PROCESS FOR MANUFACTURING HIGH CLARITY FILM CONTAINING ELASTOMERS

Abstract: An elastomer/polyolefin film of improved clarity is prepared by passing an elastomer/polyolefin melt through counterrotating rollers, one of which is a high gloss rubber roller for imparting a relatively high gloss to the film surface in contact therewith.

Description: PROCESS FOR MANUFACTURING HIGH CLARITY FILM CONTAINING ELASTOMERS This invention relates to a process for manufacturing high clarity. films composed of elastomer/polyolefin blends. In one aspect it relates to a process for manufacturing films for medical solution bags. Films for medical solution bags must possess properties of flexibility, clarity, impact resistance, and tear resistance. In addition, they must be capable of maintaining these properties after sterilization. Elastomer/polyolefin blend films are particularly suited for medical solution bags but because of their generally poor optical properties, these films have not been particularly successful in this application. Efforts have been made to improve the -optical properties of these films by passing the melt between metal rollers. This process, however, requires special equipment, has severe limitations in processing thin gauge film (less than 200 microns) uniformly across the film web, and introduces significant machine direction strain which makes the film properties anisotropic. Moreover, the line speeds for the process are slow. U.S. Patent 4,368,240 (Nauta et al) discloses a process for "polishing" synthetic thermoplastic resins such as polycarbonate, polyesters, and polysulfone using a glossy silicone rubber coated roller in combination with a metal chill roll. Significantly, the Nauta et al patent does not involve processing elastomer/polyolefin blends. Nor does it disclose the effects of the process on key physical properties such as clarity, impact resistance, tear resistance, and tensile strength. It has surprisingly been discovered that by passing an extruded molten web of an elastomer/polyolefin blend through the nip of counterrotating rollers, wherein one of the rollers has a mirror-like rubber surface, a film of improved optical properties and improved toughness is obtained. The resilient roller preferably has an outer surface of silicone rubber. In its broadest aspect, the invention comprises a process for the manufacture of a high clarity elastomer/polyolefin blend -film manufactured by (a) extruding a molten web of the blend, (b) passing the molten web at a temperature above its melting or softening point through the nip of a mirror finish chill roll and a resilient roll having a glossy rubber surface, and (c) cooling the web after the nip to form a film having a haze less than 30X and preferably less than 15%. The thickness of the film is preferably between 25 and 250 microns, and more preferably between 50 and 200 microns The polished rubber roller imparts a high gloss to the surface of the film which it contacts The film gloss should be at least 40, preferably at least 60, and most preferably at least 80, all at 600. The gloss of the film in contact with the metal surface preferably is greater than 50 and most preferably greater than 80, also at 600. The elastomer component may include EPR, EPDM elastomers, polyisobutylene, butyl rubber, halogenated butyl rubber, and blends of these. The polyolefin component may include polypropylene, copolymers of propylene, homopolymers and copolymers of ethylene or blends thereof. A preferred polyolefin blend is a blend of polypropylene and low density polyethylene, particularly linear low density polyethylene. The ethylene polymers should have short chain branching from the molecule backbone of at least 10 branches (preferably 10-30 branches) per 1000 carbon atoms For high pressure, low density polyethylene (LDPE), short chain branch lengths are C1 to C4 chains; for linear low density polyethylene (LLDPE), the short chain branches are C2, C4, or C6 branches; and for high density polyethylene (HDPE), the short chain branches are C2 or C branches. Ethylene polymers such as HDPE of low number of short chain branches (less than 10) tend to result in high internal haze The film produced by the process of the present invention possesses properties ideal for medical bag applications and for other uses such as in thermoforming. These properties include a haze value of less than 15%, MD tear strength (Elmendorf) of greater than 4 glmicron, high impact resistance, and autoclavability (at 1 10-1250C). The process of the present invention may be carried out by utilizing conventional extruders and slotted dies used in the manufacture of films. The counterrotating rollers through which the web is passed may consist of a chrome plated chill roll and a resilient roller having a glossy rubber surface. The mirror finish chill roll may be conventional, ranging from 23 to 103 cm in diameter and from 50 to 205 cm wide provided with internal cooling for maintaining the desired temperature on the surface thereof. The resilient roller may be of the type described in U.S. Patent 4,368,240, the disclosure of which is incorporated herein by reference. The roller may include a metal core provided with an intermediate layer of resilient material such as 60 to 80 Shore A durometer rubber and finally by a skin layer of glossy rubber such as silicone rubber. The skin layer and intermediate layer in combination impart a Shore A hardness value in the range of 65 to 95. The skin thickness of the inner layer and skin layer will be dictated by practical considerations for manufacturing the film and economics. Thicknesses that have worked particularly well in processing elastomeric blends of the present invention are a skin layer thickness of 250 microns and an inner layer thickness of 6250 microns. Suitable silicones for coating the roller include silicone resins sold by General Electric under the trade designation RTU 670 and sold by Dow Corning Corporation under the trade designation Sylasticr and Sylgard. These resins can be used in the manufacture of a rubber roll having a high gloss and durable surface as described in U.S. Patent 4,368,240. Moreover, silicone rubber rolls of this type may be purchased from Nauta Roll Corporation of Kensington, Conn. An air knife may be used to assist in cooling the web between the die and the nip of the counterrotating rollers. The cooling effects aid in eliminating draw resonance in this gauge film and also in preventing the web from sticking to the rubber roll. As indicated above, the elastomer/polyolefin film usable in the process of the present invention comprises two main components: an elastomer and a polyolefin. The concentration and variations of each component may be as follows: Concentration (wit.%) Most Component Types General Preferred Preferred Elastomer Blends (olefinic) EPM Elastomer EPDM Elastomer Polyisobutylene l0-85 20-70 20-50 Butyl Rubber Halogenated Butyl Rubber Polyolefin Propylene Polymers Ethylene Polymers 90-15 80-30 50-80 Blends Elastomer Component: The olefinic elastomer component of the composition may comprise an ethylene copolymer elastomer, such as a copolymer of ethylene with higher alpha-olefin. Preferred ethylene elastomer polymers include EPR (ASIA D-1418-72a designation of EPM for an ethylene-propylene elastomer copolymer), or EPDM (ASTM D-1418-72a designation for an ethylene-propylene diene elastomer terpolymer). Also usable are polyisobutylene rubbers, butyl rubbers and halogenated butyl rubbers. Preferred ethylene elastomer copolymers for use herein comprise from 30 to 90 weight percent ethylene, more preferably from 35 to 80 weight percent ethylene, and most preferably from 50 to 80 weight percent ethylene. In some cases an oil extended elastomer can be employed in the compositions of this invention. EPDM is a terpolymer of ethylene, a higher a#pha-olefin such as propylene, and a nonconjugated diene. In such elastomers the nonconiugated diolefin may be straight chain, branched chain or cyclic hydrocarbon diolefins having from 6 to 15 carbon atoms. Of the nonconjugated dienes typically used to prepare these copolymers, preferred are dicyclopentadiene, 1,4-hexadiene, 5-methylene-2-norbornene and 5-ethylidene-2-norbornene. The olefinic elastomer useful in this invention can also be a polyisobutylene, a copolymer of isobutylene and isoprene (generally known as butyl rubber) or a halogenated copolymer of isobutylene and isoprene (generally known as halogenated butyl rubber, s#uch as chlorinated, brominated and chlorobrominated butyl rubber). Butyl rubber is a vulcanizable rubber copolymer containing from 85 to 99.5 pe#rcent combined isoolefin having from 4 to 8 carbon atoms and from 0.5 to 15 percent combined conjugated diolefin having from 4 to 8 carbon atoms. Such copolymers and their preparation are well known, and generally the isoolefin is a compound such as isobutylene and the diolefin is a compound such as butadiene or isoprene. Halogenated butyl rubbers are also well known; chlorinated and brominated butyl rubber generally contain at least 0.5 weight percent combined halogen and up to 1 atom of halogen per double bond in the copolymer; chlorobrominated butyl rubber generally contains from 1.0 to 3.0 weight percent bromine and from 0.05 to 0.5 weight percent chlorine. Polyolefin Component The preferred polyolefins include polypropylene, polyethylene, copolymers of propylene and ethylene, and blends of these. The propylene homopolymer should be highly crystalline isotactic or syndiotactic. Propylene copolymers, referred to as propylene reactor copolymers, either random or block copolymers, containing minor amounts of alpha-olefin comonomer of 2-16 carbon atoms may also be used. Ethylene homopolymers may include high pressure branched low density polyethylene (LOPE). The ethylene copolymers include those of ethylene and alpha olefins having 3 to 16 carbon atoms such as propylene or l-butene (LLDPE). Also included are copolymers of ethylene with unsaturated esters of a lower carboxylic acid or with an unsaturated carboxylic acid. The ethylene copolymers to be employed generally contain from 50 to 99 weight percent ethylene, most preferably from 60 to 95 weight percent ethylene. EVA containing from 5 to 40 weight percent vinyl acetate and EAA containing 5-40 weight percent of acrylic acid are particularly preferred. A preferred melt index (ASTM D-1238, Condition L) for propylene components is from 0.5 to 20, more preferably from 2 to 10. A preferred melt index (ASTM-1238, Condition E), for polyethylene components is from 0.5 to 20, more preferably from 1 to 10. The preferred. ethylene polymer is linear low density polyethylene (LLDPE) manufactured by low pressure processes (Ziegler catalysts) and employing from 3 to 14 wt. % of butene-l, pentene-l, hexene-l, 4#methyl-pentene-l, heptene-l, and octene-l as LLDPE has a density ranging from 0.915 to 0.935 and is substantially free of long chain branching. The preferred polyolefin blends include PP/LLDPE blends ranging in a weight ratio of 1:1 to 4:1. Other Additives: The composition may also include an extender hydrocarbon oil such as that disclosed in U.S. Patent 4,303,571 which functions as a processing aid. Oils sold under the trademarks "Flexon1 and USunpar" are suitable processing aids for purposes of the present invention. The composition may also include fillers such as calcium carbonate and other conventional additives, such as processing aids, and stabilizers. Preparation of compositions usable in this invention can be achieved in several different ways. The various components may be brought into intimate contact by, for example, -dry blending these materials and then passing the overall composition through a compounding extruder. Alternatively, the components may be fed directly to a mixing device such as a compounding extruder, high shear continuous mixer, two roll mill or an internal mixer such as a Banbury mixer. The optional ingredients previously described can be added to the composition during this mixing operation. It is also possible to achieve melt mixing in an extruder section of an extrusion coating apparatus. Overall, the objective is to obtain a uniform dispersion of all ingredients and this is readily achieved by inducing sufficient shear and heat to cause the plastics component(s) to melt However, time and temperature of mixing should be controlled as is normally done by one skilled in the art so as to avoid molecular weight degradation. In operation, the elastomer/polyolefin blend is extruded from a slotted die to form a molten web which is passed through the nip of the counterrotating chill roll and resilient roll. An air knife may be used on either or both sides of the web to assist in the cooling action if the drawdown is sufficient to cause draw resonance. The web enters the nip at a temperature above the melting point of the blend. The resilient roller presses the web into intimate contact with the chill roll causing the web to cool and solidify. The web is carried around a circumferential portion of the chill roll and withdrawn and formed into a roll in the conventional manner. The following resin blends were prepared by mixing the components in the proportion indicated and extruded to form films thereof by processing described below: Polyolefin (Wt. X) Film Blend Elastomert. LLDPE PP HDPE A 401 603 B 405 603 C 256 147 613 D 309 708 7O# E 302 F 305 704 G 309 708 1 Vistanex L-100 (PIB) of Exxon Chemical Company 2 Vistanex L-120 (PIB) of Exxon Chemical Company 3 PP t4 Melt Flow Rate (MFR)) 4 HDPE [ 0.3 Melt Index (MI) ] 5 Butyl 065 (copolymer isobutylene and isoprene) of Exxon Chemical Company 6 Vistalon 719 (EPR) of Exxon Chemical Company 7 LLDPE (1 MI) 8 PP (PPRC 4MFR) 9 Vistalon 1721 (-EPDM) of Exxon Chemical Company Test Procedures: Properties of various film samples were measured using the following test procedures: : Relative haze Not on ASTM test* Tensile D882-79 X Elongation 0882-79 Tear D1922 Total Energy Do 709 Secant Modulus 0882-79 % Haze D1003-61 Gloss D2457-70 *Total haze was broken down into the internal and external contributions or sources. A 40% haze may be composed of 30% external and 10% internal haze. Relative haze would then be reported as 75% external, 25% internal. Haze: It has been surprisingly discovered that haze in elastomer/polyolefin blends is predominantly a surface phenomenon. It had previously been believed that the clarity problem with these blends was due to the extent or degree of rubber particle dispersion in the blend. However, the following experiments demonstrated that the problem is due primarily to the surface condition of the film. Haze measurements were taken in air on films that were sandwiched between microscope-Quality glass plates. The same films were then coated on both sides with droplets of oil having a refractive index of 1.492. Assuming surface scattering effects have been minimized, i.e., the R.I. (refractive index) of the oil closely matches that of the film and the glass surfaces are perfectly flat, any residual haze after the oil is applied is predominantly internal to the film. Table I Film Blend A B C D E F Thickness (microns) 100 50 150 150 50 100 Relative Haze External 82 90 93 95 9 55 Internal 18 10 7 5 91 45 The data in Table I reveals that for elastomer/HOPE (0.3 MI) blends (those used commercially in medical overwrap applications) the haze is predominantly internal and crystallite related. However, in the elastomer biblends and triblends of Films A, B, C, and 0, based on polyolefins other than HOPE, the haze is primarily a function of film surface roughness. Effects of Polishing With Silicone Rubber Roll Surface: In order to demonstrate the effects of polishing with a high gloss rubber roll/mirror finish chrome chill roll versus a 3 roll metal stack, the following experiments were conducted. The resin of film blend C was extruded from a conventional slotted die using a conventional extruder and was either cast or processed through the nip of the rubber roll arrangement. Rubber Roll Arrangement: Chromed chill roll maintained at 2l0-3a0C. Rubber roll - silicone coated (purchased from Nauta Roll Corporation, Inc.) The physical properties of the film samples were measured and are shown in Table II. Table II Cast Polished (Conventional) (This Invention) Film Thickness 100 200 300 100 200 300 (microns) Tensile, MD 46,9 33.8 28.7 49.7 42.8 31.0 (MPa) TD 36.6 26.2 23.4 42.1 28.3 19.3 XElongation MD 650 700 700 750 800 700 TD 800 650 650 900 700 650 Tear, MD 3 4 4.4 8.8 4 4.6 (g/microns)TD 12 4.4 4 17.6 4.6 4.8 Total Energy .67 .83 .88 .92 .83 .83 (cm-Kg/micron) Stiffness, MD 614 690 648 476 641 648 (MPa) TO 545 55# 586 345 545 593 The data in Table II reveals that processing by the present invention significantly improves the physical properties of the film for film thicknesses 100 and -200 microns. Heat transfer limitations encountered in the thicker films somewhat limited the effects of the present invention on the properties of those films. The thin film (100 microns) had surprisingly high MD tear. Additional tests have been conducted to compare the effects of processing on film clarity. The resin samples below were processed by the present invention or by conventional 3 roll stack of -metal (chrome) rolls such as that used in metal calendering. Table III presents the comparisons: : Table III % Haze Film Metal-to-Metal Glossy Thickness 3 Roll Silicones Gloss Film (microns) Stack Metal Comb. (600) C 100 Not Possible** 7- 96/97* 200 15 10 66/82 300 20 14 60/62 D 100 Not Possible 4 200 8 4 300 10 6 *5j rubber side/chromed chill roll side **100 microns film of uniform clarity could not be processed on the three roll stack The above gloss data was based on samples produced using mirror finish silicone rubber coated-roller having a Shore A hardness of 78. Additional tests using a dull silicone rubber coating (Shore A hardness 64) resulted in gloss (600) ranging from 7/57 to 18/80 for the blend C films. The samples produced on the three roll stack showed evidence of significant internal stress when viewed under crossed polarized sheets. There was no evidence of internal stress with films processed with this invention. The glossy silicone rubber coated roll improved the film clarity for each thickness. It is significant to note that these improved results were obtained at line speeds in excess of 10 meters/min (mpm) (actual 71.3-73.3 mpm) as compared to 3.3-5.0 mpm for the 3 roll stack arrangement. In summary, the above experiments demonstrate that the films prepared according to the present invention possess clarity, are ideally suited for medical packaging applications and other applications where these properties are important.

Claims: CLAIMS 1. A process for the manufacture of elastomeric film which comprises (a) extruding a molten blend of 10 to 85 wt. % of an elastomer and a 90 to 15 wt. X of polyolefin selected from homopolymers and copolymers -of propylene and homopolymers and copolymers of ethylene having short chain branching no less than 10 branches per 1000 carbon atoms to form a web, (b) passing the web at a temperature above its softening point through the nip of counterrotating rollers, one of said rollers being a mirror finish chill roll and the other roller being a resilient -roller having a highly glossy rubber surface-, and (c) cooling the- blend to produce a film having a haze value below 30%. 2. A process as defined in claim 1 wherein the highly glossy rubber surface imparts a gloss (at 600) of at least 40 to one film surface. 3. The process as defined in claim 1 or 2 tdhBrSiR the elastomer comprises no more than 70 wt. % of the blend. 4. The process as defined in claim 1, 2 or 3 wherein the glossy rubber surface is silicone rubber having a Snore A hardness of from 55 to 95. 5. The process as defined in any one of claims 1-4 wherein the blend comprises from 20 to 70 wt. % of an elastomer selected from EPR and EPDM and the polyolefin comprises from 80 to 30 wt. % of a homopolymer or copolymer of propylene or ethylene or blends thereof. #6. The process as defined in claim 5 wherein, the polyolefin is a blend of crystalline polypropylene and linear low density polyethylene (LLDPE). 7. The process as defined in claim 6 wherein polypropylene comprises the major weight portion of the polyolefin blend. 8. The process as defined in any one of chain 1-7 and further comprising air cooling of the melt in advance of the roller nip. 9. A process for the manufacture of film comprising (a) extruding a molten blend of a polymer blend comprising 20 to 50 wt. X of an elastomer polymer and 50 to 80 wt. % of a polyolefin comprising crystalline # i ne polypropylene and LLDPE, or blends of these, to form a molten web (b) passing the web at a temperature above its softening point through the nip of counterrotating rollers, one of said rollers having a high gloss silicone rubber surface for imparting a gloss of at least 60 to the web surface contacted thereby, and the other surface having a polished metal surface for imparting a gloss (60 ) of at least 50 to the web surface contacted thereby, forming a film having a thickness no greater than 200 microns; (c) cooling the web to produce a film having a haze less than 15%. 10. The process of claim 9 which is carried out at a film line speed of at least 10 metres, per minute. Il. The film prepared by the process of claim 1 and having the following properties: (a) haze of less than 30%, (b) MD tear greater than 4 9/micron, and (c) gloss (600) greater than 40. 12. The film prepared by the process of claim 1 and having the following properties: (a) thickness of 125 micron or less, (b) haze of less than 15%, (c) MD tensile greater than 27 MPa, (d) MD tear greater than 4 g/micron, and (e) gloss (600) greater than 60. 13. The use of film according to claim 11 or 12, or film manufactured by the process according to any one of claims 1 - 10, in medical packaging applications. 14. Medical packaging or packages which comprises film according to claim 11 or 12 or film manufactured by the process according to any one of claims 1 --10,

Inventors: HAZELTON, DONALD ROSS, MIDDLESWORTH, JEFFREY ALAN
Applicants: EXXON RESEARCH AND ENGINEERING COMPANY
Application year: 1985
Main classification: C08J5
IPC codes: B29C47, B29C59, C08L23