Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
80 words
An olefin polymerization catalyst consisting essentially of the reaction product obtained by contacting a solution in hydrocarbon medium of tetra(neophyl) zirconium with a suspension in hydrocarbon medium of a hydroxylated metal oxide free from absorbed molecular H 2 O of a metal selected from the group consisting of the metals of Groups II(a), III(a), IV(a), and IV(b) of the Bohr Periodic Table of the Elements, the proportion of said tetra(neophyl) zirconium being at least 0.05 millimoles per gram of oxide.
Claim 2
Dependent Claim
80 words
An olefin polymerization catalyst consisting essentially of the reaction product obtained by contacting a solution in hydrocarbon medium of tetra(neophyl) zirconium with a suspension in hydrocarbon medium of a hydroxylated metal oxide free from absorbed molecular H 2 O of a metal selected from the group consisting of the metals of Groups II(a), III(a), IV(a), and IV(b) of the Bohr Periodic Table of the Elements, the proportion of said tetra(neophyl) zirconium being at least 0.05 millimoles per gram of oxide.
Claim 3
Dependent Claim
12 words
A catalyst of claim 1 in which the metal oxide is alumina.
Claim 4
Dependent Claim
44 words
A catalyst of claim 2 in which the alumina is a fumed alumina having a surface area of 10-500 m 2 /g having, prior to reaction with tetra(neophyl) zirconium, HO-groups on its surfaces equivalent to from about 0.5% to about 1.5% by weight water.
Claim 5
Dependent Claim
222 words
A process for producing a catalyst for the polymerization of 1-olefins consisting essentially of neophyl zirconium aluminate on alumina which consists essentially, in combination and in sequence, of the following steps: a. heating gamma alumina in a stream of anhydrous gas comprising N 2 at 900° to 1100°C. for 1 to 10 hours to dry the alumina and convert the gamma alumina to a mixture of gamma, delta, and theta crystalline forms; b. cooling the alumina and partially hydrating it by contacting the alumina with an atmosphere comprising water vapor until from 0.5% to 5% by weight of water has reacted; c. redrying the alumina by heating at 300° to 500°C. in a stream of anhydrous gas comprising N 2 for 1 to 10 hours until the alumina is free from absorbed H 2 O and contains from 0.5% to 1.5% by weight water of hydration as HO-groups on the surfaces of the alumina; and d. reacting the activated alumina from (c), as a slurry in an anhydrous liquid hydrocarbon medium, with a solution of tetra(neophyl) zirconium in a anhydrous liquid hydrocarbon, by mixing together the slurry and the solution in a proportion of 0.1 to 0.6 millimoles of tetra(neophyl) zirconium per gram of the activated aluminum at a temperature in the range of 0° to 100°C. until the reaction is complete.
Claim 6
Dependent Claim
222 words
A process for producing a catalyst for the polymerization of 1-olefins consisting essentially of neophyl zirconium aluminate on alumina which consists essentially, in combination and in sequence, of the following steps: a. heating gamma alumina in a stream of anhydrous gas comprising N 2 at 900° to 1100°C. for 1 to 10 hours to dry the alumina and convert the gamma alumina to a mixture of gamma, delta, and theta crystalline forms; b. cooling the alumina and partially hydrating it by contacting the alumina with an atmosphere comprising water vapor until from 0.5% to 5% by weight of water has reacted; c. redrying the alumina by heating at 300° to 500°C. in a stream of anhydrous gas comprising N 2 for 1 to 10 hours until the alumina is free from absorbed H 2 O and contains from 0.5% to 1.5% by weight water of hydration as HO-groups on the surfaces of the alumina; and d. reacting the activated alumina from (c), as a slurry in an anhydrous liquid hydrocarbon medium, with a solution of tetra(neophyl) zirconium in a anhydrous liquid hydrocarbon, by mixing together the slurry and the solution in a proportion of 0.1 to 0.6 millimoles of tetra(neophyl) zirconium per gram of the activated aluminum at a temperature in the range of 0° to 100°C. until the reaction is complete.
Claim 7
Dependent Claim
26 words
A process according to claim 4 in which the alumina is a fumed alumina having a surface area of from 10 to 500 m 2 /g.
Claim 8
Dependent Claim
23 words
A process according to claim 4 in which the gas employed in steps (a) and (c) consists of pure anhydrous N 2 .
Claim 9
Dependent Claim
29 words
A process according to claim 4 in which in step (d) the proportion of tetra(neophyl) zirconium employed is from 0.15 to 0.35 millimoles per gram of suspended activated alumina.
Claim 10
Dependent Claim
36 words
A process according to claim 4 in which the reaction product of step (d) is aged for a time sufficient to allow partial reduction of the zirconium, at least in part to a valence of three.