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US4303771A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of high density ethylene polymers in fluid bed reactor

Assignee: Union Carbide Corp
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Filing: 1979-02-16
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Granted: 1981-12-01
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Expires: 1999-02-16
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Abstract

Abstract A catalytic process for preparing ethylene polymers having a density of >/=0.94 to </=0.97 and a melt flow ratio of about >/=22 to </=32 in a low pressure gas phase process at a productivity of >/=50,000 pounds of polymer per pound of Ti with a catalyst formed from selected organoaluminum compounds and a precursor composition of the formula MgmTi1(OR)nXp(ED)q wherein ED is a selected electron donor compound m is >/=0.5 to </=56 n is 0, 1 or 2 p is >/=2 to </=116 q is >1.5 m+2 R is a C1 to C14 aliphatic or aromatic hydrocarbon radical, or COR' wherein R' is a C1 to C14 aliphatic or aromatic hydrocarbon radical, and X is selected from the group consisting of Cl, Br, I or mixtures thereof, which catalyst is in particulate form and impregnated in a porous inert carrier material.

Inventors

  • 👤 Burkhard E. Wagner
  • 👤 George L. Goeke
  • 👤 Frederick J. Karol

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 11:35
CPC Classifications
C; C08; C08F; C08F10/00; C08F10/02; C08F4/00; C08F4/42; C08F4/44; C08F4/60; C08F4/62; C08F4/64; C08F110/00; C08F110/02; C08F210/00; C08F210/16

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 370 words
A continuous catalytic process for producing ethylene homopolymers or copolymers containing ≧97 mol percent of ethylene and ≦3 mol percent of one or more C 3 to C 8 alpha olefins with a Ti containing catalyst at a productivity of ≧50,000 pounds of polymer per pound of Ti under a pressure of <1000 psi in a gas phase fluid bed reaction said polymer being produced in granular form and having a density of about ≧0.94 to ≦0.97 and a melt flow ratio of about ≧22 or ≦32 which comprises polymerizing ethylene, or copolymerizing ethylene with at least one C 3 to C 8 alpha olefin, at a temperature of about 30° to 115° C. by contacting the monomer charge in the gas phase reaction zone, with particles of a non-comminuted catalyst system, comprising a precursor composition impregnated in an inert porous support and when so impregnated having the formula Mg.sub.m Ti.sub.1 (OR).sub.n X.sub.p [ED].sub.q wherein R is a C 1 to C 14 aliphatic or aromatic hydrocarbon radical, or COR' wherein R' is a C 1 to C 14 aliphatic or aromatic hydrocarbon radical, X is selected from the group consisting of Cl, Br, I, or mixtures thereof, ED is an electron donor compound, m is ≧0.5 to ≦56, n is 0, 1 or 2, p is ≧2 to ≦116 and q is >1.5 m+2 ED is a liquid organic electron donor compound in which said precursor composition and the Ti and Mg component thereof are soluble and which is selected from the group consisting of alkyl esters of aliphatic and aromatic carboxylic acids, aliphatic ethers, cyclic ethers and aliphatic ketones, said impregnated precursor composition being partially activated with >0 to ≦10 mols of activator compound per mol of Ti in said impregnated precursor composition, and completing the activation of the partially activated precursor composition in said reaction zone with >10 to ≦400 mols of activator compound per mol of Ti in said precursor composition, said activator compound having the formula Al(R").sub.c X'.sub.d H.sub.e wherein X' is Cl or OR"', R" and R"' are the same or different, and are C 1 to C 14 saturated hydrocarbon radicals, d is 0 to 1.5, e is 1 or 0 and c+d+e=3.
Claim 2
Dependent Claim 370 words
A continuous catalytic process for producing ethylene homopolymers or copolymers containing ≧97 mol percent of ethylene and ≦3 mol percent of one or more C 3 to C 8 alpha olefins with a Ti containing catalyst at a productivity of ≧50,000 pounds of polymer per pound of Ti under a pressure of <1000 psi in a gas phase fluid bed reaction said polymer being produced in granular form and having a density of about ≧0.94 to ≦0.97 and a melt flow ratio of about ≧22 or ≦32 which comprises polymerizing ethylene, or copolymerizing ethylene with at least one C 3 to C 8 alpha olefin, at a temperature of about 30° to 115° C. by contacting the monomer charge in the gas phase reaction zone, with particles of a non-comminuted catalyst system, comprising a precursor composition impregnated in an inert porous support and when so impregnated having the formula Mg.sub.m Ti.sub.1 (OR).sub.n X.sub.p [ED].sub.q wherein R is a C 1 to C 14 aliphatic or aromatic hydrocarbon radical, or COR' wherein R' is a C 1 to C 14 aliphatic or aromatic hydrocarbon radical, X is selected from the group consisting of Cl, Br, I, or mixtures thereof, ED is an electron donor compound, m is ≧0.5 to ≦56, n is 0, 1 or 2, p is ≧2 to ≦116 and q is >1.5 m+2 ED is a liquid organic electron donor compound in which said precursor composition and the Ti and Mg component thereof are soluble and which is selected from the group consisting of alkyl esters of aliphatic and aromatic carboxylic acids, aliphatic ethers, cyclic ethers and aliphatic ketones, said impregnated precursor composition being partially activated with >0 to ≦10 mols of activator compound per mol of Ti in said impregnated precursor composition, and completing the activation of the partially activated precursor composition in said reaction zone with >10 to ≦400 mols of activator compound per mol of Ti in said precursor composition, said activator compound having the formula Al(R").sub.c X'.sub.d H.sub.e wherein X' is Cl or OR"', R" and R"' are the same or different, and are C 1 to C 14 saturated hydrocarbon radicals, d is 0 to 1.5, e is 1 or 0 and c+d+e=3.
Claim 3
Dependent Claim 12 words
A process as in claim 1 in which ethylene homopolymer is produced.
Claim 4
Dependent Claim 15 words
A process as in claim 2 in which said magnesium component comprises MgCl 2 .
Claim 5
Dependent Claim 17 words
A process as in claim 2 in which said electron donor compound comprises at least one ether.
Claim 6
Dependent Claim 14 words
A process as in claim 4 in which said electron donor compound comprises tetrahydrofuran.
Claim 7
Dependent Claim 15 words
A process as in claim 2 in which said titanium component comprises TiCl 4 .
Claim 8
Dependent Claim 13 words
A process as in claim 2 wherein the inert porous support comprises silica.
Claim 9
Dependent Claim 39 words
A process as in claim 7 wherein the silica is treated with at least one activator compound of the formula AlR.sub.3 wherein the R's are the same or different, and are C 1 to C 14 saturated hydrocarbon radicals.
Claim 10
Dependent Claim 24 words
A process as in claim 1 which is conducted under a mass gas flow rate of about 1.5 to 10 times G mf .

References Cited (Backward Citations)

US2839515A Cited
US3645992A Cited
US3642746A Cited
US4107414A Cited
US4107413A Cited
US3888835A Cited
US3920621A Cited
US4107415A Cited
GB1502567A Cited
US4035560A Cited
US4143223A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-11-30 1985-06-01 1985-12-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-11-30 1989-06-01 1989-12-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-11-30 1993-06-01 1993-12-01 $7700.00 Window Closed / Lapsed

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