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US4290914A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalytic materials as for olefin polymerization

Assignee: National Petro-Chemicals Corp
•
Filing: 1980-06-16
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Granted: 1981-09-22
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Expires: 2000-06-16
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Abstract

Abstract Catalysts, especially for olefin polymerization are prepared by coating an aluminum compound on a selected high pore volume silica gel, and calcining the support at temperatures of from about 200° to 2000° F. The preferred catalyst is prepared with an inorganic support material as aforesaid, thereafter depositing an organophosphoryl chromium compound thereon, and activating the thus-treated support by heating in a non-reducing, preferably oxygen-containing, atmosphere at temperatures of from about 800° to 2000° F. The activated, supported catalyst composition may, but need not necessarily, be combined with a metallic and/or non-metallic reducing agent, to provide a catalyst system useful in the polymerization of 1-olefins.

Inventors

  • 👤 Stanley J. Katzen
  • 👤 Louis J. Rekers

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 01:38
CPC Classifications
C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 253 words
A process for the preparation of a catalyst material comprising coating a xerogel consisting of silica as the major constituent and having surface hydroxyl groups, a surface area in the range of 200 to 500 m 2 /g, a pore volume greater than about 2.0 cc/g, a major portion of which pore volume is provided by pores having pore diameters in the range of from 300 to 600 A with an aluminum compound capable of reacting with said surface hydroxyl groups and having the formula Al(X) a (OR) b , wherein X is R, a is 0-2, b is 1-3, a+b is 3, and R is an alkyl group having from 1 to 8 carbon atoms in an amount sufficient to provide from about 0.1 to 10% of aluminum by weight based on the weight of the xerogel, calcining the support material having the aluminum compound thereon at temperatures of at least 200° F., depositing on the aluminum coated calcined material an organophosphoryl chromium reaction product of chromium trioxide and an organophosphorus compound of the formula: ##STR3## wherein R is hydrogen, or alkyl, aralkyl, aryl, or cycloalkyl, but al least one R is other than hydrogen in an amount sufficient to provide from about 0.25 to 2.5% of chromium by weight based on the weight of the Xerogel; and activating the thus treated support in a non-reducing atmosphere at temperatures of from 1550° F. and up to the decomposition temperature of the support, said activating temperature being in excess of said calcining temperature.
Claim 2
Dependent Claim 253 words
A process for the preparation of a catalyst material comprising coating a xerogel consisting of silica as the major constituent and having surface hydroxyl groups, a surface area in the range of 200 to 500 m 2 /g, a pore volume greater than about 2.0 cc/g, a major portion of which pore volume is provided by pores having pore diameters in the range of from 300 to 600 A with an aluminum compound capable of reacting with said surface hydroxyl groups and having the formula Al(X) a (OR) b , wherein X is R, a is 0-2, b is 1-3, a+b is 3, and R is an alkyl group having from 1 to 8 carbon atoms in an amount sufficient to provide from about 0.1 to 10% of aluminum by weight based on the weight of the xerogel, calcining the support material having the aluminum compound thereon at temperatures of at least 200° F., depositing on the aluminum coated calcined material an organophosphoryl chromium reaction product of chromium trioxide and an organophosphorus compound of the formula: ##STR3## wherein R is hydrogen, or alkyl, aralkyl, aryl, or cycloalkyl, but al least one R is other than hydrogen in an amount sufficient to provide from about 0.25 to 2.5% of chromium by weight based on the weight of the Xerogel; and activating the thus treated support in a non-reducing atmosphere at temperatures of from 1550° F. and up to the decomposition temperature of the support, said activating temperature being in excess of said calcining temperature.
Claim 3
Dependent Claim 23 words
The process according to claim 1, wherein the activation is carried out at a temperature of from about 1550° F. to 1800° F.

References Cited (Backward Citations)

GB907579A Cited
GB912275A Cited
US3417030A Cited
GB1191774A Cited
US3780011A Cited
US3985676A Cited
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DE2525411A1 Cited
US3984351A Cited
US4100104A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-09-21 1985-03-23 1985-09-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-09-21 1989-03-23 1989-09-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-09-21 1993-03-23 1993-09-22 $7700.00 Window Closed / Lapsed

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