ADDITIVES FOR POLYMER COMPOSITIONS

Abstract: The present invention provides an additive system for vinyl chloride polymer formulations to improve both the processing of the formulations and the functional characteristics of medical products made from the formulations. The additive system surprisingly exceeds previously known systems with respect to the melt fabrication and heat stability of the polymer formulations and the desired product characteristics of the products manufactured from such materials. Preferably, the additive system of the present invention comprises optimal amounts of the combination of a zinc salt primary stabilizer with an epoxide secondary stabilizer and a polyethylene external lubricant. Other processing aids and performance additives such as bases, antioxidants and internal lubricants, may be included. The additive system can be utilized with either plasticized or non-plasticized vinyl chloride polymer formulations.

Description: ADDITIVES FOR POLYMER COMPOSITIONS BACKGROUND OF THE INVENTION The present invention relates to vinyl chloride polymer formulations for medical use. More specifically, the present invention relates to the stabilization of a flexible, plastic vinyl chloride polymer formulation for sterilizable medical devices made from the formulations. Various polymer formulae can be utilized to create extruded and molded products such as flexible containers, tubing devices and injection molded articles. As examples, flexible containers and tubing devices are utilized in the medical industry for containing and delivering inter alia, parenteral solutions such as intravenous solutions, dialysis solutions, drugs and medications, nutrition products, respiratory therapy products, blood, plasma and other blood related products. When utilized in the medical industry, these products will often contain or contact fluids or solids that are introduced into a patient's body. It is, therefore, necessary for these devices to be essentially transparent; flexible; essentially free of extractables; nonabsorbent of the fluids or solids to be contained; essentially free of particulate matter; and capable of maintaining a product contained therein under sterile conditions until the product is accessed or removed. The plastic material from which these containers, tubing and other articles are constructed must also meet these requirements. It is also important that the plastic material used in constructing these containers, tubing and other articles is sufficiently strong so that the products constructed from the plastic material have sufficient strength. Furthermore, it is desirable, for economic reasons, that any such plastic material be readily constructed into a container, tubing or other article on commercially available, or easily modified, production machinery. Factors such as production rates, material stabilization, particulate generation, scrap rates and potential regrind are critical considerations in determining the processability of any plastic material used in constructing these types of products. As set forth above, because the plastic material will be processed into flexible containers and other medical devices that either house or come into contact with a medical product that is introduced into a patient's body, it is necessary that the plastic does not contain chemicals that can be extracted by the medical product or are likely to pass with the medical product into the patient's body. This is especially critical with respect to the various additives to the polymer formulation which are utilized to make the plastic material flexible, generally processable and stable. The toxicity of such additives has been a matter of concern and an area of monitoring. It has been customary for medical devices such as intravenous solution bags, dialysis containers, blood bags, administration sets and tubing, to be sterilized thermally or by the action of a chemical sterilizing agent such as ethylene oxide gas. In the case of thermal sterilization, however, there has been the problem that the synthetic resin used in such medical containers, tubing and other articles is required to resist thermal degradation. In the case of sterilization with ethylene oxide gas, there has been the problem that, after sterilization, a good deal of time is wasted before the sterilized medical containers, tubing and other articles are free from ethylene oxide gas. As an alternative, sterilization by radiation has been proposed. Since this method is carried out at low temperatures, there is no longer a requirement that the materials of medical containers, tubing and other articles should be capable of withstanding heat and resisting thermal degradation. Nevertheless, radiation may cause such adverse effects as deterioration and discoloration of the irradiated medical containers, tubing and other articles unless the plastic materials are properly formulated. Vinyl chloride polymers ("PVC") have many excellent qualities which make it one of the world's leading commercial plastics. In the medical industry, PVC is widely used in numerous applications including intravenous and drug delivery containers, dialysis containers, blood bags, solution administration sets, tubing and other molded articles. Various plasticizers, stabilizers and other additives have been relied upon in the processing and utilization of PVC for these medical uses but at the acceptance of some other potentially adverse properties. For example, flexible IV containers are generally required to have low extractables, low absorption, low water- blush haze, low color and transparency. During manufacturing, plasticizers, stabilizers and other additives are utilized during manufacturing for improved processing of PVC, in terms of shorter production times, decreased wear and tear of equipment, absence of particulate matter, low scrap rates and high regrind rates. And ultimately, the PVC container must be stable both during manufacture, processing and use. PVC's acknowledged weakness is thermal instability during processing and use, resulting in dehydrochlorination and conjugated unsaturation, and leading to increasing discoloration as the length of the conjugation increases. Thermal degradation has been retarded by the addition of a combination of certain selected stabilizers, typically including calcium soap, zinc soap, organo-tin compounds including dialkyl tin esters such as alkyl carboxylic esters (such as laurate and stearate) , di(n-octyl)tin maleate polymer and di(n-octyl)tin-S,S'-bis(isooctyl)mercaptoacetate, epoxidized fatty esters and organic phosphite esters. To meet low amounts of extractable materials required of such medical containers, tubing and other articles, stabilization and processing difficulties maybe encountered by degradation of PVC due to low stabilizer content. This low stabilizer content however, has the opposite positive effect by reducing the aqueous extractables from the PVC film. When higher extractables are tolerable or stability of the PVC is more critical, higher amounts of processing aids and stabilizers may be used, but then processing difficulties can be encountered from the plate-out of the excess lubricant or build-up of cross-linked ("cured") epoxides and of other processing aids on the die and chill roll equipment during known extrusion and molding techniques. SUMMARY OF THE INVENTION The present invention provides additive systems for PVC formulations to further improve the processing and functional characteristics of medical devices made from PVC. These additive systems surprisingly exceed previously known systems with respect to the melt fabrication and heat stability of the PVC (e.g., increased thermal stability for faster melt flow during extrusion without discoloration or formation of black particles; decreased plate-out or build-up on the processing equipment; decreased scrap and equipment down-time; increased use of regrind) and the desired product characteristics (e.g., low color, optical haze, water-blush, extractables and particle generation) . The additive systems of the present invention include primary and secondary stabilizers and an external lubricant. Preferably, the additive systems of the present invention comprise optimal amounts of the combination of a zinc salt primary stabilizer with an epoxide secondary stabilizer and a polyethylene external lubricant. Other processing aids and performance additives such as bases (i.e., magnesium oxide, dihydrotalcite, calcium carbonate), antioxidants (i.e.,hindered phenols and amines, organophosphites or phosphonites) , colorants, antimicrobials and internal lubricants may be optionally included. These additive systems may be utilized for rigid, semi-rigid or flexible PVC applications. For example, the additive systems of the present invention provide stability and processability to low or non-plasticized PVC formulations injection molded to produce rigid or semi-rigid products such as filter housings and drip chambers. Likewise, the additive systems of the present invention also provide stability and processability to plasticized PVC formulations typically used to produce flexible IV containers for fluids such as intravenous solutions, peritoneal dialysis solutions, blood and blood products. Commonly known plasticizers include dialkyl phthalates, trialkyl trimellitates alky or aryl benzoates, citrate esters, and poly eric plasticizers such as polyurethanes, terpolymers of ethylene-vinyl acetate-carbon monoxide, and polyesters. Additional features and advantages of the present invention are described in, and will be apparent from, the detailed description of the presently preferred embodiment. DETAILED DESCRIPTION OF THE PRESENTLY PREFERRED EMBODIMENT The present invention provides additive systems for PVC formulations to further improve the processing of materials and the functional characteristics of medical containers, tubing devices and molded articles made from such materials. The preferred composition of the additive systems of the present invention comprises the optimal amounts of primary and secondary stabilizers with external lubricants where the primary stabilizer is a Lewis-acid metal compound which resists extraction from the PVC plastic by aqueous fluids. The optimal amount of primary stabilizer is selected from the group consisting of organo-tin compounds including dialkyl tin esters such as alkyl carboxylic esters (such as laurate and stearate) , di(n-octyl)tin maleate polymer and di(n- octy1)tin-S,S*-bis(isoocty1)mercaptoacetate; organo-zinc compounds including alkyl carboxylates such as zinc salts of fatty acids (laurate, palmitate, stearate, erucate, behenate, abietates, and the like) and of polymeric ionomers based on combination ' s of monomers such as ethylene, alkyl acrylates, or styrene with acrylic acid, fumaric or aleic acids and the like. This group of primary stabilizers does not include metal ions from Groups IA or IIA (of the periodic table) whose use is known to result in water-blush haze of the plastic formulation when exposed to water (either liquid or vapor) . For example, zinc acts as Lewis-acid catalyst for removing labile chlorines from the PVC, but also initiates polymerization and cross- linking of the oxirane groups of the epoxide secondary stabilizer (discussed below) , in the molten polymer bulk and on surfaces of the melt processing equipments. The primary stabilizer in the PVC formulation is in the range of 0.02 - 0.5 parts per hundred parts of PVC resin ("phr") . Preferably, the primary stabilizer is zinc stearate, preferably present in the amount of approximately 0.05 - 0.3 phr. An advantage of zinc stearate is that it provides high optical clarity before and after sterilization by steam, ethylene oxide, or irradiation. The secondary stabilizer of the present invention is selected from the group consisting of epoxides which are sufficiently compatible with PVC and the other formulation ingredients so as to provide stability of the PVC formulation. Many of these epoxides are also good plasticizers of PVC and some are suitable for being the sole and primary plasticizer in the formulation. Such epoxides may be used singly or in any combination. Suitable epoxides include but are not limited to glyceryl tris(epoxy oleate) , low oxirane content epoxidized linseed or soya oils or partially- hydrogenated unsaturated vegetable oils, propylene glycol bis(epoxy oleate), and copolymers of glycidoxy acrylate. The secondary stabilizer will contain less than approximately 5.2 oxiranes per molecule. The secondary stabilizer is used in the PVC formulation in the range of 5 to 100 phr as required by the application of the formulation. For example, if the additive system is being added to a plasticized PVC for a flexible application (i.e., a flexible medical container), then the preferred range for the secondary stabilizer is approximately 10 - 20 phr. Similarly, if the additive system is being added to a non-plasticized PVC for a flexible application, then the preferred range may be approximately 40 - 80 phr. In the present invention, the preferred secondary stabilizer is propylene glycol bis(epoxy oleate) which typically contains 2.5 oxiranes per molecule. Furthermore, the purity of the epoxides have been found to be a critical factor in obtaining PVC formulations which have low extractability in aqueous solutions, biological fluids and tissues. Melt processing is necessary for practical fabrication of PVC formulations such as those of the present invention. External lubricants provide slip against and isolation from the metals of the processing equipment; for example, film extruder screws, dies, and film cooling rolls; or injection molding screws, sprews and runners. Practical benefits of this lubrication for film extrusion are (i) faster melt flow rates, (ii) less thermal and shear-stress degradation resulting in discoloration, black specks, lower molecular weight and more water extractable byproducts, (iii) prevention of die drag lines, and (iv) prevention of loose particles on the film from buildup of degraded and cross-linked materials on the die lips, with less sticking of the film to the cooling rolls and of the finished film to itself. However, the concentration of lubricant must be sensitively .balanced to achieve such benefits without excess lubricant causing poor conveyance (e.g., throughput) of the melt , build-up of lubricant "plate-out" on the die and extrusion equipment (drag lines, loose particles, and degraded material on the film) , and build-up of "plate-out" on the cooling rolls (loose particles on the film) . External lubricants common in PVC formulations become concentrated, during processing, on the surfaces of the flowing melt, since they are incompatible with the other ingredients of the molten polymer formulation. The epoxide stabilizers and metal-complex stabilizers (and by¬ products) most common in PVC formulations are also Theologically concentrated at the surfaces of the flowing melt due to their lower viscosity relative to PVC. Therefore, the flowing melt surface has a concentrated mixture of epoxide; metal-complex by- products, lubricant, and protonic acids (HCI and carboxylic from PVC dehydrochlorination and subsequent neutralization by carboxylate soaps of the stabilizer system) . Consequently, the epoxide polymerizes, cross-links and adheres to the metal surfaces of the processing equipment and binds with the external lubricant, pulling the lubricant from the flowing melt surface. The tenacity and extent of build-up of this deposit depends not only on the viscosities, concentrations, amounts, and oxirane-reactivity of these components, but also on the polymerization molecular weight and cross-link density, which in turn are determined by the ratio of epoxide to initiator (acid or base) concentrations and the number of oxirane groups and their proximity on the epoxide (i.e., the oxirane equivalent weight of the epoxide) . Therefore, there is an optimum ratio of epoxide to initiator which gives minimum plate-out while providing adequate material stability and low extractability when used with water-based fluids. External lubricants useful in the present invention include, for example, polyethylenes, oxidized polyethylenes, polyethylene iono ers, polyfluorocarbons (e.g., polymers containing TFE, FEP, VF 2 , perfluoroether) , paraffin waxes, ester waxes, amide waxes, poly(et ene ether) , copolymers of ethylene oxide and propylene oxide, polyamides, polypeptides, poly(vinyl alcohol), poly(ethylene-co-vinyl alcohol) , poly(hydroxyalkyl acrylates and methacrylates) , copolymers of acrylic acid or its salts, copolymers of maleic anhydride with ethylene propylene or styrene, and polymers containing sulfonic acid groups and their salts, and, sulfonated poly(aryl sulfones) . Preferably, the lubricant of the present invention is stable during processing and use, and does not contaminate the medical or biological substances which contact the PVC formulation. Each of these lubricants may be used singly or in combination, provided optimization of their concentrations and the ratio of epoxy to initiators (acids or bases, added or generated as by-products) , is determined as discussed above. The performance of the PVC formulations of the present invention, as we have learned, is dependent upon the proper balance between the amounts and properties of the primary and secondary stabilizers and the external lubricants. The appropriate balance of stabilizers and lubricants are especially necessary in order to obtain low color, low extractables and little or no plate-out on melt processing equipment surfaces. Plate-out may be caused by acid or base catalyzed polymerization and cross-linking of the epoxide compounds at the surface of the molten PVC formulation during melt- processing (i.e., compounding or fabrication) which creates a strong epoxide adhesion of external lubricant to metal surfaces contacting the melt. The strength of this adhesion depends on the molecular weight and cross-link density of the polymerized epoxide, which in turn is maximized at so e intermediate stoichiometric ratio of the epoxide to the acid or base initiator, for example, the strong Lewis-acid byproducts of the primary stabilizer (e.g., the chlorides of tin or zinc) or the excess basicity from anti-acid buffers (e.g., magnesium oxide particles) . Prevention or minimization of such plate-out consequently decreases the incidences of loose particles found in the contained fluids which contact the plastic surfaces, because frequently the plate-out breaks away from the processing equipment and returns loosely attached to the plastic surface. Furthermore, avoiding plate-out also prevents contamination of the PVC articles by particles (usually black specks) released from highly degraded plate-out on the hot metal surfaces of the melt processing equipment. Using this theory, we have been able to prevent plate-out even on the troublesome surfaces which are reactive to epoxide and which have high surface energy (typically above 40 dynes per cm) , such as the metal oxide surfaces of stainless steels commonly used to melt fabricate plasticized PVC formulations. Observed extrusions and injection moldings of and analyses of plate-out material compositions the PVC formulation of the present invention support this explanation. A preferred embodiment of the present invention uses a high-density linear polyethylene of moderately high melt viscosity at approximately 0.015 weight percent in a PVC formulation and stabilized by approximately 9.1 weight percent propylene glycol bis(epoxy oleate) and approximately 0.063 weight percent zinc stearate (stearic acid buffered) . When plasticized with approximately 28 weight percent diethylhexyl phthalate, the PVC formulation having the preferred additive system is extrudable as film at high rates without plate-out, discoloration, black particles, or loose particles. Further, the PVC formulation having the preferred additive system is injection moldable without discoloration, black particles, or sticking in the mold. Articles fabricated of PVC having this preferred addivite system are sterilizable by radiation, steam, or ethylene oxide without excessive discoloration, generation of extractables or toxicity. Furthermore, PVC having this preferred additive system provides flexible containers for pharmaceutical or biological liquids which remain extraordinarily transparent after steam sterilization (e.g., little blush or permanent haze) . Several processing and functional test comparisons between film samples of the preferred embodiment of the present invention and of other commercially available PVC formulations are reported in Tables 1 and 2 and Figures 1-5. Each film sample tested is plasticized with equal amounts of diethylhexylphthalate. Table 1 indicates the components of the additive system of the preferred embodiment compared to additive systems of the other PVC formulations. TABLE 1 ADDITIVE SYSTEMS FOR PLASTICIZED PVC MATERIALS 1 Control l 2 Control 2* Control 3* Control -\- Example 3 STABILIZERS - Primary Zinc Stabilizer Zinc - calcium stearate x x Zinc stearate x x x - Secondary Epoxide ^ Approx. 5.2 oxiranes/molecule x x y» Approx. 2.5 oxiranes/molecule x x x LUBRICANTS Ethylene bis(stearamide) x x High density polyethylene x x x Plate-Out/Building-up 4 Particulate Matter 5 1 Each sample material contains diethylexylphathalate 2 Contains approximately 0.2 phr or more of Primary Stabilizer 3 Contains less than 0.2 phr of Primary Stabilizer 4 Appears during processing on extrusion dies and chill rolls 5 Appears during processing typically as black specks TABLE 2 TEST ITEM UV@ UV@ Zinc Oxidizables ΔpH Ammonium 220nm 241 nm (ppm) (ml) (ppm) Tolerance 0.08a.u. 0.05a.u. NMT 0.5 NMT 1.0ml NMT1.0 NMT 0.5 0.48 -0.74 <0.5 0.38 -0.82 <0.5 0.40 -0.73 <0.5 0.40 -0.80 <0.5 0.45 -0.82 <0.5 0.40 -0.82 <0.5 I 0.52 -0.84 <0.5 0.38 -0.84 <0.5 0.32 -0.65 <0.5 0.36 -0.57 <0.5 0.5 -0.40 <0.5 0.35 -0.2 <0.5 The characteristic progression of colors that PVC exhibits on being heated (clear, colorless to yellow to yellow-orange to red to brown) is typical of systems which develop increasingly long conjugated polyene sequences. PVC is quite sensitive to even mild heating and the formation of visible color usually is the first evident indication of degradation. These changes occur long before any of the more serious manifestations of degradation become evident. If heating is continued, physical changes will occur. Static thermal (oven) and dynamic thermal (Brabender) color stability testing provide an indication of early color generation to dehydrochlorination. These stability tests are approximations of the degradation observed during extrusion of PVC film by known processes. By measuring the yellowness index of sample films having additive systems identified in Table 1, the thermal stability is determined. Strips of the sample films were placed in a 370°F (188°C) air circulating oven with strips periodically removed for testing. The yellowness index is measured by known techniques using a Colorimeter available from the Hunter Company. The results of the yellowness index with regard to static thermal stability are plotted in Figure 1. Of the sample films evaluated, the film having the preferred additive system ("Example") displayed the best color stability over time. Further, a film sample containing the preferred additive system and produced with 30% regrind material exhibits identical static thermal stability. Melting and shearing the PVC material in a Brabender Fusion Head in air initially causes dehydrochlorination, leading to a gradual degradation of color. This dehydrochlorination is followed by cross-linking, evidenced by increased viscosity, stiffening and dramatic darkening of color of the PVC material. The Brabender test differs from the thermal heat aging test in that shear is applied to the material while it is being heated to specified temperature. Therefore, the results of the Brabender test depend not only on thermal stability but also on melt lubrication by the formulation ingredients. This is a close approximation to the conditions that the PVC material is subjected to during the melt fabrication processes, such as extrusion and injection molding. Also, recycling of ground trim or regrind means the PVC material has experienced additional heat and melt shear stress. Hence, this test can be used to simulate the addition of regrind back into an extruder or molder with virgin material, a multiple of times. The yellowness index was measured on PVC film samples having the additive systems identified in Table 1. Referring to Figure 2, original film samples were generated by known extrusion methods (number of passes = 0) . The original samples were then processed in the Brabender equipment at 370 β F (188°C), 60 rpm in air, for 20 minutes (number of passes = 1) . Recycling of regrind was completed 4 times with samples having 70 percent original film and 30 percent regrind from the immediately prior sample (number of passes = 2, 3, 4, 5). For example, samples for pass 2 were 70 percent original film and 30 percent regrind film from pass 1 samples. The results of the yellowness index are plotted in Figure 2. The film sample having the preferred additive system (Example) displayed the best color stability under processing conditions similar to conditions typical of known extrusion processes (heat, shear and contamination with regrind) . Further, we have learned that an optimal concentration of primary stabilizer, preferably zinc stearate and secondary stabilizer, epoxide, preferably propylene glycol bis(epoxy oleate), has resulted in surprising and unexpected improvements to the thermal stability and processability of the PVC material. Zinc stearate ("ZnSt 2 ") reacts to replace labile chlorocarbons on PVC in accordance with Formula 1 and to neutralize hydrochloric acid as in Formula 2. PVC + ZnSt 2 > PVC-St + ZnClSt + ZnCl 2 (1) ZnSt 2 PVC ■ > (HC1) ——> ZnClSt + HSt (2) Referring to Figure 3, excessive concentration of zinc stearate (e.g., Control 4) will result in an increase of zinc chloride which will catalyze further degradation and dehydrochlorination of PVC. We have discovered that excessive zinc chloride will also act as an initiator for the cross-linking of epoxide, causing a greater amount of plate out during the extrusion and black particles during extrusion or injection molding. In this way, excessive zinc chloride will also cause depletion of oxiranes, resulting in further loss of stability. Conversely, if the concentration of zinc stearate (e.g., Control 3) is too low, PVC will dehydrochlorinate with by-product HC1, which accelerates this degradation process and initiates the cross-linking consumption of the oxiranes. Stabilization by an optimal amount of epoxide occurs through the neutralization of HC1 (Formula 3) and the consequently lower zinc chloride formation (Formula 4) . PVC + O PVC-0- •Cl (3) / / R R R' ZnCl, + .0, ZnCl-0< 'Cl (4) \. R ZnClX + where X-is -OH or stearate. However, an excessive concentration of epoxide does not provide significantly better stabilization of color, but rather, results in more cross-linked epoxide, initiated by acids generated during heating. Otherwise, low concentration of epoxide will be rapidly consumed and, therefore, insufficient in providing stabilizing protection. By utilizing the preferred additive system, further processing efficiencies and savings are realized. As indicated in Table 1, we have surprisingly found that plate-out or build-up of material on the processing equipment is not experienced when the additive system of the present invention is used. Therefore, higher amounts of lubricant may be used for improved melt fabrication without suffering plate-out. This absence of plate-out on extrusion dies and build-up on chill rolls eliminates down time of extrusion equipment. Further, generation of dark particulate matter from build-up within the melt processing equipment during processing is not experienced. An approximate 20-30% reduction in scrap rates is achieved when using the additive system of the present invention as compared to currently available PVC materials. Improved product characteristics have also been realized when products are manufactured from PVC material having the inventive additive system. For example, medical containers, ports and tubing made from such PVC material have lower extractables and improved transparency after steam sterilization. Following Japanese Pharmacopeia XII Monograph ("JPXII") for extractive substances in medical containers, extruded film materials of PVC formulations containing various additive systems, as reported in Table 1, are examined. Film samples are cut into strips and autoclaved at 121°C for 1 hour in 200 ml of distilled, deionized water. The aqueous extract is analyzed for the presence of zinc, ammonia, and oxidizables; a change in pH; and, UV absorbing substances (at 241 and 220 nm wavelengths) . The results shown in Table 2 of the JPXII extractive substances data of film material samples with and without regrind confirm that the film material having the PVC additive system of the present invention is within the tolerance guidelines of the JPXII standards. Further, Figure 5 provides a comparison of oxidizables and Figure 6 provides a comparison of the UV absorbing substances in the aqueous extracts of film material having the PVC additive system of the present invention compared to the other PVC films. It should be understood that various changes and modifications to the presently preferred embodiment described herein will be apparent to those skilled in the art. For example, it is foreseeable this inventive additive system is useful for chlorinated polyolefins such as chlorinated polyethylene and polypropylene as well as for PVC. Such changes and modifications can be made without departing from the'spirit and scope of the present invention and without diminishing its attendant advantages. It is therefore intended that such changes and modifications be covered by the appended claims.

Claims: We claim: 1. An additive system for a polyvinyl chloride formulation for improved processability while maintaining thermal stability of the formulation, the additive system comprising: a primary stabilizer which is a Lewis acid metal compound selected from the group consisting of organo-tin compounds and organo-zinc compounds; a secondary stabilizer selected from the group consisting of epoxide compounds having less than approximately 5.2 oxirane groups per molecule; and, an effective amount of an external lubricant for lubrication of the PVC formulation, wherein the ratio of the primary stabilizer to the secondary stabilizer maximizes thermolytic color stability while limiting generation of excessive build-up, plate-out, and dark particles during the processing of the polyvinyl chloride formulation. 2. The additive system of claim 1 wherein the primary stabilizer is zinc stearate in amount of approximately 0.02 to 0.5 parts per hundred parts of the polyvinyl chloride. 3. The additive system of claim 1 wherein the secondary stabilizer is propylene glycol bis(epoxy oleate) in an amount of approximately 5 to 100 parts per hundred parts of the polyvinyl chloride. 4. The additive system of claim 1 wherein the external lubricant is a high-density polyethylene. 5. An additive system for a polyvinyl chloride formulation for improved processability while maintaining thermal stability of the formulation, the additive system comprising: a primary stabilizer is a Lewis acid metal compound selected from the group consisting of organo-tin compounds and organo-zinc compounds, in amount of approximately 0.02 to 0.5 parts per hundred parts of the polyvinyl chloride; a secondary stabilizer selected from the group consisting of epoxide compounds having less than approximately 5.2 oxirane groups per molecule, in amount of approximately 5 to 100 parts per hundred parts of the polyvinyl chloride; and, an effective amount of an external lubricant for lubrication of the polyvinyl chloride formulation. 6. The additive system of claim 5 wherein the primary stabilizer is an organo-tin compound selected from the group consisting of dialkyl tin esters, di(n-octyl)tin maleate polymer and di(n- octy1)tin-S,S'-bis(isoocty1)mercaptoacetate. 7. The additive system of claim 5 wherein the primary stabilizer is an organo-zinc compound selected from the group consisting of alkyl carboxylates including zinc salts of fatty acids and polymeric ionomers based on combinations of monomers ethylene, alkyl acrylates, or styrene with acrylic acid, fumaric or maleic acids. 8. The additive system of claim 5 wherein the primary stabilizer is zinc stearate. 9. The additive system of claim 5 wherein the secondary stabilizer has approximately 2.5 oxiranes per molecule. 10. The additive system of claim 5 wherein the secondary stabilizer is propylene glycol bis(epoxy oleate). 11. The additive system of claim 5 wherein the external lubricant is selected from the group consisting of polyethylenes, oxidized polyethylenes, polyethylene ionomers, polyfluorocarbons, paraffin waxes, ester waxes, amide waxes, poly(ethylene ether) , copolymers of ethylene oxide and propylene oxide, polyamides, polypeptides, poly(vinyl alcohol) , poly(ethylene- co-vinyl alcohol) , poly(hydroxyalkyl acrylates and methacrylates) , copolymers of acrylic acid or its salts, copolymers of maleic anhydride with ethylene propylene or styrene, and polymers containing sulfonic acid groups and their salts, and, sulfonated poly(aryl sulfones) . 12. The additive system of claim 5 wherein the external lubricant is high-density linear polyethylene. 13. The additive system of claim 5 wherein the amount of the primary stabilizer is approximately 0.05 to 0.3 parts per hundred parts of the polyvinyl chloride. 14. The additive system of claim 5 wherein the amount of the secondary stabilizer is approximately 10 to 20 parts per hundred parts of the polyvinyl chloride. 15. The additive system of claim 5 wherein the amount of the secondary stabilizer is approximately 40 to 80 parts per hundred parts of the polyvinyl chloride. 16. A medical product produced from a polyvinyl chloride formulation having an additive system, the additive system comprising: approximately 0.06 weight percent of a primary stabilizer which is a Lewis acid metal compound selected from the group consisting of organo-zinc compounds; approximately 9.1 weight percent of a secondary stabilizer selected from the group consisting of epoxide compounds having less than approximately 5.2 oxirane groups per molecule; and, approximately 0.015 weight percent of an external lubricant. 17. The medical product of claim 16 wherein the product is produced by extrusion processing of the polyvinyl chloride formulation having the additive system. 18. The medical product of claim 16 wherein the product is produced by injection mold processing of the polyvinyl chloride formulation having the additive system. 19. The medical product of claim 16 wherein the product is used to contain aqueous solutions, biological fluids and tissues. 20. The medical product of claim 16 wherein the product is tubing.

Inventors: BUAN LILLIAN, LAURIN DEAN, BUAN, LILLIAN, LAURIN, DEAN
Applicants: BAXTER INT, BAXTER INTERNATIONAL INC.
Application year: 1993
Main classification: C08K5
IPC codes: A61J1, A61L29, C08K5, C08L27, C08L63