ALUMINOSILICATE STABILIZED HALOGENATED POLYMERS

Abstract: The present invention describes halogenated polymer resins stabilized with one or more co-stabilizers, at least one co-stabilizer comprising a synthetic crystalline aluminosilicate of the formula M2/nO . Al2O3 . ySiO2 . wH2O, in which M is a charge balancing cation, n is the valence of M and is 1 or 2, y is the number of moles of SiO2 per mole of A12O3, and is 1.85 to 15 with a preferred range of about 2 to 5, and w is the moles of water of hydration per molecule of said aluminosilicate, wherein said aluminosilicate has a mean crystallite size in the range of about 0.01 mu m to about 1 mu m and a mean particle size in the range of about 0.1 to 10 mu m. Also described is a method for stabilizing halogenated polymers such as PVC and CPVC by incorporating said aluminosilicate into a formulation thereof. A zeolite process improvement for creating a dehydrated zeolite that does not substantially rehydrate is also described. The zeolite created by such process is ideal for use as a co-stabilizer of halogenated polymer resins.

Description: Aluminosilicate Stabilized Halogenated Polymers Background of the Invention This invention relates to stabilizing halogenated polymers and to an improved method for stabilization thereof. More particularly, the invention relates to thermal stabilization of halogenated polymer resms that are normally processed at elevated temperatures into formed articles. In particular, the invention relates to thermal stabilization of such resms with certain synthetic crystalline alummosihcates or zeolite molecular sieves prepared specifically for this purpose Halogen containing polymers, such as polyvmyl chloride (PVC), chloπnated polyvmyl chloπde (CPVC) and other chloπne, fluorine, or bromine containing polymers which are formed above about 150°C tend to degrade and discolor unless stabilized, even when held at these temperatures for the relatively short period of time required for processing When this occurs, the polymer is either unusable or a high rejection rate for produced articles results, and the ability to reuse scrap material from the formation process is seriously impaired. Subsequent to processing such resms, articles made from such halogenated polymers, unless stabilized and properly pigmented, also tend to deteπorate, become brittle and crack or shatter upon prolonged exposure to sunlight or other ultraviolet rays, thereby becoming useless for their intended purpose. These resms in their unstabi zed form also tend to plate out on processing equipment, for example on dies and mill or calendar rolls, as the material is being formed into a finished article This causes imperfections m articles made from such resins and tends to require frequent cleaning of processing equipment used for handling such materials, resulting in inefficiencies in production as well. For example, processing of unstabihzed PVC at elevated temperatures rapidly results in degradation whose symptoms are discoloration, elimination of hydrogen chloπde, and irreversible adhesion to the processing equipment surfaces While all mechanisms for these instabilities are not precisely known, the thermal degradation and perhaps the other indicated forms of instability of halogenated polymers, particularly polyvmyl chloπde (PVC) or chloπnated polyvmyl chloride (CPVC), is manifested in the evolution of HCl It is widely known that HCl catalyzes further degradation Prevention of this degradation requires keeping HCl at very low concentrations and/or neutralizing it dunng processing. Traditional methods for stabilizing halogenated polymers such as PVC have focused on the use of vaπous inorganic, organometalhc and organic stabilizers. Inorganic stabilizers that have been used include for example dibasic, tπbasic, and tetrabasic lead sulfate; dibasic lead phosphite; and white lead. Organometalhc stabilizers commonly used include organic adducts of such heavy metals as barium, cadmium, lead, tin, magnesium, antimony, and/or zmc, frequently m admixture with other co-stabilizers and other conventional additives. Organic stabilizers that have been used include for example, calcium soaps, polyhydπc esters of vaπous fatty acids, phosphites, thioesters, beta-diketones and the like, alone or m combination with such organometalhc compounds as stabilizers for such resms. Alummosihcates or zeolite molecular sieves have also been suggested for use as stabilizers for PVC. For example, U.S. Patent 3,245,946 discloses the use of activated Zeolite A as a stabilizer for PVC resin. And U.S. Patent 4,000,100 discloses the use of an unactivated Zeolite 3 A, 4A, or 5A molecular sieve in combination with a conventional organometalhc or organic stabilizer mixture. It is also known to utilize a complex system of pπmary and secondary stabilizers, including as one component of the stabilization system, a powdered, crystalline, synthetic hydrous aluminosilicate having a water content in the range of 13 to 25% as water of crystallization, as disclosed in U.S. Patent 4,590,233. Among the pπor art utilizing zeolites or alummosihcates as part of a stabilization system for PVC resm, focus has been on such factors as the level of water of crystallization, and/or on pore size of the aluminosilicate. Preferred particle size ranges of zeolites are also descπbed. Presumably certain size ranges give optimal dispersion and enhanced physical properties such as tensile strength and modulus as is known with other solid polymer additives such as calcium carbonate. However, we are not aware of any prior art disclosure that establishes or suggests a direct correlation between reduction in particle size and enhancement of thermal stability. Nor are aware of any significance attached in prior art disclosures to the distinction made with respect to this invention between particle size and crystallite size. Conventional zeolites consist of small cubic or prismatic crystallites and/or other geometric forms such as rhombic, dodecahedral, spheruhte, octahedral, etc., and combinations and tergrowths thereof, that agglomerate into particles. The degree of agglomeration and/or inter-growth determines the particle size distribution, which is typically determined by a light scatteπng or other spectroscopic technique, whereas crystallite size is virtually independent of particle size and is typically determined by scanning electron microscopy images. As an example of this distinction, zeolite 4A and faujasite-type zeolites currently offered on the market typically have a crystallite size of about 1.0 to 5.0 microns with a mean particle size of about 3.0 to 10.0 or more microns. Moreover, while the prior art does recognize methods for reducing particle size, it does not discuss preparative procedures for the small crystallite zeolites as claimed in the present application. While the use of factors such as complex stabilization systems and activation of zeolites has resulted in substantial improvement in the ability of alummosihcates to stabilize PVC resins, still further improvements are required, particularly m the level of thermal stabilization for PVC, CPVC, and other halogenated polymers. Accordingly, it is the pπmary object of this invention to provide an improvement m the thermal stability of halogenated polymer molding resms such as PVC, CPVC, and other halogenated polymers utilized for forming articles at elevated temperature. Brief Summary of the Invention It has now been found that these and other improvements in the stability of halogenated polymer resms are obtained m accordance with the present invention by utilizing as a stabilizing component of such halogenated polymers an aluminosilicate in which the individual crystals have a fine crystallite size in the range of about 0 01 μm to about 1 0 μm Surprisingly it has now been found that while particle size is important in the maintenance of physical properties of halogenated polymer systems, utilization of an aluminosilicate having a fine crystallite size is cπtical to obtaining further improvements in thermal stabilization of these polymers Such fine crystallite particle size stabilizers will normally be employed in combination with conventional inorganic, organometalhc, or organic co-stabihzers. Additionally, it has been found that, for example, in CPVC and rigid PVC formulations where relatively higher concentrations of aluminosilicate are needed than for flexible PVC applications, a particle size in a range of about 0.5 to about 3 μm is preferred. Furthermore, maintaining a relatively low degree of hydration of the aluminosilicate is important to prevent the creation of water bubbles. Steam calcination dehydration of the aluminosilicate to a water content of less than about 8% water by weight of the aluminosilicate prevents rehydration of the aluminosilicate above a water content of 10%. Such steam calcined dehydrated zeolites are particularly well suited for preventing or minimizing water bubbles when used m formulations with relatively high concentrations of zeolite. Detailed Description of the Invention In general, the present invention comprises a stabilized halogenated polymer composition compπsmg a halogenated polymer resin and a stabilizing amount of a synthetic crystalline aluminosihcate having a fine mean crystallite size in the range of about 0.01 μm to about 1.0 μm and preferably a mean crystallite size in the range of about 0.2 to about 1 μm and most preferably m the range of about 0.2 to about 0.85 μm. While crystallite size is cπtical to the present invention, particle size may generally vary withm a wide range, but it is preferable to employ particles having a mean particle size in the range of about 0.1 to about 5.0 μm, and more preferably, especially for CPVC and rigid PVC formulations, about 0.1 to about 3 μm. Also included m the present invention is a method for stabilizing such compounds by admixing the halogenated polymer with the foregoing aluminosilicate, alone or in combination with conventional inorganic, organometalhc, and/or organic co-stabihzers. Polymer resms suitable for use in the present invention are halogenated polymer resms including but not limited to, polyvmyl chloride (PVC), chloπnated polyvmyl chloride (CPVC), polychloroprene (Neoprene), an acrylonitπle-vmyl chloride copolymer (Dynel), a polyvmyl chlonde-vmyl acetate copolymer, polyvmyhdene chlonde, a polytetrafluoroethylene-vmyl chloride copolymer, or a polyfluoro-chloro ethylene polymer, most preferably a halogenated vmyl polymer resin. Polyvmyl chloπde and chloπnated polyvmyl chloπde are particularly preferred resms for use m the present invention. The present invention may be used in both rigid and flexible PVC formulations. As used herein, a "πgid" formulation is defined as having a plasticizer or combination of plasticizers and/or elastomers m a concentration of zero to less than about 5 parts per hundred of resin (phr). A "flexible" formulation typically has from greater than about 5 to as much as about 150 phr plastιcιzer(s). CPVC formulations are typically πgid only. The PVC used for this invention may be one of several types; its properties can vary depending on the polymeπzation method and polymerization temperature. The higher the polymerization temperature, the lower the molecular weight of PVC that is produced. Typical PVC res s have a number average molecular weight m the range of about 20,000 to about 100,000 and a Fikentscher K value ranging from about 41 to about 98. Certain molecular weight PVC resms show optimum physical properties and process performance for particular applications. Generally, suspension PVC resins are more thermally stable than PVC resms produced by mass or emulsion polymerization. Depending on the polymeπzation method and manufacturing conditions, PVC can vary in resm particle size and porosity and may perform differently m the same formulation. The alummosihcates used m the present invention are synthetic crystalline alummosihcates, commonly called 'zeolites.' Zeolites are materials with discreet channels and cages that allow the diffusion of small molecules into and out of their crystalline structures. The utility of these mateπals lies in their microstructures that allow access to large internal surface areas and that increase adsorptive and ion exchange capacity. The alummosihcates or zeolites useful m the present invention may be generally designated by the chemical formula M /n O . Al 2 O . ySιO 2 . wH 2 O m which M is a charge balancing cation, n is the valence of M and is 1 or 2, y is the number of moles of SιO 2 and is about 1.8 to about 15, and w is the number of moles of water of hydration per molecule of the aluminosilicate. Suitable charge balancing cations represented by M in the formula include such cations as sodium, potassium, zinc, magnesium, calcium, tetra-alkyl and/or -aryl ammonium, lithium, NH 4 , Ag, Cd, Ba, Cu, Co, Sr, Ni, Fe, and mixtures thereof. The preferred cations are alkali metal and/or alkaline earth metal cations, with the proviso that, when M is a mixture of alkali or alkaline earth metals compπsmg sodium and potassium and/or calcium, the preferred potassium and/or calcium content is less than about 35%) by weight of the total alkali or alkaline earth metal content. While the number of moles of S1O 2 per molecule of aluminosilicate, represented in the formula by y, may be in the range of about 1.8 or greater, it is suitably about 1.85 to about 15, more suitably about 1.85 to about 10, preferably in the range of about 2 to about 5, and with respect to certain embodiments described below, m the range of about 1.8 to about 3.5. The number of moles of water in the zeolite as water of hydration, represented m the formula by w, is suitably greater than about 0.1, more suitably in the range of about 0.1 to about 10 The zeolite framework is made up of S1O 4 tetrahedra linked by shared oxygen atoms. Substitution of aluminum for silicon creates a charge imbalance that requires a non-framework cation to balance the charge. These cations, which are contained inside the channels and cages of these mateπals, may be replaced by other cations giving πse to ion exchange properties. The water m these mateπals may typically be reversibly removed leaving the host structure intact, although some framework distortion may occur. In addition, these mateπals are typically alkaline. Suspensions of low SιO 2 /Al 2 O 3 ratio materials in water often give rise to a pH greater than 9. This combination of high alkalinity and the pore structure of these compounds is believed to be largely responsible for the ability of these zeolites to stabilize halogenated polymers by neutralizing acids released dunng processing and creating inert salts and/or scavenging excess catiomc metals. Zeolites are frequently categorized by their crystalline unit cell structure (See W.M. Meier, D.H. Olson, and Ch. Baerlocher, Atlas of Zeolite Structure Types, Elsevier Press (1996) 4 th ed.) Those suitable for use as stabilizers in the present invention include compounds charactenzed as zeolite A, zeolite P, zeolite X, and zeolite Y. While other zeolites may also be useful in the present invention, the preferred aluminosilicate is zeolite A. Preferably, there is employed a zeolite which is substantially anhydrous; that is, an aluminosilicate in which much of the water of hydration has been removed by dehydration pπor to incorporation into the halogenated polymer formulation. Such products are frequently referred to by those skilled in the art as "activated zeolites." Suitable activated zeolites particularly useful m the present invention are those which have been dehydrated to a level at which the water content thereof is m the range of about 0.1% to about 20%, advantageously in the range of about 0.5% to about 18% and most conveniently between about 1% and about 15%, by weight of the aluminosilicate. In a preferred embodiment as described below, the zeolite is steam calcined to a water content of less than about 8% by weight of the zeolite. It is also desirable that the aluminosilicate have a mean particle size m the range of about 0 1 to about 10 microns, suitably wherein at least about 90% of the particles are less than about 50 μm, advantageously less than about 25 μm, and most suitably less than about lOum. It is also desirable that the aluminosilicate have an mean micropore diameter in the range of about 2.8 to about 8 angstroms, and/or an external surface area in the range of about 3 to about 300 m 2 /g. As previously indicated, the above identified alummosihcates may suitably be formulated with the halogenated polymer and with a co-stabilizer conventionally employed for stabilization of PVC resms Suitable stabilizers include an organometalhc complex such as magnesium, antimony, cadmium, baπum, tin, calcium, zinc and/or lead, an organic complex such as polyhydπc esters of various fatty acids, β-diketones, organic phosphites, hindered amines, organic mercaptans, epoxidized oils, epoxy compounds and/or phenols, inorganic complexes such as dibasic, tπbasic and/or tetrabasic lead sulfate, dibasic lead phosphite, and/or white lead, and/or various combinations of such organo metallic, organic and inorganic complexes. In accordance with the method aspect of the invention, there is provided a method for stabilizing a halogenated polymer resin compπsing compounding the resin with a stabilizer compnsmg a synthetic crystalline aluminosilicate of the formula M 2/n O . Al O 3 . ySιO 2 . wH 2 O, m which M, n, y and w are as defined above, wherein said aluminosilicate has a mean crystallite size in the range of about 0.01 μm to about 1 μm. In carrying out the process aspect of this invention, the aluminosilicate may be admixed with the polymer during production by admixing the aluminosilicate with monomers of the resin before, during or after polymerization. As with the composition aspect of this invention, it is also preferred that the aluminosilicate have a mean particle size in the range of about 0.1 to about 10 μm. The amount of zeolite added is dependant upon the application, the type of resm employed, and the formulation. For example, in most flexible PVC formulations having a relatively high amount of plasticizer, an effective amount of zeolite typically may be in a range of about 1 phr or less, but more may be used if desired. In πgid PVC and in CPVC formulations, where little or no plasticizer is present, an effective amount of zeolite typically ranges from about 0.05 to about 10 phr. As noted above, as the amount of zeolite is increased, zeolite particle size becomes more cπtical because of potential impact on the physical properties of the plastic. For example, larger particle size zeolites may negatively affect the impact resistance and tensile and flex strength. It is desirable in rigid PVC and in CPVC applications, therefore, to use smaller particle size zeolites that readily disperse in the polymer formulation. Because it is desirable to reduce particle size without fractuπng the zeolite crystallite structure, the acceptable particle size lower limit is limited by the crystallize size. Thus, when smaller particle size zeolites are desired, it is also preferred to use zeolites with relatively smaller crystal sizes. While degree of hydration, nature of the exchangeable cations, selection of co-stabιhzer(s), and pore diameter are known to be important considerations in the ability of alummosihcates to impart thermal stability to halogenated polymers, crystallite size has generally been found to be the most critical factor in obtaining further improvements m the ability of alummosihcates to impart further thermal stability. As noted above, however, in applications where increased concentrations of zeolites are used, particle size is also cπtical Furthermore, in such applications the degree of hydration also becomes more critical. For example, in extrusion operations, concentrations greater than about 1.2 phr of zeolite were found to evolve water bubbles in the extrudate. It is known to dehydrate zeolites by a number of processes to reduce the degree of hydration. We have found, however, that steam calcination under certain conditions is preferred , as the resulting dehydrated zeolite will not substantially rehydrate following such dehydration. The seventy of a steam calcination process is well known in the art to be dependent upon time, temperature, steam content, and pressure. It is also known that sufficiently severe steam or air calcination will destroy the crystalline structure of zeolites. On the other hand, relatively mild steam calcination conditions allow the zeolite structure to be de-alummated and still retain zeolite crystallimty, but also leave the zeolite with the ability to re-hydrate. We have found subjecting low sihca-to-alumma ratio zeolites to moderate steam calcination conditions minimizes deteπoration of the crystalline structure of the zeolite and provides a dehydrated zeolite that does not significantly rehydrate. Such steam calcined dehydrated zeolites are ideal as co-stabilizers for halogenated polymers. A calcination temperature of about 400 to about 700 °C using a steam percentage of about 20% to about 100% steam, for a time and at a pressure sufficient to dehydrate the zeolite to a water content of about 8% or less by weight of the zeolite while maintaining at least 50% of the crystallinity of the zeolite, has been found to prevent rehydration of the dehydrated zeolite to a water content of more than about 10% by weight of the zeolite. For example, 50% steam at 650 °C for 1 hour at atmospheric pressure has been shown to be effective. It is also contemplated that 100% steam at 400 °C for approximately 1-5 hours, or conversely 20%-80% steam at 700 °C for 15 minutes to 1 hour may be also be effective. Surprisingly, simply grinding larger particle size material into a finer particle size alone does not contribute significantly to improvements in thermal stability. Rather the size of the crystallite itself, as opposed to the aggregated particles of crystallites, must be reduced to within the above stated range in order to obtain these improvements in stability. Although zeolite crystal size alone is critical in flexible PVC applications where stability requirements are typically lower, for applications where stability is more important, such as in rigid PVC and CPVC applications where higher concentrations of zeolite are desired, smaller mean zeolite particle size also contributes to improved performance, as described above. Thus, for relatively higher concentrations of zeolite, both particle size and crystallite size are important, and grinding larger particle size material into finer particle sizes, in conjunction with the small crystallinity, provides the desired improved performance. It is desirable to carefully carry out the particle size reduction step, however, to prevent or minimize fracturing of the fine crystallites obtained in accordance with this invention. The reduction in crystallite size may be achieved in the process of manufacturing the aluminosilicate by utilizing a solution containing nuclei to control crystal growth (Solution A) during production of the aluminosilicate, as shown in the detailed preparatory examples set forth below. Example 1 Synthesis of Solution A Reagent grade sodium hydroxide pellets (316.3 g) were added to deionized (316.3 g) water and stirred until the solution was clear. This solution was then heated until it boiled and aluminum trihydrate (63.1 g) was slowly added to the stirred solution until it dissolved. The solution was then cooled below 100°C and deionized water (1090.4 g) was added. A 2.0 ratio sodium silicate (1,237.5 g, SiO 2 /Na 2 O = 2.0, 56 wt. % water) solution was slowly added to the stirred aluminate and aged for at least 12 hours before use. Synthesis of Fine Crystallite 4A Zeolite - Example IB Reagent grade sodium hydroxide pellets (203.5 g) were added to deionized (203.5g) water and stirred until the solution was clear. This solution was then heated until it boiled and aluminum trihydrate (162.0 g) was slowly added to the heated stirred solution until it dissolved. The solution was then cooled below 100°C, diluted with deionized water (180 g), and further cooled to 60°C. Separately, a 2.0 ratio sodium silicate (395 g, SiO 2 /Na 2 O = 2.0, 56 wt. % water) solution was diluted with deionized water (1,615 g) and stirred until homogeneous. Over 15 minutes, the aluminate solution from the preceding paragraph was added to this solution using low agitation. Solution A described above (38.7 g) was then stirred into the solution. The mixture was placed into a water bath, heated to 94°C, and stirred at temperature for about one hour. The resulting slurry was filtered and re-slurried in ambient temperature deionized water (1.0 liter, pH adjusted to 10.5 using NaOH) and filtered. This washing process was repeated one more time and the powder was dried at 100°C for about 12 hours. Example IB is summarized in Table 1 below, together with additional samples (Examples 1 A and IC) prepared using the same procedure substituting the quantities of reagents shown in Table 1. Table 1. Synthesis of Small Crystallite 4 A Zeolites The following examples 2A, 2B and 3 are laboratory preparations prepared generally by adaptation of the procedures described in Zeolite Molecular Sieves, D. Breck, Krieger Publishing Company, Malabar, Florida, Chapter 4, pp. 260-274. Example 2A Synthesis of 4A Zeolite Reagent grade sodium hydroxide pellets (207 g) were added to deionized (207 g) water and stirred until the solution was clear. This solution was then heated until it boiled and aluminum trihydrate (162.0 g) was slowly added to the stirred solution until it dissolved. The solution was then allowed to cool below 100°C, deionized water (240 g) was added, and it was allowed to cool to 60°C. A 2.0 ratio sodium silicate (408 g, SiO 2 /Na 2 O = 2.0, 56 wt. % water) solution was then diluted with deionized water (1,130 g) and stirred until homogeneous. Over 15 minutes, this solution was added to the aluminate using low agitation. The mixture was then placed into a water bath, heated to 94°C, and stirred at temperature for about one hour. The resulting slurry was filtered and re-slurried in ambient temperature deionized water (1.0 liter, pH adjusted to 10.5 using NaOH) and filtered. This washing process was repeated one more time and the powder was dried at 100°C for about 12 hours. The resulting zeolite crystals had a mean crystallite size of 3.0 μm and a mean particle size of 6.53 μm. Example 2B Synthesis of 4A Zeolite Reagent grade sodium hydroxide pellets (207 g) were added to deionized (207 g) water and stirred until the solution was clear. This solution was then heated until it boiled and aluminum trihydrate (162.0 g) was slowly added to the stirred solution until it dissolved. The solution was then allowed to cool below 100°C, deionized water (240 g) was added, and it was allowed to cool to 60°C. A 2.0 ratio sodium silicate (408 g, SiO 2 /Na 2 O = 2.0, 56 wt. % water) solution was then diluted with deionized water (1,130 g) and stirred until homogeneous. The aluminate was added to this solution over 15 minutes using low agitation. The mixture was then placed into a water bath, heated to 94°C, and stirred at temperature for about one hour. The resulting slurry was filtered and re-slurried in ambient temperature deionized water (1.0 liter, pH adjusted to 10.5 using NaOH) and filtered. This washing process was repeated one more time and the powder was dried at 100°C for about 12 hours. The resulting product had a mean crystallite size of 1.25 μm and a mean particle size of 3.07 μm. Table 2. Synthesis of 4A Zeolites Example 3 Synthesis of Small Crystal 13X Zeohte- A solution of 50 weight % NaOH (141 g) was heated until it boiled and aluminum tπhydrate (81 g) was slowly added to the stirred solution until it dissolved. The solution was then allowed to cool below 100°C, deionized water (55 g) was added, and it was allowed to cool to ambient temperature. A 3.2 ratio sodium silicate (194 g, SιO 2 /Na 2 O = 3.2, 62 wt. % water) solution was then diluted with deionized water (901 g) water and stirred until homogeneous. To this solution, over 15 minutes, the aluminate was added using low agitation. Solution A (387.5 g) descπbed above was then added to the solution. The mixture was then placed into a water bath, heated to 94°C, and left at temperature for about six hours. The resulting slurry was filtered and re-slurπed m ambient temperature deionized water (2.0 liters, pH adjusted to 10.5 using NaOH) and filtered This washing process was repeated one more time and the powder was dried at 100°C for about 12 hours. This is Example 3D below. Additional examples, 3A-3C, were prepared using a similar procedure with varying amounts of Solution A. Crystal sizes are summanzed in Table 3. Table 3. Synthesis of Small Crystal 13X Zeolite Example 4 Samples of 4A zeolite varying in crystallite size were compounded into plasticized PVC formulations as shown in Table 4. The formulations for each set of tests were prepared from a common master batch and the indicated amount of zeolite was then added. The master batch was prepared as follows: A Henschel high intensity laboratory mixer was preheated to about 77°C. The PVC resm (l,200g) and epoxidized soybean oil (ESO) were then charged and the mix was agitated at 3000 RPM. When the blend reached 70°C, the di-octyl phthalate (DOP) plasticizer was slowly added. At 75°C, zinc stearate and oxidized polyethylene wax were added and at 80°C, the blend was cooled and agitation was reduced to about 1900 RPM. The mixer was emptied when the temperature dropped below 45°C. The zeolite was then added to each formulation as follows: PVC master batch (300 g) and zeolite (0.59 g) were added to a food-processmg mixer. The powder blend was mixed for 15 minutes. The thermal stability testing of the powder PVC compounds was performed using the Dynamic Thermal Stability (DTS) test. (ASTM method D 2538-95) DTS is defined m the following examples as the time required to reach a 20% increase in torque after equilibrium torque has been established. The DTS test was done using a Haake torque rheometer at the following conditions: 190°C, 100 RPM, and 63 g samples. Table 4. Formulations and Properties * parts per hundred parts resm """Control containing no zeolite As observed from data in Table 4, performance of 4A zeolite as a stabilizer is significantly improved when the size of the crystallites is reduced from 3 to 0.4μm. Further reduction of the crystal size increases the external surface area, but does not improve its performance as a stabilizer. No direct correlation with particle size is observed. Example 5 This example demonstrates the relative effects of particle size reduction using large and small crystallite 4 A zeolite on its performance as a stabilizer for PVC. The 4 A zeolites described in Example 2 were milled using a micronizer™ jet mill at 120 psi to reduce their particle size. The zeolites were then compounded into the plasticized PVC formulation as in Example 4 and tested at the same conditions. Example 5 formulations and testing results are shown below in Table 5. Table 5. Formulations and Properties *For comparative purposes, Advera™ 40 IP, a commercial 4A aluminosilicate zeolite, was used. Advera™ is a trademark of the PQ Corporation. As observed from the data in Table 5, reduction of particle size does not improve the performance of 4A zeolite as a PVC stabilizer for either small or large crystallite zeolites. It should be noted, however, that this example deals with a flexible PVC formulation in which a relatively low concentration of zeolite has been used. As described below with respect to Example 12, decreasing particle size does improve performance in CPVC and rigid PVC formulations at higher zeolite loading. Example 6 Example 6 demonstrates the effect of reducing the crystallite size of the faujasite structure zeolite 13X on its performance as a stabilizer for PVC. The X zeolites were compounded into a flexible PVC formulation and tested as in Example 4. Metrastat™ static heat stability tests were performed using the Metrastat™ oven according to DIN 5381F and AFNOR T51-224 at 190°C for 2 hours. The formulations were extruded at 175 °C stock temperature using a Haake™ twin screw extruder to make 1 x 0.04-inch strips for the testing. Metrastat™ early color for the following examples is defined as the time to observable color change and Metrastat™ stability is defined as the time to complete degradation observed as a color change to dark brown or black. Table 6 shows the formulations and testing results. Table 6. Formulations and Properties *For comparative purposes, Advera™ 201, a commercial 13X aluminosilicate zeolite, was used. Advera™ is a trademark of the PQ Corporation. Analysis of results from Table 6 demonstrates that reduction of X zeolite crystallite size improves its performance as a PVC stabilizer. However, no direct correlation with particle size is observed. It should be noted here also, however, that particle size may be a factor at higher zeolite loading. Example 7 Example 7 shows performance of small crystallite Zeolite A and 13X at higher stabilizer loading. The plasticized PVC compounds were prepared and tested at conditions shown in Example 4. Presented below is Table 7, which lists the prepared PVC formulations and their properties. Table 7. Formulations and Properties As shown in Table 7, increased levels of zeolite A and X improve DTS of the PVC formulation. However, zeolite A is preferred. Example 8 Example 8 compares the performance of other zeolites as stabilizers for PVC. The PVC formulations were prepared and tested as described in Example 4. Their evaluations are described in Table 8 below. Table 8. Formulations and Properties *Zeolyst™ is a trademark of Zeolyst International The results in Table 8 demonstrate that not all zeolites perform equally as stabilizers for PVC. Zeolite A is the preferred zeolite. Example 9 Example 9 demonstrates the effect of thermally activating zeolite 4A. The zeolites, having 1.5 and 0.4 μm crystal sizes, were heated for four hours at the temperatures shown below. The moisture level in the zeolite A samples were tested by loss on ignition (LOI) at 1000°C. The PVC formulations were prepared and tested as described in Example 4. Table 9 lists the PVC formulations and their properties. Table 9. Formulations and Properties *For comparative purposes, Advera™ 40 IP, a commercial 4A aluminosilicate zeolite, was used. Advera™ is a trademark of the PQ Corporation. The results in Table 9 demonstrate that the level of hydration of 4A zeolite influences its performance as a PVC stabilizer. Optimal ranges are from about 4% to 22%. It should be noted, however, that this example relates to a flexible PVC formulation with a relatively low zeolite loading. Example 10 Example 10 demonstrates the performance of Example IB where a portion of the exchangeable sodium cations was replaced with potassium. The samples were prepared using conventional ion exchange methods. (Zeolite Molecular Sieves, D. Breck, Krieger Publishing Company, Malabar, Florida Chapter 7, pp 537-549) The potassium exchanged A zeolites were compounded into flexible PVC formulation and tested as in Example 4 and are shown below in Table 10. Table 10. Formulations and Properties *For comparative purposes, Advera™ 40 IP, a commercial 4A aluminosilicate zeolite, was used. Advera™ is a trademark of the PQ Corporation. Example 11 Example 11 demonstrates the performance of Advera 40 IP and Example IB where a portion of the exchangeable sodium cations was replaced with calcium. The samples were prepared using conventional ion exchange methods. (Zeolite Molecular Sieves, D. Breck, Chapter 7, pp 537- 549) The calcium exchanged A zeolites were compounded into flexible PVC formulation and tested as in Example 4 and are shown below in Table 11. Table 11. Formulations and Properties *For comparative purposes, Advera™ 40 IP, a commercial 4A aluminosilicate zeolite, was used. Advera™ is a trademark of the PQ Corporation. Example 12 The following example shows the positive effect of reduction of both zeolite crystallite size and particle size on dynamic thermal stability performance in CPVC pipe formulations. Table 12. Formulations and Properties. aBimodal distribution with an 80/20 ratio of small to large crystals. ^Crystallinity relative to starting crystallinity as measured by X-ray diffraction. cTempRite® 3114 is a powder CPVC pipe compound sold by the BF Goodrich Company. "Anomalous result. Example 12A was prepared at the same ratios as Example IB. Example 12B was prepared by rota-jet milling the material of Example 12 A. Synthesis of Example 12C Example 12C was prepared by first preparing a sodium aluminate solution by dissolving reagent grade sodium hydroxide pellets (298.0 g) in (298.0 g) de-ionized water. This solution was heated to 100 °C and aluminum trihydrate (324 g) was slowly added with stirring until it dissolved. The resulting sodium aluminate solution was then cooled to below 75 °C and then an additional (1212.5 g) of de-ionized water was added. This solution was then cooled to room temperature. A 1.5 ratio sodium silicate (903.0 g, Si0 2 /Na O = 1.5, 57 wt. % water) solution was diluted with (1510.5 g) de-ionized water. To this solution, the sodium aluminate solution was added with vigorous agitation over a period of 30 minutes, and then homogenized for another 15 minutes. The reaction mixture was aged for 1 hour at 65.5 °C. This reaction mixture was then heated to 93.3 °C for 3 hours. The contents were then filtered, washed with de-ionized water and analyzed. The product consisted of pure zeolite A as determined by X-ray diffraction and had a chemical composition of 1.0 Na 2 O: 1 Al 2 O 3 : 2.00 SιO 2 . Synthesis of Example 12D Example 12D was prepared by first prepaπng a sodium aluminate solution by the procedure as descnbed above in Example 12C using reagent grade sodium hydroxide pellets (307.6 g), aluminum tπhydrate (280.0 g) in (1290.0 g) deionized water and then cooling to room temperature. A 1.5 ratio sodium silicate (792.0 g, SιO 2 /Na 2 O = 1.5, 57 wt. % water) solution was diluted with (1290.0 g) deionized water. To this solution, the sodium aluminate solution was added with vigorous agitation over a period of 60 minutes. Then, solution A (31.2 g) was added to the reaction mixture and well mixed for 15 minutes. This reaction mixture was then heated to 93.3 °C for 1.5 hours. The contents were then filtered, washed with deionized water and analyzed. The product consisted of pure zeolite A as determined by X-ray diffraction. Example 12E was prepared by the same ratios as Example 12D, and then mechanically crushed using a roll-milling process. Synthesis of Example 12F Example 12F was prepared by first prepanng a sodium aluminate solution as descπbed above in Example 12C using reagent grade sodium hydroxide pellets (335.0 g), aluminum trihydrate (324.0 g) m (1100.0 g) de-ionized water and then cooling to room temperature. A 3.2 ratio sodium silicate (820.0 g, SιO 2 /Na 2 O = 3.2, 62 wt. % water) solution was diluted with (1100.0 g) de-ionized water. Then, solution A (2.4 g) was added to the silicate solution and well mixed for 15 minutes. To this solution, the sodium aluminate solution was added with vigorous agitation over a period of 30 minutes, and then homogenized for another 15 minutes. This reaction mixture was then heated to 93.3 °C for 3 hours. The contents were then filtered, washed with de-ionized water, dπed at 100 °C for 12 hours and analyzed. The product consisted of pure zeolite A as determined by X-ray diffraction and had a chemical composition of 1.0 Na 2 O: 1 Al 2 O 3 : 2.00 SιO 2 . Synthesis of Example 12F Example 12G was prepared as follows. The sodium aluminate solution was prepared as descπbed above in Example 12C using reagent grade sodium hydroxide pellets (334.0 g), aluminum trihydrate (324.0 g) in (1100.0 g) de-ionized water and then cooling to room temperature. A 3.2 ratio sodium silicate (814.0 g, SιO 2 /Na 2 O = 3.2, 62 wt. % water) solution was diluted with (1100.0 g) de-ionized water. Then, solution A (16.0 g) was added to the silicate solution and well mixed for 15 minutes. To this solution, the sodium aluminate solution was added with vigorous agitation over a period of 30 minutes, and then homogenized for another 15 minutes. This reaction mixture was then heated to 93.3 °C for 3 hours. The contents were then filtered, washed with de-ionized water, dπed at 100 °C for 12 hours and analyzed. The product consisted of pure zeolite A as determined by X-ray diffraction and had a chemical composition of 1.0 Na 2 O: 1 Al 2 O 3 : 2.00 SιO 2 . All of the above samples were calcined at 400 °C for 4 hours. As shown in Table 12, peak performance is obtained by samples with a combination of small particle size and small crystal size. Unlike Example 5, which related to a flexible PVC formulation with a relatively low concentration of zeolite and with a relatively high concentration of plasticizers, and wherein zeolite particle size had no apparent correlation with stability, this example relates to a CPVC formulation. In the CPVC formulation of this example, the amount of zeolite added is significantly greater and there are no plasticizers. Example 13 The following example shows the impact of the amount of zeolite on a PVC calendeπng formulation. Table 13A. Formulation of non-zeolite ingredients. To the formulation given in Table 13 A, the amounts of zeolite A shown in Table 13B were added. Table 13B. Zeolite formulation and properties. a Dried at 300 deg. C for 4 hours to 3.8% LOI. D Estimated decomposition time at 20% increase of torque above equilibrium. c Estimated decomposition time at 25% increase of torque above equilibrium. d The DTS test was performed with a Haake torque rheometer at 190°C and 50 RPM, using 60g samples. It was found necessary to dry the zeolite because without such drying, as the formulations were extruded, undesirable moisture bubbles arising from water evaporation were observed in the extruded product at zeolite concentrations of 1.2 phr or above. Example 14 This example shows dynamic thermal stability testing of chlorinated polyvmyl chloride (CPVC) powder compounds. For each test, 3.44 g zeolite samples were added to 200 g of TempRite® 3114 powder CPVC pipe extrusion compound and blended in a food processing mixer for 15 minutes. As with the previous examples, thermal stability testing of the powder CPVC compounds was performed using the dynamic thermal stability (DTS) test according to ASTM method D 2538-95 where DTS performance is defined as the time required to reach a point of rapid CPVC decomposition and torque increase after the equilibrium torque has been established. The dynamic thermal stability tests for this example were performed using a Haake rheometer at 195 or 205 °C and 35 RPM for 70.5 g samples, after preheating for 3 min. (1 min. at 10 RPM, 2 min. at 5 RPM). Each test was repeated and the reported result is the average of two or three tests for each compound. Table 14. Formulations and Properties. a Steam calcined at 650 °C in an atmosphere of 50% steam for 1 hour. water adsorption at 4.6 Torr. cCrystallinity relative to starting crystallinity as measured by X-ray diffraction. "Anomalous result. The McBain-Bakr test, as is well known in the art, comprises measuring the equilibrium weight gain of a sample in a controlled atmosphere of vapor at a given pressure. For the testing related to this invention, a water vapor pressure of 4.6 Torr was used.

Claims: We claim: 1. A stabilized halogenated polymer composition comprising a halogenated polymer resin and a stabilizer comprising a synthetic crystalline aluminosilicate of the formula M 2 n O . Al 2 O 3 . ySiO 2 . wH 2 O, in which M is a charge balancing cation, n is the valence of M and is 1 or 2, y is the number of moles of SiO 2 and is about 1.8 to about 15 , and w is the number of moles of water of hydration per molecule of said aluminosilicate, wherein said aluminosilicate has a mean crystallite size in the range of about 0.01 μm to about 1 μm. 2. The stabilized halogenated polymer composition of claim 1 in which M is a charge balancing cation selected from the group consisting of sodium, potassium, zinc, magnesium, calcium, tetraalkyl ammonium, tetraaryl ammonium, lithium, NH 4 , Ag, Cd, Ba, Cu, Co, Sr, Ni, Fe, and mixtures thereof. 3. The stabilized halogenated polymer composition of claim 1 in which M is a charge balancing cation selected from the group consisting of alkali metal and alkaline earth metal, with the proviso that, when M is a mixture of alkali metal and alkaline earth metal comprising sodium and potassium or calcium, the potassium and calcium content is less than about 35% of the total alkali and alkaline earth metal content. 4. The stabilized halogenated polymer composition of claim 1 in which, y is in the range of about 2 to about 5, wherein said aluminosilicate has a mean crystallite size in the range of about 0.01 μm to about 1 μm and a mean particle size in the range of about 0.1 to about 10 μm. 5. The stabilized halogenated polymer composition of claim 4 in which, said aluminosilicate has a mean particle size in the range of about 0.1 to about 3 μm. 6. The composition of claim 5 wherein the composition comprises a CPVC formulation or a rigid PVC formulation. 7. The composition of claim 1, in which the halogenated polymer resin is selected from the group consisting of polyvinyl chloride (PVC), chlorinated polyvinyl chloride (CPVC), polychloroprene (Neoprene), an acrylonitrile-vinyl chloride copolymer (Dynel), a polyvinyl chloride-vinyl acetate copolymer, polyvinylidene chloride, a polytetrafluoroethylene-vinyl chloride copolymer, and a polyfluoro-chloro ethylene polymer. 8. The composition of claim 1 in which the halogenated polymer resin comprises a halogenated-vinyl polymer resin. 9. The composition of claim 8 in which the halogenated-vmyl polymer resm is selected from polyvmyl chloride or chlonnated polyvinyl chloπde. 10. The composition of claim 9 in which said polymer resm is polyvinyl chloπde. 11. The composition of claim 10 in which the polyvinyl chloride has a number average molecular weight in the range of 20,000 to 100,000 and a Fikentscher K value m the range of 41 to 98 made by any conventional polymenzation method. 12 The composition of claim 1 in which said aluminosilicate is a zeolite selected from the group consisting of zeolite A, zeolite P, zeolite X, zeolite Y, and mixtures thereof. 13 The composition of claim 12 m which said aluminosilicate is zeolite A. 14 The composition of claim 12 in which said zeolite is dehydrated to a water content between about 0.1% and about 20% by weight of the aluminosilicate. 15. The composition of claim 14 in which said zeolite comprises a steam calcined dehydrated zeolite dehydrated to a water content between about 0.1% and about 8% by weight of the aluminosilicate. 16. The composition of claim 15 m which said zeolite does not rehydrate to a water content greater than about 10% by weight of the aluminosilicate. 17. The composition of claim 12 in which the zeolite has an average pore diameter m the range of about 2.8 to about 8 angstroms. 18. The composition of claim 12 in which the zeolite has an external surface area in the range of about 3 to about 300 m 2 /g. 19. The composition of claim 1 in which the stabilizer is, in combination, the aluminosilicate and one or more co-stabihzers. 20. The composition of claim 19 m which the co-stabihzer is a conventional organometalhc complex stabilizer selected from the group consisting of magnesium, antimony, cadmium, barium, tin, calcium, zinc and lead, a conventional organic complex stabilizer selected from the group consisting of polyhydπc esters of various fatty acids, beta-diketones, organic phosphites, hindered ammes, organic mercaptans, epoxidized oils, epoxy compounds, and phenols, a conventional inorganic complex stabilizer selected from the group consisting of dibasic, tribasic, and tetrabasic lead sulfate; dibasic lead phosphite; white lead, and mixtures thereof. 21. A method for stabilizing a halogenated polymer resin comprising admixing the resin with: a stabilizer comprising a synthetic crystalline aluminosilicate of the formula M 2/n O . Al 2 O 3 . ySi0 2 . wH 2 O, in which M is a charge balancing cation selected from sodium, potassium, magnesium, lithium, zinc, calcium, tetraalkyl ammonium, tetraaryl ammonium, and mixtures thereof, with the proviso that, when M is a mixture of alkali metals and alkaline earth metals comprising sodium and potassium or calcium, the potassium and calcium content is not more than about 35% of the total alkali metal and alkaline earth content, n is the valence of M and is 1 or 2, y is the number of moles of SiO 2 and is about 1.85 to about 10, and w is the moles of water of hydration per molecule of said aluminosilicate, wherein said aluminosilicate has a mean crystallite size in the range of about 0.01 μm to about 1 μm. 22. The method of claim 21 in which said aluminosilicate has a mean particle size in the range of about 0.1 to about 10 μm. 23. The method of claim 21 in which y is in the range of about 2 to about 5. 24. The method of claim 21 , in which the halogenated polymer resin comprises a member selected from the group consisting of polyvinyl chloride (PVC), chlorinated polyvinyl chloride (CPVC), polychloroprene (Neoprene), an acrylonitrile-vinyl chloride copolymer (Dynel), a polyvinyl chloride-vinyl acetate copolymer, polyvinylidene chloride, a polytetrafluoroethylene- vinyl chloride copolymer, a polyfluoro-chloro ethylene polymer, and a combination thereof. 25. The method of claim 21 in which the halogenated polymer resin is a halogenated- vinyl polymer resin. 26. The method of claim 21 in which the halogenated-vinyl polymer resin is selected from polyvinyl chloride or chlorinated polyvinyl chloride. 27. The method of claim 21 in which said polymer resin is polyvinyl chloride. 28. The method of claim 27 in which the polyvinyl chloride has a number average molecular weight in the range of about 20,000 to about 100,000 and a Fikentscher K value in the range of about 41 to about 98 made by any conventional polymerization method. 29. The method of claim 21 in which said aluminosilicate is a zeolite selected from the group consisting of zeolite A, zeolite P, zeolite X, zeolite Y, and mixtures thereof. 30. The method of claim 29 in which said aluminosilicate is zeolite A. 31. The method of claim 29 in which said zeolite is dehydrated to a water content within a range of about 0.1% to about 20% by weight of the aluminosilicate. 32. The method of claim 29 in which the zeolite has an average pore diameter in the range of about 2.8 to about 8 angstroms. 33. The method of claim 29 in which the zeolite has an external surface area in the range of about 3 to about 300 m 2 /g. 34. The method of claim 21 in which said stabilizer is, in combination, the aluminosilicate and at least one co-stabilizer. 35. The method of claim 34 in which the co-stabilizer is a conventional organometalhc complex selected from the group consisting of cadmium, magnesium, antimony, barium, tin, calcium, zinc, lead and mixtures thereof, a conventional organic complex selected from the group consisting of polyhydric esters of various fatty acids, beta-diketones, organic phosphites, hindered amines, organic mercaptans, and phenols, a conventional inorganic complex selected from the group consisting of dibasic, tribasic, and tetrabasic lead sulfate; dibasic lead phosphite, and white lead, and mixtures thereof. 36. The method of claim 21, wherein said mixing takes place before, during or after polymerization of said resin. 37. A synthetic crystalline aluminosilicate having a formula M 2/n O . Al 2 O 3 . ySi0 2 . wH 2 O, in which M is a charge balancing cation, n is the valence of M and is 1 or 2, y is the number of moles of SiO 2 and is about 1.8 to about 3.5, and w is the number of moles of water of hydration per molecule of said aluminosilicate, wherein said aluminosilicate has a mean crystallite size in a range of about 0.01 μm to about 1 μm and a particle size in a range of about 0.5 to about 3 μm. 38. The aluminosilicate of claim 37 wherein the aluminosilicate comprises zeolite A. 39. The aluminosilicate of claim 37 further comprising a water content between about 0.1% and about 20% by weight of the aluminosilicate. 40. The composition of claim 39 in which said aluminosilicate is a steam calcined dehydrated aluminosilicate dehydrated to a water content between about 0.1 % and about 8% by weight of the aluminosilicate. 41. The composition of claim 40 in which said steam calcined dehydrated aluminosilicate does not rehydrate to a water content greater than about 10% by weight of the aluminosilicate. 42. The composition of claim 40 in which said steam calcined dehydrated aluminosilicate has a crystallinity that is no less than about 50% of a starting crystallinity of the aluminosilicate prior to steam calcination. 43. In a process for making a synthetic crystalline aluminosilicate of the formula M 2/n O . Al 2 O 3 . ySiO 2 . wH 2 O, in which M is a charge balancing cation, n is the valence of M and is 1 or 2, y is the number of moles of SiO 2 and is 1.8 to 3.5 , and w is the number of moles of water of hydration per molecule of said aluminosilicate, the improvement comprising: (a) steam calcining the aluminosilicate to a water content between 0.1% and about 8% by weight of the aluminosilicate while retaining at least 50% of the starting crystallinity, such that the resulting dehydrated aluminosilicate does not rehydrate to a water content greater than about 10% by weight of the aluminosilicate. 44. The process of claim 43 wherein the improvement further comprises forming an aluminosilicate having a mean crystallite size in a range of about 0.01 μm to about 1 μm and a particle size in a range of about 0.5 to about 3 μm.

Inventors: CORMIER WILLIAM EDWARD, LOCKLEDGE SCOTT POTTER, RAV GAYATRI SIDART, WYPART ROMAN, CORMIER, WILLIAM, EDWARD, LOCKLEDGE, SCOTT, POTTER, RAV, GAYATRI, SIDART, WYPART, ROMAN
Applicants: CORMIER WILLIAM EDWARD, LOCKLEDGE SCOTT POTTER, PQ HOLDING INC, RAV GAYATRI SIDART, WYPART ROMAN, CORMIER, WILLIAM, EDWARD, LOCKLEDGE, SCOTT, POTTER, PQ HOLDING, INC., RAV, GAYATRI, SIDART, WYPART, ROMAN
Application year: 2000
Main classification: C08K3
IPC codes: C08K3, C08K5, C08L11, C08L27