Patent US4433123A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4433123A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymerization process for drag reducing substances

Assignee: ConocoPhillips Co
•
Filing: 1981-05-12
•
Granted: 1984-02-21
•
Expires: 2001-05-12
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A method is provided for the production of ultrahigh molecular weight drag reducing substances and the like comprising: (a) preparing under an inert atmosphere a catalyst comprising: p1 (1) titanium halide of the general formula TiX m wherein m=2.5 to 4.0; (2) a co-catalyst of the formula AlR n X 3-n where R is a hydrocarbon radical, X is a halogen or hydrogen and n is 2 or 3; (3) a phosphorous compound of the formula PR 1 R 2 R 3 or P(OR 1 ) (OR 2 ) (OR 3 ) where R 1 , R 2 , and R 3 are, independently, aryl, alkyl, aralkyl, or alkaryl, containing from 1 to 12 carbon atoms and placing the catalyst in contact with; (b) alpha-monoolefinic hydrocarbons from C 2 -C 30 under suitable temperature conditions to provide a hydrocarbon soluble ultrahigh molecular weight polymer, then ceasing polymerization at a polymer content level of 20% by weight or less, based on the total reaction mixture.

Inventors

  • 👤 Mark P. Mack

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 12:22
CPC Classifications
C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 153 words
A method for the production of ultrahigh molecular weight non-crystalline hydrocarbon soluble polymers comprising: (a) preparing under an inert atmosphere a catalyst comprising (1) titanium trichloride, (2) a co-catalyst of the formula AlR n X 3-n where R is a hydrocarbon radical containing from 1 to 20 carbon atoms, X is hydrogen or halogen, and n is 2 or 3, and a phosphorus compound of the formula PR 1 R 2 R 3 , wherein R 1 , R 2 , and R 3 are, independently, aryl, alkyl, aralkyl, or alkaryl, each containing from 1 to 12 carbon atoms and placing the catalyst in contact with (b) C 2 to C 30 monoolefinic hydrocarbons, said contacting occurring at temperatures of from about -10° C. to about 40° C. to polymerize said olefins, then (c) ceasing polymerization at a polymer content level of 20% by weight or less based on the total reaction mixture.
Claim 2
Independent Claim 153 words
A method for the production of ultrahigh molecular weight non-crystalline hydrocarbon soluble polymers comprising: (a) preparing under an inert atmosphere a catalyst comprising (1) titanium trichloride, (2) a co-catalyst of the formula AlR n X 3-n where R is a hydrocarbon radical containing from 1 to 20 carbon atoms, X is hydrogen or halogen, and n is 2 or 3, and a phosphorus compound of the formula PR 1 R 2 R 3 , wherein R 1 , R 2 , and R 3 are, independently, aryl, alkyl, aralkyl, or alkaryl, each containing from 1 to 12 carbon atoms and placing the catalyst in contact with (b) C 2 to C 30 monoolefinic hydrocarbons, said contacting occurring at temperatures of from about -10° C. to about 40° C. to polymerize said olefins, then (c) ceasing polymerization at a polymer content level of 20% by weight or less based on the total reaction mixture.
Claim 3
Dependent Claim 46 words
A method as described in claim 1 wherein the catalyst comprises a crystalline titanium trichloride prepared by a method selected from the group consisting of reducing titanium tetrachloride with (1) aluminum, or (2) hydrogen, or (3) organo-aluminum compound, and (4) milling titanium trichloride with aluminum chloride.
Claim 4
Dependent Claim 105 words
A method as described in claim 1 wherein the catalyst comprises: (a) crystalline titanium trichloride prepared by a method selected from the group consisting of (1) reducing titanium tetrachloride with aluminum, (2) reducing titanium tetrachloride with hydrogen, (3) reducing titanium tetrachloride with an organo metallic compound and (4) milling titanium trichloride with aluminum trichloride (b) 2.5 to 10 weight percent based on the weight of the titanium trichloride component of a ketone and, (c) 0-1.0 weight percent based upon the total weight of the titanium trichloride component of an ionic or polar compound selected from the group consisting of Group IA or IIA metal halides.
Claim 5
Dependent Claim 25 words
A method as described in claim 2 wherein the catalyst has the general formula TiCl 3 .mAlcl 3 wherein m is from 0.00 to 1.0.
Claim 6
Dependent Claim 27 words
A method as described in claim 2 wherein polymerization is ceased at a polymer content level of about 10-12% by weight, based on the total reaction mixture.
Claim 7
Dependent Claim 50 words
A method as described in claim 2 wherein the organo-aluminum compound is selected from the group consisting of trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri(2-methyl pentyl) aluminum, tri-n-octylaluminum, diethylaluminum hydride, diisobutylaluminum hydrides, dimethylaluminum chloride, diethylaluminum chloride, diethylaluminum bromide, diethylaluminum iodide, di-n-propylaluminum chloride, di-n-butylaluminum chloride, diisobutylaluminum chloride, and mixtures of these.
Claim 8
Dependent Claim 22 words
A method as described in claim 4 wherein the mole ratio of aluminum to phosphorus compound is from about 0.01 to 0.99.
Claim 9
Dependent Claim 20 words
A method as described in claim 7 wherein the ratio of aluminum to titanium compound is from 0.1 to 500.
Claim 10
Dependent Claim 26 words
A method as described in claim 5 wherein the mole ratio of the phosphine component to the cocatalyst is from about 0.01 to about 1, respectively.
Claim 11
Dependent Claim 18 words
A method as described in claim 6 wherein the polymerization is carried out in an inactive hydrocarbon solvent.
Claim 12
Dependent Claim 28 words
A method as described in claim 7 wherein the solvent is selected from the group consisting of pentane, hexane, heptane, octane, benzene, toluene, xylene, and mixtures of these.
Claim 13
Dependent Claim 17 words
A method as described in claim 8 wherein the polymerization is carried out under an inert atmosphere.
Claim 14
Dependent Claim 22 words
A method as described in claim 12 wherein the inert atmosphere is selected from the group consisting of nitrogen, xenon, and argon.
Claim 15
Dependent Claim 25 words
A method as described in claim 3 wherein the ketone is selected from the group consisting of camphor, carbomenthone, fenchone, menthone, thujone, verbanone, or verbenone.

References Cited (Backward Citations)

GB918740A Cited
US3502634A Cited
US3692676A Cited
US4340705A Cited
US4124530A Cited
US4358572A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-02-20 1987-08-22 1988-02-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-02-20 1991-08-22 1992-02-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-02-20 1995-08-22 1996-02-21 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag