JPH0443783B2 - - Google Patents

Info

Publication number
JPH0443783B2
JPH0443783B2 JP2330999A JP33099990A JPH0443783B2 JP H0443783 B2 JPH0443783 B2 JP H0443783B2 JP 2330999 A JP2330999 A JP 2330999A JP 33099990 A JP33099990 A JP 33099990A JP H0443783 B2 JPH0443783 B2 JP H0443783B2
Authority
JP
Japan
Prior art keywords
nylon
package
laminate
tubular
layer
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.)
Expired - Lifetime
Application number
JP2330999A
Other languages
Japanese (ja)
Other versions
JPH03187743A (en
Inventor
Jooji Shaamaa Hanrii
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
WR Grace and Co
Original Assignee
WR Grace and Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by WR Grace and Co filed Critical WR Grace and Co
Publication of JPH03187743A publication Critical patent/JPH03187743A/en
Publication of JPH0443783B2 publication Critical patent/JPH0443783B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered 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
    • B32B27/08Layered 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion 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
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion 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
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/16Articles comprising two or more components, e.g. co-extruded layers
    • B29C48/18Articles comprising two or more components, e.g. co-extruded layers the components being layers
    • B29C48/21Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/32Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
    • B29C48/335Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/90Thermal 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
    • B29C48/901Thermal 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
    • B29C48/902Thermal 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/90Thermal 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
    • B29C48/901Thermal 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
    • B29C48/903Thermal 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/90Thermal 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
    • B29C48/908Thermal 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/91Heating, e.g. for cross linking
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9115Cooling of hollow articles
    • B29C48/912Cooling of hollow articles of tubular films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C71/00After-treatment of articles without altering their shape; Apparatus therefor
    • B29C71/0009After-treatment of articles without altering their shape; Apparatus therefor using liquids, e.g. solvents, swelling agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C71/00After-treatment of articles without altering their shape; Apparatus therefor
    • B29C71/02Thermal after-treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B1/00Layered products having a general shape other than plane
    • B32B1/08Tubular products
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/34Layered products comprising a layer of synthetic resin comprising polyamides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B37/00Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
    • B32B37/06Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the heating method
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B37/00Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
    • B32B37/08Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the cooling method
    • B32B37/085Quenching
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00Layered 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
    • B32B7/04Interconnection of layers
    • B32B7/12Interconnection of layers using interposed adhesives or interposed materials with bonding properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0018Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0019Combinations of extrusion moulding with other shaping operations combined with shaping by flattening, folding or bending
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING 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
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING 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
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/08Copolymers of ethylene
    • B29K2023/083EVA, i.e. ethylene vinyl acetate copolymer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING 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
    • B29K2077/00Use of PA, i.e. polyamides, e.g. polyesteramides or derivatives thereof, as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING 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
    • B29K2995/00Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037Other properties
    • B29K2995/0041Crystalline
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2023/00Tubular articles
    • B29L2023/001Tubular films, sleeves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/704Crystalline
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2439/00Containers; Receptacles
    • B32B2439/70Food packaging

Description

【発明の詳細な説明】[Detailed description of the invention]

産業上の利用分野 本発明は一般に、積層フイルムから成る管状の
食品用包装体に関し、更に詳細には、包装体中に
押出されあるいは詰められた食料品をきつちりと
包むことができる包装体に関する。 従来の技術及び発明が解決しようとする問題点 多くの加工食品は、その加工の間に包装体中に
詰められる、即ち、食品が流動状態にある間に圧
力下に管状の包装体中に流入させられる。食料品
は包装体中に含まれている間に更に加工されるこ
ともあるし、あるいは後の加工又は販売まで包装
体内に貯蔵されることもある。例えば、チーズロ
ールは一般に、管状の食品用包装体中に加熱チー
ズ溶融物又は固体カードチーズを加圧充填するこ
とによつて形成される。包まれたチーズを次いで
固化させるか又は引き締めるが、理想的な条件下
では、包装体は均一な直径のチーズロールを形成
するように均一に充填される。 理想的には、これらの管状の包装体は、「厳密
適合」を形成するといわれるような材料特性を有
している。これは、加圧充填の間に包装体が半径
方向に均一に変形して、その結果包装体内に形成
される食品のロールがその長さに沿つて実質的に
均一な直径を有していることを意味する。更に包
装体を弱めその張り裂けと食品のはみ出しを助長
するおそれがある半径的に不均一な変形が防がれ
る。その上、「厳密適合」という用語は、理想的
な包装体は、詰めた食料品を冷却又は引き締める
ときに、包装体の収縮が包装体内に含まれた縮ん
だ食品のロール上にしつかりと且つ均一に伸びた
状態で包装体を保持するのに十分であるような寸
法的な記憶を有していることをも意味する。 通常、このような包装体は一般に、米国特許第
4026985号によつて代表的に示されているように、
場合によつては、例えば酸素及び水蒸気の低透過
率というような、特定の用途に対して必要な複合
性を与えるために種々の合成重合体で含浸又は積
層してある、不織紙の繊維ウエブから成る。使用
に際して、これらのセルロース性の包装体は、し
わのよつた状態から均一な充填に対して充分に柔
軟且つ弾性的な状態にするために、及び保存剤を
洗い去るために、充填前に短時間熱水中に浸漬し
なければならない。熱水浸漬を必要とするので、
万一作業が中止になつた場合に、浸漬した包装体
を保存しておくことができないという点で、この
種の包装体の使用には多くの欠点がある。更に、
水が汚染源となり、且つ、比較的高い水分透過性
のために、食品を詰めた包装体の保存期間は食品
の乾燥を防ぐために比較的短期でなければならな
い。これらの充填した包装体が脆性破壊によつて
破れる可能性があることも重大な問題である。 問題点を解決するための手段 上記の問題は、本発明により、結晶化され含湿
したナイロンの外層と、内側の防湿層とを有する
管状の溶融成形した重合体状積層物から成り、該
ナイロンは実質的に無定形状態から加熱結晶化さ
れ旦つ同時に湿らされることを特徴とする厳密適
合食品用包装体によつて解決される。 本発明により、更に、 a ナイロンの外層を有する管状の重合体状積層
物を溶融形成し、 b 該ナイロンを実質的に無定形にならしめるよ
うに、該発生期の管状の積層物を冷却しそして
固化させ、 c 該管状の積層物を熱処理して、該ナイロンを
実質的に結晶化させ、そして、 d 該ナイロンを湿らせる ことから成る厳密適合食品用包装体の製造方法が
提供される。 更に、本発明により、 a ナイロンの外層を有する管状の重合体状積層
物を溶融形成する手段と、 b 該ナイロンを実質的に無定形にならしめるよ
うに、該発生期の管状の積層物を冷却しそして
固化させる手段と、 c 該管状の積層物を熱処理して、該ナイロンを
実質的に結晶化させる手段と、 d 該ナイロンを湿らせる手段、 とから成ることを特徴とする厳密適合食品用包装
体の製造装置が提供される。 本発明の包装体は、脆性破壊を生じるおそれが
なく、包装体にその弾性限界を超えて不適当に充
填した場合にも、詰めた食料がこぼれ出ることの
ない極めて均一な可塑性変形を生じる一方、増大
した見掛けの弾性を与え、それによつて、きつち
りした、一層均一な適合を増進することができ
る。その上、本発明の包装体は、充填に先んじて
よく湿らすことができ、しかも湿つた状態でも乾
燥しているように見える。しかしながら、若し包
装体が保存中に完全に乾燥してしまつたとして
も、それを再び浸漬することができ、それ故再び
使用することが可能である。 かくして、本発明の包装体は、結晶化し且つ湿
らしたナイロンの外層を有する非繊維質重合体の
管状積層物を包含しており、それによつて塑性的
な破壊モードを維持しながら包装体の弾性範囲及
び弾性限界を最大とする。一使用方法において
は、ナイロンの外層の完全な乾燥を防ぐために包
装体を湿つた環境中で保存する。保存中の完全な
乾燥が許される別の方法においては、食品を詰め
る前にナイロン層を最び湿らせる。包装体には食
品が詰め込まれ、その際、半径方向の変形が管状
の包装体の長さに沿つて均一となるように、ほぼ
その弾性限界よりも小さい詰め込み負荷が与えら
れる。露出した外層のナイロンが乾いたときに、
多層包装体は意外なことに均一に収縮し、かくし
て中に入つている詰め込んだ食品のロール上で更
に弾性的にきつく張られた状態となる。乾燥時の
この収縮は、実際上、包装体の弾性の見掛けの増
大を与える。食品の詰め物が熱い場合には、この
遅延した収縮が食品の詰め物の冷却時の熱的な収
縮を相殺し、それによつてしわのないきつちりし
た包装を与える。 本発明の積層構造物は、1層以上の防湿層を包
含する1層以上の内側層上に接着した外側のナイ
ロン層を有する多層管状食品用包装体、例えばナ
イロン(外層)/接着剤/バリヤー(内層)構造
物である。通常、酸素の内側への拡散を阻止する
ための酸素バリヤーとして役立たせるため及び積
層物に比較的高い強度を付与するためにナイロン
を食品用包装体積層物中に存在させ、一方、例え
ばポリエチレンのようなポリオレフイン、EVA、
サラン、又はナイロン及びそれらの共重合体及び
三元重合体が、比較的水分不透過性で且つ多くの
食料品に対して化学的に不活性である内側表面と
して用いられている。しかしながら、上記の複合
物配置は一例であること、及び本発明の包装体
は、本発明の基本的な特色に依存して、用途にお
ける必要に応じて望ましい複合性能を達成するよ
うに選ぶことができる多数の内層をも包含し得る
ということは重要である。後述するように、選択
した熱処理、湿気の付与及び乾燥条件に即応する
ように、包装体の外層としてナイロン層を形成せ
しめることが肝要である。本発明の特に有利な方
式においては、ナイロンは更に、選択した加工工
程によつて発現する選択された結晶の微細構造に
よつて特徴付けられる。この選択された微細構造
は、同じく後述するように、選択した応力−歪み
曲線によつて明らかにされるが、湿つた状態にお
いて大きな塑性伸びを有する塑性的な非脆性破壊
モードを保持しながら、従来の管状食品用包装体
と比較して、増大した降伏点と弾性伸び及び吸湿
性を示す。管状の食品用包装体における選択され
た応力−歪み曲線の発現の問題について一般的な
興味のあるものとしては米国特許第4303711号の
包装体があるが、この特許は包装体の弾性領域を
2軸配向を含む選択した加工工程によつて最大応
力の近くまで拡大し、それによつて加圧充填中の
包装体の不可逆的な塑性変形の受け易さを減少さ
せることを開示している。 本発明の包装体のナイロン層は、例えばナイロ
ン4,6又は66のような、少なくとも約8%、
更に好ましくは約15%の吸水性を有する加熱によ
り結晶化し得るナイロンから成ることが有利であ
る。包装体のための好適な積層構造物は、ナイロ
ン6又は66/プレクサー/ポリエチレンであ
る。接着剤プレクサー(商標)はケムプレツクス
社から市販されている。プレクサーの各品種は参
考としてここに挙げる前記米国特許第4087587号、
4087588号及び4303711号に記されている。プレク
サー2は一般に高密度ポリエチレンと少なくとも
1種の不飽和の縮合環カルボン酸無水物のグラフ
ト共重合体、及びエチレンとエチレン性不飽和エ
ステルの1種以上の樹脂共重合体のブレンド物か
ら成る種類の接着剤として特徴付けられる。プレ
クサー3が前記実施形態において好適であつて、
これは1種以上のエチレンのホモポリマー、エチ
レンとアルフアーオレフインの共重合体又はこれ
らの何れかあるいは全部から成るポリエチレン樹
脂とブレンドされた高密度ポリエチレン及び少な
くとも1種の不飽和縮合環カルボン酸無水物のグ
ラフト共重合体のブレンド物から成る。更に一般
的には、本発明において適当な接着剤は、ナイロ
ンに対して強い親和性を有し且つ例えば米国特許
第4233367号に示されるように共押出しの加熱及
び圧力下においてナイロンへの強い結合を形成す
る官能基を重合体に供与することによつてそれぞ
れ化学的に変性した、エチレン−酢酸ビニル共重
合体、高密度ポリエチレン及びゴム変性高密度ポ
リエチレンから成るグループから選択された、化
学的に変性したポリオレフインから成るものであ
る。好適性は低いが、代替的な構造物は、「架橋
したアミド/オレフイン重合体管状フイルム共押
出し積層物」についての米国特許第4104404号に
記された技術を部分的に応用している。参考のた
めにここに挙げたこの特許においては、加熱条件
において使用する場合に比較的耐剥離性が大きい
アミド/オレフインフイルムを開示している。用
いている接着剤は、照射によつて架橋し得る単量
体単位を有し且つオレフイン単位を主成分として
いる種類のものであり、更に接着剤中のオレフイ
ンとポリオレフイン層中のオレフインは同一であ
ることを必要としている。 以下図面に基づいて本発明を詳細に説明する。 第1図は本発明の包装体の製造のための好適方
法を概念的に示している。13で示すように、管
12をダイから軽く引張るようにしながら多層包
装体を通常のダイ11を通じて、例えば約25〜80
フイート/分(約7.6〜24.4m/分)の速度で、
管状に共押出しする。管12は、ニツプローラー
14によつて、寸法定めのマンドレル15の上を
且つ通常の水環からの流下水により又は注水ある
いは噴霧により冷却を提供する冷却手段16の間
で、軽く引張られる。押出し速度は、管12が外
側のナイロン層を実質的に無定形の状態に保つた
まま冷却区域に入るのに充分なものとする。冷却
手段16は、押出したときのナイロン内の無定形
状態を保つたままナイロン層をそのガラス転移温
度より低くまで急冷するのに充分な能力を有して
いる。寸法定めのマンドレル15を、冷却速度を
増大させるために、冷却剤管路17で示すよう
に、内部的に冷却することが好ましい。後に更に
説明するように、マンドレル15の直径は、包装
体について所望する最終の使用直径に従つて、即
ち内部に入れる食品ロールの所望直径に従つて、
概ね選択する。冷却後に、進行する包装体をニツ
プローラー14の間でつぶし且つ引張り、次いで
連続的に巻取りロール18へと送る。次いで包装
体のロールを、湿気の存在下で包装体中の無定形
ナイロン層を実質的に結晶化させるのに充分な温
度及び時間で、熱処理する。熱処理は充填したロ
ールを熱水浴(図中に示してない)中へ浸漬する
ことによつて行なうことが好ましい。典型的に
は、このような熱処理は、望ましい結晶化の程度
に依存して、約1〜12時間、好ましくは約1〜4
時間にわたり、且つ約180〜212〓(約82〜100℃)
の範囲の温度で継続する。別法として、熱処理
は、巻取りロール上に巻く前に、進行する管を直
接熱処理媒体中に連続的に通すことによつて行な
うこともできるが、この場合には熱処理にさらさ
れるナイロンの比較的急速な応答によつて、一般
に約1分乃至1時間の短かい処理時間が適当であ
る。前述した方法は、本発明の包装体の一元的な
成形に対して特に適している。別法では、好適性
は低いけれども、ナイロン層を単独層のシートと
して溶融成形し、結晶化させそして含湿させ、所
望の基材と積層したのち、管状に成形することが
できる。 「結晶性」という用語は通常の意味で用いら
れ、材料内に長い範囲の三次元的原子配列即ち原
子的規模での周期性の存在を意味する。「無定形」
という用語は同じく通常の意味で用いられ、「非
結晶性」という表現と同義語であり、材料内に長
い範囲の原子の周期性の不在を意味する。原子配
列の程度は、例えば放射状の原子確率密度を測定
するためのX線回析方法によるような通常の方法
によつて決定することができる。第一近似とし
て、材料が一定の溶融温度又は範囲を有している
場合には実質的に結晶性として特徴付けることが
でき、一方、材料が加熱して一定の融点又は範囲
を示すことなく徐々に粘度が低くなる場合には、
その材料を実質的に無定形として特徴付けること
ができる。 包装体は最終的に食品のロールの形成のために
用いられるが、この場合、例えば熱いチーズ溶融
物のようなペースト状の食品を、所望の長さに切
断しそしてクリツプで留めた包装体中に圧力下に
詰め込む。包装体は一般に、例えば折り畳んだ包
装体の予備処理に対しての米国特許第4307489号
に示すような、通常の食品充填装置を用いて、折
り畳み状態から詰める。この場合、包装体の柔軟
性が包装体の均一な充填のために重要であるもの
と思われる。本発明においては、上記の熱処理段
階の後の未充填の包装体は充分に湿つており、か
くして比較的柔軟な状態にある。包装体を平らに
置いた積み重ねとして束ね、切断し且つ留めて乾
燥を防ぐために実質的に飽和した湿つた環境中で
保存することが好ましい。あるいは、貯蔵中に包
装体の完全な乾燥を許す場合には、詰める前に包
装体を再び湿らして柔軟性を回復させる。詰める
ときには、チーズの溶融物を圧力下に、包装体が
その弾性範囲内の応力を受け、それによつて不均
一な充填及び不規則なチーズロールの形成を伴な
う包装体の不均一な塑性的変形を防ぐような具合
に、包装体中に押出す。ナイロン層の厚さは、包
装体の力−伸び曲線の弾性範囲が最終使用充填物
の範囲と少なくともほぼ同じとなるように選ぶ。 次いで詰めた包装体をクリツプで留め、冷却し
そして乾燥する。冷却又は熱処理における食料品
の収縮は、食料品上の包装体の適合をゆるめる傾
向がある。しかしながら例えば約0.5時間で生じ
る包装体のナイロン層の完全乾燥によつて、残留
する弾性と乾燥のために包装体が収縮し、それに
よつてチーズロールの熱的な収縮を相殺して、き
つちりしたしわのない適合を維持する。かくし
て、包装体は普通に定義するような弾性範囲を超
える増大した見掛けの弾性を有しているものとい
うことができる。前述のように、本発明の鍵とな
る結果は、マンドレル15の直径と最終的に充填
した包装体の直径の間の関係、即ち充填しそして
乾燥した包装体の直径が選択されたマンドレル1
5の直径とほぼ等しいということにかかわりがあ
る。例えば、3.243インチ(約82.37mm)の直径を
有するマンドレルを用いて2ミル(約0.051mm)
のナイロン6/0.5ミル(約0.013mm)のプレクサ
ー3/1.5ミル(約0.038mm)のLDPE(内層)の複
合構造を有する包装体を上記の方法によつて製造
する。熱処理後の飽和状態を保つた新鮮な包装体
は3.104インチ(約78.84mm)の直径を有し、乾燥
後には3.024インチ(約76.81mm)の直径を有す
る。湿つている包装体中に約160〓(約71.1℃)
のチーズ溶融物を3.275インチ(約83.19mm)の直
径にて詰める。冷却しそして乾燥した後の充填し
た包装体は3.25インチ(約82.55mm)の直径を有
する。かくして、最後的に充填された包装体の直
径は、寸法を定めるためのマンドレル15の直径
と極めて近似している。更に、包装体が包装体の
弾性範囲に対して約3%という実質的な量の乾燥
収縮を示すということに注目すべきである。その
上、多層包装体が一元的な具合にこの収縮を行な
うということ、即ち、しわや成分層間の分離を生
じることなしに全包装体が外側のナイロン層に追
従することが認められる。 更に、本発明の包装体は、従来の繊維質包装体
と比較して、その他の点でもかなりの利点を有し
ているこのが認められた。充填直前の水中浸漬の
必要がなくなり、それによつて包装体の表面上の
水が除かれる。ナイロンが飽和した状態にあつた
としても見たところでは湿つているように見え
ず、そのために充填装置の区域の周辺における湿
つた状態を除くことができる。包装体はその長さ
に亙り寸法安定性を有していることが認められ、
例えば、充填後の直径は0.02インチ(約0.51mm)
の許容差内にあり、それ故実質的に均一なチーズ
ロールを形成することが認められている。充填中
に包装体の弾性範囲を超える場合においても、包
装体は塑性的に伸びて脆性破壊を生じることがな
く、それ故食品が包装体から吹き出て廃物となる
ことがない。例えば、本発明の包装体は前記の従
来の包装体に対する約20%の伸びと対照的に、約
500%の典型的な塑性伸びを有することが認めら
れている。本発明の包装体は非多孔性であるため
に貯蔵中に食料が著るしく乾燥することがなく、
それによつてかなりの貯蔵寿命が与えられる。本
発明の包装体の含湿状態は可逆的であるから、貯
蔵中に包装体が完全に乾燥した場合には食品を詰
める前に再び湿らせることができる。この工程は
本発明の包装体に対して可逆的であるから、食品
の充填工程をかなりの時間に亙つて中断する場合
にも包装体の無駄を防ぐことができる。最後に、
ぴつたりした第二の皮膚状の適合を与える包装体
の増大した見掛けの弾性のために、その中に入れ
られた食料品は、食品ロールから包装体をはいだ
後にも、見ばのよい半光沢性の表面を有してい
る。 第2図に、弾性領域における横方向の力−伸び
曲線を、上記の本発明の包装体の実施例を従来の
不織繊維質の包装体と比較して示す。曲線A及び
Bは、それぞれ、乾燥及び湿潤状態における従来
の包装体の弾性応答を示している。従来の包装体
は湿つた状態で詰めなければならず、それ故、曲
線Bが曲線Aよりも著るしく下方にあることから
みて、過充填による破裂を比較的生じやすい。曲
線Cは典型的な本発明の含湿包装体の弾性曲線で
あるが、これは乾燥状態における従来の包装体の
極めて高い強度に匹敵することが認められる。 本発明には強調すべき幾つかの特色がある。前
記のように、本発明の包装体は、充填した包装体
の湿つた外部ナイロン層が乾燥して収縮するとき
に表われそしてそれによつてぴつたりした均一な
適合を増進する、増大した見掛けの弾性範囲を有
している。もう1つの特色は、前記のように結晶
化熱処理によつて生じる増大した降伏強さと増大
した弾性範囲である。これらの増大は、それぞれ
包装体の弾性範囲を拡げ、それによつて充填中の
寸法安定性を増進する、即ち、充填した包装体の
不均一な塑性的で不可逆変形又は膨らみの受け易
さを低下させるように働らく。弾性範囲のこの増
大は、しかしながら、たとえ包装体をうつかり過
充填したとしても塑性性伸びを犠性にすることが
なく、この場合、包装体は脆性破壊的ではなく可
塑的に破れる。本発明の包装体の有利な機械的性
質は外側のナイロン層の結晶化の仕方によつて更
に増進させることができる。第一に、好適方式に
おいては、溶融物からの結晶化と異なつて、実質
的に固体無定形の冷却した状態からの再加熱によ
つてナイロンを結晶化させる。少なくとも、熱処
理の直前のナイロンの性質が一定であるという点
で包装体の製造のための極めて再現性のある方法
を提供する。第二に、結晶化のための熱処理は水
分の存在で行なうことが好ましく、水は結晶化の
仕方及びナイロンの高い吸水性と可塑性の望まし
い増進に影響するものと思われる。更に一般的
に、本発明の広い特色は、弾性範囲における機械
的性質を増進させるための外側ナイロン層の結晶
化、及び塑性的柔軟性並びに塑性的伸張性を増進
し且つ乾燥時の付加的な見掛けの弾性を提供する
ためのナイロン層への水分付与を包含するが、こ
のとき多層包装体は実質的に一元的にナイロン外
層のこれらの性質を表わすという全体的な結果を
もたらす。 第1表中に、ナイロン外層を有する包装体試料
と、包装体積層物の内側にナイロン層を有する試
料との間の機械的性質の比較を示す。包装体試料
は実質的に上記の好適方法に従つて製造し、それ
故、それぞれのナイロン層は最初に実質的に無定
形の状態にあつた。比較は一般的な熱充填温度で
ある160〓(約71.7℃)で行なつた。SDX244型の
包装体はナイロン6(外層)/接着剤/PE/接
着剤/PEの構造を有する積層物から成り、ナイ
ロン層の厚さは2ミル(約0.051mm)であり積層
物全体の厚さは4ミル(約0.102mm)であつた。
SDX246型の試料は上記試料と同じく4ミル(約
0.102mm)の全体的な厚さと2ミル(約0.051mm)
のナイロン層の厚さを有するが、その構造は
PE/接着剤/ナイロン6/接着剤/PEであつ
た。表中のデータは、それぞれ、未熱処理の乾燥
状態である状態A、180〓(約82℃)の熱水浴中
で1分の熱処理を示す状態B、及び180〓(約82
℃)の熱水中で1時間の熱処理を示す状態Cに対
する、降伏強さ及び降伏時の伸びを示している。
「降伏強さ」という用語は通常の意味で用いられ、
試験材料中に小さな不可逆的な変形即ち永久歪み
を生じる応力値を示すものとする。降伏強さは一
定の伸張速度で試料を伸張して増大する伸びの値
と共に力の測定値を記録するインストロン型の通
常の力−伸び引張試験機を用いて測定した。試料
は幅1インチ(約25.4mm)、長さ4インチ(約102
mm)の帯状とし、1分当り約2インチ(約50.8
mm)の一定のクロスヘツド速度で引張つた。ナイ
ロン外層を有するSDX244型試料は、状態A及び
Bの比較によつて明らかなように、迅速に、即ち
1分以内に熱処理に応答することがわかる。更に
熱処理を続けると、1時間後に降伏強さと降伏時
の伸びの何れについても、実質的な増加が更に達
成されることが認められる。これに対して、熱水
熱処理に対して直接暴されることがない内側のナ
イロン層を有するSDX246型の試料においては、
1分間以内では実質的に何の効果もない。1時間
後に多少の効果が生じることが認められる。本質
的に、本発明に従がうナイロン外層を有する
SDX244型の試料は、極めて短時間で熱処理に対
する劇的な反応を有することが認められる。括弧
内に示した各試験状態に対する標準偏差は、試料
の挙動が比較的不変であることを指示する狭い統
計的拡がりを有していることに注目すべきであ
る。第2表中で、同様な比較を73〓(約23℃)で
行なつて、同様な全般的な結果が得られた。
INDUSTRIAL APPLICATION FIELD OF THE INVENTION This invention relates generally to tubular food packages made of laminated films, and more particularly to packages capable of tightly enclosing food products extruded or stuffed into the package. . PRIOR ART AND PROBLEMS TO BE SOLVED BY THE INVENTION Many processed foods are packed into packages during their processing, that is, flowed under pressure into tubular packages while the food is in a fluid state. I am made to do so. The food product may be further processed while contained in the package, or may be stored within the package until further processing or sale. For example, cheese rolls are commonly formed by pressure filling a heated cheese melt or solid curd cheese into a tubular food package. The wrapped cheese is then allowed to solidify or tighten; under ideal conditions, the package is evenly filled to form a cheese roll of uniform diameter. Ideally, these tubular packages have material properties that are said to form a "close fit." This is due to the uniform radial deformation of the package during pressure filling so that the roll of food product formed within the package has a substantially uniform diameter along its length. It means that. Furthermore, radially non-uniform deformations which could weaken the package and encourage its tearing and extrusion of the food product are prevented. Furthermore, the term "close fit" means that an ideal package would allow the shrinkage of the package to cling onto the shrunken food roll contained within the package as the packaged food product cools or tightens. It is also meant to have a dimensional memory sufficient to hold the package in a uniformly stretched state. Typically, such packaging is generally referred to as U.S. Pat.
As exemplified by No. 4026985,
Nonwoven paper fibers, in some cases impregnated or laminated with various synthetic polymers to provide the required composite properties for specific applications, such as low oxygen and water vapor permeability. Consists of the web. In use, these cellulosic packages are briefly blanched before filling to bring them from a wrinkled state to a sufficiently flexible and elastic state for uniform filling, and to wash away preservatives. Must be soaked in hot water for an hour. Because it requires hot water immersion,
The use of this type of packaging has a number of disadvantages, in that it is not possible to save the soaked packaging in the event that the operation is stopped. Furthermore,
Because water is a source of contamination and because of its relatively high moisture permeability, the shelf life of packages filled with food must be relatively short to prevent the food from drying out. The potential for these filled packages to break due to brittle fracture is also a significant problem. Means for Solving the Problems The above problems are solved in accordance with the present invention, which comprises a tubular melt-formed polymeric laminate having an outer layer of crystallized, moistened nylon and an inner moisture barrier layer, the nylon is solved by a closely conforming food packaging which is characterized in that it is heated and crystallized from a substantially amorphous state and simultaneously moistened. The invention further comprises: a) melt forming a tubular polymeric laminate having an outer layer of nylon, and b cooling the nascent tubular laminate so as to render the nylon substantially amorphous. c. heat treating the tubular laminate to substantially crystallize the nylon; and d. wetting the nylon. The invention further provides: a) means for melt forming a tubular polymeric laminate having an outer layer of nylon; and b) forming the nascent tubular laminate so as to render the nylon substantially amorphous. a means for cooling and solidifying; c) means for heat treating the tubular laminate to substantially crystallize the nylon; and d) a means for moistening the nylon. An apparatus for manufacturing a packaging body for use in a vehicle is provided. The packaging of the present invention is free from the risk of brittle fracture, and even if the packaging is improperly filled beyond its elastic limit, it will undergo extremely uniform plastic deformation without spilling of the packed food. , can provide increased apparent elasticity, thereby promoting a tighter, more uniform fit. Furthermore, the packaging of the present invention can be well moistened prior to filling and yet appears dry even when wet. However, even if the package becomes completely dry during storage, it can be soaked again and therefore used again. Thus, the package of the present invention includes a tubular laminate of non-fibrous polymer with an outer layer of crystallized and moistened nylon, thereby increasing the elasticity of the package while maintaining a plastic failure mode. Maximize range and elastic limit. In one method of use, the package is stored in a humid environment to prevent complete drying of the nylon outer layer. In another method, which allows complete drying during storage, the nylon layer is moistened to the maximum before packaging the food product. The package is stuffed with the food product, with a stuffing load approximately below its elastic limit so that the radial deformation is uniform along the length of the tubular package. When the exposed outer layer of nylon dries,
The multilayer packaging surprisingly shrinks uniformly and thus becomes more elastically taut over the roll of stuffed food contained therein. This shrinkage upon drying actually provides an apparent increase in the elasticity of the package. When the food stuffing is hot, this delayed shrinkage offsets the thermal shrinkage of the food stuffing as it cools, thereby providing a tight, wrinkle-free package. The laminate structure of the present invention comprises a multilayer tubular food package having an outer nylon layer bonded onto one or more inner layers including one or more moisture barrier layers, e.g. nylon (outer layer)/adhesive/barrier. (inner layer) structure. Typically, nylon is present in food packaging laminates to serve as an oxygen barrier to prevent oxygen from diffusing inward and to impart relatively high strength to the laminate, whereas for example polyethylene Polyolefin, EVA, etc.
Saran, or nylon and their copolymers and terpolymers, have been used as inner surfaces that are relatively moisture impermeable and chemically inert to many food products. However, it should be noted that the composite arrangement described above is an example, and that the packaging of the invention can be chosen to achieve the desired composite performance as needed in the application, depending on the basic features of the invention. Importantly, it can also include as many internal layers as possible. As will be discussed below, it is important that the nylon layer be formed as the outer layer of the package so as to be responsive to the selected heat treatment, humidification and drying conditions. In a particularly advantageous manner of the invention, the nylon is further characterized by a selected crystalline microstructure developed by the selected processing steps. This selected microstructure, also explained below, is revealed by selected stress-strain curves, while retaining a plastic non-brittle failure mode with large plastic elongation in the wet state. Exhibits increased yield point, elastic elongation and hygroscopicity compared to conventional tubular food packaging. Of general interest in the question of the development of selected stress-strain curves in tubular food packages is the package of U.S. Pat. It is disclosed that selected processing steps, including axial orientation, can increase near maximum stresses, thereby reducing the susceptibility of the package to irreversible plastic deformation during pressure filling. The nylon layer of the package of the present invention comprises at least about 8%, such as nylon 4, 6 or 66,
More preferably, it is made of nylon which can be crystallized by heating and has a water absorption of about 15%. A preferred laminate construction for the package is nylon 6 or 66/plexer/polyethylene. Adhesive Plexor™ is commercially available from Chemplex Corporation. Various varieties of Plexor are described in US Pat. No. 4,087,587, which is hereby incorporated by reference.
Nos. 4087588 and 4303711. Plexer 2 is generally of the type consisting of a blend of a graft copolymer of high density polyethylene and at least one unsaturated fused ring carboxylic acid anhydride, and a resin copolymer of ethylene and one or more ethylenically unsaturated esters. It is characterized as an adhesive. Plexer 3 is preferred in the embodiment, and
This is a high-density polyethylene blended with one or more homopolymers of ethylene, copolymers of ethylene and alpha olefin, or polyethylene resins consisting of any or all of these, and at least one unsaturated fused ring carboxylic acid anhydride. It consists of a blend of graft copolymers of More generally, adhesives suitable in the present invention have a strong affinity for nylon and exhibit strong bonding to nylon under the heat and pressure of coextrusion, as shown for example in U.S. Pat. No. 4,233,367. ethylene-vinyl acetate copolymers, high-density polyethylene, and rubber-modified high-density polyethylene, each chemically modified by donating functional groups to the polymer to form It is made of modified polyolefin. Although less preferred, an alternative construction partially adapts the technology described in US Pat. No. 4,104,404 for "Crosslinked Amide/Olefin Polymer Tubular Film Coextrusion Laminate." This patent, incorporated herein by reference, discloses amide/olefin films that have relatively high peel resistance when used in heated conditions. The adhesive used has a monomer unit that can be crosslinked by irradiation and is mainly composed of olefin units, and furthermore, the olefin in the adhesive and the olefin in the polyolefin layer are the same. need something. The present invention will be explained in detail below based on the drawings. FIG. 1 conceptually illustrates a preferred method for manufacturing the packaging of the present invention. As shown at 13, the multilayer package is passed through a conventional die 11 while gently pulling the tube 12 out of the die, e.g.
At a speed of feet/min (approx. 7.6 to 24.4 m/min),
Coextrude into a tube. The tube 12 is pulled lightly by a nip roller 14 over a sized mandrel 15 and between cooling means 16 which provide cooling by running water from a conventional water ring or by water injection or spraying. The extrusion speed is sufficient to allow the tube 12 to enter the cooling zone while keeping the outer nylon layer substantially amorphous. The cooling means 16 has sufficient capacity to rapidly cool the nylon layer below its glass transition temperature while preserving the amorphous state within the nylon as extruded. Preferably, the sized mandrel 15 is cooled internally, as shown by coolant lines 17, to increase the cooling rate. As will be explained further below, the diameter of the mandrel 15 is determined according to the desired final use diameter of the package, i.e. according to the desired diameter of the food roll placed therein.
Generally selected. After cooling, the advancing package is crushed and pulled between nip rollers 14 and then continuously fed to take-up rolls 18. The roll of wrapper is then heat treated in the presence of moisture at a temperature and time sufficient to substantially crystallize the amorphous nylon layer in the wrapper. Preferably, the heat treatment is carried out by immersing the filled roll in a hot water bath (not shown). Typically, such heat treatment is for about 1 to 12 hours, preferably about 1 to 4 hours, depending on the degree of crystallization desired.
over an hour and approximately 180~212〓 (approximately 82~100℃)
Continue at temperatures in the range of. Alternatively, the heat treatment may be carried out by continuously passing the advancing tube directly through the heat treatment medium before winding onto a take-up roll, but in this case the nylon exposed to the heat treatment Due to the rapid response, short processing times of about 1 minute to 1 hour are generally appropriate. The method described above is particularly suitable for the integral shaping of the packaging according to the invention. Alternatively, although less preferred, the nylon layer can be melt-formed as a single layer sheet, crystallized and moistened, laminated with the desired substrate, and then formed into a tube. The term "crystalline" is used in its conventional sense and refers to the presence of long-range three-dimensional atomic arrangements or periodicity on the atomic scale within a material. "Amorphous"
The term is also used in its usual sense and is synonymous with the expression "amorphous", meaning the absence of long range atomic periodicity within the material. The degree of atomic alignment can be determined by conventional methods, such as by X-ray diffraction methods for measuring the radial atomic probability density. As a first approximation, a material can be characterized as substantially crystalline if it has a constant melting temperature or range, whereas a material can be heated gradually without exhibiting a constant melting point or range. If the viscosity decreases,
The material can be characterized as substantially amorphous. The package is ultimately used to form a roll of food, in which case a pasty food product, such as a hot cheese melt, is cut into the desired length and clipped into the package. Pack under pressure. Packages are generally filled from the folded state using conventional food filling equipment, such as that shown in US Pat. No. 4,307,489 for pre-treatment of folded packages. In this case, the flexibility of the package appears to be important for uniform filling of the package. In the present invention, the unfilled package after the heat treatment step described above is sufficiently moist and thus in a relatively flexible state. Preferably, the packages are bundled, cut and secured in a flat stack and stored in a substantially saturated, humid environment to prevent desiccation. Alternatively, if the package is allowed to dry completely during storage, the package can be rewetted to restore flexibility before filling. When packing, when the cheese melt is put under pressure, the package is subjected to stresses within its elastic range, thereby causing uneven plasticity of the package with uneven filling and the formation of irregular cheese rolls. extruded into the package in such a way as to prevent physical deformation. The thickness of the nylon layer is selected such that the elastic range of the force-elongation curve of the package is at least approximately the same as the range of the end-use fill. The filled package is then clipped, cooled and dried. Shrinkage of the food product upon cooling or heat treatment tends to loosen the fit of the package on the food product. However, complete drying of the nylon layer of the package, which occurs for example in about 0.5 hours, causes the package to shrink due to residual elasticity and dryness, thereby offsetting the thermal shrinkage of the cheese roll and making it tighter. Maintains a wrinkle-free fit. Thus, the package can be said to have increased apparent elasticity beyond the normally defined elastic range. As previously mentioned, a key result of the present invention is the relationship between the diameter of the mandrel 15 and the diameter of the final filled package, i.e. the diameter of the filled and dried package depends on the selected mandrel 1.
This is related to the fact that it is approximately equal to the diameter of 5. For example, using a mandrel with a diameter of 3.243 inches,
A package having a composite structure of Nylon 6/0.5 mil Plexor 3/1.5 mil LDPE (inner layer) is manufactured by the method described above. The fresh saturated package after heat treatment has a diameter of 3.104 inches and after drying has a diameter of 3.024 inches. Approximately 160〓 (approximately 71.1℃) in a damp package
of cheese melt to a diameter of 3.275 inches. After cooling and drying, the filled package has a diameter of 3.25 inches. The diameter of the final filled package is thus very similar to the diameter of the sizing mandrel 15. Additionally, it should be noted that the package exhibits a substantial amount of drying shrinkage of about 3% relative to the elastic range of the package. Moreover, it is observed that the multilayer package performs this contraction in a unitary manner, ie, the entire package follows the outer nylon layer without wrinkling or separation between the component layers. Additionally, the packaging of the present invention has been found to have significant other advantages over conventional fibrous packaging. The need for immersion in water immediately before filling is eliminated, thereby removing water on the surface of the package. Even when the nylon is saturated, it does not appear visually wet, thereby eliminating damp conditions around the area of the filling device. The package is found to be dimensionally stable over its length,
For example, the diameter after filling is 0.02 inch (approximately 0.51 mm)
has been found to be within tolerances of , thus forming substantially uniform cheese rolls. Even if the elastic range of the package is exceeded during filling, the package will not stretch plastically and cause brittle fracture, and therefore the food will not blow out of the package and become waste. For example, the wraps of the present invention have an elongation of about 20% for the conventional wraps mentioned above.
It is recognized to have a typical plastic elongation of 500%. Since the packaging body of the present invention is non-porous, the food will not dry out significantly during storage.
This provides a considerable shelf life. The moisture content of the packaging according to the invention is reversible, so that if the packaging has completely dried out during storage, it can be re-moistened before being filled with food. Since this process is reversible for the packaging of the present invention, waste of the packaging can be prevented even if the food filling process is interrupted for a considerable period of time. lastly,
Because of the increased apparent elasticity of the wrapper that provides a tight second skin-like fit, the food product placed therein remains in an aesthetically pleasing semi-finished state even after the wrapper is removed from the food roll. It has a glossy surface. FIG. 2 shows the lateral force-elongation curves in the elastic region for the embodiment of the inventive package described above in comparison with a conventional non-woven fibrous package. Curves A and B show the elastic response of conventional packaging in dry and wet conditions, respectively. Conventional packages must be packed wet and are therefore relatively prone to bursting due to overfilling, given that curve B is significantly lower than curve A. Curve C is the elasticity curve of a typical wet package of the invention, which is found to be comparable to the extremely high strength of conventional packages in the dry state. There are several features of the invention that are worth highlighting. As noted above, the wrappers of the present invention exhibit increased apparent density that is revealed as the wet outer nylon layer of the filled wrapper dries and shrinks, thereby promoting a tight and uniform fit. It has an elastic range. Another feature is the increased yield strength and increased elastic range produced by the crystallization heat treatment as described above. These increases each extend the elastic range of the package, thereby increasing its dimensional stability during filling, i.e. reducing the susceptibility of the filled package to uneven plastic and irreversible deformation or bulging. I work to make people do what they want. This increase in elastic range, however, does not come at the expense of plastic elongation, even if the package is bent and overfilled, in which case the package ruptures plastically rather than brittlely. The advantageous mechanical properties of the packaging according to the invention can be further enhanced by the manner in which the outer nylon layer is crystallized. First, in a preferred manner, the nylon is crystallized by reheating from a substantially solid, amorphous, cooled state, as opposed to crystallizing from a melt. At least in that the properties of the nylon immediately before heat treatment are constant, it provides a highly reproducible method for manufacturing the packaging. Second, the heat treatment for crystallization is preferably carried out in the presence of moisture, which appears to influence the manner of crystallization and the desirable enhancement of high water absorption and plasticity of the nylon. More generally, a broad feature of the invention is the crystallization of the outer nylon layer to enhance mechanical properties in the elastic range, and to enhance plastic flexibility as well as plastic extensibility and additional drying properties. Including hydration of the nylon layer to provide apparent elasticity, with the overall result that the multilayer package substantially uniformly exhibits these properties of the nylon outer layer. Table 1 shows a comparison of mechanical properties between a package sample with an outer nylon layer and a sample with a nylon layer on the inside of the packaging laminate. The package samples were manufactured substantially in accordance with the preferred method described above, so that each nylon layer was initially in a substantially amorphous state. The comparison was made at a common hot filling temperature of 160㎓ (approximately 71.7°C). The SDX244 package consists of a laminate with a structure of nylon 6 (outer layer)/adhesive/PE/adhesive/PE, with the nylon layer having a thickness of 2 mils (approximately 0.051 mm) and a total thickness of the laminate. The diameter was 4 mils (approximately 0.102 mm).
The SDX246 type sample is 4 mil (approx.
0.102mm) overall thickness and 2 mils (approximately 0.051mm)
The thickness of the nylon layer is
It was PE/adhesive/nylon 6/adhesive/PE. The data in the table are for state A, which is a dry state without heat treatment, state B, which shows heat treatment for 1 minute in a hot water bath at 180〓 (about 82 °C), and 180〓 (about 82 °C), respectively.
The yield strength and elongation at yield are shown for condition C, which shows heat treatment for 1 hour in hot water at a temperature of 0.05 °C.
The term "yield strength" is used in its usual meaning,
shall indicate the stress value that causes a small irreversible deformation or permanent set in the test material. Yield strength was determined using a conventional force-elongation tensile tester of the Instron type that stretches the sample at a constant extension rate and records the force measurements with increasing elongation values. The sample is 1 inch wide (approximately 25.4 mm) and 4 inches long (approximately 102
mm), and approximately 2 inches (approximately 50.8 mm) per minute.
It was pulled at a constant crosshead speed of mm). It can be seen that the SDX244 type sample with the nylon outer layer responds quickly to heat treatment, ie within 1 minute, as evidenced by the comparison of Conditions A and B. If the heat treatment is continued further, it is observed that a further substantial increase in both yield strength and elongation at yield is achieved after 1 hour. In contrast, in samples of type SDX246, which has an inner nylon layer that is not directly exposed to hydrothermal heat treatment,
There is virtually no effect within 1 minute. It is observed that some effect occurs after 1 hour. essentially having a nylon outer layer according to the invention
It is observed that samples of type SDX244 have a dramatic response to heat treatment in a very short time. It should be noted that the standard deviations for each test condition shown in parentheses have a narrow statistical spread indicating that the behavior of the samples is relatively unchanged. In Table 2, a similar comparison was made at 73°C (approximately 23°C) with similar general results.

【表】 イロン)
[Table] Iron)

Claims (1)

【特許請求の範囲】 1 結晶化され含湿したナイロンの外側と、内側
の防湿層とを有する管状の溶融成形した重合体状
積層物から成り、該ナイロンは実質的に無定形状
態から加熱結晶化され且つ同時に湿らされること
を特徴とする厳密適合食品用包装体。 2 前記ナイロンの外層の厚さは、包装体の力−
伸び曲線の弾性範囲が最終使用充填の範囲と少な
くともほぼ同じとなるように選択される特許請求
の範囲第1項に記載の包装体。 3 前記ナイロンの外層が乾燥するとき、包装体
は均一な収縮を示す特許請求の範囲第1項に記載
の包装体。 4 前記管状の積層物に所定の最終使用直径を付
与する間、前記ナイロンは予備的に実質的に無定
形にさせられる特許請求の範囲第1項に記載の包
装体。 5 前記ナイロンは、少なくとも約8%の吸水率
を有する加熱により結晶化し得るナイロンから成
る特許請求の範囲第1項に記載の包装体。 6 前記管状の積層物は、ナイロン(外層)/接
着剤層/ポリオレフイン層(内層)から成る特許
請求の範囲第5項に記載の包装体。 7 前記ナイロンはナイロン6又はナイロン66
から成る特許請求の範囲第6項に記載の包装体。 8 前記ポリオレフインはポリエチレンから成
り、前記接着剤は、それぞれ、ナイロンに対する
強い親和力を有し且つ共押出しの熱及び圧力下で
ナイロンへの強い結合を形成する官能基を重合体
に付与することによつて化学的に変成した、エチ
レン−酢酸ビニル共重合体、高密度ポリエチレン
及びゴム変成高密度ポリエチレンから成るグルー
プから選択された、化学的に変成されたポリオレ
フインから成る特許請求の範囲第7項に記載の包
装体。 9 外側及び内側の表面は潤滑剤で被覆されてい
る特許請求の範囲第6項に記載の包装体。 10 a ナイロンの外層を有する管状の重合体
状積層物を溶融形成し、 b 該ナイロンを実質的に無定形にならしめるよ
うに、該管状の積層物を冷却しそして固化さ
せ、 c 該管状の積層物を熱処理して、該ナイロンを
実質的に結晶化させ、そして、 d 該ナイロンを湿らせる ことを特徴とする厳密適合食品用包装体の製造方
法。 11 前記熱処理及び湿らせる処理は同時にそし
て前記ナイロンの実質的に自然の熟成が生じる前
に行われる特許請求の範囲第10項に記載の方
法。 12 前記熱処理及び湿らせる処理は熱水浴中で
行われる特許請求の範囲第11項に記載の方法。 13 前記管状の積層物を使用時まで湿つた環境
中で保存することを更に包含する特許請求の範囲
第10項に記載の方法。 14 前記冷却は、前記管状の積層物に所定の最
終使用直径とほぼ等しい直径を与える間に同時に
行われる特許請求の範囲第10項に記載の方法。 15 前記管状の積層物は、所定のほぼ最終使用
直径のマンドレル上を通る間に冷却される特許請
求の範囲第14項に記載の方法。 16 前記冷却は水冷による特許請求の範囲第1
5項に記載の方法。 17 前記溶融形成は共押出しによる特許請求の
範囲第10項に記載の方法。 18 前記熱処理は、約180〓(約82℃)乃至約
212〓(約100℃)で、約1分乃至12時間行われる
特許請求の範囲第10項に記載の方法。 19 前記マンドレルは内部冷却されている特許
請求の範囲第15項に記載の方法。 20 前記ナイロンは、少なくとも約8%の吸水
率を有する加熱により結晶化し得るナイロンから
成り、前記管状の積層物は内側の防湿層を有して
いる特許請求の範囲第10項に記載の方法。 21 前記管状の積層物は、ナイロン(外層)/
接着剤層/ポリオレフイン層(内層)から成る特
許請求の範囲第20項に記載の方法。 22 前記ナイロンはナイロン6又はナイロン6
6から成る特許請求の範囲第21項に記載の方
法。 23 前記ポリオレフインはポリエチレンから成
り、前記接着剤は、それぞれ、ナイロンに対する
強い親和力を有し且つ共押出しの熱及び圧力下で
ナイロンへの強い結合を形成する官能基を重合体
に付与することによつて化学的に変成した、エチ
レン−酢酸ビニル共重合体、高密度ポリエチレン
及びゴム変成高密度ポリエチレンから成るグルー
プから選択された、化学的に変成されたポリオレ
フインから成る特許請求の範囲第22項に記載の
方法。 24 外側及び内側の表面は潤滑剤で被覆されて
いる特許請求の範囲第21項に記載の方法。 25 a ナイロンの外層を有する管状の重合体
状積層物を溶融形成する手段と、 b 該ナイロンを実質的に無定形にならしめるよ
うに、該管状の積層物を冷却しそして固化させ
る手段と、 c 該管状の積層物を熱処理して、該ナイロンを
実質的に結晶化させる手段と、 d 該ナイロンを湿らせる手段、 とから成ることを特徴とする厳密適合食品用包装
体の製造装置。 26 ナイロンを熱処理すると同時にナイロンを
湿らせる手段を具備する特許請求の範囲第25項
に記載の装置。 27 前記管状の積層物を冷却すると同時に、該
積層物を所定の最終使用直径とほぼ等しい直径に
する手段を具備する特許請求の範囲第25項に記
載の装置。 28 前記溶融成形する手段は共押出し装置から
成る特許請求の範囲第25項に記載の装置。 29 積層物を所定の最終使用直径とほぼ等しい
直径にする前記手段は、所定のほぼ最終使用直径
を有するマンドレルから成る特許請求の範囲第2
7項に記載の装置。 30 前記冷却手段は水冷手段から成る特許請求
の範囲第29項に記載の装置。 31 前記マンドレルは内部冷却される特許請求
の範囲第29項に記載の装置。
Claims: 1. Consisting of a tubular melt-formed polymeric laminate having an outer crystallized and moistened nylon and an inner moisture barrier layer, the nylon is heated from a substantially amorphous state to crystallized. 1. A tightly conforming food packaging, characterized in that it is moistened and moistened at the same time. 2 The thickness of the nylon outer layer is determined by the force of the package -
A package according to claim 1, wherein the elastic range of the elongation curve is selected to be at least approximately the same as the end-use fill range. 3. The package of claim 1, wherein the package exhibits uniform shrinkage when the nylon outer layer dries. 4. The package of claim 1, wherein the nylon is previously rendered substantially amorphous while imparting a predetermined end-use diameter to the tubular laminate. 5. The package of claim 1, wherein the nylon is a heat-crystallizable nylon having a water absorption of at least about 8%. 6. The package according to claim 5, wherein the tubular laminate is composed of nylon (outer layer)/adhesive layer/polyolefin layer (inner layer). 7 The nylon is nylon 6 or nylon 66
A package according to claim 6, comprising: 8. The polyolefin consists of polyethylene, and the adhesive is prepared by imparting functional groups to the polymer that have a strong affinity for nylon and form a strong bond to nylon under the heat and pressure of coextrusion. Claim 7 comprising a chemically modified polyolefin selected from the group consisting of ethylene-vinyl acetate copolymer, high density polyethylene and rubber modified high density polyethylene. packaging. 9. The package according to claim 6, wherein the outer and inner surfaces are coated with a lubricant. 10 a. melt forming a tubular polymeric laminate having an outer layer of nylon; b. cooling and solidifying the tubular laminate so as to render the nylon substantially amorphous; c. A method of manufacturing a closely conforming food packaging comprising: heat treating a laminate to substantially crystallize the nylon; and d moistening the nylon. 11. The method of claim 10, wherein the heat treatment and wetting treatment are performed simultaneously and before substantially natural ripening of the nylon occurs. 12. The method of claim 11, wherein the heat treatment and moistening treatment are performed in a hot water bath. 13. The method of claim 10, further comprising storing the tubular laminate in a moist environment until use. 14. The method of claim 10, wherein said cooling is performed simultaneously while providing said tubular laminate with a diameter approximately equal to a predetermined end-use diameter. 15. The method of claim 14, wherein the tubular laminate is cooled while passing over a mandrel of approximately a predetermined final use diameter. 16 The cooling is water cooling according to Claim 1
The method described in Section 5. 17. The method of claim 10, wherein said melt forming is by coextrusion. 18 The heat treatment is carried out at a temperature of about 180°C (about 82°C) to about
11. The method according to claim 10, wherein the method is carried out at a temperature of about 100° C. for about 1 minute to 12 hours. 19. The method of claim 15, wherein the mandrel is internally cooled. 20. The method of claim 10, wherein the nylon comprises a heat-crystallizable nylon having a water absorption of at least about 8%, and wherein the tubular laminate has an inner moisture barrier. 21 The tubular laminate is made of nylon (outer layer)/
21. The method according to claim 20, comprising an adhesive layer/polyolefin layer (inner layer). 22 The nylon is nylon 6 or nylon 6
22. The method of claim 21, comprising: 6. 23 The polyolefin consists of polyethylene, and the adhesives are each made by imparting functional groups to the polymer that have a strong affinity for nylon and form a strong bond to nylon under the heat and pressure of coextrusion. Claim 22 comprising a chemically modified polyolefin selected from the group consisting of ethylene-vinyl acetate copolymer, high density polyethylene and rubber modified high density polyethylene. the method of. 24. The method of claim 21, wherein the outer and inner surfaces are coated with a lubricant. 25 a means for melt forming a tubular polymeric laminate having an outer layer of nylon; b means for cooling and solidifying the tubular laminate so as to render the nylon substantially amorphous; An apparatus for manufacturing a tightly conforming food packaging, comprising: c) means for heat-treating the tubular laminate to substantially crystallize the nylon; and d) means for moistening the nylon. 26. The apparatus of claim 25, comprising means for simultaneously heat treating the nylon and moistening the nylon. 27. The apparatus of claim 25, comprising means for simultaneously cooling the tubular laminate and bringing the laminate to a diameter approximately equal to a predetermined end use diameter. 28. The apparatus of claim 25, wherein said means for melt forming comprises a coextrusion device. 29. The means for rendering the laminate approximately equal to the predetermined final use diameter comprises a mandrel having approximately the predetermined final use diameter.
The device according to item 7. 30. The apparatus of claim 29, wherein said cooling means comprises water cooling means. 31. The apparatus of claim 29, wherein the mandrel is internally cooled.
JP2330999A 1982-03-15 1990-11-30 Nylon multiple layer packaging body and method and device for its manufacture Granted JPH03187743A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US35755082A 1982-03-15 1982-03-15
US357550 1982-03-15

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP58040856A Division JPS58168524A (en) 1982-03-15 1983-03-14 Nylon multilayer packing

Publications (2)

Publication Number Publication Date
JPH03187743A JPH03187743A (en) 1991-08-15
JPH0443783B2 true JPH0443783B2 (en) 1992-07-17

Family

ID=23406074

Family Applications (3)

Application Number Title Priority Date Filing Date
JP58040856A Pending JPS58168524A (en) 1982-03-15 1983-03-14 Nylon multilayer packing
JP2331000A Pending JPH03200555A (en) 1982-03-15 1990-11-30 Manufacture of nylon multi- layer package and its manufacturing device
JP2330999A Granted JPH03187743A (en) 1982-03-15 1990-11-30 Nylon multiple layer packaging body and method and device for its manufacture

Family Applications Before (2)

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JP58040856A Pending JPS58168524A (en) 1982-03-15 1983-03-14 Nylon multilayer packing
JP2331000A Pending JPH03200555A (en) 1982-03-15 1990-11-30 Manufacture of nylon multi- layer package and its manufacturing device

Country Status (14)

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)

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Also Published As

Publication number Publication date
GB2117702B (en) 1985-10-02
ATA91883A (en) 1986-08-15
DK119183D0 (en) 1983-03-14
JPS58168524A (en) 1983-10-04
NO830892L (en) 1983-09-16
DK119183A (en) 1983-09-16
JPH03187743A (en) 1991-08-15
NL8300515A (en) 1983-10-03
DE3308296A1 (en) 1983-09-15
NZ203558A (en) 1986-03-14
IT1194163B (en) 1988-09-14
ZA83848B (en) 1984-08-29
FR2523031A1 (en) 1983-09-16
FR2523031B1 (en) 1988-04-15
GB8306464D0 (en) 1983-04-13
AU1247383A (en) 1983-09-22
IT8320087A1 (en) 1984-09-15
GB2117702A (en) 1983-10-19
AU565829B2 (en) 1987-10-01
JPH03200555A (en) 1991-09-02
IT8320087A0 (en) 1983-03-15
BR8300782A (en) 1983-11-16
IL68112A0 (en) 1983-06-15
AT382498B (en) 1987-02-25

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