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US4042769A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalysts for the polymerization of ethylene

Assignee: Gulf Research and Development Co
•
Filing: 1975-03-12
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Granted: 1977-08-16
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Expires: 1995-03-12
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Abstract

Abstract A process is disclosed for the preparation of a polymerization catalyst useful for the polymerization of ethylene. The catalyst consists of a chromium catalyst supported on a silica aerogel having a surface area of at least 300 square meters per gram and a pore volume of at least 2 milliliters per gram, said values being determined by isothermal liquid nitrogen desorption. The silica aerogel is prepared by a modification of the method disclosed by Kistler in U.S. Pat. No. 2,249,767.

Inventors

  • 👤 Thomas J. Lynch

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 23:04
CPC Classifications
C; C08; C08F; C08F110/00; C08F110/02

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 269 words
In a Particle Form Process for the manufacture of an ethylene polymer in which ethylene is contacted with a chromium catalyst supported on silica; the improvement which consists essentially of employing as the polymerization initiator an olefin polymerization catalyst consisting essentially of a chromium polyerization catalyst supported on a silica aerogel having a surface area of at least about 300 square meters per gram and a pore volume of at least about 2 milliliters per gram, said values being determined by isothermal liquid nitrogen desorption analysis; said silica aerogel having been prepared by a modified Kistler process consisting essentially of the steps of: a. preparing a silica hydrogel, b. treating the silica hydrogel with an oranic solvent that will dissolve at least least 10 weight % water to free the silia hydrogel of water, at least the final contact being with a rigorously anhydrous organic solvent so that the organic solvent, after reaching equilibrium with the silica hydrogel, contains less than about 200 ppm of water, c. removing the organic solvent from the organic solvent-silica hydrogel mixture of step (b) by heating the mixture to above the critical point in a pressure-resistant vessel and releasing the organic solvent therefrom at a pressure at least equal to the critical pressure of the organic solvent, d. cooling the silica aerogel from step (c) to ambient temperature and pressure under rigorously ahydrous conditions, and e. calcining the silica aerogel from step (d) at an elevated temperature in a rigorously anhydrous environment; said ethylene polymerization catalyst having been prepared by contacting said chromium polymerization catalyst with said silica aerogel under rigorously anhydrous conditions.
Claim 2
Dependent Claim 269 words
In a Particle Form Process for the manufacture of an ethylene polymer in which ethylene is contacted with a chromium catalyst supported on silica; the improvement which consists essentially of employing as the polymerization initiator an olefin polymerization catalyst consisting essentially of a chromium polyerization catalyst supported on a silica aerogel having a surface area of at least about 300 square meters per gram and a pore volume of at least about 2 milliliters per gram, said values being determined by isothermal liquid nitrogen desorption analysis; said silica aerogel having been prepared by a modified Kistler process consisting essentially of the steps of: a. preparing a silica hydrogel, b. treating the silica hydrogel with an oranic solvent that will dissolve at least least 10 weight % water to free the silia hydrogel of water, at least the final contact being with a rigorously anhydrous organic solvent so that the organic solvent, after reaching equilibrium with the silica hydrogel, contains less than about 200 ppm of water, c. removing the organic solvent from the organic solvent-silica hydrogel mixture of step (b) by heating the mixture to above the critical point in a pressure-resistant vessel and releasing the organic solvent therefrom at a pressure at least equal to the critical pressure of the organic solvent, d. cooling the silica aerogel from step (c) to ambient temperature and pressure under rigorously ahydrous conditions, and e. calcining the silica aerogel from step (d) at an elevated temperature in a rigorously anhydrous environment; said ethylene polymerization catalyst having been prepared by contacting said chromium polymerization catalyst with said silica aerogel under rigorously anhydrous conditions.
Claim 3
Dependent Claim 25 words
The process of claim 1 in which the chromium catalyst is a chromium oxide, at least a portion of which is in the hexavalent state.
Claim 4
Dependent Claim 20 words
The process of claim 1 in which the organic solvent employed in the preparation of the silica aerogel is ethanol.
Claim 5
Dependent Claim 20 words
The process of claim 1 in which the organic solvent employed in the preparation of the silica aerogel is tetrahydrofuran.

References Cited (Backward Citations)

US3239498A Cited
US3378540A Cited
US3562241A Cited
US3671432A Cited
US3819598A Cited
US3862104A Cited
US3867306A Cited
US3890249A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-15 1981-02-14 1981-08-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-15 1985-02-14 1985-08-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-15 1989-02-14 1989-08-16 $7700.00 Window Closed / Lapsed

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