COMPOSITE POLYMERIC ARTICLES

Abstract: Composite polymeric articles, which may be in layer or film form, comprise a larger portion of a polymer which is water-soluble at 20 DEG C against a smaller proportion of a polymer which is substantially water-insoluble at that temperature. For example, a layer product may have a thin layer (e.g. less than 5 mu m) of insoluble polymer superimposed on a thicker layer (e.g. at least 20 mu m) of soluble polymer. Both polymers are conveniently polyvinyl alcohol, which is non-toxic and useful in a number of domestic applications e.g. as a nappy backing sheet. The insoluble portion gives water resistance but negligible mechanical strength; the soluble part gives the mechanical strength. On dissolution of the soluble portion, the insoluble portion disintegrates mechanically. Articles may be made by co-extrusion or by moulding.

Description: COMPOSITE POLYMERIC ARTICLES FIELD OF THE INVENTION This invention relates to articles, and in particular aspects to articles in sheet form, which are composites of two organic polymers having- different properties. Important applications of this invent-i-or- concern articles and materials which can readily be disposed of when no longer required. BACKGROUND OF THE INVENTION It has been known to make polymeric articles which are purposely designed to be able to be destroyed by dissolving them, using soluble polymers such as polyvinyl alcohol. Polyvinyl acetate is a water-insoluble polymer which is obtained by polymerization of vinyl acetate. This polymer is used for the production of polyvinyl alcohol by hydrolysis or alcoholysis to remove the acetyl groups from polyvinyl acetate. This removal of acetyl groups may be carried to partial completion so as to give a product which is a copolymer of vinyl alcohol and vinyl acetate. If vinyl alcohol predo .nates, but there is still a substantial quantity of vinyl acetate present. such a copolymer is soluble in cold water and is frequently referred to as "partially hydrolysed" polyvinyl alcohol. The residual vinyl acetate content is typically about 11 wt% corresponding to about 12 mol%. If the reaction is taken further, close to completion, the crystallinity of the polyvinyl alcohol increases and the solubility in cold water decreases very markedly. Material of this type is referred to as "fully hydrolysed" polyvinyl alcohol. Its content of residual vinyl acetate is typically no greater than 3 mol%. Polyvinyl alcohol can be made into film or sheet form. US-A-4444839 (Hoechst) describes PVA labels which are soluble only in hot water, but which have an adhesive fixing layer which can dissolve in cold water enabling easy detachment of the label. The adhesive may be a polyvinyl alcohol. It is also known 'to make hospital laundry bags from partially hydrolysed polyvinyl alcohol sheet. The idea is that such bags can be filled with dirty laundry and the entire bag with its contents can then be put into a hospital washing machine where the polyvinyl alcohol will dissolve on contact with the wash water, thus releasing the laundry into the wasn water. In practice there is a difficulty that the laundry may itself be wet and if the wet laundry contacts the material of the bag it can dissolve it prematurely so that the bag falls apart. Unsuccessful attempts have been made to rectify this by modifying the solubility properties of the polyvinyl alcohol. For example, DE-A- 3017246 (Melchior) describes laundry bags made primarily of relatively insoluble PVA which will not disintegrate except in hot water. To enable the desired emptying of the bag in a cold wash, a subsidiary inner layer of the bag is made of cold-soluble PVA which can form releasacie welds. [The Invention] Broadly, this invention provides an article or material comprising a first organic polymer which is water-soluble at a given temperature, typically 20°C, and a second organic polymer located directly adjacent thereto, which second organic polymer dissolves more slowly or not at all in water at the same given temperature e.g. 20°C, with the quantity by weight of the first (water-soluble) polymer being greater than the quantity of the second polymer. It will be explained in more detail below that the first, water-soluble, polymer is preferably partially hydrolysed polyvinyl alcohol. The water-insoluble organic polymer may be fully hydrolysed polyvinyl alcohol. Generally both polymers will feel dry, not tacky, to the touch. In certain forms of this invention the article or 4 material is laminar with adjacent layers of the two polymers. Such a form of the invention could be polymer film or sheet to be used in industrial production processes. Further forms of the invention are articles comprising pieces of such polymer sheet or film. In particular, the pieces of polymer sheet or film may be shaped to have curvature in more than one direction. Articles and materials of this invention have the property that if an exposed surface of the first polymer is brought into contact with water, it dissolves but where a first polymer surface is overlaid by the second polymer that surface is protected. The second polymer acts as a barrier and protects the first polymer against dissolution if the protected surface gets wet. Usually, the two types of polymer will be substantially co-extensive in the article or material e.g. a continuous uniform multilayer laminate film, or a body of the soluble polymer substantially surrounded by a coat of the insoluble polymer. The second polymer can be a surprisingly thin layer, so thin that it does not remain intact after the first polymer dissolves. Then the first polymer s relied upon to provide mechanical strength while the second polymer is relied on for a water-barrier. Such functionality has a wide range of applications. In general the articles and materials of the invention can be used where it can be arranged that at first the slower-dissolving second polymer acts as a barrier protecting the water-soluble polymer from a material which is, or might be, wet and then at a later stage an unprotected surface of the water-soluble polymer is allowed to come into contact with water. The consequence of this is that dissolution cf the soluble polymer takes place when desired but premature dissolution s prevented by the second polymer. One possibility, mentioned here as an illustration, is laundry bags made from polymer film which is water- soluble with a very thin layer of water-insoluble polymer on the inside of the bags. If the laundry happens to be wet, it will not cause the bags to dissolve prematurely because of the barrier function of the very thin insoluble layer. When the bags are put intact into a hospital washing machine the soluble layer is now contacted by the waεn water en the outside cf the oaσε and dissolves. The very thin insoluble layer rapidly breaks up, releasing the laundry into the wash water. The pieces of the insoluble layer are washed into the sewage system with the wash water at the end of the washing procedure. The presence cf insoluble polymer in the sewage system need not be a problem because the preferred material, namely fully hydrolysed polyvinyl alcohol, is 1556 PCI7GB91/01237 - 6 bio-degradabl . Another possibility is to have a piece or layer of the first polymer surrounded by the second polymer, so that the article can maintain its integrity in the presence of water unless broken or ruptured, allowing water to attack the first polymer. The preferred soluble polymer is partially hydrolysed polyvinyl alcohol. As already mentioned above this is a copolymer of polyvinyl alcohol with vinyl acetate. Generally these copolymers are hydrolysed to an extent between 75 and 95 mol%, more commonly between 80 and 90 mol%. Thus, the mol ratio of vinyl alcohol to vinyl acetate lies between 75:25 and 95:5, more preferably 80:20 and 90:10. Partially hydrolysed polyvinyl alcohol is fully bio-degradable. This has the considerable benefit that if the polymer is allowed to dissolve in water which is then run to waste, the polymer which enters the sewage system will degrade into ecologically acceptable products. For this reason it may be desirable that the soluble polymer does not incorporate any other monomer although the possibility of incorporating a further comonomer is not excluded by this invention. The speed with which the more rapidly soluble first polymer dissolves can be altered by selection of the polymer and also by selection of processing conditions. as will be mentioned below. The length of time for this polymer to dissolve can be chosen according to the use envisaged for the article or material and can range from a matter of seconds to several hours. The speed with which partially hydrolysed polyvinyl alcohol dissolves decreases somewhat with increasing molecular weight of the polymer. Higher degrees of hydrolysis ( so long as the material remains only partially hydrolysed) tend to decrease speed of solution. Subjecting the polymer to heat during processing also retards the speed with which the eventual processed polymer will dissolve. The more rapidly soluble polymer used in the present invention will generally have a speed of solution such that when a sheet of the polymer with at least one side face of the sheet exposed is placed in distilled water at 20°C, the sheet dissolves sufficiently to break up within a period of time not longer than 24 hours, usually not longer than 8 hours and possibly very much shorter than this e.g. less than 10 sees for a test sheet 50um thick. The relatively less soluble polymer should of course dissolve more slowly than the more soluble polymer. For many applications it will be desirable that the polymer is essentially insoluble, to the extent that if a test sheet of the material with sufficient thickness to be handled, e.g. 50μm, is placed in sterile distilled water 8 at 20°C, the sheet remains undissolved and intact for a period exceeding 8 hours and perhaps more than 24 hours. It is however possible that a soluble polymer which dissolves slowly will provide adequate barrier protection for a faster dissolving polymer in certain applications. The relatively slowly dissolving polymer is preferably fully hydrolysed polyvinyl alcohol or a suitably insoluble polyvinyl alcohol copolymer. Fully- hydrolysed PVAs are over 96 mol% hydrolysed; commonly over 98 mol%. They are in fact appreciably water- soluble at raised temperatures, e.g. over about 50°C, and usually highly soluble over about 80°C, although some special types can withstand such temperatures for some time without dissolving. At about room temperature, however, solubility is sparing and particularly so for the more highly polymerised PVAs. It will frequently be preferred that both polymers are biodegradable, meaning that when discarded into sewage or otherwise exposed to water and natural bacteria, they decompose to naturally occurring chemical species within a few months at most. Using polyvinyl alcohol for both layers achieves this result. The articles of the invention will usually have the "insoluble" polymer exposed to the exterior. The soluble polymer may also be exposed, or may be enclosed by the insoluble polymer. However the insoluble layer will usually contact only the exterior and the more soluble polymer; not any adhesive or other type of layer. In the article or material, the weight ratio of the more soluble to the less soluble polymer will preferably be at least 2:1, more preferably at least 3:1, still more preferably at least 5:1 and perhaps above 10:1 up to even 100:1, particularly for thick or three-dimensional articles. In an alternative preferred aspect, the less soluble polymer covers the more soluble polymer with a general thickness which is preferably not more than 20μm, more preferably not more than lOμm, most preferably not more than 5μm. It may be as thin as 2μm or thinner. In a film product, the total film thickness may range typically from 5μm to 1mm, more typically from lOμm to 200μm. Each polymer may be used in admixture with other substances. In particular, a plasticiser is usually desirable to achieve a pliable film product. Glycerol, trimethylol propane, and glycols are suitable plasticisers. Colours and/or fillers may also be used if desired, in one or both layers. These may be conventional. Articles may take various forms, for example, a film may comprise just two layers, one of each kind of polymer. Or, the film may be a sandwich of more soluble 10 polymer between layers of less soluble polymer. Non-film articles may comprise a "core" of the soluble polymer substantially or entirely covered by the less soluble polymer. Such an article can resist attack by water, but when it is broken water can dissolve the exposed core and hence the entire article may be disintegrated. In another aspect, the invention provides processes for preparing composite articles and materials as described above. There are a number of ways of forming respective portions e.g. layers of the two polymers superimposed and bonded together as a composite article e.g. film or sheet. Broadly these are various (a) casting/moulding and (b) extrusion processes. A cast/mould process for film or sheet involves forming a first of the layers - the less soluble one if PVA - on a flat or shaped surface and subsequently applying the second layer on top of it. Application may be e.g. by spraying or by a dripped feed. PVA can be applied with water e.g. as an aqueous solution or dispersion optionally containing plasticisers, thickeners etc. as appropriate, from which water is evaporated in forming the two layers of polymer. Extrusion preferably involves co-extrusion of the two layers. Blown film co-extrusion is preferred. The process can be an adaptation of the known process for forming a blown film from a single PVA polymer. The conventional production of PVA film by extrusion entails feeding a plasticised volume e.g. an aqueous solution or dispersion of the PVA, to a die with an annular extrusion orifice surrounding an air inlet. As the plasticised polyvinyl alcohol is extruded from the orifice it forms a tube which is blown out into a larger diameter tube by the pressure of air introduced through the air inlet. The blown tube is drawn off between a pair of nip rollers which close off the air space. A high pressure, short screw extruder is suitable. This usually has a smooth bush, and e.g. a vibrating trickle feeder to avoid overloading the screw, which can be a problem with PVA. A film-blowing process which is one aspect cf this invention comprises supplying an appropriate extrudable form e.g. solution or dispersion of the polymers tc respective extrusion orifices of a die, the orifices being annular and one within the other, so as to extrude tubes of the polymers from the orifices, while also supplying gas pressure to the interior of the inner tube thereby expanding both tubes and uniting the inner tube with the outer tube to form a single tube made up from layers of the two polymers. The extrusion machinery can resemble conventional machinery for forming blown films of polyvinyl alcohol except however that its extrusion die has two annular orifices instead of the usual single orifice and a feed screw for each orifice with associated means for supply to each feed screw. The gas which is blown in is suitably hot air, via an inlet within the inner annular slit. The heated air can also evaporate water from the PVA so that the film bubble dries and can be passed through e.g. nip rollers above the die. Extrusion of PVA, including blown film extrusion, is known technology and the skilled man will be able to select suitable conditions, for example a die temperature in the region of 150°C, etc. The relative rates of feed to the die orifices and concentrations of the polymers can be adjusted to achieve the desired ratio of thickness of the two layers. Processing aids such as antifoamers and lubricants may be used if desired. In a third aspect, the invention provides a co- extrusion apparatus adapted for producing bubble-blown film as described above. Particular uses envisaged for the laminar articles include disposable packaging material and barrier layers in sanitary products e.g. nappies and bed-pan liners. These need to be able to withstand wetness on one side; by using film embodying the present invention they can after use be dropped, with their contents, into a WC bowl to disintegrate. The whole can then be flushed away. The advantage in terms of convenience is apparent, while from the environmental point of view PVA is not only biodegradable to harmless CO- and water, but also has no known toxicity and hence does not present.a risk before chemical degradation. Embodiments of the invention are now described by way of example, with reference to the accompanying drawings in which: Fig 1 is a schematic side view of a blown film co- extrusion apparatus; Fig 2 is a schematic top view of the apparatus; Fig 3 is a schematic cross-section of the co- extrusion die of the apparatus; Fig 4 shows steps in making a baby's potty liner; Fig 5 shows a disposable nappy. Fig 6 shows a two layer film; Fig 7 shows a three-layer laminar article, and Fig 8 shows a three-dimensional moulded article. Materials Used In the following embodiments, both the insoluble and soluble layers were made from PW . The PVAs used were "Mowiol" (Registered Trade Mark) obtainable from Hoechst AG. The soluble layers were made using Mowiol 26-88, a partially-hydrolysed PVA having a mean molecular weight of 103000, an 88 mol% degree of hydrolysis and whose viscosity, measured as a 4% aqueous solution, is 26 2 mPa.s . The insoluble layers were made using (i) Mowiol 20-98, a fully-hydrolysed grade in which the mean molecular weight, viscosity and hydrolysis values are 2 70,000, 20 mPa.s and 98.4 mol% respectively, and (ii) a 50:50 blend of Mowiol 56/98 and Mowiol 28/99 which are fully-hydrolysed grades having viscosities and hydrolysis values substantially as indicated by their respective specification numbers, as before. For the cast processes, each of these was made up in a respective aqueous composition containing, by weight, 15% PVA granules 5% glycerine (plasticiser) 80% water. The PVA granules were added to the water and glycerine and then heated at 93°C for fifteen to twenty minutes to form a solution. For the coextrusion process, the make-up of the individual PVA compositions can be selected in accordance with known criteria. Co-extrusion Apparatus An experimental apparatus was set up as shown schematically in Figs 1 to 3. A pair of heated supply tanks 1 were provided, one for each PVA type, and connected to respective intakes of a pair of 10 cm-long feed screws 2. A variable electric drive 3 was connected to drive the feed screws at predetermined proportional rates. Outputs from the feed screws 2 passed in conventional manner to respective extrusion inputs of an upwardly opening co-extrusion die 5. This had two circular and concentric extrusion slit openings 10,11. In the experimental apparatus the outer slit 10 had a diameter of 35 mm and the inner slit a diameter of 25 mm. The width of the outer slit 10 was approximately 0.5 mm and this was approximately four times the width of the inner slit 11. A centrally-opening hole 15 was provided in the die for blowing warm air up through the extrusion rings in conventional manner. Vertically above the die, a. pair of nip rollers 16 were mounted with a take off to a collecting point inot shown) for the film produced. Co-extrusion Process Aqueous extrudable PVA compositions are prepared as described above e.g. from Mowiol 26-88 and Mowiol 20-98, and each put in a respective heated tank 1 of the apparatus. The tank of Mowiol 26-88 (soluble, partially hydrolysed) composition communicates via its feed screw 2 with the outer, wider extrusion slit 10. The Mowiol 20- 98 (insoluble, fully hydrolysed) composition communicates via its feed screw 2 with the inner, narrower extrusion slit 11. The die is heated to 150°C and the heated PVA compositions then fed to the die by their respective screws 2 at rates of e.g. 5:1 ( soluble:insoluble) . At the same time, warm air is blown to the air inlet 17 and out through the hole in the centre of the die 5. A blown film bubble 20 can thereoy be formed above the die, with the thin insoluble PVA layer on the inside. Cooling air is blown, again in conventional manner, over the outside of the bubble above the die. The two extruded layers emerging from their respective slits 10,11 coalesce to form the composite film within a few millimeters of exiting the die. The blown air dries the bubble rapidly to a non- tacky state such that it can be flattened between the nip rollers 16 and collected folded flat, to be cut open into single sheet form subsequently. The process was repeated using the blend of Mowiol 56/98 and 28/99 in place of the Mowiol 20/98, to produce a still less soluble protective thin layer in the film. Mould Process This process was used to make a liner for a child's potty. A convex mould surface 25 (see Fig 4a) was prepared, made from a shaped metal sheet. This had a hat shape, with an upwardly-projecting central portion 26 and a surrounding bottom rim 27 for forming the rim of the liner. An insoluble PVA layer was formed by spraying a solution of Mowiol 20-98 onto the outer, convex mould surface. The solution was as described previously under "Materials Used", but with the substitution of 10% cellulose ether thickener ( "Tylose" (Registered Trade Mark)) for 10% of the water to improve adhesion cf the PVA layer to the sloping sides of the mould 25. This first layer was then dried to tackiness by blowing it with warm air, and a second layer of a corresponding thickened aqueous solution of Mowiol 26-88 was sprayed over it to a considerably greater thickness. In particular, a pronouncedly thick layer was formed on the brim 27 of the former, to strengthen the rim of the liner. After drying the water from this second coat using warm air blowers, the basic composite PVA liner 30 was lifted from the mould 25. An absorbent pad 31 of cellulose wadding was placed in its base, and the flat upper surface of the rim was given a coating of PVA adhesive 32 which was then covered by a ring of siliconised release paper 33. In use, the insoluble inner layer of the liner was able to contain the potty content 1 .; for an extended period without leakinα. To disϋose of both liner and contents the release paper 33 was lifted off and two opposing sides of the rim stuck together face-to-face using the PVA adhesive coat 32, so as to form a sealed bag completely enclosing the contents. The whole was then taken to a WC and dropped into the water where after about ten seconds it had already broken up so much as to be fully flushable. Again, the process was repeated using instead the 56/98 and 28/99 blend to form the insoluble layer. Improved resistance to water was noted. Disposable Nappy A backing sheet 40 for a disposable nappy was made by sequential spraying and drying of two different PVA layers as described above for the liner, but this time o a flat steel surface and without the Tylose thickener. The thicker, soluble layer formed the outside of the nappy and the thin, insoluble layer the inside (uppermost in Fig 5). In the cast sheet, the more soluble layer ma be about 0.1 mm thick and the less soluble layer about 0.02 mm, but these can be adjusted according to the required strength. A conventional cellulosic absorbent pad 41 was affixed to the thin insoluble layer using a commercial PVA adhesive. In an experiment, aqueous liquid was poured onto the padding and the nappy was then rolled up. After being left for eight hours, the nappy was still intact and there was no leakage. However, on putting the rolled-up nappy into a bowl of water, it broke up in seconds and dispersed. Figures 6 to 8 illustrate schematically various forms of article embodying the invention. Figure 6 shows a two-layer flexible film comprising a layer .50 of fully-hydrolysed PVA, 3μm thick, superimposed on a layer ' 51 of partially-hydrolysed (soluble) PVA 25μm thick. Figure 7 shows a disposable drinking cup made from a three layer laminar product. This has a thick intermediate layer 61 of partially-hydrolysed PVA, perhaps 0.5mm thick, giving mechanical strength to the cup. The inner and outer surfaces of the cup have a thin, 5μm coating 60 of fully-hydrolysed PVA which prevents outside moisture, and liquid in the cup, from attacking the intermediate layer 61. To render the cup disposable it need only be torn up, whereupon the intermediate layer is exposed and can be dissolved. Fig. 8 shows a moulded golf tee having a central core 71 of partially-hydrolysed PVA forming the basic shape of the tee. 5μm coating 70 of insoluble PVA covers the tee. The coating may be applied to the moulded "soluble" tee by conventional methods. The tee can withstand normal use. If it is lost, any natural wear or damage will allow natural moisture to destroy it quickly 20 and hence avoid a litter problem.

Claims: CLAIMS : 1. A polymeric composite comprising a first organic polymer which is water-soluble at 20 β C and a second organic polymer located adjacent to the first polymer, the second polymer being substantially less soluble than the first polymer, or insoluble, in water at 20 β C, the quantity of the first polymer in the composite being substantially greater than the quantity of the second polymer. 2. A polymeric composite according to claim 1 in which the second polymer forms a layer less than 20μm thick on the first polymer. 3. A polymeric composite according to claim 2 in which the second polymer forms a layer less than 5μm thick on the first polymer. 4. A polymeric composite according to any one of the preceding claims in which the weight proportion of the first polymer to the second polymer is at least 3:1. 5. A polymeric composite according to claim 4 in which said weight proportion is at leart 5:1. 6. A polymeric composite according to any one of the preceding claims which is laminar, comprising adjacent layers (50,51;60,61) of the polymers. 7. A method of forming a polymeric composite in which a first organic polymer which is water-soluble at 20 β C is formed against a second organic polymer which is insoluble, or substantially less soluble than the first organic polymer, at 20°C, the quantity of the first polymer in the composite being substantially greater than the quantity of the second polymer. 8. A method according to claim 7 in which the second polymer forms a layer less than 20μrn thick on the first polymer. 9. A method according to claim 8 in which the second polymer forms a layer less than 5μm thick on the first polymer. 10. A method according to any one of claims 7 to 9 in which the weight proportion of the first polymer to the second polymer is at least 3:1. 11. A method according to claim 10 in which said weight proportion is at least 5:1. 12. A method according to any one of claims 7 to 11 in which the composite is laminar, comprising adjacent layers (50,51;60,61) of the two polymers. 13. A method according to claim 1 in which the polymers are co-extruded. 14. A method according to claim 13 in which the polymers are blown-film co-extruded.

Inventors: STEVENS HENRY GUY, STEVENS, HENRY, GUY
Applicants: BHP PLASTICS LTD, BHP PLASTICS LIMITED
Application year: 1991
Main classification: B32B7
IPC codes: B29C47, B32B7, B32B27, B32B37, B65D65