Whitening-resistant, highly melt-viscoelastic ethylene-propylene copolymer and process for producing the same

Claim 2

A whitening-resistant, highly melt viscoelastic ethylene-propylene copolymer, obtained by copolymerizing propylene with ethylene, in the presence of a catalyst prepared by reacting an organoaluminum compound (I) or a reaction product (VI) of an organoaluminum compound (I) with an electron donor (A), with titanium tetrachloride (C), further reacting the resulting solid product (II) with an electron donor (A) and an electron acceptor (B), and combining the resulting solid product (III) with an organoaluminum compound (IV) and an aromatic caboxylic acid ester (V), the molar ratio (V/III) of the aromatic carboxylic acid ester to the solid product (III) being in the range of 0.1 to 10.0, at the following four stages: (1) the first stage wherein propylene or a mixed gas of ethylene with propylene, containing 0 to 7.5% by weight of ethylene, is fed to a reactor to form a polymer; successively (2) the second stage wherein propylene or a mixed gas of ethylene with propylene, containing 0 to 15% by weight of ethylene is fed to the reactor to form a polymer; (3) the amount of ethylene fed at the first stage and the second stage being in the range of 0.7 to 7.5% by weight based on the total amount of the mixed gas; (4) 60 to 89% by weight of the total polymerization amount (excluding soluble copolymer) being polymerized at the first stage and the second stage, and the proportion of the polymerization amount at the first stage to that at the second stage being in the range of 0.65:0.35 to 0.35:0.65; (5) between the intrinsic viscosities of the polymers formed at the first stage and the second stage, the intrinsic viscosity of the polymer having a higher molecular weight [η] H and that of the polymer having a lower molecular weight [η] L having a relationship satisfying the following equation: 3.0≦[η].sub.H -[η].sub.L ≦6.5 (1); successively, (6) the third stage wherein ethylene or a mixed gas of ethylene with propylene, containing 70 to 100% by weight of ethylene, is fed to the reactor to polymerize 5 to 17% by weight of the total polymerization amount (excluding soluble copolymer); (7) the intrinsic viscosity of a polymer formed at the third stage [η] 3 having a relationship satisfying the following equation: [η].sub.L ≦[η].sub.3 ≦[η].sub.H ( 2); successively (8) the fourth stage wherein a mixed gas of ethylene with propylene containing 40 to 70% by weight of ethylene is fed to the reactor to copolymerize 6 to 23% by weight of the total polymerization amount (excluding soluble copolymer); and (9) the intrinsic viscosity of the copolymer formed at the fourth stage [η] 4 satisfying the following equation: [η].sub.L ≦[η].sub.4 ≦[η].sub.H ( 3).

Claim 3

A copolymer according to claim 1 wherein the organo-aluminum compound (IV) is a dialkylaluminum monohalide.

Claim 4

A copolymer according to claim 1 wherein a small amount of an α-olefin is reacted with the combination of the solid product (III) with the organoaluminum compound (IV) and the resulting preactivated catalyst is used as the catalyst.

Claim 5

A copolymer according to claim 1 wherein at each of the first stage to the fourth stage, hydrogen is used to adjust the intrinsic viscosities of the respective polymers.

Claim 6

A copolymer according to claim 1 wherein the respective ethylene contents in the polymers or copolymers formed at the first stage to the fourth stage are in the ranges of 0 to 5% by weight, 0 to 10% by weight, 85 to 100% by weight and 65 to 80% by weight in the order of the stage number, but the ethylene content in the total of the polymers or copolymers formed throughout the first stage and the second stage is in the range of 0.5 to 5% by weight.

Claim 7

A copolymer according to claim 1 wherein the respective ethylene contents in the polymers or copolymers formed at the first stage to the fourth stage are in the range of 1.0 to 3.0% by weight, 1.0 to 6.0% by weight, 90 to 98% by weight and 70 to 75% by weight in the order of the stage number, but the ethylene content in the total of the polymers or copolymers formed throughout the first stage and the second stage is in the range of 1.0 to 3.0% by weight.

Claim 8

A process for producing a whitening-resistant, highly melt-viscoelastic ethylene-propylene copolymer, which process comprises copolymerizing propylene with ethylene, in the presence of a catalyst obtained by reacting an organoaluminum compound (I) or a reaction product (VI) or an organoaluminum compound (I) with an electron donor (A), with titanium tetrachloride (C), further reacting the resulting solid product (II) with an electron donor (A) and an electron acceptor (B), and combining the resulting solid product (III) with an organoaluminum compound (IV) and an aromatic carboxylic acid ester (V), the molar ratio (V/III) of the aromatic carboxylic acid ester to the solid product (III) being in the range of 0.1 to 10.0, at the following four stages: (1) the first stage wherein propylene or a mixed gas of ethylene with propylene, containing 0 to 7.5% by weight of ethylene, is fed to a reactor to form a polymer; succesively (2) the second stage wherein propylene or a mixed gas of ethylene with propylene, containing 0 to 15% by weight of ethylene is fed to the reactor to form a polymer; (3) the amount of ethylene fed at the first stage and the second stage being in the range of 0.7 to 7.5% by weight based on the total amount of the mixed gas; (4) 60 to 89% by weight of the total polymerization amount (excluding soluble copolymer) being polymerized at the first stage and the second stage, and the proportion of the polymerization amount at the first stage to that at the second stage being in the range of 0.65:0.35 to 0.35:0.65; (5) between the intrinsic viscosities of the polymers formed at the first stage and the second stage, the intrinsic viscosity of the polymer having a higher molecular weight [η] H and that of the polymer having a lower molecular weight [η] L having a relationship satisfying the following equation: 3.0≦[η].sub.H -[η].sub.L ≦6.5 (1); successively (6) the third stage wherein ethylene or a mixed gas of ethylene with propylene, containing 70 to 100% by weight of ethylene, is fed to the reactor to polymerize 5 to 17% by weight of the total polymerization amount (excluding soluble copolymer); (7) the intrinsic viscosity of a polymer formed at the third stage [η] 3 having a relationship satisfying the following equation: [η].sub.L ≦[η].sub.3 ≦[η].sub.H ( 2); successively (8) the fourth stage wherein a mixed gas of ethylene with propylene containing 40 to 70% by weight of ethylene is fed to the reactor to copolymerize 6 to 23% by weight of the total polymerization amount (excluding soluble copolymer); and (9) the intrinsic viscosity of the copolymer formed at the fourth stage [η] 4 satisfying the following equation: [η].sub.L ≦[η].sub.4 ≦[η].sub.H ( 3).

Claim 9

A process for producing a whitening-resistant, highly melt-viscoelastic ethylene-propylene copolymer, which process comprises copolymerizing propylene with ethylene, in the presence of a catalyst obtained by reacting an organoaluminum compound (I) or a reaction product (VI) or an organoaluminum compound (I) with an electron donor (A), with titanium tetrachloride (C), further reacting the resulting solid product (II) with an electron donor (A) and an electron acceptor (B), and combining the resulting solid product (III) with an organoaluminum compound (IV) and an aromatic carboxylic acid ester (V), the molar ratio (V/III) of the aromatic carboxylic acid ester to the solid product (III) being in the range of 0.1 to 10.0, at the following four stages: (1) the first stage wherein propylene or a mixed gas of ethylene with propylene, containing 0 to 7.5% by weight of ethylene, is fed to a reactor to form a polymer; succesively (2) the second stage wherein propylene or a mixed gas of ethylene with propylene, containing 0 to 15% by weight of ethylene is fed to the reactor to form a polymer; (3) the amount of ethylene fed at the first stage and the second stage being in the range of 0.7 to 7.5% by weight based on the total amount of the mixed gas; (4) 60 to 89% by weight of the total polymerization amount (excluding soluble copolymer) being polymerized at the first stage and the second stage, and the proportion of the polymerization amount at the first stage to that at the second stage being in the range of 0.65:0.35 to 0.35:0.65; (5) between the intrinsic viscosities of the polymers formed at the first stage and the second stage, the intrinsic viscosity of the polymer having a higher molecular weight [η] H and that of the polymer having a lower molecular weight [η] L having a relationship satisfying the following equation: 3.0≦[η].sub.H -[η].sub.L ≦6.5 (1); successively (6) the third stage wherein ethylene or a mixed gas of ethylene with propylene, containing 70 to 100% by weight of ethylene, is fed to the reactor to polymerize 5 to 17% by weight of the total polymerization amount (excluding soluble copolymer); (7) the intrinsic viscosity of a polymer formed at the third stage [η] 3 having a relationship satisfying the following equation: [η].sub.L ≦[η].sub.3 ≦[η].sub.H ( 2); successively (8) the fourth stage wherein a mixed gas of ethylene with propylene containing 40 to 70% by weight of ethylene is fed to the reactor to copolymerize 6 to 23% by weight of the total polymerization amount (excluding soluble copolymer); and (9) the intrinsic viscosity of the copolymer formed at the fourth stage [η] 4 satisfying the following equation: [η].sub.L ≦[η].sub.4 ≦[η].sub.H ( 3).

Claim 10

A process for producing an ethylene-propylene copolymer according to claim 7, wherein (1) at the first stage, a mixed gas of ethylene with propylene containing 1.5 to 4% by weight of ethylene is fed to the reactor to form a copolymer; successively (2) at the second stage, a mixed gas of ethylene with propylene containing 1.5 to 8% by weight of ethylene is fed to the reactor to form a copolymer; (3) the amount of ethylene fed at the first stage and the second stage is in the range of 1.5 to 4.0% by weight based on the total amount of the mixed gas; (4) 70 to 86% by weight of the total polymerization amount (excluding soluble copolymer) is polymerized at the first stage and the second stage, and the proportion of the polymerization amount at the first stage to that at the second stage is in the range of 0.65:0.35 to 0.35:0.65; (5) between the intrinsic viscosities of the polymers formed at the first stage and the second stage, the intrinsic viscosity of the polymer having a higher molecular weight [η] H and that of the polymer having a lower molecular weight [η] L have a relationship satisfying the following equation:

Claim 11

0≦[η] H -[η] L ≦6.5 (1); successively (6) at the third stage, a mixed gas of ethylene with propylene containing 80 to 95% by weight is fed to the reactor to copolymerize 7 to 14% by weight of the total polymerization amount (excluding soluble copolymer); (7) the intrinsic viscosity of a polymer formed at the third stage [η] 3 has a relationship satisfying the following equation: [η].sub.L ≦[η].sub.3 ≦[η].sub.H ( 2); successively (8) at the fourth stage, a mixed gas of ethylene with propylene containing 45 to 55% by weight is fed to the reactor to copolymerize 8 to 15% by weight of the total polymerization amount (excluding soluble copolymer); and (9) the intrinsic viscosity of a copolymer formed at the fourth stage [η] 4 satisfies the following equation: [η].sub.L ≦[η].sub.4 ≦[η].sub.H ( 3).

Claim 12

0≦[η] H -[η] L ≦6.5 (1); successively (6) at the third stage, a mixed gas of ethylene with propylene containing 80 to 95% by weight is fed to the reactor to copolymerize 7 to 14% by weight of the total polymerization amount (excluding soluble copolymer); (7) the intrinsic viscosity of a polymer formed at the third stage [η] 3 has a relationship satisfying the following equation: [η].sub.L ≦[η].sub.3 ≦[η].sub.H ( 2); successively (8) at the fourth stage, a mixed gas of ethylene with propylene containing 45 to 55% by weight is fed to the reactor to copolymerize 8 to 15% by weight of the total polymerization amount (excluding soluble copolymer); and (9) the intrinsic viscosity of a copolymer formed at the fourth stage [η] 4 satisfies the following equation: [η].sub.L ≦[η].sub.4 ≦[η].sub.H ( 3).

Claim 13

A process for producing a copolymer according to claim 7 wherein the organaluminum compound (IV) is a dialkylaluminum monohalide.

Claim 14

A process for producing a copolymer according to claim 7 wherein a small amount of an α-olefin is reacted with the combination of the solid product (III) with the organoaluminum compound (IV) and the resulting preactivated catalyst is used as the catalyst.

Claim 15

A process for producing a copolymer according to claim 7 wherein at each of the first stage to the fourth stage, hydrogen is used to adjust the intrinsic viscosities of the respective polymers.