Patent US4011382A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4011382A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of low and medium density ethylene polymer in fluid bed reactor

Assignee: Union Carbide Corp
•
Filing: 1975-03-10
•
Granted: 1977-03-08
•
Expires: 1995-03-10
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A supported catalyst is used in the low pressure catalytic copolymerization of ethylene with C 3 to C 6 α-olefins in a fluid bed reactor to produce polymers having a density of less than 0.941 and a melt index of >0.0 to at least about 2.0. The supported catalyst contains about 0.05 to 3.0 weight % of chromium, about 1.5 to 9.0 weight % of titanium and >0.0 to about 2.5 weight % of fluorine.

Inventors

  • 👤 Isaac J. Levine
  • 👤 Frederick J. Karol

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 03:45
CPC Classifications
C; C08; C08F; C08F210/00; C08F210/16; C08L; C08L23/00; C08L23/02; C08L23/04; C08L23/08; C08L23/0807; C08L23/0815

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 165 words
A process for producing solid ethylene polymers having a density of less than 0.941 and a melt index of >0.0 to at least about 2.0 under relatively low pressure conditions which comprises copolymerizing ethylene with sufficient quantities of C 3 to C 6 α-olefin monomer to provide the desired density in the copolymer product in a fluid bed process at a temperature of about 30° to 105° C., under a pressure of less than about 1000 psi, and under a mass gas flow rate of about 1.5 to 10 times G mf by contacting the monomers with fluidized particles of a supported catalyst wherein said particles have an average diameter of about 50 to 200 microns said supported catalyst having been activated in air or oxygen at a temperature of about 300° to 900° C., and comprising, based on the total weight of the support and the catalyst, about 0.05 to 3.0 weight percent of chromium, about 1.5 to 9.0 weight percent of titanium, and
Claim 2
Dependent Claim 165 words
A process for producing solid ethylene polymers having a density of less than 0.941 and a melt index of >0.0 to at least about 2.0 under relatively low pressure conditions which comprises copolymerizing ethylene with sufficient quantities of C 3 to C 6 α-olefin monomer to provide the desired density in the copolymer product in a fluid bed process at a temperature of about 30° to 105° C., under a pressure of less than about 1000 psi, and under a mass gas flow rate of about 1.5 to 10 times G mf by contacting the monomers with fluidized particles of a supported catalyst wherein said particles have an average diameter of about 50 to 200 microns said supported catalyst having been activated in air or oxygen at a temperature of about 300° to 900° C., and comprising, based on the total weight of the support and the catalyst, about 0.05 to 3.0 weight percent of chromium, about 1.5 to 9.0 weight percent of titanium, and
Claim 3
Dependent Claim 23 words
>0. 0 to about 2.5 weight percent of fluorine, said chromium and said titanium being in the form of oxides after said activation.
Claim 4
Dependent Claim 23 words
>0. 0 to about 2.5 weight percent of fluorine, said chromium and said titanium being in the form of oxides after said activation.
Claim 5
Dependent Claim 20 words
A process as in claim 1 for producing solid ethylene polymers having a melt index of about 0.1 to 1.0.
Claim 6
Dependent Claim 19 words
A process as in claim 2 for producing solid ethylene polymers having a density of about 0.900 to 0.925.
Claim 7
Dependent Claim 19 words
A process as in claim 2 for producing solid ethylene polymers having a density of about 0.926 to 0.940.
Claim 8
Dependent Claim 14 words
A process as in claim 1 for producing solid copolymers of ethylene and propylene.
Claim 9
Dependent Claim 14 words
A process as in claim 1 for producing solid copolymers of ethylene and butene-1.
Claim 10
Dependent Claim 14 words
A process as in claim 1 for producing solid copolymers of ethylene and hexane-1.
Claim 11
Dependent Claim 45 words
A process as in claim 1 for producing solid ethylene polymers at a temperature of about 85° to 100° C., under a pressure of about 200 to 350 psi and under a mass gas flow rate of about 3 to 6 times G mf .
Claim 12
Dependent Claim 36 words
A process as in claim 8 in which said catalyst comprises about 0.2 to 1.0 weight percent of chromium, about 4 to 7 weight percent of titanium, and about 0.1 to 1.0 weight percent of fluorine.
Claim 13
Dependent Claim 12 words
A process as in claim 9 in which said support comprises silica.

References Cited (Backward Citations)

US3023203A Cited
US2953552A Cited
US3445367A Cited
US3513143A Cited
US3509116A Cited
US3622521A Cited
US3798202A Cited
US3876602A Cited
US3879362A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-03-07 1980-09-06 1981-03-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-03-07 1984-09-06 1985-03-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-03-07 1988-09-06 1989-03-08 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag