IMPROVED BLENDS OF LINEAR LOW DENSITY ETHYLENE COPOLYMERS

Abstract: Polymer blends are provided comprising a linear low density polyethylene (LLDPE) compounded with a minor amount of (a) an at least partially isotactic, partially crystalline butene-1 polymer comprising at least about 80 wt.% of polymerized butene-1; or (b) an ABS resin; or (c) a mixture of (a) with (b). The blends can be fabricated with better processability into blown films having improved antiblocking impact and MD tear resistance properties.

Description: This invention relates to improved blends of linear low density polyethylene (LLDPE); more particularly, this invention relates to blends of LLDPE having improved processability; to films, especially blown films, prepared therefrom; and to the use of certain polymeric additives, in minor amounts, in such blends to accomplish the improved processability. In this description 1 ft = 0.305 m ; 1 inch = 25.4 mm ; 1 mil = 25.4 µm ; 1 lb = 0.454 kg and 1 psi = 6.8g kPa According to one aspect of this invention there is provided a polymer blend which comprises: (i) a linear low density polyethylene; and (ii) a minor amount of (a) an at least partially isotactic, partially crystalline butene-1 polymer comprising at least 80 wt.% of polymerised butene-1; or (b) an ABS resin; or (c) a mixture of (a) with (b). Suitably, (i) comprises at least 50 wt.% of the polymer blend. The term "linear low density polyethylene" is used in its customary usage to denote a low density copolymer of ethylene with a minor amount of a higher olefin. The blends of this invention can be fabricated with better processability into blown films having improved antiblocking, impact and machine direction (MD) tear resistance properties. The linear low density polyethylene used in this invention is desirably a linear copolymer of ethylene and a minor amount, preferably from 2 to 10 wt.%, of an olefin, preferably a 1-olefin, containing 4 to 10 carbon atoms and having a specific gravity from 0.9 to 0.94, a melting point from 110 to 130°C, and a melt index from 0.2 to 10. The preferred olefin comonomers are 1-butene, 1-hexene and 1-octene. The LLDPE may be prepared by any of various methods known in the art: for example, by relatively low pressure methods as disclosed in U.S. Patent 4,076,698; or, for example, by relatively high pressure methods as disclosed in U.S. Patents 4,405,774 and 4,530,983. The butene-1 polymer contemplated for use in this invention is an at least partially isotactic, partially crystalline polymer comprising at least 80 wt.%, preferably at least 90 wt.% of polymerized butene-1. The polymers may comprise a homopolymer of butene-1 or a copolymer of at least 80 wt.% of butene-1 and up to 20 wt.% of at least one polymerized comonomer; for example, an olefin, preferably a 1-olefin, containing from 2 to 10 carbon atoms, and preferably have a number average molecular weight of at least 25,000, a specific gravity from 0.890 to 0.920, and a melt index from 0.1 to 40, (ASTM condition E). Some of these polymers are described in the articles on "Polymers of Higher Olefins" in Kirk-Othmer, Encyclopedia of Chemical Technology , Third Edition, Wiley-Interscience, 1981, pages 470-477. The polymers may be prepared using a Ziegler-Natta type catalyst as described in U.S. Patent 3,362,940 or the foregoing Kirk-Othmer article. In general, the butene-1 polymers in unblended form are capable of being formed into shaped articles such as films. The "ABS resin" contemplated for use in this invention comprises a rubbery or elastomeric butadiene polymer dispersed in a rigid or glassy styrene-acrylonitrile copolymer matrix. Preferably, the rubbery butadiene polymer contains, at various points along it backbone, grafted segments of styrene-acrylonitrile copolymer, which have the effect of improving compatability between the two polymer phases. Also contemplated within the term "ABS resin" are physical blends of a rubbery butadiene polymer containing no grafted polymer segments dispersed in a rigid styrene-acrylonitrile copolymer phase. Generally, there is some degree of cross-linking within the rubbery butadiene polymer phase. The rubbery butadiene polymer, independent of any grafted polymer segments which may be present, usually contains at least 60 wt.% of polymerized butadiene. Some examples of these polymers are polybutadiene (a butadiene homopolymer), and copolymers of butadiene and acrylonitrile and/or styrene. The rubbery butadiene polymer may be present, for example, in an amount from 10 to 30 wt.% of the total polymer content of the ABS resin, and the overall amounts of polymerized acrylonitrile, butadiene, and styrene in the ABS resin are within the weight percent ranges of 15-25:5-45:80-30, respectively, preferably 15-22:7-40:78-38. The ABS resins contemplated for use in this invention may have, for example, a 3.2 mm notched Izod impact strength at 23°C of about 2 to 12 ft-lb/in (ASTM 0256), a tensile strength at 23°C of 4800 to 7500 psi (ASTM D638), a tensile modulus at 23°C of 2.5 to 3.8 x 10⁵ psi (ASTM D638), a Rockwell hardness at 23°C of 88 to 110 HRC (ASTM D785), a specific gravity at 23°C of 1.02 to 1.06 (ASTM D792), a thermal deflection temperature of annealed samples at 264 psi of 93 to 112°C (ASTM D648), and a linear coefficient of thermal expansion of 6.5 to 11.0 x 10⁻⁵ cm/cm/°C (ASTM 0696). Some suitable ABS resins for use in the compositions and processes of this invention are described in the previously cited Kirk-Othmer and Hawley references. The blends of this invention may be prepared using any of various methods known in the art. For example, pellets of the two, or of the three, polymers may be dry blended and the blend added directly to a blown film extruder; for example, a Sterling extruder, to produce films having a thickness, for example of 0.5 to 5 mils. The blends of this invention contain (a) over 50 wt.% of (i) and (b) under 50 wt.% of (ii), based on the total polymer content. Preferably, the blend comprises from 1 to 25 wt.%, more preferably from 2 to 10 wt.%, of (ii)(a) or (ii)(b) or from 1 to 20 wt.%, more preferably from 1 to 10 wt.%, of each component of (ii)(c). The polymer content of the blend preferably consists of the LLDPE and (ii). In addition to the polymer components, the blend may also contain any of various additives conventionally added to polymer compositions; for example, lubricants such as microtalc, stabilizers, compatibilizers or pigments. This invention also provides a film, preferably a blown film, of a polymer blend as herein described. This invention further provides the use of (ii), as herein defined, to improve the processibility of LLDPE into blown films having improved antiblocking, impact or MD tear resistance properties. The following Examples illustrate the invention. COMPARATIVE EXAMPLES 1 TO 4 AND EXAMPLES 1 TO 8 Films of 1.0 and 1.5 mils nominal gauge were prepared from the blends shown in Table 1 in a 2.5 inch Sterling blown film extruder under the following fabrication conditions: BUR (blow-up ratio) of 2.5; production rate of 150 lb/hr; die gap of 80 mils; and a 6 inch die. Table 2 shows the RPM; screw tip pressure; and screw amperes at which the extruder was operated; and the Induced Blocking Force (ASTM D3354); MD tear (ASTM D1922); Spencer Impact (ASTM D3420); and Dart Drop F₅₀ Impact (ASTM D1709) of the prepared films. COMPARATIVE EXAMPLE 5 AND EXAMPLES 9 AND 10 Using the same procedures as in the previous Examples, films of 1.0 mil nominal thickness were prepared from the blends shown in Table 3. Table 4 shows the extruder operating conditions and the results obtained. wherein A, C, D and E are defined above.

Claims: A polymer blend which comprises: (i) a linear low density polyethylene; and (ii) a minor amount of (a) an at least partially isotactic, partially crystalline butene-1 polymer comprising at least 80 wt.% of polymerised butene-1; or (b) an ABS resin; or (c) a mixture of (a) with (b). A blend according to claim 1 wherein (i) comprises at least 50 wt.% of the polymer blend. A blend according to claim 1 or 2 wherein (i) comprises from 2 to 10 wt.% of polymerised C₄ to C₁₀ olefin. A blend according to any preceding claim wherein the olefin comprises a 1-olefin. A blend according to claim 4 wherein the 1-olefin comprises 1-butene, 1-hexene or 1-octene. A blend according to any preceding claim wherein (i) has a specific gravity from 0.9 to 0.94; a melting point from 110° to 130°C; and a melt index from 0.2 to 10. A blend according to any preceding claim wherein (ii) comprises from 1 to 25 wt.% of (a) or (b) or from 1 to 20 wt.% of each component of (c). A blend according to claim 6 wherein (ii) comprises from 2 to 10 wt.% of (a) or (b) or from 1 to 10 wt.% of each component of (c). A blend according to any preceding claim wherein (ii) comprises a butene-1 polymer having a number average molecular weight (M - / n) of at least 25,000. A blend according to any preceding claim wherein (ii) comprises a homopolymer of butene-1. A blend according to any preceding claim wherein (ii) comprises a copolymer of butene-1 with ethylene. A blend according to any preceding claim wherein (ii) comprises a butene-1 polymer having a specific gravity from 0.89 to 0.92 and a melt index from 0.1 to 40. A film which comprises a blend according to any preceding claim. A film according to claim 13 which is a blown film. The use of (ii) as defined in any preceding claim to improve the processibility of LLDPE into blown films having improved antiblocking, impact or MD tear resistance properties.

Inventors: SHIRODKAR, PRADUP PANDURANG
Applicants: MOBIL OIL CORPORATION
Application year: 1989
Main classification: C08L23
IPC codes: C08L23, G02B6, C08L55, C08L57