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US4093789A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing polyolefins

Assignee: Eneos Corp
•
Filing: 1976-07-15
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Granted: 1978-06-06
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Expires: 1996-07-15
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Abstract

Abstract According to the present invention, there is provided a process for preparing polyolefins by polymerizing or copolymerizing olefins in the presence of a catalyst consisting of a solid component and an organometallic compound component, characterized in that said solid component is obtained by copulverizing (1) a magnesium halide and/or a manganese halide, (2) an aromatic hydrocarbon, (3) a tetravalent titanium compound, and (4) a trivalent titanium compound And in that said organometallic compound component is a mixture of (5) a trialkylaluminum and (6) a compound represented by the general formula AlR n X 3-n wherein R is alkyl having 1 to 10 carbon atoms and may be the same or different, X is halogen and O<n<3.

Inventors

  • 👤 Nobuyuki Kuroda
  • 👤 Toru Nakamura
  • 👤 Takeichi Shiraishi
  • 👤 Kazuo Matsuura
  • 👤 Mituji Miyoshi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 23:33
CPC Classifications
C; C08; C08F; C08F10/00; C08F4/00; C08F4/02; C08F4/022; Y; Y10; Y10S; Y10S526/00; Y10S526/903; Y10S526/906

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 337 words
A process for preparing polyolefins by polymerizing or copolymerizing alpha- olefins at a temperature in the range of from 20° to 120° C and at a pressure in the range of atmospheric pressure to 70 Kg/cm. 2 G., in the presence of a catalyst comprising a solid component and an organometallic compound component, characterized in that said solid component is obtained by copulverizing (1) a magnesium dihalide and/or a manganese dihalide, (2) an aromatic hydrocarbon selected from the group consisting of monocylic aromatic hydrocarbon and the halogen-and/or alkyl-substituted derivatives thereof and polycyclic aromatic hydrocarbon, the ratios of magnesium dihalide and/or manganese dihalide to said aromatic hydrocarbon being in the range of from 1:0.5 to 1:0.1, (3) a tetravalent titanium compound represented by the general formula Ti(OR) n X 4-n wherein R is an alkyl, allyl, aryl or aralkyl group having 1 to 20 carbon atoms, X is a halogen atom and n is a whole number of from 0 to 4, and (4) a trivalent titanium compound selected from the group consisting of titanium trihalides obtained by reducing titanium tetrachloride with hydrogen, aluminum, titanium or an oganometallic compound, and trivalent titanium compounds obtained by reducing tetravalent titanium alkoxyhalides represented by the general formula Ti(OR) n X 4-n wherein R is alkyl, allyl, aryl or aralkyl having 1 to 20 carbon atoms, X is a halogen atom and n is a whole number of from 1 to 4, with an organometallic compound of a metal of the groups I to III of the periodic table present in a molar ration with tetravalent titanium compound (3) of from 50:1 to 1:50 and in that said organometallic compound component is a mixture of (5) a trialkylaluminum and (6) a compound represented by the general formula AlR.sub. n X 3-n wherein R is alkyl having 1 to 10 carbon atoms and may be same or different, X is halogen and 0 < n < 3, said compound being present in a molar ratio with trialkylaluminum (5) of from 2:1 to 1000:1.
Claim 2
Dependent Claim 337 words
A process for preparing polyolefins by polymerizing or copolymerizing alpha- olefins at a temperature in the range of from 20° to 120° C and at a pressure in the range of atmospheric pressure to 70 Kg/cm. 2 G., in the presence of a catalyst comprising a solid component and an organometallic compound component, characterized in that said solid component is obtained by copulverizing (1) a magnesium dihalide and/or a manganese dihalide, (2) an aromatic hydrocarbon selected from the group consisting of monocylic aromatic hydrocarbon and the halogen-and/or alkyl-substituted derivatives thereof and polycyclic aromatic hydrocarbon, the ratios of magnesium dihalide and/or manganese dihalide to said aromatic hydrocarbon being in the range of from 1:0.5 to 1:0.1, (3) a tetravalent titanium compound represented by the general formula Ti(OR) n X 4-n wherein R is an alkyl, allyl, aryl or aralkyl group having 1 to 20 carbon atoms, X is a halogen atom and n is a whole number of from 0 to 4, and (4) a trivalent titanium compound selected from the group consisting of titanium trihalides obtained by reducing titanium tetrachloride with hydrogen, aluminum, titanium or an oganometallic compound, and trivalent titanium compounds obtained by reducing tetravalent titanium alkoxyhalides represented by the general formula Ti(OR) n X 4-n wherein R is alkyl, allyl, aryl or aralkyl having 1 to 20 carbon atoms, X is a halogen atom and n is a whole number of from 1 to 4, with an organometallic compound of a metal of the groups I to III of the periodic table present in a molar ration with tetravalent titanium compound (3) of from 50:1 to 1:50 and in that said organometallic compound component is a mixture of (5) a trialkylaluminum and (6) a compound represented by the general formula AlR.sub. n X 3-n wherein R is alkyl having 1 to 10 carbon atoms and may be same or different, X is halogen and 0 < n < 3, said compound being present in a molar ratio with trialkylaluminum (5) of from 2:1 to 1000:1.
Claim 3
Dependent Claim 23 words
A process according to claim 1 wherein the magnesium dihalide and the manganese dihalide are substantially anhydrous magnesium chloride and manganese chloride, respectively.
Claim 4
Dependent Claim 33 words
A process according to claim 1 wherein the copulverization is made for 0.5 to 50 hours in an inert gas atmosphere at a temperature in the range of from 0° to 200° C.
Claim 5
Dependent Claim 18 words
A process according to claim 1 wherein the solid component contains 0.5 to 20 weight percent of titanium.
Claim 6
Dependent Claim 46 words
A process according to claim 1 wherein the mixing ratio of a trialkylaluminum and a compound represented by the general formula AlR.sub. n X 3-n is such that the molar ratio of the former to the latter is in the range of from 1:200 to 1:3.
Claim 7
Dependent Claim 32 words
A process according to claim 1 wherein the oganometallic compound component is used in an amount corresponding to 0.1 to 1000 moles per mole of a trivalent and a tetravalent titanium compounds.
Claim 8
Dependent Claim 22 words
A process according to claim 1 wherein the polymerization or copolymerization of olefins is conducted with hydrogen added into the polymerization system.
Claim 9
Dependent Claim 21 words
The process of claim 1 wherein the monocyclic aromatic hydrocarbon is benzene, toluene, xylene and/or the halogen- and/or alkyl-substituted derivatives thereof.
Claim 10
Dependent Claim 43 words
The process of claim 1 wherein the polycyclic aromatic hydrocarbon is naphthalene, phenanthrene, triphenylene, chrysene, 3,4-benzophenanthrene, 1,2-benzochrysene, picene, anthracene, tetraphene, 1,2,3,4-dibenzanthracene, pentaphene, 3,4-benzopentaphene, tethracene, 1,2-benzotethracene, hexaphene, heptaphene, diphenyl, fluorene, biphenylene, perylene, coronene, bisantene, ovalene, pyrene, perinaphthene, and/or halogen- and/or alkyl- substituted derivatives thereof.

References Cited (Backward Citations)

US3769373A Cited
US3357967A Cited
US3491073A Cited
GB1314258A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-06-05 1981-12-05 1982-06-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-06-05 1985-12-05 1986-06-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-06-05 1989-12-05 1990-06-06 $7700.00 Window Closed / Lapsed

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