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Method of preparing catalyst supports

Assignee: Enron Chemical Co
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Filing: 1980-04-18
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Granted: 1981-07-21
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Expires: 2000-04-18
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Abstract

Abstract A method of preparing large pore volume zirconia-silica catalyst supports, the resulting supports and a method of polymerizing olefins comprising contacting an olefin or mixture of olefins with a catalyst prepared with these supports. The supports are prepared by 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 equal to at least 11, then adding an acidic solution to a pH of about 5-9 to produce a hydrocogel. The hydrocogel is then aged and washed free of soluble by-products first with water, then with aqueous ammonium nitrate and again with water. The water is removed from the washed hydrocogel by azeotropic distillation or by washing with a water miscible solvent, then residual water is removed by chemically reacting this water with a ketal of the formula RC(OR) 2 R where R is the same or different and is an alkyl group of 1-5 carbon atoms, and then calcining the resulting xerocogel.

Inventors

  • 👤 Robert A. Dombro

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 16:18
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/16; B01J23/24; B01J23/26; B01J21/00; B01J21/06; B01J21/08; C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 245 words
The method of preparing large pore volume zirconia-silica useful as a catalyst support for a catalyst for polymerizing and copolymerizing olefins, comprising: 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 first with water, then with aqueous ammonium nitrate and again with water; 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 an alkyl group of 1-5 carbon atoms; and f. calcining the resulting xerocogel at a temperature of about 1000°-1850° F. preparatory to its use as an olefin polymerization catalyst support.
Claim 2
Independent Claim 245 words
The method of preparing large pore volume zirconia-silica useful as a catalyst support for a catalyst for polymerizing and copolymerizing olefins, comprising: 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 first with water, then with aqueous ammonium nitrate and again with water; 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 an alkyl group of 1-5 carbon atoms; and f. calcining the resulting xerocogel at a temperature of about 1000°-1850° F. preparatory to its use as an olefin polymerization catalyst support.
Claim 3
Dependent Claim 12 words
The method of claim 1 wherein M is an alkali metal ion.
Claim 4
Dependent Claim 11 words
The method of claim 1 wherein M is an ammonium ion.
Claim 5
Dependent Claim 21 words
The method of claim 1 wherein said acidic compound in said aqueous solution is sulfuric acid, hydrochloric acid or ammonium sulfate.
Claim 6
Dependent Claim 27 words
The method of claim 1 wherein water is partially removed from the washed hydrocogel by azeotropic distillation with a compound capable of forming an azeotrope with water.
Claim 7
Dependent Claim 19 words
The method of claim 1 wherein water is partially removed by washing the hydrocogel with a water miscible solvent.
Claim 8
Dependent Claim 10 words
The method of claim 1 wherein said ketal comprises 2,2-dimethoxypropane.
Claim 9
Dependent Claim 10 words
The method of claim 1 wherein said ketal comprises 2,2-dimethoxybutane.
Claim 10
Dependent Claim 10 words
The method of claim 1 wherein said ketal comprises 2,2-diethoxypropane.
Claim 11
Dependent Claim 10 words
The method of claim 1 wherein said ketal comprises 2-methoxy-2-ethoxypropane.

References Cited (Backward Citations)

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US3867306A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-07-20 1985-01-19 1985-07-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-07-20 1989-01-19 1989-07-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-07-20 1993-01-19 1993-07-21 $7700.00 Window Closed / Lapsed

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