Method for improving the clarity of propylene polymers

Abstract: An injection blow molding grade resin of improved clarity and processability is obtained by incorporating N,N¹-ethylene bisstearamide and an ethoxylated amine into a sodium benzoate nucleated propylene polymer.

Description: Propylene polymers produced in the presence of support-based, high activity coordination catalysts generally do not require deashing prior to use and therefore contain acidic catalytic residues which need to be neutralized before 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 as great as what would be desired. In concurrently filed EPC Application No. 86306040.6 there is provided a method for synergistically improving the clarity and also color of a propylene polymer nucleated with sodium benzoate which comprises adding an ethoxylated amine to the polymer in the absence of calcium stearate. It was unexpectedly found that the incorporation of the ethoxylated amine into the sodium benzoate-nucleated polypropylene resin 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. However, a drawback of the resulting resins is that they do not process satisfactorily on injection blow molding equipment. In accordance with this invention, there is provided a method for improving the processability and unexpectedly further improving the clarity of an undeashed propylene polymer, which has been 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, N,N¹-ethylene bisstearamide and an ethoxylated amine in the absence of calcium stearate, melting the resulting mixture and solidifying the molten mixture. 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 0.940g/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 or 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 agents 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 quanitites 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-t-butyl-4-hydroxy-hydrocinnamate)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 N,N¹-ethylene bisstearamide suitably is added to provide a concentration between 0.01 and 1 wt%, preferably between 0.05 and 2 wt%, based on the polymer weight. The ethoxylated amine suitably is a saturated, fatty acid alkanol amine derived from fatty acids containing from 8 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 and antiblocking agents, 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 1-3 The resin used in each of the blends of Examples 1 - 3 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. 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 5 minutes under nitrogen atmosphere the blend was dried under nitrogen at about 65°C for 3 hours. The blends were then extruded at a nominal 260°C (500°F) melt temperature and pelletized. 1.3 mm (50 mil) plaques were injection molded from the pellets and these were tested for percent haze (ASTM D1003). Also, from each pelletized blend 20, 3.8 litre (4-U.S.qt) size Boston round bottles were injection blow-molded on a Jomar molding machine. The bottles were tested for visual clarity employing a rating scale from 1 to 5, with the value of 5 being designated as the worst see-through clarity. The molding process performance was measured and was based on the degree of sticking during the injection blow-molding using the following ratings: Good - bottles molded without any sticking to core-pins. Fair - slight sticking to core-pins during molding. Poor - excessive sticking requiring manual release of bottles from pins. The test results are shown in Table I: The results from Comparative Experiments 1 and 2 show that the test samples of sodium benzoate nucleated resin also containing an ethoxylated amine (in this case bis-hydroxyethyl cocamine sold under the trademark Armostat 410) had improved clarity properties, i.e. reduction in percent haze as well as in visual clarity. However, the resin of Comparative Example 2 processed poorly in the injection blow-molding machine due to the absence of calcium stearate lubricant which, if present, would have interacted with the sodium benzoate and caused an unwanted poor clarity. By the addition of N,N¹-ethylene bisstearamide (available commercially, e.g. under the trademark Acrawax C) in Example 3 to the composition of Example 2, not only was the processability completely restored, but also, and entirely unexpectedly, the haze was further improved to a much lower value than previously possible.

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, N,N¹-ethylene bisstearamide and an ethoxylated amine in the absence of a metal stearate, (b) melting the resulting mixture and (c) solidifying the molten mixture. A method according to claim 1 wherein the propylene 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 1, 2 or 3 wherein the amount of sodium benzoate is between 0.01 and 1 wt%, based on the weight of the polymer. 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(hydroxyethyl) cocoamine. A method according to any one of the preceding claims wherein the amount of N,N¹-ethylene bisstearamide is from 0.01 to 1 wt%, based on the weight of the polymer. A method according to any one of the preceding claims wherein aluminum magnesium hydroxy carbonate is added to the propylene polymer as neutralizer. A method according to any one of the preceding claims which comprises the additional step of shaping the resulting propylene polymer to provide a shaped article."

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