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Method of preparing low-density ethylene copolymers

Assignee: Enichem Anic SpA
•
Filing: 1983-05-26
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Granted: 1984-11-06
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Expires: 2003-05-26
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Abstract

Abstract Method for the copolymerization of ethylene with C 4 -C 8 alpha-olefins by means of a suspension method in an organic liquid, at a temperature of from 50° C. to 70° C., at a pressure of less than about 10 bar, on a Ziegler catalyst constituted by: (a) an alkylaluminum or alkylaluminum halide; (b) the product of the reaction of a halogenated derivative of titanium with a support material; the support material being the solid, spheroidal product of the spray drying of a solution of magnesium chloride in ethanol containing at least one additional compound chosen from the following classes: aliphatic, cycloaliphatic or aromatic liquid hydrocarbons with a boiling point higher than that of ethanol at atmospheric pressure; polar, organic hydroxy or ester compounds which are solid or liquid with a boiling point higher than that of ethanol at atmospheric pressure; the solid, spheroidal, spray-dried product also having the following characteristics: particle form: spherical with a size of from 1 to 100 microns. Apparent density of the particles: from 0.1 to 1 g/ml; alcoholic hydroxyl group content: from 1.5 to 20% by weight; surface area: from 10 to 100 m 2 /g; porosity from 1.2 to 3.5 ml/g; pore radius: from 1,000 to 65,000 Angstroms.

Inventors

  • 👤 Renzo Invernizzi
  • 👤 Ferdinando Ligorati

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 09:22
CPC Classifications
C; C08; C08F; C08F210/00; C08F210/16

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 210 words
Method for preparing copolymers of ethylene and alpha-olefins, with densities of from 0.915 to 0.942 g/ml characterized by polymerizing ethylene and an alpha-olefin having from 4 to 8 carbon atoms in an inert (unreactive) organic liquid medium at a temperature of from 50° to 70° C. and at a pressure less than 10 bars, while maintaining a concentration of from 5 to 25% by wt. of the said alpha-olefin in the said medium during the reaction, in the presence of a Ziegler supported catalyst consisting of a compound selected from alkylaluminums and alkylaluminum halides and the product of the reaction of a halogenated derivative of titanium with the solid spheroidal product of the spray drying of a solution of magnesium chloride in ethanol containing at least one additional compound with a boiling point higher than that of ethanol at atmospheric pressure selected from the group consisting of aliphatic, cycloaliphatic or aromatic liquid hydrocarbons or polar organic hydroxy compounds, said solid, spheroidal product of the spray drying having a residual alcoholic hydroxyl group content of from 1.5% to 20% by wt., a surface area of from 10 to 100 m 2 /g and a porosity of from 1.2 to 3.5 ml/g with a pore radius of from 1,000 to 65,000 Angstroms.
Claim 2
Dependent Claim 210 words
Method for preparing copolymers of ethylene and alpha-olefins, with densities of from 0.915 to 0.942 g/ml characterized by polymerizing ethylene and an alpha-olefin having from 4 to 8 carbon atoms in an inert (unreactive) organic liquid medium at a temperature of from 50° to 70° C. and at a pressure less than 10 bars, while maintaining a concentration of from 5 to 25% by wt. of the said alpha-olefin in the said medium during the reaction, in the presence of a Ziegler supported catalyst consisting of a compound selected from alkylaluminums and alkylaluminum halides and the product of the reaction of a halogenated derivative of titanium with the solid spheroidal product of the spray drying of a solution of magnesium chloride in ethanol containing at least one additional compound with a boiling point higher than that of ethanol at atmospheric pressure selected from the group consisting of aliphatic, cycloaliphatic or aromatic liquid hydrocarbons or polar organic hydroxy compounds, said solid, spheroidal product of the spray drying having a residual alcoholic hydroxyl group content of from 1.5% to 20% by wt., a surface area of from 10 to 100 m 2 /g and a porosity of from 1.2 to 3.5 ml/g with a pore radius of from 1,000 to 65,000 Angstroms.
Claim 3
Dependent Claim 18 words
Method as claimed in claim 1, wherein said additional compound is heptane, octane, nonane, decane, benzene or cyclohexane.
Claim 4
Dependent Claim 31 words
Method as claimed in claim 1, wherein said additional compound is propyl alcohol, polyvinyl alcohol, polyethylene glycol, butylhydroxytoluene, hydroxymethyl cellulose, dimethylglyoxime, methylcellulose or phenols including phenols with substituents in the nucleus.
Claim 5
Dependent Claim 24 words
Method as claimed in claim 1, wherein the weight ratio of said ethanol to said additional compound is in the range 0.5/1 to 50/1.
Claim 6
Dependent Claim 22 words
Method as claimed in claim 1, wherein said halogenated derivative of titanium is selected from the halides, oxyhalides and alkoxyhalides of titanium.
Claim 7
Dependent Claim 16 words
Method as claimed in claim 5, wherein said halogenated derivative of titanium is TiCl 4 .
Claim 8
Dependent Claim 19 words
Method as claimed in claim 1, wherein said halogenated derivative of titanium is selected from the halogeno-alcoholates of titanium.

References Cited (Backward Citations)

US3953414A Cited
US4293673A Cited
US4298713A Cited
US4347162A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-11-06 1988-05-07 1988-11-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-11-06 1992-05-07 1992-11-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-11-06 1996-05-07 1996-11-06 $7700.00 Window Closed / Lapsed

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