CA1172819A

CA1172819A - Pasteurizable thermoplastic film and receptacle therefrom

Info

Publication number: CA1172819A
Application number: CA000404718A
Authority: CA
Inventors: Norman D. Bornstein; Johnnie J. Walters
Original assignee: WR Grace and Co
Current assignee: Cryovac LLC
Priority date: 1981-07-02
Filing date: 1982-06-08
Publication date: 1984-08-21
Also published as: AR242148A1; JPH0424223B2; EP0069495A3; AU8449482A; NZ200836A; JPH02243324A; US4391862A; JPH02238945A; MX162370A; BR8203759A; JPH0358908B2; AU555732B2; EP0069495A2

Abstract

Abstract of the Disclosure Disclosed is a multi-layer, heat shrinkable, thermoplastic packaging film which can be heat sealed to itself to provide strong seals at pasteurizing temperatures. The preferred film has four layers including, in order, a sealing surface layer comprising a blend of propylene-ethylene copolymer and (butene-1)-ethylene copolymer, a layer comprising ethylene-vinyl acetate copolymer which may be cross-linked to further increase high temperature strength of the film as desired; a relatively gas impermeable layer comprising a copolymer of vinylidene chloride; and a surface layer of the same blend as the sealing layer.
Receptacles such as end seal and side seal begs can be made from the film at a faster rate than with prior art films and these receptacles have the high temperature seal qualities of propylene polymers and the hot water shrink capabilities of ethylene polymers.

Description

g FIELD OF INVENTION:
This invention relates generally to a heat~shrinkable, relatively gas impermeable, thermoplastic packaging film which can be heat sealed to itself to form a bag, pouch, casing or other receptacle~ The invention relates specifically to bags for food products in which the product is held at an elevated temperature for an extended period of time BACKGROUND OF ~IE INVENTION:
A heat shrinkable, thermoplastic, multi-layer packaging film which has enjoyed considerable commercial success for making bags having low gas transmission is described in United States Patent No. 3,741,253 which issued on June 26, 1973 to H.J. ~rax et al. One preferred film in the Brax et al patent may be produced by extruding a first or substrate layer of ethylene-vinyl acetate copolymer as an unstretched tube and then flatting the tube and moving it in a series oE passes through an electron beam to cross-link the molecules of the copolymer. Next, the film is inflated, but not substantially stretched, and passed through an annular coating die where it receives a second layer which comprises a copolymer of vlnylldene chloride. This two layer tube then passes thro~lgh another annu~ar die in which Lt recelves a coating of ethylene-vlnyl acetate copolymer. The tube whlch now has a wall of three polymer:Lc layers and ls cooled, collapsed, and fed through a hot water bath where the tube is sufficlently softened so that lt can be inflated into a bubble which is trapped between two spaced apart pairs of pinch rollers. The inflation causes the tubing to be thinned as it is stretched into film, and, as the bubble leaves the hot water bath it cools quickly in air and becomes oriented. After the bubble is collapsed, the film is wound up as flattened, seamless, tubular film to be later used to make . ....
, :., .,.. ~ .

~7~ 3 bags, e.g. both (1) end-seal bags which are typically made by transversely heat seallng across the width of flattened tubing followed by severing the tubing 80 that the transverse seal forms the bottom of a bag, and (2) side-seal bags in which the tran9verse seals form the sides and one edge of the tubing forms the bottom so the bags can readily be made from the tubing.
In making bags as described above in a rapid commercial operation by pressing the flattened tubing walls together with heated seal bars, the dwell time of the seal bars should be as short as possible yet sufficiently long to fuse and bond the inside surface layer of the tube to itself in a smooth~ continuous, strong seal. The importance of a strong reliable seal is readily understood when the use and function of the bag is described. This type of bag is primarily used to package a large variety of fresh and processed meats by placing the meat in the bag, evacuating the bag, gathering and applying a metal clip around the gathered mouth o the bag to hermetically seal it, and then immersing the bag in a hot water bath at approximately the same temperature at which the film was stretched-oriented. This temperature in the past has typically run from 160 to 205F. ~lot water immersion is one oE the quickest and most economical means oE transEerrlng suEEiclent heat to the film to shrlnk lt unlEormly. Ilowever, one oE the obJec~s of the present inventlon ls to extend the t:Lme at whlch a bag can malntaln its lntegrlty at hlgh temperatures beyond the time normally required for shrinking so that the product in the bag can become pasteurized.
A problem which is associated with the manufacture of side seal bags on certain commercially available machines is that at rapid speeds the seals do not have time to "set-up" and the tension when transporting the tubing can cause the seals to pull apart. For example, when side-seal bags are made from flattened tubing a transverse double seal with a perforation line therebetween is made across the tubing.
The double seal comprises ~wo parallel 7 spaced apart seals and between the two seals and parallel to them a series or line of perforations ls cut. One longitudinal side of the flattened tubing i9 tr:Lmmed off ither be~ore or af~er the d~ble se~al is æ~pli~d to I~rm the top or mouth of the bag. rrhe distance ketween perforation lines is the cverall width of the ~ag.
Inten mttent notion is necessary as k~gs are moved to and ~rom the seal station as there must be a time when the tubing is stopped while the transverse seals are made. T~ n~ve the kags away from the seal station a k~g can ~e threaded around a reciprocating rol~er to pull the tubing for the next bag into pla oe as is the case with the side seal bag machine of Gloucester Engineering Co. of Gloucester, Mass. At a high bag making rate if the side seals are n~t strong, tbe force due to the rapid a- oe]era~ion of the ~ea~i~g bag from a dead stop to advan oe the next kag into th~ æal station will cause the newly forn~d side seals t~ ke Fu~le~ apart as the seals are still wcrm. Prior prac~ice was ~o simply redu oe machine s~e2d and bag ma~ing rate to allow the æ al to cool. Hbwever, it is an cbject of this invention to provide a film ~hich will have strong seals at high k~g making rates.
In addition to end and side seal bags, other rec_ptacles such as pouches and casings can ~e made from ~rm~plastic materials. A
pouch can be fo~m~d ~y placing a product between two ~ep~-ate sheets of film and th~n heat sealing the sheets tcgether ge~erally around the periphery of the product to encloYa it. A casiny can be formed from either seamless tubing by sealing or closing one end of the blbe in a gatherPd closure or ~y forming a tube frcm a sheet by overlapping or butt heat sealing of o~osed edg~s of the sheet together to form a tube afterwhich a g~thered closure is used to close one end of the t~be. A
satisfactory and comm~nly used gathere~ closure m3ans is a m~tal clip.
After filliny the c2siny the c~Pn end usually will be closed also w~th a clip. P~cordingly, æn c~ject of the present invention is to provide a film from which pou~hes _nd c2sings c n be made wnich will withstand pasteuri~ation t~r~Pr2_-~es.

_~

~ ~7'~
Another object of this invention is to provide a film with superior high temperature seal strength and which also will produce a bag having gas transmission characteristics'at least approximately equal to prior art films. Many food products require pasteurization if they are hermetically packaged. The pasteurization is necessary to destroy harmful microbes which grow in the absence of air. In some countries~
for certain products, the requirement of the health 1aws and regulations will be to hold the food product in the evacuated, hermetically closed bag at a temperature of at least 93~C (200DF) for 3 minutes. In other countries the requirement may be to hold the product at 82DC (180~F) temperature for 30 minutes. Thus, it is yet another object of this invention to provide a bag which will maintain seal integrity for extended time periods at temperatures up to the boiling point of water.
Still another object is to provide in one film the high temperature strength of propylene polymers and the hot water shrink capability of ethylene polymers. Propylene homopolymers and copolymers tend to have high melting points, in excess of 300DF, whereas ethylene polymers and copolyrners tend to melt near and be'low the boiling point of water, general'ly below 2ZO~F.
The foregoing objects are achieved by the present invention which is summarized in the paragraphs below.

_ It has ~een surprisingly discc~ered that the problems set forth above can be solved ar~ the objects of the invention can be achieved by a r~lti-layer, heat shrinXable film ~hich includes at ]east four layers, and comprises: (a) a first or sur~ace s~aling layer ccmprising a blend wherein one constituent of the blend is selected ~rom the group consisting of propylene homopolymers an~ oopolyrners and the other constitutent of the blend is selected frcm the group consisti~g of butene-l horropolymiers and cc~olyr~ers; (b) a second or a heat shrink~ble lay~r comprising a p~lyner selected from the group consisting of ethylene hcmopolyners and c~polymPrs; (c) a third or low gas transmission layer ccmprising a polyner selected from the group consisting of vinylidene chloride ccpolyn~rs, vinylidene chloride-acrylate copolymers, and hydrolyzed ethyle.~_ vinyl acetate copolymers; and, ~d~ a fourth or outer sur.ace layer comprising a blend selected from the group of blends sEecified for the first layer, th~ first and fourth layers not nec-essarily comprising iden~ical blends.
In another aspect, the present invention includes the r~]ti-layer film above wherein the ethylene pDlym~r or oopolymer of the second layer is cross-lir~d.
In yet anothe.r a.spect, the present inven~ion is a process of nF~-ing a multi-layer, heat .shrin~able film o~mprising the steps of:
(a) coextruding first and second pDly~eric layers, the first lay OE
comprising a blend selected from the group oonsisting of (1) propylene, homopolymers and oopolymers and (2) butene-l Foly~rs and copolymers and the s~cond layer c~p~ising a polymer selected from the group co~sisting of ethylene pol~ s and oopolymers; and (b) irra~iating said o~e~tluded layers to a d-~age level of at least 2 I~R to cross-link the ethy]ene polymer or copol~ r.

~ ~7~
r ~lCSURE Sl~ E~
~le folla~ g patents are listed and briefly e~plaine~ in compliance with 37 C.F.R. 1.97 and 1.98. For better appreciation of the disclosure in e~ch patent, reference should ~e made to the F~tent itself.

1) U.S. Patent N~. 3,496,061 issued on February 17, 1970 to 0. A. Freshour et al and disclo~es a nu~er of larninated p~irs of layers of two different ,colyolefin materials. Particu-larly, t~o ~yer films are disclosed wnerei~ the layers comprise blends polyisobutylene with ethylene-butene copoly~r, polypropylene wi~h ethylene-pr~pylene copolyrrer, and ethy]ene-butene c~polymer with polyisobutene and low density poly-ethylene.

2) ~.S. Patent No. 3,634,553 issu~d o~ Janu~y 11, 1972 to A. J. Foglia et al and discloses a heat shrinkable film having 10~ to 90% high isotactic polypropylene resin blended with 10%
to 90~ high isotactic content et~ylene/ butene-l copolyrner.

3) ~.S. Patent No. 4,169,910 issued on October 2, lg79 to J. J. Gra~oski and discloses a fi1m suitable for a tras~ b~g having strong seals and including outer layers which (;~n ke ethylene-vinyl acetat~ copolyn~r and a core laye~ which is a blend of p~lyk~tylene with polypropylene.

4) U.S. Patent No. 4,207,363 issued on June 10, 1980 to Stanley Lustig et al and discloses a multi-layel- film for packaging primal meat cuts wherein the fir5t outer layer is a blend ~f pr~p~71ene-ethylene copolymer having less than 6~
ethylene, a (butene-l)-ethylene, and a therm~plastic elastomer;
~ a first core layer oomprising an extrudable adhesive whic-h may ,c be ethylene-vinyl acetate oopolymer having 12% to 24~ vinyl acetate; a s~cond core layel which is a polyvinylidene chloride ccpolymer; an~, a second cuter layer c~prising et~ylene vinyl ac2tate cop~lymer having 10~ to 14~ vinyl acetate.

~FERR~D ~ ~ DI~ r~ 8~ ~3 .
Several crit-eria are net ~ the film of the prese~t invention A film was desired t~at could shrink at }~t w-dter temperatures (160~-205~), could withstand elevated tel~peratures for an extended Feriod of time s~ that foods Eackaged in the film could ~e pasteurized, and could be sea]ed so t-hat b3gs c~u]d be made at a com~ercially acceptable rate.
It was discovered that t-~ combination of layers in t-he multi-layer film of the present invention net all these criteria. An especiall~ surprising feature is that the first layer o~prising the blend of propylene-ethylene ccpolymer and Foly~utylene or (butene~ ethylene co~olymer did not c~servably degrade or lose its sealing ~roperties when irradiated with electrons as described below. Ihe first and æ cond layers are coeitruded toaether and irradiat~d to cross-link the naterial of the second layer. ~rn~ally, non-cross-lin~ a polymers such as propylene-ethylene copolyner, ~kutene-l)-ethylene o~poly~er or Fol~butylene w~uld be exDected to degrade at the dosage le~els used; however, as stated previously, no significant changes in properties wore detected.
Perh3ps the n~st im~ortant featllre of the invention is the ability of the heat seals in bags of the preferred film to withst~nd pasteurization t~rat~res. ~len filled with a product such as c~lred ham ~nd ~rdcuated and hermetically closed, the seals of sid~-seal bags n~ade with film of the preferred emkodiment ~ere able to withstand pasteurization at 93DC (2~0~F) for S minutes and pasteurization at 82~C
(180DF) for 30 minutes.
me seals which al-e reerred to are used to form reoe p~acles such as bags as previousl~ c-scribed hereina~ove.

lhe ~re~err~d e~'t~ m~nt of the iTJt~ntiO,~ can ke r~e ~y t~
p ess similar to that dr-scribr~d for the Bra~ et al p~tent ab~ve exc~pt that the substrate is coextruded in two layers rather than as a single layer. In other words, in ~he first step of maXing the preferred fi1m two eYtruders feed a single annular ~ooPxtrusion die ~here the inner or first layer is a 50-50 b]~nd ~y weight of propylene-ethylene ~aopolymer hav m g 3~ to 4% ethylene by weight and (butene~ ethylene copolymer having ap~roxi~ately 0.65~ ethylene ~y weight. At this point, the outer layer or second layer is ethylene-vinyl acetate ccpolymer having 6%
vinyl acetate content and a melt flow of approximately 2. lhe second layer is about twice as thick as the first layer and will be about 10 mils thick wnereas the first layer will be about 5 mils thick. Ihis coextru~ed t~e has a dianeter of approx~imately 4 1/2 inches. After cooling it is flattened and ~ay be used as a substrate to wnich addi-tional film layers are joined or it ~ay ke guided through a shielded irradiation vault where it passes under the keam of an electron accel-erator to receive a radiation dosage in the range of 2 to 6 me~arads, pre~erably about 3 ~R. Ihe dosaye may be higher, up t~ 10 MR or higher kut the higher d~sages d~ not necessari.ly i~2r~ve ~roperties. Irra-diation by electrons to cross-link t~le molecules in polymeric material is w~ll }-~nown in the art. As stated above, it was surprisingly dis-ccvered that the.material of the f.irst layer could ~e irradiated without obseLvable degradation. ~he film after irradiation can also ke a sukstrate to which additional layers are joined or it could ke heated and stretch oriented to f~rm a tw~ layer, heat shrinkable packaging film.

~ I

Next, a relatively gas impermeable ~ayer or third layer ls applled by inflating the tubing but not stretching it and then passing the inflated tubing through a coating die where the tubing receives a coating of a copolymer of vinylidene chloride and vinyl chloride. The preferred copolymer is a lightly plasticized copolymer of vinylidene chloride and vinyl chloride being a mixture of 10% suspension polymerized and 90% emulsion polymerized copolymer. The emulsion polymerized copolymer consists of about 70%
vinylidene chloride and 30% vinyl chloride and the suspension polymerized copolymer consists of about 80% vinylidene chloride and 20% vinyl chloride.
In the preferred embodiment, the thickness of this vinylidene chloride copolymer layer will be in the range of 3.5 mils to 4.0 mils.
After receiving the vinylidene chloride copolymer layer the coated tubing is fed through another coating die where it receives a fourth or final layer of approximately 6 mils of the same blend as used Eor the first layer. ~f course, this layer and the third layer will not have been irradiated.
The preferred struc~ure at this point has the ~o:Llowing arrangement of layers:
50% PEC E~ VDC-VC 50~ PEC
50% BEC 50% BEC
PEC = Propylene-Ethylene Copolymer: REXENE Polymers Co.
BEC = (Butene-l)-Ethylene Copolymer: SHELL Chemical Co.
EVA = Ethylene Vinyl Acetate Copolymer: "Alathon" (trade mark) brand of du Pont Chemical Co.
VDC-VC = Vinylidene chloride-vinyl chloride copolymer from Dow Chemical Co.

~10~

t7~ 9 After the final layer has been applied, the film is then ~gain cooled and collapsed afterwhich it is fed into a hot water tank haY;ng water at about l90DF where it passes through pinch rolls, is softened by the hot water, and is inflated into a bubble and stretched to a point where the thickness is approximately 2 mils. Suitable thicknesses will range from 1.0 to 4.0 mils. This will be the final thickness of the multi-layer film of the preferred embodiment. As the bubble emerges from the hot water tank it cools rapidly in air and then is collapsed and rolled up into flattened tubing. It is from this tubing of this final thickness that bags are made as described above. This film has low gas transmission rates as does the preferred filrn described in the above mentioned Brax et al patent. Significant properties are su~arized in the table below:

TABLE A

Oxygen ~ransmission Rate: 30 to 40 cc/m /mil/24 hrs./atm.
Shrink Temperature Range: 80DC (176F) to 96DC (205DF) Shrink ~ension: 85DC (185DF) 2 Machine Direction: 245 lhs./in (Longitudinal) ~ransverse Direction: 225 lbs/in2 Optics:
Haze, % 9 Total Transmission, X 91 -- From the flattened tubing of the preferred embodiment side seal bags can be produced at t~ice the rate of unirradiated bags on a Gloucester side-seal bag making machine. If the film i5 not irradiated 7~
th~n th~ seals tend to pull a~lrt ~en an incr~a.se in prodvction rate is attemp~Ed. A~so~ these k~gs nr~et Fasteurization rc~uir~Tents in that when loaded with a p~oduct such as ham, evacvated, and }~rmetically closed the s~als wil~ remain in tact at 93~C 1200F) for 5 munut~s or 82C (180F) for 30 minutes.
~ ne resins or kasic polyn~ric materials fed into the extru~ers to make the film of the present invention can ~e purchased ~rom any of a number of suppliers and these can ke found ky consulting trade publi-cations such as ~odern Plastics~ ia, 1980-1981 on F~ges 815-826 under the heading "Resins and Molding Ccmp~unds." Earlier editions of said Encyclopedia should also be consulted.
The blend of a prcpylene h~mopolymer or copolymer with a b-~tene-l polymer or copolymer for the first layer which is also the sealing surface layer F~ovides a layer ~hich wnen sPaled to itself to form a ~ag gives an exceptionally strong seal at elevated te~¢eratures.
To a here the first layer adequately to the second or shrin~ layer the two are coextruded so that ~le tw~ layers are melt joined or ~onded.
The æ oond layer is believed to control or initiate the shrinkaye of the film, and t~ first and æcond layers compat~ ly shrink with each other.
The seoond lay~rl which can be oriented at a lower temperat~lre, ~r~ly, below the boiling point of wate~, will consc~quently shrink at B lower temperature. The propylene polymers of the first lay~r have shrink temF~ratures significantly above 212DF ~lOOqC) hut ~h~n blended wqth butene-l polym~rs produc~ a composite which will also shrink belo~ 212~F
(lOODC) when properly oriented. Thus, the coextLuded combination of first and qecond layers -~en placed in a hot water bath will exhibit I ' shri ~ proF~rties li~e -~~se o~ ethylene-vinyl ace'~ate coF~lymel. ~his is another surprising ~eature of t}~ invention, i.e., that a film having a significant proportion of propylene Folyner will shrink ~elcw the hoiliny point of water. Ihe first layer is needed for its seal streng*h arld high tem~erature strength kut the higher shrink ten~erature of propylene polylr~rs alorle is not desired and is overcome by the cor~bination of the blend of the first layer and ~y the second layer.
Ihe blend ratio of 50-50 by w~ight for th~ polymers of the first layer is preferred but the blend can be varied from 90:10 ~propylene:
butene) to 40:60 depending on the specific poly~ers used. Fbr example, the propylene ~olymers which are re~dily used and form the preferred propylene constituent of the first layer are propylene h~m~polyners and propylene-ethylene ccp~lymers having an ethylene content in the range from 3.0% to 4.0~ but the e-hylene cont~nt may range from 1% t~ 6~ or greater. Ihe properties of the prc~ylen_ cthylene oopoly~r may vary someH~at with the proportion of ethylene and this will c~use the blend ratio to ke varied. Cptical properties tend to be adversely affecte~ if the butene-l constituent begins to exceed 60%. Ihe butene-1 o~nstituent may com?rise isotactic polybutene-l or (butene-1)-ethylene aopolymer having up to 6~ ethylene.
In the second or shxink laye~ , the vinyl acetate conterlt may range from 3% to 12~ and the nelt flow range from 0.5 to 10.0 with the orientation t~nperature decreasing as the vinyl acetate oontent of the ethylene-vinyl acetate co~olymPr increases. P~lyethylene can also be used as it, too, is cross-linXable b~t ethylene-vqnyl ace ate oopolyner is preferred. End seal bags can be readily n-ade without rradiation of this layer kut in order to produce side seal ~ags at hig~ rates this layer sh~uld ke irradiated.

~7~83l~
For t}~ third or relatively ~dS in~erne~ble ]~yer, hydrolyzed ethylen~-vinyl acetate c~lyner or a vinylidene chloride-aGrylate copol~ner can ke substituted for the vinylidene chloride ocp~lyn~r to effectively decrease gas transn~ssion. It is gnerally not desLrable to irradiate the third layer ~hen vinylidene ch]oride cc$olymer is used besause of its tendency to degrade and discolor. H~ever, radiation do~s not adversely-affect hydrolyzed ethy]ene-vinyl ~setate copolylT~r.
The gas of n~in ooncPrn is oxygen and transmission is considered to be low or the material is relatively gas innper~able w~len its transmission rate is below 70 cc/m2/mil thickness/29 hrs./atms. IhQ multi-layer film of the present in-~ention has a transmission rate ~elcw this value as shown in Table A a~ove.
In the fourth layer, the same blend as the first is preferred but another blend se~ected fro~ the same polymers could ~e selected.
The third and b~urth layers are, zs indicated ab~-~e, not irradiated.
In an alternate emkodiment which is especi~lly suitable for m~king bags ~en the first and second layers are not irradiated, the 50:50 bl~nd b~r the ~irst and fourth layers is again used with the polymers of t~e second and third layers also ren~LirLLng the same. Hbwever, it is preferred thP layer thicknesses before st~et~lm g should ke approximately as follcr~: first layer: 9 to 11 mils; se-ond, 2 to 3 mils; third: 3 to 4 ~ils, and fourth, 3 to 6 mils. l~nen stretched, the final thickness will be a~out 2 mils. End seal bags and side seal kags m~de frc~ this fil~ meet the pasteurization conditions described above.
Plso, using the thicXnesses set forth immediately above, film znd bags ~ee,ins Fasteurizat~on conditions were made with the first and fourth "
layers comprising z ~lend ratio of 70:30, propylenc cth~lene copolymer bD (but~ne~ eth~ e c~polymer.
Havin~ ~a~-ri~ed our invention, we claim:

lg

Claims

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:

1. A multi-layer, heat shrinkable, thermoplastic packaging film which will produce heat seals having improved seal strength at elevated temperatures comprising:
a) a first or surface sealing layer comprising a blend wherein one constituent of the blend is selected from the group consisting of propylene homopolymers and copolymers and the other constituent of the blend is selected from the group consisting of butene-1 homopolymers and copolymers;
b) a second heat shrinkable layer comprising a polymer selected from the group consisting of ethylene homopolymers and copolymers;
c) a third or low gas transmission layer comprising a polymer selected from the group consisting of vinylidene chloride copolymers and hydrolyzed ethylene-vinyl acetate copolymers; and d) a fourth or outer surface layer comprising a blend selected from the group of blends as specified for the first layer.

2. The film of claim 1 wherein the blend for the first and fourth layers comprises a blend of 90% to 40% by weight of propylene-ethylene copolymer having 1.5% to 4.0% ethylene and 10% to 60% by weight of butene-1 homopolymer or (butene-1)-ethylene copolymer having up to 6.0% by weight of ethylene.

3. The film of claim 1 wherein the second layer comprises an ethylene-vinyl acetate copolymer having 3% to 12% vinyl acetate content by weight.

4. The film of claim 1 wherein the second layer comprises polyethyl-ene.

5. The film of claim 3 wherein the second layer comprises an ethylene-vinyl acetate copolymer and the first and second layers have been irradiated to a dosage level of at least 2 MR.

6. The film of claim 3 wherein the ethylene-vinyl acetate copolymer comprises about 6% vinyl acetate by weight and the copolymer has been cross-linked to the equivalent of a dosage level in the range of 2 to 6 MR.

7. The multi-layer film of claim 6 wherein said film has been stretch oriented and has a thickness in the range of 1.0 to 4.0 mils.

8. A process for making a multi-layer, heat shrinkable, thermoplastic packaging film, which will produce heat seals having improved seal strength immediately after being heat sealed to itself, comprising the steps of:
a) coextruding first and second polymeric layers, the first layer comprising a blend selected from the group consisting of (1) propylene homopolymers and copolymers and (2) butene-1 polymers and copolymers and the second layer comprising a polymer selected from the group consisting of ethylene polymers and copolymers;
b) irradiating said coextruded layers to a dosage level of at least 2 MR; and c) after the irradiation step has been completed, joining a third layer of polymeric material to the second layer, and a fourth layer to the third layer.

9. The process of claim 8 including the step of stretching the multi-layer film to orient same.

10. The process of claim 8, wherein the first layer comprises a blend of 90% to 40% by weight propylene-ethylene copolymer with 10% to 60% by weight of (butene-1)-ethylene copolymer or butene-1 homopolymer and the second layer comprises an ethylene-vinyl acetate copolymer.

11. The process of claim 8 wherein the third layer is joined to the second layer by the step of extrusion coating a third layer onto the second, said third layer comprising a polymer selected from the group consisting of vinylidene chloride copolymers and hydrolyzed ethylene-vinyl acetate copolymers.

12. The process of claim 11 wherein the fourth layer is joined to the third layer by the step of coating a fourth layer onto the third, said fourth layer comprising a blend selected from the group consisting of blends specified for the first layer.

13. A receptacle formed by heat sealing together selected surface areas of the film of claim 1.

14. A receptacle formed by heat sealing together selected surface areas of the film of claim 7.

15. A casing formed from the film of claim 7 by heat sealing together two opposed edges of a sheet of said film to form a tube and thereafter gathering and closing one end of said tube.