Low density polyethylene

Claim 2

An ethylene-hexene-1 copolymer having a density of 0.910-0.935 and a relative comonomer dispersity of over 100%.

Claim 3

An ethylene-hexene-1 copolymer having a density of 0.910-0.935 and a relative comonomer dispersity of over 100% and a melt index of 1 to 10.

Claim 4

An ethylene-hexene-1 copolymer having a density of 0.910-0.935 and a relative comonomer dispersity of over 100% and a melt index of 1 to 10.

Claim 5

A copolymer in accordance with claim 1 containing 1 to 6 mole percent 1-hexene and 99 to 94 mole percent ethylene, said copolymer having a maximum relative comonomer dispersity which is the sum of 100% plus the concentration of 1-hexene in mole percent.

Claim 6

A process to produce ethylene-monoolefin copolymers comprising contacting a gas mixture containing ethylene and another monoolefin selected from the group consisting of 1-butene, 1-hexene, 1-octene and 4-methyl-1-pentene with a silica/titania/chromium oxide catalyst, said silica and titania being coprecipitated, under gas phase polymerization conditions in a polymerization zone such as to produce an ethylene-monoolefin-copolymer having a density in the range of 0.915 to 0.935 g/cc wherein said 1-butene, when used, is used in a concentration in mole percent in the gas phase on total olefins in the gas phase in the polymerization zone as 100 mole percent which is defined by the following formula ##EQU10## wherein CGB is the concentration of 1-butene in mole percent in the gas phase, CPB is the concentration of 1-butene in the copolymer and K4 is a factor in the range of 0.6 to 1.2; wherein said 1-hexene, when used, is used in a concentration in mole percent in the gas phase based on total olefins in the gas phase in the polymerization zone as 100 mole percent which is defined by the following formula ##EQU11## wherein CGH is the concentration of 1-hexene in mole percent in the gas phase, CPH is the concentration of 1-hexane in the copolymer and K6 is a factor in the range of 1.4 to 2.5; wherein said 1-octene, when used, is used in a concentration in mole percent in the gas phase based on total olefins in the gas phase in the polymerization zone as 100 mole percent which is defined by the following formula ##EQU12## wherein CGO is the concentration of 1-octene in mole percent in the phase phase, CPO is the concentration of 1-octene in the copolymer and K8 is a factor in the range of 4 to 7; wherein said 4-methyl-1-pentene, when used, is used in a concentration in mole percent in the gas phase based on total olefins in the gas phase in the polymerization zone as 100 mole percent which is defined by the following formula ##EQU13## wherein CGF is the concentration of 4-methyl-1-pentene in mole percent in the phase phase, CPF is the concentration of 4-methyl-1-pentene in the copolymer and K51 is a factor in the range of 1 to 1.4; with the proviso that the higher values of the range of K4 or respectively K6 or respectively K8 or respectively K51 are associated with the lower densities and conversely wherein the lower values of these values K4, K6, K8 or K51 are associated with the higher densities of the copolymer produced.

Claim 7

A process to produce ethylene-monoolefin copolymers comprising contacting a gas mixture containing ethylene and another monoolefin selected from the group consisting of 1-butene, 1-hexene, 1-octene and 4-methyl-1-pentene with a silica/titania/chromium oxide catalyst, said silica and titania being coprecipitated, under gas phase polymerization conditions in a polymerization zone such as to produce an ethylene-monoolefin-copolymer having a density in the range of 0.915 to 0.935 g/cc wherein said 1-butene, when used, is used in a concentration in mole percent in the gas phase on total olefins in the gas phase in the polymerization zone as 100 mole percent which is defined by the following formula ##EQU10## wherein CGB is the concentration of 1-butene in mole percent in the gas phase, CPB is the concentration of 1-butene in the copolymer and K4 is a factor in the range of 0.6 to 1.2; wherein said 1-hexene, when used, is used in a concentration in mole percent in the gas phase based on total olefins in the gas phase in the polymerization zone as 100 mole percent which is defined by the following formula ##EQU11## wherein CGH is the concentration of 1-hexene in mole percent in the gas phase, CPH is the concentration of 1-hexane in the copolymer and K6 is a factor in the range of 1.4 to 2.5; wherein said 1-octene, when used, is used in a concentration in mole percent in the gas phase based on total olefins in the gas phase in the polymerization zone as 100 mole percent which is defined by the following formula ##EQU12## wherein CGO is the concentration of 1-octene in mole percent in the phase phase, CPO is the concentration of 1-octene in the copolymer and K8 is a factor in the range of 4 to 7; wherein said 4-methyl-1-pentene, when used, is used in a concentration in mole percent in the gas phase based on total olefins in the gas phase in the polymerization zone as 100 mole percent which is defined by the following formula ##EQU13## wherein CGF is the concentration of 4-methyl-1-pentene in mole percent in the phase phase, CPF is the concentration of 4-methyl-1-pentene in the copolymer and K51 is a factor in the range of 1 to 1.4; with the proviso that the higher values of the range of K4 or respectively K6 or respectively K8 or respectively K51 are associated with the lower densities and conversely wherein the lower values of these values K4, K6, K8 or K51 are associated with the higher densities of the copolymer produced.

Claim 8

A process in accordance with claim 4 wherein said catalyst is selected from the group consisting of one or more of (a) silica-titania-chromium tergels and (b) chromium supported on silica-titania cogels.

Claim 9

Process in accordance with claim 4 wherein said polymerization step is carried out a pressure of about 50 to about 1000 psig and at a temperature below 120° C.

Claim 10

Process in accordance with claim 6 wherein the polymerization temperature is in the range of 70° to 95° C.

Claim 11

Process in accordance with claim 4 wherein the polymerization is carried out with free hydrogen present in the gas phase of the polymerization zone.