US2854435A - Process of preparing a polyethylenepolyisoolefin blend - Google Patents

Process of preparing a polyethylenepolyisoolefin blend Download PDF

Info

Publication number
US2854435A
US2854435A US541836A US54183655A US2854435A US 2854435 A US2854435 A US 2854435A US 541836 A US541836 A US 541836A US 54183655 A US54183655 A US 54183655A US 2854435 A US2854435 A US 2854435A
Authority
US
United States
Prior art keywords
polyethylene
polyisobutylene
molecular weight
blend
mixture
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
US541836A
Inventor
John R Briggs
Raymond G Newberg
Robert E Clayton
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.)
ExxonMobil Technology and Engineering Co
Original Assignee
Exxon Research and Engineering 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 Exxon Research and Engineering Co filed Critical Exxon Research and Engineering Co
Priority to US541836A priority Critical patent/US2854435A/en
Priority to GB28340/56A priority patent/GB809484A/en
Priority to DEE13105A priority patent/DE1155966B/en
Application granted granted Critical
Publication of US2854435A publication Critical patent/US2854435A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/18Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
    • C08L23/20Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
    • C08L23/22Copolymers of isobutene; Butyl rubber ; Homo- or copolymers of other iso-olefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L25/00Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
    • C08L25/02Homopolymers or copolymers of hydrocarbons
    • C08L25/04Homopolymers or copolymers of styrene
    • C08L25/08Copolymers of styrene
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S206/00Special receptacle or package
    • Y10S206/819Material

Definitions

  • This invention is concerned with the preservation of food in thin, flexible and impervious casings and relates particularly to an improved material for'the formation of such casings.
  • this invention is applicable to any food product in the preservation of which the use of thin, flexible and impervious casings is desirable and is applicable to preservation at any temperature, it is particularly suitable for use in preserving meats by refrigeration or low temperature treatment.
  • vulcanized rubber bags may impart obnoxious odors or tastes to vulcanized rubber bags must be coated with soaps or dusted with talc, starch or an equivalent material to reduce their stickiness so that they can be shipped and stored and so that the completed packages can behandled conveniently and stored without adhering to eachother. Unless these materials are removed from the inside of the bags before the food products are inserted they may leave an objectionable coating on the food. It is, of course, an expensive and commercially impracticable procedure to remove the material from the inside of the bag without removing it from the outside at the same time. Starch, recognized as the most satisfactory of these materials, tends to promote the growth of molds.
  • the bags heretofore proposed are subject to puncturing and tearing in handling, even at low temperatures. This defect has necessitated the use of bags having relatively thick walls, adding to the expense and'interfering with the heat transfer through the bags when the products are frozen.
  • Envelopes made from such materials exhibit a high degree of permanent set after stretching, particularly at low extrusion temperatures, that is, the envelopes, when to their original size. In this condition they are unstable to a rise in temperature, springing back when'heated to a size about-25% smaller than the original size. 7
  • advantage may be taken of this property of heretofore proposed, however, have i.
  • Bags of other materials which have been proposed are defective either because they require "after application heat treatment at undesirably high temperatures or because of the high cost of fabricating thematerial into a completed food covering or because of a low degree of pliability and deformability.
  • solid polyethylene having a molecular weight in the range of 10,000 to 100,000, or more, preferably 15,000" to 25,000, such as may be made by'known methods, e.g., polymerization under high pressure and temperature" by the use of a small'amount of oxygen o'r'other agent as promoter, has been found to have'many valuable characteristics for this purpose but it requires" temperatures of 215 to 230 F. in order to obtain adequate shrinking.
  • a still further object of the invention is to provide an envelope which may be shrunk down onto the product by a simple method to cause the covering to cling to a product such as beef as if it were the skin of the animal, and to produce covers which in their shrunken condition are transparent and relatively free from wrinkles and folds.
  • the polyiso-olefin may contain about 10% of a low molecular weight copolymer of an iso-olefin and a A particularly suitable composition is one composed of 70% polyethylene, 27% polyisobutylene of 140,000-300,000 molecular weight, 3% of a copolymer of isobutylene and styrene containing 55 to ,6S,.% styrene and having an intrinsic viscosity below 0.5.
  • the polyiso-olefin used in this invention is prepared by polymerizing an iso-olefin of 4 to 5 carbon atoms per molecule, preferably isobutylene, by a low temperature procedure and in the'presence of a solution of a-Friedel- Crafts type catalyst in a low-freezing solvent which does not form a complex therewith such as methyl or ethyl chloride or carbon di-sulfide.
  • the temperatures applied range from about -40 C. to 'l00 C. or -l50 C. or lower, the preferred range being from C. to -103 C.
  • This polymer has an average molecular weight ranging between 100,000 and 500,000 Staudinger.
  • the iso-olefin-vinyl aromatic hydrocarbon copolymer may be made broadly within the'teachings' of Patent 2,274,749 but for the purposes of this invention, it must be made under certain restricted combinations of conditions; namely, by copolymerizing 40 to-.70% by weight, preferably 55 to 65% by weight of a polymerizable monoolefinic aromatic compound with an alkene of 3 to 8, preferably 4 to 5 carbon atoms, at a temperature between about -l0 C. and l00 C. Temperaturesbetwe'en -l0 C. and -50 C., preferably between -'-18" -C. and
  • a lower alkyl halide liquid is used as solvent for the reaction mixture.
  • the catalyst may appropriately be a solution of aluminum chloride in a lower alkyl halide such as methyl chloride or ethyl chloride.
  • Other known Friedel-Crafts catalysts preferably predissolved in a solvent, may be used.
  • a copolymer of isobutylene and styrene containing to styrene and having an intrinsic viscosity below 0.5 is particularly suitable.
  • the various polymers must be blended in just the correct manner in order to obtain a mixture which will form expanded films capable of being shrunk at 212 F. This is accomplished, according to this invention by preparing and aminor proportion of polyethylene, the softer polyethylene beingadded to the tougher isobutylene. A portion of the blend is then removed and replaced with a sufficient amount of polyethylene to give the desired final blend. -The blend is then formed into an expanded envelope by tubular extrusion at 250 F.
  • the carcass is placed in one of the expanded rubber envelopes.
  • the open end of the bag i. e., the neck portion of the envelope, is twisted and securely tied to form an air tight 4 down against the carcass so tightly that it appears almost as a transparent skin and hardly any spot is left on complicated cuts where the envelope is not in close contact with the meat.
  • the meat may merely go to a chill room and be chilled according to conventional practice, but, in all cases to secure the best results from the invention, the envelope should be left on the meat until it must be cut up for sale by the retail butcher.
  • Example I Films were prepared from 100% polyethylene; mixtures of polyethylene, 30% polyisobutylene of 200,000 molecular weight; mixtures of 70% polyethylene and 30% polyisobutylene of 300,000 molecular weight; 70% polyethylene, 27% polyisobutylene of 200,000 molecular weight and 3% of a copolymer of isobutylene and styrene containing 60% styrene and having an intrinsic viscosity less than 0.5; and a similar composition containing 27% isobutylene of 300,000 molecular weight. These compositions were extruded at 250 F. into tubular film, the film was then formed into bags and shrunk at 212 F. The following data were obtained:
  • the polymer blend in an expanded or extended condition is physically unstable to a rise in temperature. At room temperature it will contract toward its original size very slowly or not at all, but, if the temperature be raised approximately to ZOO-212 F. it springs back to about of its original size almost instantaneously. Therefore the wrapped carcass is heated very briefly in order to cause the restoring forces in the rubber bag to become active and to cause the folds and wrinkles to disappear. This may be done by dipping the carcass for no more than a few seconds into boiling or near boiling water or the carcass may be pushed quickly through a hot room at about 200-212 F. on its way to the cooler. Only this momentary heating is necessary to shrink the coating i of between about 200 F. and
  • a process for blending polyisobutylene having a molecular weight of at least about 140,000 with polyethylene which comprises homogenizing the polyisobutylene, removing about 30% of the homogenized polyisobutylene and replacing it with an equivalent amount of polyethylene, homogenizing the mixture, removing a sufficient amount of homogenized mixture ethylene and about 30% polyisobutylene, and mixing the resulting blend until it is capable of shrinking at least about 6% to 25% when heated to a temperature level about 212 F.
  • a process for preparing a blend of about 60 to 75 wt. percent of polyethylene having a molecular weight between about 10,000 and about 100,000 and about to wt. percent of a polyisoolefin having a molecular weight of between about 140,000 and about 300,000 which comprises mixing the polyisoolefin until substantially homogeneous, removing a substantial portion up to about 30 wt. percent of the polyisoolefin and replacing it with an equivalent amount of polyethylene, homogenizing the mixture formed, removing a suflicient amount of the resulting homogenized mixture and replacing it with an equal amount of polyethylene so that the resulting mixture contains about to wt. percent of polyethylene and about 25 to 40 wt.
  • ethylene has a molecular weight and 25,000.

Description

stretched return only slightly States F PREPARING A POLYETHYLENE- POLYISOOLEFIN BLEND to Esso Research and Engineering Company, a corpo ration of Delaware PROCESS No Drawing. Application October 20, 1955 Serial No. 541,836
Claims. (Cl. 260-455) This invention is concerned with the preservation of food in thin, flexible and impervious casings and relates particularly to an improved material for'the formation of such casings.
Although this invention is applicable to any food product in the preservation of which the use of thin, flexible and impervious casings is desirable and is applicable to preservation at any temperature, it is particularly suitable for use in preserving meats by refrigeration or low temperature treatment.
It has been proposed to enclose foodstuffs to be preserved by freezing or chilling in thin-walled bags of flexible materials, such as rubber or a rubber hydrohalide, and to evacuate the air from the bag and seal it hermetically. Very quick freezing may then be obtained because the covered carcass may be brought into direct contact with the refrigeration medium, such as air or brine, without sufiering either contamination or desiccation. Meats stored in such bags after freezing have shown an improved quality over those not so protected.
Casing materials lacked to a serious degree various of the propertiesdesired. If ordinary rubber is used, the vulcanizing agents the food. Un-
may impart obnoxious odors or tastes to vulcanized rubber bags must be coated with soaps or dusted with talc, starch or an equivalent material to reduce their stickiness so that they can be shipped and stored and so that the completed packages can behandled conveniently and stored without adhering to eachother. Unless these materials are removed from the inside of the bags before the food products are inserted they may leave an objectionable coating on the food. It is, of course, an expensive and commercially impracticable procedure to remove the material from the inside of the bag without removing it from the outside at the same time. Starch, recognized as the most satisfactory of these materials, tends to promote the growth of molds.
The bags heretofore proposed are subject to puncturing and tearing in handling, even at low temperatures. This defect has necessitated the use of bags having relatively thick walls, adding to the expense and'interfering with the heat transfer through the bags when the products are frozen.
Many of the advantages of using envelopes in food preservation result from the decreased evaporation and decreased possibility of contamination that an impervious wrapping secures. Rubber materials heretofore proposed lack the high degree of moisture irnpermeability desired in envelopes in which food products are likely to be stored for long periods of time.
Envelopes made from such materials exhibit a high degree of permanent set after stretching, particularly at low extrusion temperatures, that is, the envelopes, when to their original size. In this condition they are unstable to a rise in temperature, springing back when'heated to a size about-25% smaller than the original size. 7 In packaging articles in the bags, advantage may be taken of this property of heretofore proposed, however, have i.
atent 7 vinyl aromatic.
- 2,854,435.. Patented Sept. 30, 1958..
ice
2 the material to shrink the bag into intimate contact with the article by subjecting the bag momentarily to a temperature of about 212 F. or higher.
Bags of other materials which have been proposed are defective either because they require "after application heat treatment at undesirably high temperatures or because of the high cost of fabricating thematerial into a completed food covering or because of a low degree of pliability and deformability. For example, solid polyethylene, having a molecular weight in the range of 10,000 to 100,000, or more, preferably 15,000" to 25,000, such as may be made by'known methods, e.g., polymerization under high pressure and temperature" by the use of a small'amount of oxygen o'r'other agent as promoter, has been found to have'many valuable characteristics for this purpose but it requires" temperatures of 215 to 230 F. in order to obtain adequate shrinking. However, since the simplest method of heating"tl ie'poly mer is by dipping in hot water, it is necessary to add a high boiling liquid such as propylene glycol to the water to increase its boiling point. This raises problems of getting rid of the glycol and is therefore urides'irable' It is accordingly the principal aim and object or the invention to provide an inexpensive "envelope, suitable for packaging food products, which is non-tacky, pliable and deformable, impermeable to moisture and both thin and strong. A further object is to provide an envelope which possesses to a high degree the mechanical properties desired in food casings and which at the same time is transparent and attractive in appearance and will form a saleable commercial package. A still further object of the invention is to provide an envelope which may be shrunk down onto the product by a simple method to cause the covering to cling to a product such as beef as if it were the skin of the animal, and to produce covers which in their shrunken condition are transparent and relatively free from wrinkles and folds.
In accordance with the present invention it has now been discovered that the peculiar physical characteristics which are necessary to adapt polyethylene to the covering of foods and particularly to the preservation of meats are obtained by a special blending of about 25-40%, preferably about 30% of a polyiso-olefin having a molecular weight above 140,000 with the polyethylene. If desired the polyiso-olefin may contain about 10% of a low molecular weight copolymer of an iso-olefin and a A particularly suitable composition is one composed of 70% polyethylene, 27% polyisobutylene of 140,000-300,000 molecular weight, 3% of a copolymer of isobutylene and styrene containing 55 to ,6S,.% styrene and having an intrinsic viscosity below 0.5.
The polyiso-olefin used in this invention is prepared by polymerizing an iso-olefin of 4 to 5 carbon atoms per molecule, preferably isobutylene, by a low temperature procedure and in the'presence of a solution of a-Friedel- Crafts type catalyst in a low-freezing solvent which does not form a complex therewith such as methyl or ethyl chloride or carbon di-sulfide. The temperatures applied range from about -40 C. to 'l00 C. or -l50 C. or lower, the preferred range being from C. to -103 C. This polymer has an average molecular weight ranging between 100,000 and 500,000 Staudinger.
The iso-olefin-vinyl aromatic hydrocarbon copolymer may be made broadly within the'teachings' of Patent 2,274,749 but for the purposes of this invention, it must be made under certain restricted combinations of conditions; namely, by copolymerizing 40 to-.70% by weight, preferably 55 to 65% by weight of a polymerizable monoolefinic aromatic compound with an alkene of 3 to 8, preferably 4 to 5 carbon atoms, at a temperature between about -l0 C. and l00 C. Temperaturesbetwe'en -l0 C. and -50 C., preferably between -'-18" -C. and
C. are suitable for low molecular weight material having intrinsic viscosities below 0.5. Temperatures below C., preferably below 70 C., are suitable for high molecular weight polymers having intrinsic viscosity A lower alkyl halide liquid is used as solvent for the reaction mixture. The catalyst may appropriately be a solution of aluminum chloride in a lower alkyl halide such as methyl chloride or ethyl chloride. Other known Friedel-Crafts catalysts, preferably predissolved in a solvent, may be used. A copolymer of isobutylene and styrene containing to styrene and having an intrinsic viscosity below 0.5 is particularly suitable.
The various polymers must be blended in just the correct manner in order to obtain a mixture which will form expanded films capable of being shrunk at 212 F. This is accomplished, according to this invention by preparing and aminor proportion of polyethylene, the softer polyethylene beingadded to the tougher isobutylene. A portion of the blend is then removed and replaced with a sufficient amount of polyethylene to give the desired final blend. -The blend is then formed into an expanded envelope by tubular extrusion at 250 F.
At the food packing plant, after the animal is slaughtered and properly cleaned and prepared, the carcass is placed in one of the expanded rubber envelopes. The open end of the bag, i. e., the neck portion of the envelope, is twisted and securely tied to form an air tight 4 down against the carcass so tightly that it appears almost as a transparent skin and hardly any spot is left on complicated cuts where the envelope is not in close contact with the meat.
After the envelope has been shrunk into contact with the meat by heating, the meat may merely go to a chill room and be chilled according to conventional practice, but, in all cases to secure the best results from the invention, the envelope should be left on the meat until it must be cut up for sale by the retail butcher.
The advantages of the invention will be better understood from a consideration of the following experimental data which are given for the sake of illustration, but without the intention of limiting the invention thereto.
Example I Films were prepared from 100% polyethylene; mixtures of polyethylene, 30% polyisobutylene of 200,000 molecular weight; mixtures of 70% polyethylene and 30% polyisobutylene of 300,000 molecular weight; 70% polyethylene, 27% polyisobutylene of 200,000 molecular weight and 3% of a copolymer of isobutylene and styrene containing 60% styrene and having an intrinsic viscosity less than 0.5; and a similar composition containing 27% isobutylene of 300,000 molecular weight. These compositions were extruded at 250 F. into tubular film, the film was then formed into bags and shrunk at 212 F. The following data were obtained:
Polyethylene, 21,000 mol. wt
Polylsobutylene, 300,000 mol. wt: I
Polyisobutylene, 200,000 mol. wt copolymer of styrene (I. V. 0.5)
Total Banbury Timej'ididfiiilj degrees Dump Temperature,
Mixing Procedure (see below) Tensiles, p. s. i.* Elongation, percent Blend Homogeneity.
Percent shrinking 212 styrene and isobut A B C D E 1,530 800 1,150 950 1,350 1.350 600 360 525 530 680 700 good poor poor good good good 1.0 1.0 1.0 13. 5 6. 4 15.1
Made on molded test pads. (A) Banbury hotPolyethyle parable to the following condltio (B) Banbury hot-Polyisobuty mixed for the remainder of th ne pellets added to hanbury to give simular work to polymer so as to be comns.
lene homogenized for 2 minutes in the banbury. Polyethylene pellets added e total time.
(0) Banbury hot-Polylsobutylene homogenized for 2 minutes in the banbury. Polyethylene pellets added and mixed for the remainder of seal. A vacuum line is attached to a small tube formed on the envelope, and the air which may be trapped between the carcass and the bag is sucked out. At this moment, the bag, which very loosely enfolds the carcass, is pushed against it by the outside atmospheric pressure, forming a great number of wrinkles and folds. Alternatively, instead of exhausting the air by vacuum, it may be pressed out from between the carcass and the bag by means of external pressure.
The polymer blend in an expanded or extended condition is physically unstable to a rise in temperature. At room temperature it will contract toward its original size very slowly or not at all, but, if the temperature be raised approximately to ZOO-212 F. it springs back to about of its original size almost instantaneously. Therefore the wrapped carcass is heated very briefly in order to cause the restoring forces in the rubber bag to become active and to cause the folds and wrinkles to disappear. This may be done by dipping the carcass for no more than a few seconds into boiling or near boiling water or the carcass may be pushed quickly through a hot room at about 200-212 F. on its way to the cooler. Only this momentary heating is necessary to shrink the coating i of between about 200 F. and
the total tim Banbury hot-Polyisobutylene homogenized for removed and polyethylene pellets added minutes. 30% of the Banburied for 15 minutes. The with additional polyethylene to make a final blend of isobutylene-styrene copolymer.
The above data clearly show that polyethylene shrinks only about 1.0% at 212 F. and that blends of polyisobutylene and polyethylene likewise shrink only slightly at 212 F. unless they are prepared in accordance with the blending technique of this invention, when up to about 15% shrinkage occurs.
The nature of the present invention having been thus secured by Letters Patent is:
1. A process for blending polyisobutylene having a molecular weight of at least about 140,000 with polyethylene which comprises homogenizing the polyisobutylene, removing about 30% of the homogenized polyisobutylene and replacing it with an equivalent amount of polyethylene, homogenizing the mixture, removing a sufficient amount of homogenized mixture ethylene and about 30% polyisobutylene, and mixing the resulting blend until it is capable of shrinking at least about 6% to 25% when heated to a temperature level about 212 F.
2. A process for preparing a blend of about 60 to 75 wt. percent of polyethylene having a molecular weight between about 10,000 and about 100,000 and about to wt. percent of a polyisoolefin having a molecular weight of between about 140,000 and about 300,000, which comprises mixing the polyisoolefin until substantially homogeneous, removing a substantial portion up to about 30 wt. percent of the polyisoolefin and replacing it with an equivalent amount of polyethylene, homogenizing the mixture formed, removing a suflicient amount of the resulting homogenized mixture and replacing it with an equal amount of polyethylene so that the resulting mixture contains about to wt. percent of polyethylene and about 25 to 40 wt. percent of the polyisoolefin, and homogenizing the mixture formed until it is capable of shrinking at least about 6 to 15% when heated to a temperature level of between about 200 F. and about 3. Process according to claim 2 in which the polyisoolefin is polyisobutylene.
4. Process according to claim 2 ethylene has a molecular weight and 25,000.
5. Process according to claim 2 in which the polyisoolefin is initially blended with up to about 10 wt. percent of a copolymer of isobutylene and styrene before the addition of polyethylene.
in which the polybetween about 15,000
References Cited in the file of this patent UNITED STATES PATENTS 2,339,958 Sparks Jan. 25, 1944 2,369,471 Latham Feb. 13, 1945 2,686,725 Cornwell Aug.- 17, 1954 2,699,396 Francis Jan. 11, 1955 OTHER REFERENCES Modern Packaging, pages -102, March 1955.

Claims (1)

1. A PROCESS FOR BLENDING POLYISOBUTYLENE HAVING A MOLECULAR WEIGHT OF AT LEAST ABOUT 140,000 WITH POLYETHYLENE WHICH COMPRISES HOMOGENIZING THE POLYISOBUTYLENE, REMOVING ABOUT 30% OF THE HOMOGENIZED POLYISOBUTYLENE AND REPLACING IT WITH AN EQUIVALENT AMOUNT OF POLYETHYLENE, HOMOGENIZING THE MIXTURE, REMOVING A SUFFICIENT AMOUNT OF THE RESULTING HOMOGENIZED MIXTURE AND REPLACING IT WITH AN EQUAL AMOUNT OF POLYETHYLENE SO THAT THE RESULTING MIXTURE CONTAINS ABOUT 70% POLYETHYLENE AND ABOUT 30% POLYISOBUTYLENE, AND MIXING THE RESULTING BLEND UNTIL IT IS CAPABLE OF SHRINKING AT LEAST ABOUT 6% TO 25% WHEN HEATED TO A TEMPERATURE LEVEL OF BETWEEN ABOUT 200*F. AND ABOUT 212*F.
US541836A 1955-10-20 1955-10-20 Process of preparing a polyethylenepolyisoolefin blend Expired - Lifetime US2854435A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US541836A US2854435A (en) 1955-10-20 1955-10-20 Process of preparing a polyethylenepolyisoolefin blend
GB28340/56A GB809484A (en) 1955-10-20 1956-09-17 Polyethylene compositions
DEE13105A DE1155966B (en) 1955-10-20 1956-10-19 Polyethylene-containing film wrapping suitable for holding meat and other foods

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US541836A US2854435A (en) 1955-10-20 1955-10-20 Process of preparing a polyethylenepolyisoolefin blend

Publications (1)

Publication Number Publication Date
US2854435A true US2854435A (en) 1958-09-30

Family

ID=24161279

Family Applications (1)

Application Number Title Priority Date Filing Date
US541836A Expired - Lifetime US2854435A (en) 1955-10-20 1955-10-20 Process of preparing a polyethylenepolyisoolefin blend

Country Status (3)

Country Link
US (1) US2854435A (en)
DE (1) DE1155966B (en)
GB (1) GB809484A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2993876A (en) * 1957-04-22 1961-07-25 Phillips Petroleum Co Ethylene polymer-polyisobutylene composition, method of making same, and electrical wire coated therewith
US3074616A (en) * 1959-07-13 1963-01-22 Phillips Petroleum Co Article of blend of a copolymer of ethylene and 1-butene and polyisobutylene
DE1168072B (en) * 1961-08-12 1964-04-16 Kalle Ag Process for the production of molded articles from ethylene polymers
US3192288A (en) * 1961-08-21 1965-06-29 Exxon Research Engineering Co High impact strength blend of isotactic polypropylene, polyethylene and polyisobutylene
US3210306A (en) * 1962-04-06 1965-10-05 Exxon Research Engineering Co Wax compositions
DE1218137B (en) * 1961-01-10 1966-06-02 Skandinavisk Akryl Ind V F Hje Edge seal for molds for polymerisation casting of polymethyl methacrylate sheets
DE1248290B (en) * 1961-07-04 1967-08-24 Ibm Molding and coating compounds made of polyethylene and polyisobutylene
DE1289655B (en) * 1964-12-18 1969-02-20 Continental Gummi Werke Ag Process for improving the injectability of ethylene propylene terpolymer rubber
US4877840A (en) * 1987-01-28 1989-10-31 Du Pont Canada Inc. Polyolefin concentrate

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4996096A (en) * 1988-10-17 1991-02-26 James River Ii, Inc. Coextruded matte film

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2339958A (en) * 1939-09-14 1944-01-25 Jasco Inc Composition of matter containing polyethylene and polyisobutylene
US2369471A (en) * 1939-04-28 1945-02-13 Du Pont Compositions comprising solid ethylene polymers
US2686725A (en) * 1952-02-27 1954-08-17 American Viscose Corp Casing for stuffed products
US2699396A (en) * 1951-01-04 1955-01-11 Lamitex Products Inc Meat-wrap process and product

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL59835C (en) * 1943-04-02
GB676499A (en) * 1950-10-20 1952-07-30 Dow Chemical Co Container for and process of preserving perishable foodstuffs
GB715366A (en) * 1952-04-09 1954-09-15 Ici Ltd Improved process for applying protective coverings

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2369471A (en) * 1939-04-28 1945-02-13 Du Pont Compositions comprising solid ethylene polymers
US2339958A (en) * 1939-09-14 1944-01-25 Jasco Inc Composition of matter containing polyethylene and polyisobutylene
US2699396A (en) * 1951-01-04 1955-01-11 Lamitex Products Inc Meat-wrap process and product
US2686725A (en) * 1952-02-27 1954-08-17 American Viscose Corp Casing for stuffed products

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2993876A (en) * 1957-04-22 1961-07-25 Phillips Petroleum Co Ethylene polymer-polyisobutylene composition, method of making same, and electrical wire coated therewith
US3074616A (en) * 1959-07-13 1963-01-22 Phillips Petroleum Co Article of blend of a copolymer of ethylene and 1-butene and polyisobutylene
DE1218137B (en) * 1961-01-10 1966-06-02 Skandinavisk Akryl Ind V F Hje Edge seal for molds for polymerisation casting of polymethyl methacrylate sheets
DE1248290B (en) * 1961-07-04 1967-08-24 Ibm Molding and coating compounds made of polyethylene and polyisobutylene
DE1168072B (en) * 1961-08-12 1964-04-16 Kalle Ag Process for the production of molded articles from ethylene polymers
US3192288A (en) * 1961-08-21 1965-06-29 Exxon Research Engineering Co High impact strength blend of isotactic polypropylene, polyethylene and polyisobutylene
US3210306A (en) * 1962-04-06 1965-10-05 Exxon Research Engineering Co Wax compositions
DE1289655B (en) * 1964-12-18 1969-02-20 Continental Gummi Werke Ag Process for improving the injectability of ethylene propylene terpolymer rubber
US4877840A (en) * 1987-01-28 1989-10-31 Du Pont Canada Inc. Polyolefin concentrate

Also Published As

Publication number Publication date
DE1155966B (en) 1963-10-17
GB809484A (en) 1959-02-25

Similar Documents

Publication Publication Date Title
US2854435A (en) Process of preparing a polyethylenepolyisoolefin blend
US4073782A (en) Wrapping film
US4851245A (en) Smokable synthetic food-packaging film
US5279872A (en) Multilayer stretch/shrink film
NL7908391A (en) ARTIFICIAL RESIN HOSE FOR THE PACKING OF PASTY FOODSTUFFS, IN PARTICULAR OF SAUSAGE AND CHEESE.
US2538025A (en) Container for and process of preserving prerishable foodstuffs
CA1115888A (en) Thermoplastic polyolefin film compositions
US3222191A (en) Novel packaging film and processes therefor
US2992201A (en) Extrusion composition consisting of polyethylene and liquid dimethyl polysiloxanes
US2956671A (en) Composite film wrapping
US2538002A (en) Container for and process of preserving perishable foodstuffs
CN108892900A (en) A kind of PVDC composition and preparation method thereof for cooked product packaging
US3205077A (en) Coated polyolefin film and moisture emitting product enclosed therein
US5236728A (en) Process for packaging food having a bag puncturing surface
AU774119B2 (en) Packaging to enhance shelf life of foods
KR890000317A (en) Freshwater packaging and processing method
WO1993005104A1 (en) Process and composition for protecting and cushioning protrusions
US2995452A (en) Ground beef product and method of producing the same
US2261466A (en) Food casing
US2477614A (en) Vinylidene chloride-vinyl chloride copolymer composition for making shrinkable, translucent films
US3498962A (en) Non-fogging polyolefin film
US2849319A (en) Coated food product and coating composition therefor
CA2097908A1 (en) Food package comprised of polymer with thermally responsive permeability
US2477612A (en) Vinylidene chloride-vinyl chloride copolymer composition for making shrinkable, translucent films
JPH04159344A (en) Flexible polymer composition