt har funnet sted. Det ér vesentlig at som det fremgår av prøven merket SDX24 4 med et ytre nylonlag, i henhold til oppfinnelsen, viser en betydelig respons til varmebehandlingen i løpet av meget kort tid. Det bør bemerkes at 1 standard avvik for hver prøvi-betingelse er angitt i parentes og viser at den statistiske spredning av-prøveresultatene var relativ snever, hvilket j indikerer god reproduserbarhet for prøven. I tabell II ér !. den samme sammenligning utført ved 23°C, hvilket ga detJ In a conventional force-elongation breaking load machine "Instron"<1>where a sample is stretched under constant extension rate j and where force and extension are measured. The samples were strips j with a width of 2.5 cm and a length of 10 cm and were drawn with ei at a constant clamping speed of approx. 5 cm/min. The sample labeled SDX244 with an outer nylon layer can be seen to react quickly to the heat treatment, i.e. within a minute as can be seen by comparing columns A and B. With further continued heat treatment it can be seen that after one hour a significant increase is achieved in further buoyancy as well as elongation : by displacement. In contrast, it can for the sample ! marked SDX24 6 which has an inner nylon layer which is not directly exposed to hot water during the heat treatment then is achieved ! essentially no effect within 1 min. After , 1 hour it can be seen that a certain effect has taken place. It is significant that, as can be seen from the sample marked SDX24 4 with an outer nylon layer, according to the invention, shows a significant response to the heat treatment within a very short time. It should be noted that 1 standard deviation for each test condition is given in parentheses and shows that the statistical spread of the test results was relatively narrow, indicating good reproducibility of the test. In table II is !. the same comparison carried out at 23°C, which gave itJ
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US35755082A | 1982-03-15 | 1982-03-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| NO830892L true NO830892L (en) | 1983-09-16 |
Family
ID=23406074
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO830892A NO830892L (en) | 1982-03-15 | 1983-03-14 | PROCEDURE FOR PREPARING A CLOSELY WRAPPING PACKAGING |
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| Country | Link |
|---|---|
| JP (3) | JPS58168524A (en) |
| AT (1) | AT382498B (en) |
| AU (1) | AU565829B2 (en) |
| BR (1) | BR8300782A (en) |
| DE (1) | DE3308296A1 (en) |
| DK (1) | DK119183A (en) |
| FR (1) | FR2523031B1 (en) |
| GB (1) | GB2117702B (en) |
| IL (1) | IL68112A0 (en) |
| IT (1) | IT1194163B (en) |
| NL (1) | NL8300515A (en) |
| NO (1) | NO830892L (en) |
| NZ (1) | NZ203558A (en) |
| ZA (1) | ZA83848B (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3436682A1 (en) * | 1984-10-05 | 1986-04-10 | Hoechst Ag, 6230 Frankfurt | TUBULAR PACKING SLEEVE, ESPECIALLY SAUSAGE SLEEVE, ON A POLYAMIDE BASE |
| DE3845009B4 (en) * | 1987-05-21 | 2004-03-11 | Gunze Ltd., Ayabe | Food packaging multilayer plastics film |
| DE3908585A1 (en) | 1989-03-16 | 1990-09-27 | Pi Patente Gmbh | VACUUM PACKING HOSE MADE OF A WELDABLE MATERIAL |
| DE4001131C2 (en) * | 1990-01-17 | 1999-04-08 | Hoechst Ag | Multi-layer artificial sausage casing based on polyamide |
| DE19932836A1 (en) * | 1999-07-14 | 2001-01-25 | Christof Stimpfl | Method and apparatus for making elongated food |
| JP2010208163A (en) * | 2009-03-10 | 2010-09-24 | Sekisui Chem Co Ltd | Multilayered olefin pipe |
| JP5879618B2 (en) * | 2011-07-25 | 2016-03-08 | Mics化学株式会社 | Method for producing low warpage multilayer film |
| JP6251891B2 (en) * | 2014-01-09 | 2017-12-27 | Mics化学株式会社 | Method for producing low warpage multilayer film |
| JP6645019B2 (en) * | 2015-03-23 | 2020-02-12 | 住友ベークライト株式会社 | Multilayer film and package |
| CN109275689B (en) * | 2017-07-20 | 2023-09-29 | 维斯克凡科技(苏州)有限公司 | Method for obtaining a tender-to-bite artificial collagen casing and casing obtained by said method |
| CN118163391B (en) * | 2024-04-01 | 2024-08-16 | 宁波艾德生仪器有限公司 | Energy-saving nylon humidifying and toughening treatment box |
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| DE1404350A1 (en) * | 1958-06-02 | 1968-10-03 | Dow Chemical Co | Manufacture of tubular thermoplastic films |
| US4048428A (en) * | 1961-12-05 | 1977-09-13 | W. R. Grace & Co. | Method for preparing a film of vinylidene chloride polymer |
| FR1313689A (en) * | 1962-02-06 | 1962-12-28 | Grace W R & Co | Polyolefin extrusion process |
| FR1428171A (en) * | 1965-02-23 | 1966-02-11 | Chemical Investors Sa | Polyamide film production process |
| FR1473550A (en) * | 1965-03-26 | 1967-03-17 | Allied Chem | Improved polyamide films having reduced haze and method of preparation thereof |
| DE1901634A1 (en) * | 1969-03-13 | 1970-08-13 | Standard Packaging Corp | Laminated film material, process for its manufacture and its use |
| US3873667A (en) * | 1971-03-18 | 1975-03-25 | Continental Can Co | Process for preparing articles fabricated from polyolefin/polyamide blends having low permeability to gases |
| US3741253A (en) * | 1971-03-30 | 1973-06-26 | Grace W R & Co | Laminates of ethylene vinyl acetate polymers and polymers of vinylidene chloride |
| GB1398853A (en) * | 1971-11-17 | 1975-06-25 | Ici Ltd | Production of polymeric films |
| JPS5734784B2 (en) * | 1972-12-30 | 1982-07-24 | ||
| DE2352553C3 (en) * | 1973-10-19 | 1979-03-22 | Alkor-Werk Karl Lissmann Gmbh & Co Kg, 8000 Muenchen | Use of a PA-PE composite hose as a sausage casing for cooked sausages |
| AR207667A1 (en) * | 1974-12-23 | 1976-10-22 | Grace W R & Co | PROCEDURE TO OBTAIN ORIENTED POLYAMIDE LAMINATES AND THE LAMINATE SO OBTAINED |
| JPS5179192A (en) * | 1974-12-28 | 1976-07-09 | Nippon Petrochemicals Co Ltd | Tasofuirumuno seizohoho |
| US3997383A (en) * | 1975-03-10 | 1976-12-14 | W. R. Grace & Co. | Cross-linked amide/olefin polymeric laminates |
| DE2559318C3 (en) * | 1975-12-31 | 1979-11-29 | Naturin-Werk Becker & Co, 6940 Weinheim | Use of an elastic polyurethane for producing an at least one-layer, optionally biaxially stretched sausage casing for cooked and scalded sausages |
| US4131137A (en) * | 1976-12-23 | 1978-12-26 | Union Carbide Corporation | Composite tubular casing for processed foods and method of fabricating the casing |
| US4233367A (en) * | 1977-01-06 | 1980-11-11 | American Can Company | Coextruded multilayer film |
| DE2724252C2 (en) * | 1977-05-28 | 1982-12-16 | Hoechst Ag, 6000 Frankfurt | Tubular packaging material, preferably for use as a sausage casing |
| JPS5935332B2 (en) * | 1977-07-29 | 1984-08-28 | 三菱化学株式会社 | Multilayer film manufacturing method |
| CA1111372A (en) * | 1978-07-03 | 1981-10-27 | Henry G. Schirmer | Cross-linked nylon/polyolefin laminates |
| JPS6035257B2 (en) * | 1978-07-22 | 1985-08-13 | 三菱樹脂株式会社 | Process dome packaging materials |
| DE2903117A1 (en) * | 1979-01-27 | 1980-08-14 | Wolff Walsrode Ag | COUPLED TUBULAR SLEEVE, METHOD FOR THE PRODUCTION THEREOF, DEVICE FOR EXERCISING THE METHOD AND USE OF THE HOSE SLEEVE AS A PACKAGING MEANS |
| JPS5611250A (en) * | 1979-07-09 | 1981-02-04 | Daicel Ltd | Packing material |
| JPS5631257A (en) * | 1979-08-22 | 1981-03-30 | Nec Corp | Noise eliminating circuit |
| JPS6037796B2 (en) * | 1979-12-11 | 1985-08-28 | 東洋製罐株式会社 | Transparent laminated film container and its manufacturing method |
| JPS56131135A (en) * | 1980-03-13 | 1981-10-14 | Sumitomo Bakelite Co | Package |
-
1983
- 1983-02-08 ZA ZA83848A patent/ZA83848B/en unknown
- 1983-02-11 NL NL8300515A patent/NL8300515A/en not_active Application Discontinuation
- 1983-02-18 BR BR8300782A patent/BR8300782A/en not_active IP Right Cessation
- 1983-03-09 DE DE19833308296 patent/DE3308296A1/en not_active Ceased
- 1983-03-09 GB GB08306464A patent/GB2117702B/en not_active Expired
- 1983-03-13 IL IL68112A patent/IL68112A0/en unknown
- 1983-03-14 NO NO830892A patent/NO830892L/en unknown
- 1983-03-14 JP JP58040856A patent/JPS58168524A/en active Pending
- 1983-03-14 DK DK119183A patent/DK119183A/en not_active Application Discontinuation
- 1983-03-14 NZ NZ203558A patent/NZ203558A/en unknown
- 1983-03-14 FR FR8304156A patent/FR2523031B1/en not_active Expired
- 1983-03-15 AT AT0091883A patent/AT382498B/en not_active IP Right Cessation
- 1983-03-15 IT IT20087/83A patent/IT1194163B/en active
- 1983-03-15 AU AU12473/83A patent/AU565829B2/en not_active Ceased
-
1990
- 1990-11-30 JP JP2331000A patent/JPH03200555A/en active Pending
- 1990-11-30 JP JP2330999A patent/JPH03187743A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| ZA83848B (en) | 1984-08-29 |
| AU1247383A (en) | 1983-09-22 |
| NZ203558A (en) | 1986-03-14 |
| NL8300515A (en) | 1983-10-03 |
| GB2117702A (en) | 1983-10-19 |
| GB8306464D0 (en) | 1983-04-13 |
| JPH03187743A (en) | 1991-08-15 |
| IL68112A0 (en) | 1983-06-15 |
| BR8300782A (en) | 1983-11-16 |
| DK119183D0 (en) | 1983-03-14 |
| JPH03200555A (en) | 1991-09-02 |
| FR2523031B1 (en) | 1988-04-15 |
| JPS58168524A (en) | 1983-10-04 |
| DK119183A (en) | 1983-09-16 |
| GB2117702B (en) | 1985-10-02 |
| DE3308296A1 (en) | 1983-09-15 |
| IT8320087A0 (en) | 1983-03-15 |
| ATA91883A (en) | 1986-08-15 |
| JPH0443783B2 (en) | 1992-07-17 |
| IT8320087A1 (en) | 1984-09-15 |
| FR2523031A1 (en) | 1983-09-16 |
| AT382498B (en) | 1987-02-25 |
| AU565829B2 (en) | 1987-10-01 |
| IT1194163B (en) | 1988-09-14 |
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