Method for the production of low density polyethylene

Claim 1

A method for the production of a low density ethylene copolymer of not higher than 0.945 g/cm 3 by copolymerizing ethylene and an α-olefin, which comprises: (i) using a catalyst consisting essentially of (A) a catalyst component having titanium tetrachloride supported on a magnesium compound or a mixture or reaction product thereof with an aluminum compound and (B) an organoaluminum compound, (ii) subjecting ethylene to pre-polymerization in the presence of said catalyst prior to the copolymerization, the amount of ethylene to be pre-polymerized being within the range of 1.0 to 50 g per 1.0 g of said catalyst component (A), (iii) conducting the copolymerization of ethylene and an α-olefin in a two-step process of: (a) first, conducting the copolymerization until polymers of 10 to 80% by weight based on a finally resulting polymer have been formed while controlling the copolymerization ratio of α-olefin to ethylene at less than 3.0% by weight, and (b) completing the polymerization reaction while elevating the copolymerization ratio of α-olefin to ethylene to the range of 3.0 to 20% by weight, and (iv) conducting said copolymerization in slurry state in the presence of a hydrocarbon solvent having a boiling point of not higher than 40° C. at temperature of not higher than 100° C.

Claim 2

A method for the production of a low density ethylene copolymer of not higher than 0.945 g/cm 3 by copolymerizing ethylene and an α-olefin, which comprises: (i) using a catalyst consisting essentially of (A) a catalyst component having titanium tetrachloride supported on a magnesium compound or a mixture or reaction product thereof with an aluminum compound and (B) an organoaluminum compound, (ii) subjecting ethylene to pre-polymerization in the presence of said catalyst prior to the copolymerization, the amount of ethylene to be pre-polymerized being within the range of 1.0 to 50 g per 1.0 g of said catalyst component (A), (iii) conducting the copolymerization of ethylene and an α-olefin in a two-step process of: (a) first, conducting the copolymerization until polymers of 10 to 80% by weight based on a finally resulting polymer have been formed while controlling the copolymerization ratio of α-olefin to ethylene at less than 3.0% by weight, and (b) completing the polymerization reaction while elevating the copolymerization ratio of α-olefin to ethylene to the range of 3.0 to 20% by weight, and (iv) conducting said copolymerization in slurry state in the presence of a hydrocarbon solvent having a boiling point of not higher than 40° C. at temperature of not higher than 100° C.