Dual reactor polyethylene resins for medical packaging - films, bags and pouches
AssigneeNOVA Chemicals (International) S.A.
InventorsShivendra Goyal, Ishkmandeep Boparai
Life of this patent
Estimating the term…
Abstract
Medical packaging films, bags and pouches having excellent optical properties and heat sealability, low hexane extractables and a good balance of physical properties may be prepared from linear low density polyethylene having a melt flow ratio (I21/I2) from about 23 to about 32, prepared in a tandem dual reactor solution phase polymerization in the presence of a phosphinimine catalyst and a co-catalyst system which comprises an aluminum based co-catalyst, an ionic activator or a mixture thereof.
Claims26
A medical packaging film, bag or pouch made from a linear low density polyethylene having a density from 0.914 to 0.945 g/cm3 and a melt flow ratio (MFR (I21/I2) determined according to ASTM D 1238) from 23 to 32 prepared by A) polymerizing ethylene optionally with one or more C3-12 alpha olefins, in solvent in a first stirred polymerization reactor at a temperature of from 80 to 200° C. and a pressure of from 10,500 to 35,000 KPa, (1,500 to 5,000 psi) in the presence of (a) a catalyst which is an organometallic complex of a group 3, 4 or 5 metal, characterized by having at least one phosphinimine ligand;
- and (b) co-catalyst selected from the group consisting of:
- (i) an aluminoxane compound of the formula R122AlO(R12AlO)mAlR122 wherein each R12 is independently selected from the group consisting of C1-20 hydrocarbyl radicals and m is from 3 to 50, and optionally a hindered phenol to provide a molar ratio of Al:hindered phenol from 2:1 to 5:1 if the hindered phenol is present;
- (ii) an ionic activator that may be selected from the group consisting of:
- (A) compounds of the formula [R13]+ [B(R14)4]− wherein B is a boron atom, R13 is a cyclic C5-7 aromatic cation or a triphenyl methyl cation and each R14 is independently selected from the group consisting of phenyl radicals which are unsubstituted or substituted with 3 to 5 substituents selected from the group consisting of a fluorine atom, a C1-4 alkyl or alkoxy radical which is unsubstituted or substituted by a fluorine atom;
- and a silyl radical of the formula —Si—(R15)3;
- wherein each R15 is independently selected from the group consisting of a hydrogen atom and a C1-4 alkyl radical;
- and
- (B) compounds of the formula [(R18)tZH]+[B(R14)4]− wherein B is a boron atom, H is a hydrogen atom, Z is a nitrogen atom or phosphorus atom, t is 2 or 3 and R18 is selected from the group consisting of C1-8 alkyl radicals, a phenyl radical which is unsubstituted or substituted by up to three C1-4 alkyl radicals, or one R18 taken together with the nitrogen atom may form an anilinium radical and R14 is as defined above;
- and
- (C) compounds of the formula B(R14)3 wherein R14 is as defined above;
- and
- (iii) mixtures thereof;
- and
- B) passing said first polymer solution into a second stirred polymerization reactor at a pressure from 10,500 to 35,000 KPa (1,500 to 5,000 psi) and a temperature at least 20° C. higher than the first reactor and polymerizing further ethylene, optionally with one or more C3-12 alpha olefins, in said second stirred polymerization reactor in the presence of (a) a catalyst which is an organometallic complex of a group 3, 4 or 5 metal, characterized by having at least one phosphinimine ligand;
- and (b) a co-catalyst as described above;
- said polyethylene, having a melt index less than 2 as measured by ASTM D 1238, when formed into a monolayer or a co-extruded multi-layer film at a blowup ratio from 2 to 4 and a thickness from 0.5 to 6 mils using a blown film line at a production rate that is greater than 6 lbs/hr/inch (1 kg/hr/cm) of die circumference, has haze values 59 to 65% lower, gloss 45° values 49 to 55% higher, hexane extractables 58 to 79% lower, a plateau seal temperature of about 110° C., hot tack strength (at 115° C.) 25 to 70% higher, dart impact strengths 97 to 142% higher, machine direction (MD) tear strengths 26 to 95% higher, and puncture energy values 74 to 124% higher than films made from resin produced by conventional Ziegler-Natta catalysis, wherein the conventional Ziegler-Natta resin has a melt index of up to 0.15 g/10 min lower than the melt index of the linear low density polyethylene prepared according to said steps A) and B.
(canceled)
Dependencies are inferred from the claim text.