Olefin polymerization catalysts adapted for gas phase processes

Claim 2

A multi-component Ziegler or Ziegler-Natta type high activity catalyst composition consisting of: (a) about 50 to 95 weight % of solid inert particulate organic support material having an average particle size of 0.05 to 0.35 mm, a melting point of about 70° to 170° C., and a density of about 0.9 to 1.5 grams/cc, and (b) about 5 to 50 weight % of solid particulate transition metal based low pressure olefin polymerization catalyst precursor, said particulate catalyst precursor being embedded in said particulate organic support material, and said catalyst composition having been formed by mixing said (a) and (b) components together in a high speed bladed finishing device.

Claim 3

A composition as in claim 1 in which said (a) support material is a polyolefin resin.

Claim 4

A composition as in claim 2 in which said (a) support material is a polyethylene resin.

Claim 5

A composition as in claim 2 in which said (a) support material is a polypropylene resin.

Claim 6

A composition as in claim 3 in which said (b) catalyst precursor is a Ziegler catalyst precursor.

Claim 7

A composition as in claim 4 in which said (b) catalyst precursor is a Ziegler-Natta stereospecific catalyst precursor.

Claim 8

A catalyst composition comprising (a) a catalytic precursor prepared according to claim 1, and (b) activating quantities of organometallic reducing agent compound.

Claim 9

A catalyst composition as in claim 7 in which said (a) precursor is based on a Group IVa, Va or VIa transition metal compound, and said (b) reducing agent is based on a Group Ia, IIa or IIIa metal compound.

Claim 10

A catalyst composition as in claim 8 in which said (b) and (a) compounds are used in an atomic ratio of about 10 to 400 based on the primary metal content of said compounds.

Claim 11

A process for preparing an olefin polymerization catalyst composition for use in a fluidized bed polymerization process which comprises mixing, in a high speed bladed finishing device (a) about 50 to 95 weight % of solid inert particulate organic support material having an average particle size of 0.05 to 0.35 mm, a melting point of about 70° to 170° C., and a density of about 0.9 to 1.5 grams/cc, and (b) about 5 to 50 weight % of solid particulate transition metal based low pressure olefin polymerization catalyst precursor which is a precursor of a high activity Ziegler or Ziegler-Natta type catalyst, said mixing being conducted under such friction induced heat conditions, and for a period of time, as are sufficient to cause the (a) particles of support material to soften, but not to fuse with each other, and the (b) particles of catalyst precursor to become embedded in and/or adhered to said (a) particles, without causing any deterioration in the chemical nature of either the (a) or (b) particles.

Claim 12

A process for preparing an olefin polymerization catalyst composition for use in a fluidized bed polymerization process which comprises mixing, in a high speed bladed finishing device (a) about 50 to 95 weight % of solid inert particulate organic support material having an average particle size of 0.05 to 0.35 mm, a melting point of about 70° to 170° C., and a density of about 0.9 to 1.5 grams/cc, and (b) about 5 to 50 weight % of solid particulate transition metal based low pressure olefin polymerization catalyst precursor which is a precursor of a high activity Ziegler or Ziegler-Natta type catalyst, said mixing being conducted under such friction induced heat conditions, and for a period of time, as are sufficient to cause the (a) particles of support material to soften, but not to fuse with each other, and the (b) particles of catalyst precursor to become embedded in and/or adhered to said (a) particles, without causing any deterioration in the chemical nature of either the (a) or (b) particles.

Claim 13

A process as in claim 10 in which said finishing device is operated at a blade tip speed of at least 150 inches/second.

Claim 14

A process as in claim 11 which is operated until a sticking efficiency of about at least 45 weight % is achieved.

Claim 15

A process as in claim 12 which is operated until a sticking efficiency of about at least 75 to 90 weight % is achieved.