METHOD OF IMPROVING THE CLARITY OF PROPYLENE POLYMERS

Abstract: Incorporation of an ethoxylated amine in a sodium benzoate nucleated propylene polymer synergistically improves as well as yellowness over what is achieved by use of sodium benzoate or ethoxylated amine alone.

Description: The present invention relates to a method of improving the clarity and yellowness of propylene polymers produced in the presence of support-based, high activity coordination catalysts. These polymers generally do not require deashing prior to use and therefore contain acidic catalytic residues which need to be neutralized prior to processing of the polymer. In order to improve polymer clarity, sodium benzoate can be added as a nucleating agent. However, because of the presence of catalytic residues and neutralizing agents in the polymer, the improvement in clarity has not been great as desired. Also, the polymer color as measured by the yellowness index, has not been quite satisfactory. In accordance with this invention, there is provided a method for synergistically improving the clarity and color of an undeashed propylene polymer prepared in the presence of a high-activity catalyst composition containing a magnesium halide-supported titanium halide catalyst component, which method comprises mixing the polymer with sodium benzoate and an ethoxylated amine in the absence of calcium stearate, melting the resulting mixture and solidifying the molten mixture. It was unexpectedly found that the incorporation of an ethoxylated amine into the sodium benzoate-nucleated propylene polymer improved the clarity, as measured by percent haze, and reduced the yellowness index in a synergistic manner, i.e. these properties were far better than what could be predicted from those obtained by use of sodium benzoate alone and ethoxylated amine alone. The polymers which are useful in this invention are derived predominantly from propylene (usually at least 75% by weight) and are produced by well-known processes involving the use of any of the recently developed supported, highly active and stereospecific catalysts. Generally, these catalysts are comprised of an aluminum alkyl component and a titanium compound supported on magnesium dihalide as a second component. Homopolymers, copolymers of propylene with other simple 1-olefins such as ethylene and butene-1, and blends thereof can be used. Also, other 1-olefin resins can be blended with any of the aforementioned propylene resins, e.g. linear low density polyethylene (LLDPE) which is an interpolymer of ethylene and at least one C₄-C₈ 1-olefin. The LLDPE resins are mainly categorized according to density rather than chemical composition and should have a density of between 0.915 and 0.940 g/cm³. The polymerized propylene content of the total polymer, whether it be composed of one or more components, preferably is at least 80% by weight. Random copolymers of propylene and ethylene containing between 2 and 10 wt% ethylene, and mixtures of such random copolymers with an LLDPE resin are especially suitable. In order to improve the lack of clarity generally associated with highly crystalline propylene polymers, sodium benzoate has been added to the propylene polymer, thereby controlling the rate of crystal growth as the molten polymer solidifies upon cooling in the final molding step. Any known process may be used to incorporate the sodium benzoate, which is usually added to provide a concentration of from 0.01 to 1% by weight based on the polymer weight, preferably from 0.05 to 0.5 wt%. For instance, the techniques disclosed in US-A-3,207,739, US-A-3, 367,926, US-A-3,637,634 and US-A-4,184,026 are all suitable. A neutralizing agent preferably is added to the polymer in quantities effective to reduce the corrosive effect of the support-based catalyst residues present in the polymer and to increase the thermal stability of the polymer. Such neutralizing agents are well-known and commercially available. Suitable neutralizing compounds include the hydroxides of sodium, potassium and calcium, oxides of calcium and magnesium, sodium carbonate, calcium carbonate, magnesium hydroxycarbonate and mixtures thereof. Generally, the concentration of neutralizer is from 0.01 to 3% by weight based on the polymer weight. This concentration does not include the sodium benzoate and the ethoxylated amine, which also act as neutralizers. To increase the thermal and oxidative stability of the polymer, any of the well-known commercially available antioxidants such as hindered phenols, phenolic phosphites and secondary aryl amines, can be incorporated into the polymer, usually in quantities from 0.01 to 1%, preferably from 0.05 to 0.5% by weight, based on the polymer weight. Examples of such antioxidants include butylated hydroxytoluene, tetrakis methylene-(3,5-di-5-butyl-4-hydroxyhydrocinnamate)methane, (1,3,5-trimethyl-2,4,6-tris (3,5-t-butyl-4-hydroxy-benzyl)benzene, bis(2,4-di-t-butylphenyl)pentaerythritol diphosphite, phenylenediamines and 3,5-di-tert-butyl-4-hydroxyhydrocinnamic acid triester with 1,3,5-tris (2-hydroxyethyl)-s-triazine-2,4,6(1H,3H,5H)-trione. The ethoxylated amine suitably is a fatty acid alkanol amine derived from fatty acids containing 3 to 20 carbon atoms. Examples of such ethoxylated amines are bis(hydroxyethyl)cocoamine, bis (hydroxyethyl)tallow amines, and bis(hydroxyethyl)myritylamine. These compounds are commercially available to be used as internal antistatic agents. When used as a clarifying agent in accordance with the invention, the concentration preferably is from 0.05 to 0.5% by weight, based on the weight of the polymer. Other special function additives can also be incorporated into the polymer such as colorants, antiblocking agents and lubricants, provided that the additive is not a metal stearate such as calcium stearate. Any conventional nucleation technique may be used for uniformly dispersing the additives within the polymer, for melting the polymer and for solidifying the polymer, and therefore need not be discussed in further detail. Shaped articles may be manufactured from polymers treated according to this invention by casting, compression molding or injection molding; films may be obtained by blowing or by slit extrusion; filaments, bars and tapes may be obtained by extrusion. The invention is illustrated by the embodiments described in the following Examples. EXAMPLES 1 - 6 The resin used in each of the blends of Examples 1 - 6 was a random copolymer of 97.2 wt% propylene and 2.8 wt% ethylene having a melt flow rate of 2.7 g/10 min (ASTM 1238D) and containing 200 ppm of butylated hydroxytoluene (BHT). The polymer was undeashed and had been produced in the presence of a high activity magnesium chloride-supported titanium chloride catalyst in a slurry polymerization process employing propylene monomer as liquid diluent. Most of the blends were prepared to contain the same amount of antioxidant stabilizer, in this case 1,3,5-trimethyl-2,4,6-tris (3,5-t-butyl-hydroxybenzyl) benzene (Ethyl 330), and also of primary neutralizer, i.e. aluminum magnesium hydroxycarbonate (Kyowa DHT-4A). The additives incorporated into each of the blends are indicated in Table 1. Where included, the sodium benzoate was added to the resin as a 10 wt% solution in a n-propanol/water azeotrope solvent (71.8/28.2 wt% composition). After intensive mixing for about 3 minutes under nitrogen atmosphere the blend was dried under nitrogen at about 65°C for 3 hours. Any other components to be included were then added into the blend by mixing under nitrogen atmosphere for about 3 minutes. All blends were prepared by this general technique. The blends were then extruded at a nominal 260°C (500°F) melt temperature and pelletized. 1.3 mm (50 mil) and 3.18 mm (125 mil) plaques were pressure molded from the pellets. The 1.3 mm (50 mil) plaques were tested for percent haze (ASTM D 1003), and yellowness index (YI) (ASTM D 1925) was measured on the 3.18 mm (125 mil) plaques. The test results are shown in Table 1. Comparison of the results from Comparative Examples 1 and 2 show that the resin nucleated with sodium benzoate had an improved clarity, i.e. a reduction in percent haze. However, the yellowness index was barely affected by the sodium benzoate. Comparative Example 3 shows that the addition of an ethoxylated amine (Armostat TM 410 - bis(hydroxyethyl) cocoamine) to the blend of Comparative Example 1 resulted in a reduction of yellowness index only, and the same result was obtained in the absence of calcium stearate, as shown by the data from Comparative Example 4. No significant difference in properties were obtained in Comparative Example 5 using the blend of Comparative Example 3 but nucleated with sodium benzoate. In Example 6, however, the blend which was nucleated with sodium benzoate and contained an ethoxylated amine, showed an unexpected further reduction in both haze and yellowness index indicating that the ethoxylated amine acts as a synergist provided that no calcium stearate is present in the blend. These findings are particularly evident from a comparison of the results from Comparative Examples 2, 4 and 5. EXAMPLES 7 - 9 The blends of these examples were essentially similar to those of Examples 2, 4 and 6 except that the antioxidant was replaced with tetrakis methylene-(3,5-di-t-4-hydroxyhydrocinnamate)methane (Irganox TM 1010). The synergistic effect of the ethoxylated amine is again demonstrated by a comparison of the data from Example 9 with those of Comparative Examples 7 and 8, as shown in Table II. EXAMPLES 10 and 11 The blends of Examples 10 and 11 were similar to those of Examples 2 and 6 except that the resin was a blend of 90 wt% of a random copolymer of proplene and ethylene (2.8 wt% ethylene and 2.7 melt flow rate) and 10 wt% of a linear low density polyethylene (0.1 melt index, 0.9191 g/cm³ density and 3.5 polydispersity). Haze measurements on samples prepared from these blends showed a decrese in haze and increase invisual clarity of the resin blend of Example 11 containing Armostat 410, illustrating the synergistic effect of ethoxylated amines on the clarity of propylene polymer resins nucleated with sodium benzoate The results are shown in Table III.

Claims: A method for improving the processability and clarity of an undeashed propylene polymer prepared in the presence of a high-activity catalyst composition containing a magnesium halide-supported titanium halide catalyst component, which method comprises: (a) mixing the polymer with sodium benzoate and an ethoxylated amine in the absence of calcium stearate, (b) melting the resulting mixture, and (c) solidifying the molten mixture. A method accordig to claim 1 wherein the polymer contains at least 75% by weight of polymerized propylene. A method according to claim 2 wherein at least a portion of the propylene polymer is a random copolymer of from 10 to 2 wt% of ethylene and from 90 to 98 wt% of propylene. A method according to claim 3 wherein the propylene polymer also contains a linear low density polyethylene component having a density between 0.915 and 0.940 g/cm³. A method according to any one of the preceding claims wherein the amount of ethoxylated amine is from 0.05 to 0.5 wt%, based on the weight of the polymer. A method according to any one of the preceding claims wherein the ethoxylated amine is bis(hydroxethyl) cocoamine. A method according to any one of the preceding claims wherein between 0.01 and 3 wt% of aluminum magnesium hydroxy carbonate is added to the propylene polymer as neutralizer. A method accordin g to any one of the preceding claims wherein the amount of sodium benzoate is between 0.01 and 1 wt%, based on the weight of the polymer. Shaped articles of a propylene polymer treated by a method as claimed in any one of the preceding claims.

Inventors: FICKER, HAROLD KURT, TESKIN, FREDERICK MICHAEL
Applicants: REXENE PRODUCTS COMPANY (A DELAWARE CORPORATION)
Application year: 1986
Main classification: C08K5
IPC codes: C08F10, C08L23, C08L21, C08K5, C08L7, C08J3, C08L101, C08F6