Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
245 words
An olefin polymerization catalyst prepared by the steps of: a. reacting a zirconium compound of the formula M 4 Zr(C 2 O 4 ) 4 .nH 2 O, where M is an alkali metal or ammonium ion and n equals 0 to 10, with a silicon compound of the type A 2 SiO 3 , where A is an alkali metal, in an aqueous solution at a pH of at least 11 and then adding an acidic material to a pH of about 5-9, to produce a hydrocogel; b. aging said hydrocogel at a temperature between about ambient to 90° C. for at least one hour; c. washing said hydrocogel of b with an aqueous liquid; d. partially dehydrating the resulting washed hydrocogel of c by azeotropic distillation by mixing with a compound capable of forming an azeotrope with water or by washing the hydrocogel with a water miscible solvent to produce a substantially water-free, large pore volume zirconia-silica catalyst support; e. removing residual water from the product of d by chemically reacting this water with a ketal of the formula RC(OR) 2 R in which R is the same or different and is hydrogen or an alkyl group of 1-5 carbon atoms; f. calcining the resulting zerocogel at a temperature of about 1000°-1850° F. preparatory to its use as an olefin polymerization catalyst support; g. introducting a chromium compound onto said calcined support of f; and h. activating to produce an active polymerization catalyst.
Claim 2
Dependent Claim
245 words
An olefin polymerization catalyst prepared by the steps of: a. reacting a zirconium compound of the formula M 4 Zr(C 2 O 4 ) 4 .nH 2 O, where M is an alkali metal or ammonium ion and n equals 0 to 10, with a silicon compound of the type A 2 SiO 3 , where A is an alkali metal, in an aqueous solution at a pH of at least 11 and then adding an acidic material to a pH of about 5-9, to produce a hydrocogel; b. aging said hydrocogel at a temperature between about ambient to 90° C. for at least one hour; c. washing said hydrocogel of b with an aqueous liquid; d. partially dehydrating the resulting washed hydrocogel of c by azeotropic distillation by mixing with a compound capable of forming an azeotrope with water or by washing the hydrocogel with a water miscible solvent to produce a substantially water-free, large pore volume zirconia-silica catalyst support; e. removing residual water from the product of d by chemically reacting this water with a ketal of the formula RC(OR) 2 R in which R is the same or different and is hydrogen or an alkyl group of 1-5 carbon atoms; f. calcining the resulting zerocogel at a temperature of about 1000°-1850° F. preparatory to its use as an olefin polymerization catalyst support; g. introducting a chromium compound onto said calcined support of f; and h. activating to produce an active polymerization catalyst.
Claim 3
Dependent Claim
21 words
The catalyst of claim 1 wherein said acidic compound in said aqueous solution is sulfuric acid, hydrochloric acid or ammonium sulfate.
Claim 4
Dependent Claim
10 words
The catalyst of claim 1 wherein said ketal comprises 2,2-dimethoxypropane.
Claim 5
Dependent Claim
10 words
The catalyst of claim 1 wherein said ketal comprises 2,2-dimethoxybutane.
Claim 6
Dependent Claim
10 words
The catalyst of claim 1 wherein said ketal comprises 2,2-diethoxypropane.
Claim 7
Dependent Claim
10 words
The catalyst of claim 1 wherein said ketal comprises 2-methoxy-2-ethoxypropane.
Claim 8
Dependent Claim
32 words
The catalyst of claim 1 wherein said washing step (c) is carried out with an aqueous liquid comprising at least one of water and an aqueous solution of a thermally decomposible salt.
Claim 9
Dependent Claim
24 words
The catalyst of claim 7 wherein said thermally decomposible salt is selected from the group consisting of ammonium nitrate, ammonium carbonate, and ethylenediamine diacetate.
Claim 10
Dependent Claim
225 words
A catalyst support prepared by the steps of: a. reacting a zirconium compound of the formula M 4 Zr(C 2 O 4 ) 4 .nH 2 O, where M is an alkali metal or ammonium ion and n equals 0 to 10, with a silicon compound of the type A 2 SiO 3 , where A is an alkali metal, in an aqueous solution at a pH of at least 11 and then adding an acidic material to a pH of about 5-9, to produce a hydrocogel; b. aging said hydrocogel at a temperature between about ambient to 90° C. for at least one hour; c. washing said hydrocogel of b with an aqueous liquid; d. partially dehydrating the resulting washed hydrocogel of c by azeotropic distillation by mixing with a compound capable of forming an azeotrope with water or by washing the hydrocogel with a water miscible solvent to produce a substantially water-free, large pore volume zirconia-silica catalyst support; e. removing residual water from the product of d by chemically reacting this water with a ketal of the formula RC(OR) 2 R in which R is the same or different and is hydrogen or an alkyl group of 1-5 carbon atoms; and, f. calcining the resulting zerocogel at a temperature of about 1000°-1850° F. prepatory to its use as an olefin polymerization catalyst support.
Claim 11
Dependent Claim
225 words
A catalyst support prepared by the steps of: a. reacting a zirconium compound of the formula M 4 Zr(C 2 O 4 ) 4 .nH 2 O, where M is an alkali metal or ammonium ion and n equals 0 to 10, with a silicon compound of the type A 2 SiO 3 , where A is an alkali metal, in an aqueous solution at a pH of at least 11 and then adding an acidic material to a pH of about 5-9, to produce a hydrocogel; b. aging said hydrocogel at a temperature between about ambient to 90° C. for at least one hour; c. washing said hydrocogel of b with an aqueous liquid; d. partially dehydrating the resulting washed hydrocogel of c by azeotropic distillation by mixing with a compound capable of forming an azeotrope with water or by washing the hydrocogel with a water miscible solvent to produce a substantially water-free, large pore volume zirconia-silica catalyst support; e. removing residual water from the product of d by chemically reacting this water with a ketal of the formula RC(OR) 2 R in which R is the same or different and is hydrogen or an alkyl group of 1-5 carbon atoms; and, f. calcining the resulting zerocogel at a temperature of about 1000°-1850° F. prepatory to its use as an olefin polymerization catalyst support.
Claim 12
Dependent Claim
22 words
The catalyst support of claim 9 wherein said acidic compound in said aqueous solution is sulfuric acid, hydrochloric acid or ammonium sulfate.
Claim 13
Dependent Claim
11 words
The catalyst support of claim 9 wherein said ketal comprises 2,2-dimethoxypropane.
Claim 14
Dependent Claim
11 words
The catalyst support of claim 9 wherein said ketal comprises 2,2-dimethoxybutane.
Claim 15
Dependent Claim
11 words
The catalyst support of claim 9 wherein said ketal comprises 2,2-diethoxypropane.
Claim 16
Dependent Claim
11 words
The catalyst support of claim 9 wherein said ketal comprises 2-methoxy-2-ethoxypropane.
Claim 17
Dependent Claim
33 words
The catalyst support of claim 9 wherein said washing step c is carried out with an aqueous liquid comprising at least one of water and an aqueous solution of a thermally decomposible salt.
Claim 18
Dependent Claim
25 words
The catalyst support of claim 15 wherein said thermally decomposible salt is selected from the group consisting of ammonium nitrate, ammonium carbonate, and ethylenediamine diacetate.