Claims
- 1. A process for polymerizing ethylene at a high temperature under high pressure, which comprises contacting ethylene alone or along with an .alpha.-olefin at a temperature of 120.degree. C. or more at a pressure of 350 kg/cm.sup.2 or more with a catalyst consisting essentially of (A) a previously mutually contacted product of (A1) a titanium compound having at least one titanium-nitrogen bond with (A2) an organomagnesium compound and (B) an organoaluminum compound represented by the general formula R.sup.3.sub.a AlZ.sup.1.sub.3-a wherein R.sup.3 represents a hydrocarbon group having 1 to 20 carbon atoms: Z.sup.1 represents at least one member selected from the group consisting of hydrogen atom and alkoxy group; and a represents a number satisfying 0<a.ltoreq.3.
- 2. The process according to claim 1, wherein the titanium compound having at least one titanium-nitrogen bond (A1) is a titanium compound represented by the general formula (R.sup.1 R.sup.2 N).sub.4-(m+n) TiX.sub.m Y.sub.n [R.sup.1 and R.sup.2 represent hydrocarbon groups having 1 to 30 carbon atoms and may be the same or different; X represents a halogen atom; Y represents an alkoxy group, m is a number satisfying 0.ltoreq.m.ltoreq.3, n is a number satisfying 0.ltoreq.n.ltoreq.3; and (m+n) is a value satisfying 0.ltoreq.(m+n).ltoreq.3].
- 3. The process according to claim 2, wherein R.sup.1 and R.sup.2 represent aliphatic hydrocarbon groups.
- 4. The process according to claim 3, wherein the aliphatic hydrocarbon groups have 8 to 30 carbon atoms.
- 5. The process according to claim 3, wherein m represents 0 or 2.
- 6. The process according to claim 1, wherein R.sup.3 is a hydrocarbon group having 1 to 10 carbon atoms.
- 7. The process according to claim 1, wherein a is 3.
- 8. The process according to claim 1, wherein the temperature is 120.degree.-350.degree. C. and the pressure is 350-3,500 kg/cm.sup.2.
- 9. The process according to claim 1, wherein the temperature is 150.degree.-280.degree. C.
- 10. The process according to claim 1, wherein the pressure is 600-1,800 kg/cm.sup.2.
- 11. The process according to claim 1, wherein the component (B) is used in a proportion of 0.01-10,000 moles per mole of titanium atom of the component (A).
- 12. The process according to claim 1, wherein the .alpha.-olefin is propylene, butene-1, pentene-1, hexene-1, 4-methylpentene-1, octene-1, decene-1, octadecene-1 or eicosene-1.
Priority Claims (1)
Number |
Date |
Country |
Kind |
4-241750 |
Sep 1992 |
JPX |
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Parent Case Info
This application is a continuation of application Ser. No. 08/112,998, filed Aug. 30, 1993.
US Referenced Citations (5)
Foreign Referenced Citations (2)
Number |
Date |
Country |
0349886 |
Jan 1990 |
EPX |
0571945 |
Dec 1993 |
EPX |
Non-Patent Literature Citations (1)
Entry |
Patent Abstracts of Japan, vol. 7, No. 91 (C-162), 15 Apr. 1983, & JP-A-58 021 407 (Sumitomo Chemical Co., Ltd.), 8 Feb. 1983. |
Continuations (1)
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Number |
Date |
Country |
Parent |
112998 |
Aug 1993 |
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