Liquid catalyst component, catalyst system containing the same, and process for producing ethylene-alpha-olefin copolymers using the catalyst system

Abstract: A liquid catalyst component (A) for use in the production of ethylene-α-olefin copolymers obtained by reacting: (a) a titanium compound represented by general formula (R¹R²N) 4-(m+n) TiX m Y n , with (b) at least one compound selected from the compounds represented by general formula R³- -CH₂- -R⁴ wherein R¹, R², R³, R⁴, X, Y, m and n are defined as in claim 1, or by reacting: (a) with (c) at least one compound selected from the group consisting of hydroxyaldehydes and ketoalcohols having both carbonyl group and hydroxyl group in their molecule represented by general formulas (I) to (VI) according to claim 1. This liquid catalyst component can be used as a component of a catalyst system in combination with an organoaluminum compound (B) for producing ethylene-α-olefin copolymers.

Description: This invention relates to a liquid catalyst component, a catalyst system containing the same and a process for producing ethylene-α-olefin copolymers, using the catalyst system. More particularly, this invention relates to a liquid catalyst component, a catalyst system containing the same and a process using the catalyst system for producing ethylene-α-olefin copolymers having a narrow composition distribution and excellent in weather resistance, colorizability, corrosion resistance, dynamic properties and solution polymerization performances. As a process for producing ethylene-α-olefin copolymers, the method using the so-called Ziegler-Natta catalyst comprising a compound of a transition metal belonging to Group IV-VI of the periodic table and a compound of an organometal belonging to Group I-III of the periodic table is widely known generally. On the other hand, from the viewpoint of practical properties, ethylene-α-olefin copolymers are desired to have a narrow composition distribution. Thus, they are industrially produced by the use of a catalyst system comprising a vanadium compound such as VCl₃, VOCl₃ or VO(OR)₃ and an alkylaluminum halide. Although such a catalyst system gives an ethylene-α-olefin copolymer having a narrow composition distribution, the catalyst system has a low polymerization activity at high temperatures, and hence it is low in productivity. Further, it has problems of coloration, deterioration in weathering and corrosion caused by the residual vanadium and chlorine, and the formed copolymer must be made free from ash sufficiently in order to prevent these problems. Further, if ethylene is copolymerized with an α-olefin having a large carbon number with this type of catalyst system, the resulting ethylene-α-olefin copolymer is so low in molecular weight as unsatisfactory from the viewpoint of practical properties. In view of the above-mentioned situation, processes using a catalyst system comprising a titanium compound or a zirconium compound and an aluminum compound have hitherto been disclosed with the aim of solving these problems, and particularly in the recent time a process using a catalyst system comprising a titanium compound or a zirconium compound and an aluminoxane has been proposed. However, the ethylene-α-olefin copolymer obtained with such a catalyst system is so low in molecular weight as unsatisfactory in practical properties. On the other hand, as a process for polymerizing or copolymerizing an olefin by the use of a catalyst system comprising a compound having titanium-nitrogen bond and an organolauminum compound, the process of polymerizing ethylene by the use of a catalyst system comprising an organoaluminum compound and a solid component prepared by supporting a titanium amide compound or an alkali metal salt of titanium amide compound on magnesium halide (DE-A-2030753), the process of copolymerising ethylene and an α-olefin by the use of a catalyst system comprising a titanium amide compound having π aryl ligand and an aluminoxane [JP-A-87-121708], a process of polymerizing ethylene or copolymerizing ethylene and α-olefin by the use of a catalyst system comprising a titanium diphenylamide compound and an organoaluminum compound (EP-A-0104374), a process of copolymerizing α-olefin or ethylene and α-olefin by the use of a catalyst system comprising a titanium amide compound having aryl substituent and an organoaluminum compound (JP-B-67-22691), a process of homopolymerizing ethylene or α-olefin or copolymerizing ethylene and α-olefin by the use of a catalyst system comprising a titanium amide compound having a lower alkyl group such as diethylaminotitanium trichloride and an organoaluminum compound [JP-B-66-5379; J. Polym. Sci. Part A-1, 241, 6 (1968)] and a process of polymerizing ethylene by the use of a catalyst system comprising tetrakis(diphenylamido)titanium and an organoaluminum compound (JP-B-67-11646), have been disclosed. However, if ethylene and α-olefin are copolymerized by the use of the catalyst systems disclosed above, the following disadvantages arise. Thus, the Process of DE-A-2030753 is disadvantageous in that the resulting ethylene-α-olefin copolymer has a broad composition distribution. The process of JP-A-87-121708 is disadvantageous in that the resulting copolymer has a low molecular weight. According to the processes disclosed in EP-A-0104374, JP-B-66-5379, JP-B-67-22691 and J. Polym. Sci. Part A-1, 241, 6 (1968), composition distribution of the resulting copolymer is yet unsatisfactory in the narrowness. The process disclosed in JP-B-67-11646 is yet unsatisfactory in the narrowness of resulting copolymer and catalyst activity. Further, if ethylene and α-olefin are copolymerized with this catalyst system, a polymer insoluble in solvent is formed at the time of polymerization which is entangled with stirring wheel of reactor. This is a fatal disadvantage from the viewpoint of continuous operation of the process. On the other hand, as a process for producing α-olefin polymers by the use of an electron donor such as a diketone compound or a diester compound, the process of producing α-olefin polymer by the use of a catalyst system comprising an organoaluminum and a solid catalyst composed of a titanium halide, an electron donor such as a diketone or diester compound and a magnesium halide is known, for example from JP-A-82-151603. However, if ethylene/α-olefin copolymerization is carried out with this catalyst system, the resulting copolymer is so broad in composition distribution that its practical properties are unsatisfactory. In FR-A-2103071 there is disclosed a catalyst system for the polymerization of ethylene with α-olefins and/or di-olefins. The catalyst system consists of a metal compound from the groups I, II, III of the Periodic Table of the Elements and the product of the reaction of a titanium compound and a support formed of a mixture of a magnesium halide and a metal compound from the groups I and II of the Periodic Table of the Elements. In EP-A-271874 there is disclosed a process for producing crystalline vinyl aromatic polymers. Vinyl aromatic polymers are copolymerized with ethylenically unsaturated monomers in the presence of the reaction product between a titanium compound which contains at least one Ti-N bond and an organo-aluminum compound. In US-A-4528339 there is described a process for the copolymerization of an α-olefin and an ethylenically unsaturated monomer in the presence of a supported Ziegler-Natta catalyst. The transition metal component of the catalyst is the reaction product of a titanium compound with a compound containing at least one aliphatic hydroxyl group or an α-hydroxyketone. In view of the above-mentioned situation, an object of this invention is to provide a novel liquid catalyst component, a catalyst system containing the liquid catalyst component and a process using the catalyst system for producing ethylene-α-olefin copolymers which is improved in ethylene/α-olefin copolymerization performance and can give a copolymer having a narrow composition distribution, a high molecular weight, an excellent weather resistance, an excellent colorizability, a high corrosion resistance and a high solution polymerization performance. According to the present invention, there is provided a liquid catalyst component (A) for use in the production of ethylene-α-olefin copolymers obtained by reacting: (a) a titanium compound represented by the following general formula: (R¹R²N) 4-(m+n) TiX m Y n wherein R¹ and R², same or different from each other, represent a hydrocarbon group having 1 to 30 carbon atoms; X represents halogen; Y represents an alkoxy group; m represents a number satisfying 1 ≦ m ≦ 3; and n represents a number satisfying 0 ≦ n < 3, provided that (m+n) satisfies 1 ≦ (m+n) ≦ 3; with (b) at least one compound selected from the compounds represented by the following general formula: wherein R³ and R⁴, same or different from each other, each represents a hydrocarbon group having 1 to 30 carbon atoms and/or an alkoxy group having 1 to 30 carbon atoms; or by reacting: (a) with (c) at least one compound selected from the hydroxyaldehydes and ketoalcohols having both carbonyl group and hydroxyl group in their molecule which are represented by the following general formulas (I) to (VI): wherein R⁵ to R¹⁸ each represents a hydrocarbon group having 1 to 30 carbon atoms and/or a hydrogen atom; E, F and G each represents a straight or branched hydrocarbon chain having 1 to 30 carbon atoms, provided that said hydrocarbon chain may optionally have an unsaturated bond; g, h, i and j each represents a number of 1 to 4; and k and ℓ each represents a number of 0 to 2, and, after the reaction of (a) with (b) or (c), removing the resulting solid substance from the reaction mixture, said liquid catalyst component being free from the components (b) or (c). Further, according to this invention, there are also provided a catalyst system for use in the production of ethylene-α-olefin copolymers which can be obtained by reacting said liquid catalyst component with an organo-aluminum compound, as well as a process for producing said copolymers by the use of said catalyst system. Figure 1 is a flow chart diagram for facilitating understanding of this invention. This flow chart diagram is a mere typical example of the embodiment of this invention, and this invention is by no means limited by it. Hereunder, this invention will be illustrated in more detail. The titanium compound (a) used in this invention for the synthesis of catalyst component (A) is represented by general formula (R¹R²N) 4-(m+n) TiX m Y n , wherein R¹ and R², same or different from each other, each represents a hydrocarbon group having 1 to 30 carbon atoms; X represents halogen; Y represents an alkoxy group; m represents a number satisfying 1 ≦ m ≦ 3; and n represents a number satisfying 0 ≦ n < 3, preferably 0.5 ≦ n ≦ 2, provided that (m+n) satisfies 1 ≦ (m+n) ≦ 3. Concrete examples of the preferable titanium compound include dimethylamidotitanium trichloride, bis(dimethylamido)titanium dichloride, tris(dimethylamido)titanium chloride, diethylamidotitanium trichloride, bis(diethylamido)titanium dichloride, tris(diethylamido)titanium chloride, di-isopropylamidotitanium trichloride, bis(di-isopropylamido)titanium dichloride, tris(di-isopropylamido)titanium chloride, di-isobutylamidotitanium trichloride, bis(di-isobutylamido)titanium dichloride, tris(di-isobutylamido)titanium chloride, di-tert-butylamidotitanium trichloride, bis(di-tert-butylamido)titanium dichloride, tris(di-tert-butylamido)titanium chloride, dibutylamidotitanium trichloride, bis(dibutylamido)titanium dichloride, tris(dibutylamido)titanium chloride, dihexylamidotitanium trichloride, bis(dihexylamido)titanium dichloride, tris(dihexylamido)titanium chloride, dioctylamidotitanium trichloride, bis(dioctylamido)titanium dichloride, tris(dioctylamido)titanium chloride, didecylamidotitanium trichloride, bis(didecylamido)titanium dichloride, tris(didecylamido)titanium chloride, dioctadecylamidotitanium trichloride, bis(dioctadecylamido)titanium dichloride, tris(dioctadecylamido)titanium chloride, diallylamidotitanium trichloride, bis(diallylamido)titanium dichloride, tris(diallylamido)titanium chloride, di-propenylamidotitanium trichloride, bis(dipropenylamido)titanium dichloride, tris(di-propenylamido)titanium chloride, ethoxy(dimethylamido)titanium dichloride, ethoxy(dioctylamido)titanium dichloride, butoxy(dioctylamido)titanium dichloride, hexyloxy(dioctylamido)titanium dichloride, 2-ethylhexyloxy(dioctylamido)titanium dichloride, didecyloxy(dioctylamido)titanium dichloride, ethoxy(didecylamido)titanium dichloride, hexyloxy(didecylamido)titanium dichloride, 2-ethylhexyloxy(didecylamido)titanium dichloride, decyloxy(dioctylamido)titanium dichloride, ethoxy(dioctadecylamido)titanium dichloride, 2-ethylhexyloxy(dioctadecylamido)titanium dichloride, decyloxy(dioctylamido)titanium dichloride, hexyloxybis(dioctylamido)titanium chloride, 2-ethylhexyloxybis(dioctylamido)titanium chloride, decyloxybis(dioctylamido)titanium chloride, hexyloxybis(didecylamido)titanium chloride, 2-ethylhexyloxybis(didecylamido)titanium chloride and decyloxybis(didecylamido)titanium chloride. Among these titanium compounds, composition distribution becomes more narrow when R¹ and R² each represents straight chain hydrocarbon groups. Accordingly, the following compounds are more preferable among the above-mentioned ones: dimethylamidotitanium trichloride, bis(dimethylamido)titanium dichloride, tris(dimethylamido)titanium chloride, dibutylamidotitanium trichloride, bis(dibutylamido)titanium dichloride, tris(dibutylamido)titanium chloride, dioctylamidotitanium trichloride, bis(dioctylamido)titanium dichloride, tris(dioctylamido)titanium chloride, didecylamidotitanium trichloride, bis(didecylamido)titanium dichloride, tris(didecylamido)titanium chloride, dioctadecylamidotitanium trichloride, bis(dioctadecylamido)titanium dichloride, tris(dioctadecylamido)titanium chloride, ethoxy(dioctylamido)titanium dichloride, ethoxy(didecylamido)titanium dichloride and ethoxy(dioctadecylamido)titanium dichloride. Further, among these titanium compounds, those wherein R¹ and R² are straight chain aliphatic saturated hydrocarbon groups and particularly those having 8 or more carbon atoms are liquid substances and the composition distribution of the resulting copolymer is more narrow. Accordingly, as particularly preferable titanium compound, the followings can be referred to: dioctylamidotitanium trichloride, bis(dioctylamido)titanium dichloride, tris(dioctylamido)titanium chloride, didecylamidotitanium trichloride, bis(didecylamido)titanium dichloride, tris(didecylamido)titanium chloride, dioctadecylamidotitanium trichloride, bis(dioctadecylamido)titanium dichloride, tris(dioctadecylamido)titanium chloride, 2-ethylhexyloxy(didecylamido)titanium dichloride, decyloxy(dioctylamido)titanium dichloride and ethoxy(dioctadecylamido)titanium dichloride. This invention is by no means limited by the compounds mentioned above. As the method for synthesizing a secondary amide group-containing transition metal compound, the methods mentioned in JP-B-67-11646; H. Buerger et al.: J. Organometal. Chem. 108 (1976) 69-84; H. Buerger et al.: J. Organomet. Chem. 20 (1969) 129-139; etc. can be used. In this invention, the synthesis was carried out by first reacting (i) a secondary amine compound represented by general formula wherein R¹⁹R²⁰NH wherein R¹⁹ and R²⁰ each represents a saturated hydrocarbon group having 8 to 30 carbon atoms (from the viewpoint of obtaining a liquid titanium compound, R¹⁹ and R²⁰ preferably each represents an aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms and more preferably a straight chain aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms) and (ii) an alkyl-(alkali metal) represented by general formula wherein R²¹M wherein R²¹ represents a hydrocarbon group having 1 to 30 carbon atoms and M represents an alkali metal such as Li and K, to form an amide compound of alkali metal, and thereafter reacting said amide compound of alkali metal with (iii) titanium tetrahalide represented by TiX₄ wherein X represents a halogen such as chlorine, bromine, iodine and the like and preferably chlorine. In the next place, the compound (b) used in this invention for the synthesis of catalyst component (A) is represented by the following general formula: wherein R³ and R⁴, same or different from each other, each represents a hydrocarbon group having 1 to 30 carbon atoms and/or an alkoxyl group having 1 to 30 carbon atoms. Next, the compound (c) used in this invention for the synthesis of catalyst component (A) is at least one compound selected from the group consisting of the hydroxyaldehydes and ketoalcohols having both carbonyl group and hydroxyl group in their molecule represented by the following general formulas (I) to (VI): wherein R⁵ to R¹⁸ each represents a hydrocarbon group having 1 to 30 carbon atoms and/or a hydrogen atom; E, F and G each represents a straight or branched hydrocarbon chain having 1 to 30 carbon atoms, provided that said hydrocarbon chain may optionally have an unsaturated bond; g, h, i and j each represents a number of 1 to 4; and k and ℓ each represents a number of 0 to 2. As concrete examples of said compound (b), the followings can be referred to: β-diketone compounds such as CH₃(CO)CH₂(CO)CH₃, CH₃(CO)CH₂(CO)C₂H₅, CH₃(CO)CH₂(CO)C₃H₇, CH₃(CO)CH₂(CO)(iso-C₃H₇), CH₃(CO)CH₂(CO)C₄H₉, CH₃(CO)CH₂(CO)C₆H₁₃, CH₃(CO)CH₂(CO)C₁₀H₂₁, CH₃(CO)CH₂(CO)(cyclo-C₆H₁₂), C₂H₅(CO)CH₂(CO)C₂H₅, C₂H₅(CO)CH₂(CO)C₃H₇, C₂H₅(CO)CH₂(CO)C₄H₉, C₂H₅(CO)CH₂(CO)C₆H₁₃, C₂H₅(CO)CH₂(CO)C₁₀H₂₁, C₂H₅(CO)CH₂(CO)C₁₂H₂₅, C₂H₅(CO)CH₂(CO)(cyclo-C₆H₁₂), C₆H₁₃(CO)CH₂(CO)CH₃, C₆H₁₃(CO)CH₂(CO)C₃H₇, C₆H₁₃(CO)CH₂(CO)(iso-C₃H₇), C₆H₁₃(CO)CH₂(CO)(tert-C₄H₉), C₆H₁₃(CO)CH₂(CO)C₆H₁₃, C₆H₁₃(CO)CH₂(CO)(cyclo-C₆H₁₂), cyclo-C₆H₁₂(CO)CH₂(CO)(cyclo-C₆H₁₂), CH₃(CO)CH₂(CO)CH=CH₂, CH₃(CO)CH₂(CO)CH₂-CH=CH₂, CH₃(CO)CH₂(CO)-(CH₂)₂CH=CH₂, CH₃(CO)CH₂(CO)(CH₂)₄CH=CH₂, CH₃(CO)CH₂(CO)-C(CH₃)=CH₂, CH₃(CO)CH₂(CO)CH₂-C(CH₃)=CH₂, CH₃(CO)CH₂(CO)-CH=CH-CH₃, C₂H₅(CO)CH₂(CO)CH=CH₂, C₂H₅(CO)CH₂(CO)(CH₂)₂CH=CH₂, C₂H₅(CO)CH₂(CO)-C(CH₃)=CH₂, C₂H₅(CO)CH₂(CO)CH₂-CH=CH₂, C₄H₉(CO)CH₂(CO)CH=CH₂, C₄H₉(CO)CH₂(CO)C(CH₃)=CH₂, C₆H₁₃(CO)CH₂(CO)CH=CH₂, C₆H₁₃(CO)CH₂(CO)CH₂-CH=CH₂, cyclo-C₆H₁₂(CO)CH₂(CO)CH=CH₂, C₁₀H₂₁(CO)CH₂(CO)CH=CH₂, C₁₀H₂₁(CO)CH₂(CO)C(CH₃)=CH₂, CH₃(CO)CH₂(CO)C₆H₅, C₂H₅(CO)CH₂(CO)C₆H₅, C₃H₇(CO)CH₂(CO)C₆H₅, (iso-C₃H₇)(CO)CH₂(CO)C₆H₅, C₄H₉(CO)CH₂(CO)C₆H₅, (tert-C₄H₉)(CO)CH₂(CO)C₆H₅, C₆H₁₃(CO)CH₂(CO)C₆H₅, C₁₀H₂₁(CO)CH₂(CO)C₆H₅, (Cyclo-C₆H₁₂)(CO)CH₂(CO)C₆H₅, CH₃(CO)CH₂(CO)C₁₂H₁₀, C₃H₇(CO)CH₂(CO)C₁₂H₁₀, C₄H₉(CO)CH₂(CO)C₁₂H₁₀, C₁₀H₂₁(CO)CH₂(CO)C₁₂H₁₀, C₁₂H₂₅(CO)CH₂(CO)C₁₂H₁₀, CH₂=CH(CO)CH₂(CO)CH=CH₂, CH₂=CH(CO)CH₂(CO)CH₂-CH=CH₂, CH₂=CH(CO)CH₂(CO)CH₂-CH=CH₂, CH₂=CH(CO)CH₂(CO)(CH₂)₂CH=CH₂, CH₂=CH(CO)CH₂(CO)C(CH₃)CH=CH₂, CH₂=CH(CH₃)C(CO)CH₂(CO)C(CH₃)CH=CH₂, CH₂=CH(CO)CH₂(CO)C₆H₅, CH₂=CH(CH₃)C-(CO)CH₂(CO)C₆H₅, C₄H₉-CH=CH-CH₂(CO)CH₂(CO)C₆H₅, CH₂=CH(CO)CH₂(CO)C₁₂H₁₀, CH₂=CH(CH₃)C-(CO)CH₂(CO)C₁₂H₁₀ and C₄H₉-CH=CH-CH₂-(CO)CH₂(CO)C₁₂H₁₀ ; β=keto acid compounds such as CH₃(CO)CH₂(CO)OCH₃, CH₃(CO)CH₂(CO)OC₃H₇, CH₃(CO)CH₂(CO)O(iso-C₃H₇), CH₃(CO)CH₂(CO)OC₄H₉, CH₃(CO)CH₂(CO)O(t-C₄H₉), CH₃(CO)CH₂(CO)OC₆H₁₃, CH₃(CO)CH₂(CO)O(cyclo-C₆H₁₂), CH₃(CO)CH₂(CO)OC₁₀H₂₁, C₂H₅(CO)CH₂(CO)OC₂H₅, C₂H₅(CO)CH₂(CO)OC₄H₉, C₂H₅(CO)CH₂(CO)O(t-C₄H₉), C₂H₅(CO)CH₂(CO)OC₁₀H₂₁, C₂H₅(CO)CH₂(CO)C₁₂H₂₅, C₂H₅(CO)CH₂(CO)(cyclo-C₆H₁₂), C₄H₉(CO)CH₂(CO)OC₃H₇, C₄H₉(CO)CH₂(CO)OC₄H₉, C₄H₉(CO)CH₂(CO)OC₁₀H₂₁, C₆H₁₃(CO)CH₂(CO)OCH₃, C₆H₁₃(CO)CH₂(CO)OC₃H₇, C₆H₁₃(CO)CH₂(CO)O(iso-C₃H₇), C₆H₁₃(CO)CH₂(CO)OC₆H₁₃, C₆H₁₃(CO)CH₂(CO)O(cyclo-C₆H₁₂), C₆H₁₃(CO)CH₂(CO)OC₁₀H₂₁, (Cyclo-C₆H₁₂) (CO)CH₂(CO)(cyclo-C₆H₁₂), CH₃(CO)CH₂(CO)-O-CH₂-CH=CH₂, CH₃(CO)CH₂(CO)O-(CH₂)₂CH=CH₂, CH₃(CO)CH₂(CO)O(CH₂)₄CH=CH₂, CH₃(CO)CH₂(CO)O-CH₂C(CH₃)=CH₂, CH₃(CO)CH₂(CO)-O-CH=CH-CH₃, C₂H₅(CO)CH₂(CO)OCH₂-CH=CH₂, C₂H₅(CO)CH₂(CO)OC(CH₃)=CH₂, C₂H₅(CO)CH₂(CO)OCH₂-CH=CH₂, C₄H₉(CO)CH₂(CO)OCH₂-CH=CH₂, C₄H₉(CO)CH₂(CO)OC(CH₃)=CH₂, C₆H₁₃(CO)CH₂(CO)-OCH₂-CH=CH₂, (cyclo-C₆H₁₂)(CO)CH₂(CO)OCH₂-CH=CH₂, C₁₀H₂₁(CO)CH₂(CO)OCH₂-CH=CH₂, C₁₀H₂₁(CO)CH₂(CO)OC(CH₃)=CH₂, CH₃(CO)CH₂(CO)OC₆H₅, C₂H₅(CO)CH₂(CO)OC₆H₅, (iso-C₃H₇)(CO)CH₂(CO)OC₆H₅, (tert-C₄H₉)(CO)CH₂(CO)OC₆H₅, (Cyclo-C₆H₁₂)(CO)CH₂(CO)OC₆H₅, C₆H₁₃(CO)CH₂(CO)OC₆H₅, C₁₀H₂₁(CO)CH₂(CO)OC₆H₅, CH₃(CO)CH₂(CO)OC₁₂H₁₀, C₃H₇(CO)CH₂(CO)OC₁₂H₁₀, C₄H₉(CO)CH₂(CO)OC₁₂H₁₀, C₁₀H₂₁(CO)CH₂(CO)OC₁₂H₁₀ and C₁₂H₂₅(CO)CH₂(CO)C₁₂H₁₀; and malonic diester compounds such as CH₃O(CO)CH₂(CO)OCH₃, CH₃O(CO)CH₂(CO)OC₂H₅, CH₃O(CO)CH₂(CO)O(i-C₃H₇), CH₃O(CO)CH₂(CO)O(t-C₄H₉), CH₃O(CO)CH₂(CO)OC₆H₁₃, CH₃O(CO)CH₂(CO)O(cyclo-C₆H₁₂), CH₃O(CO)CH₂(CO)OC₁₀H₂₁, C₂H₅O(CO)CH₂(CO)OC₃H₇, C₂H₅O(CO)CH₂(CO)O(t-C₄H₉), C₂H₅O(CO)CH₂(CO)OC₆H₅, C₂H₅O(CO)CH₂(CO)O(cyclo-C₆H₁₂), C₂H₅O(CO)CH₂(CO)OC₁₀H₂₁, C₆H₁₃O(CO)CH₂(CO)OC₃H₇, C₆H₁₃((CO)CH₂(CO)OC₄H₉, C₆H₁₃O(CO)CH₂(CO)OC₆H₁₃, C₆H₁₃O(CO)CH₂(CO)O(cyclo-C₆H₁₂), C₆H₁₃O(CO)CH₂(CO)OC₁₀H₂₁, C₁₀H₂₁O(CO)CH₂(CO)OC₁₀H₂₁, CH₃O(CO)CH₂(CO)OCH₂-CH=CH₂, CH₃O(CO)CH₂(CO)O(CH₂)₂-CH=CH₂, CH₃O(CO)CH₂(CO)OC(CH₃)=CH₂, CH₃O(CO)CH₂(CO)O-CH=CH-CH₃, C₄H₉O(CO)CH₂(CO)OCH₂-CH=CH₂, C₄H₉O(CO)CH₂(CO)O(CH₂)₂-CH=CH₂, C₄H₉O(CO)CH₂(CO)OC(CH₃)=CH₂, C₄H₉O(CO)CH₂(CO)OCH=CH-CH₃, C₆H₁₃O(CO)CH₂(CO)OCH₂-CH=CH₂, C₆H₁₃O(CO)CH₂(CO)O(CH₂)₂-CH=CH₂, C₆H₁₃O(CO)CH₂(CO)OC(CH₃)=CH₂, C₆H₁₃O(CO)CH₂(CO)OCH=CH-CH₃, (Cyclo-C₆H₁₂)O(CO)CH₂(CO)O(CH₂)₂CH=CH₂, C₁₀H₂₁O(CO)CH₂(CO)OCH₂-CH=CH₂, C₁₀H₂₁O(CO)CH₂(CO)OC(CH₃)=CH₂, CH₃O(CO)CH₂(CO)OC₆H₅, C₃H₇O(CO)CH₂(CO)OC₆H₅, (iso-C₃H₇)O(CO)CH₂(CO)OC₆H₅, (tert-C₄H₉)O(CO)CH₂(CO)OC₆H₅, C₆H₁₃O(CO)CH₂(CO)OC₆H₅, (cyclo-C₆H₁₂)O(CO)CH₂(CO)OC₆H₅, C₁₀H₂₁O(CO)CH₂(CO)OC₆H₅, CH₃O(CO)CH₂(CO)OC₁₂H₁₀, C₃H₇O(CO)CH₂(CO)OC₁₂H₁₀, C₄H₉O(CO)CH₂(CO)OC₁₂H₁₀, (Cyclo-C₆H₁₂)O(CO)CH₂(CO)OC₁₂H₁₀, C₁₂H₂₅O(CO)CH₂(CO)OC₁₂H₁₀, CH₂=CH-CH₂O(CO)CH₂(CO)OCH₂CH=CH₂, CH₂=CH-CH₂O(CO)CH₂(CO)OC(CH₃)=CH₂, CH₂=CH-CH₂O(CO)CH₂(CO)O(CH₂)₂CH=CH₂, CH₂=CH-CH₂O(CO)CH₂(CO)OC₆H₅, C₄H₉-CH=CH-CH₂-O(CO)CH₂(CO)OCH₂CH=CH-C₄H₉, C₆H₅O(CO)CH₂(CO)OC₆H₅, C₆H₅O(CO)CH₂(CO)OC₁₂H₁₀ and C₆H₅O(CO)CH₂(CO)OCH₂-CH=CH₂. These compounds may be used as a mixture of two or more members. Among these compounds, β-diketone compounds and β-keto acids are preferable, and β-diketone compounds are particularly preferable. This invention is by no means limited by the compounds mentioned above. Next, as concrete examples of said compound (c), the followings can be referred to. First, concrete examples of the compound of general formula (I), the following aliphatic α-hydroxyaldehydes and aliphatic ketoalcohols can be referred to. As concrete examples of the compound of general formula (II), the following aliphatic hydroxyaldehydes and aliphatic ketoalcohols can be referred to. As concrete examples of the compound of general formula (III), the following aliphatic α-hydroxyketones and the like can be referred to. As concrete examples of the compound of general formula (IV), the following aliphatic hydroxyketones and the like can be referred to. As concrete examples of the compound of general formula (V), the following aromatic hydroxyaldehydes or aromatic hydroxyketones can be referred to. As concrete examples of the compound of general formula (VI), the following aromatic hydroxyaldehydes or aromatic hydroxyketones can be referred to. Among the above-mentioned compounds, hydroxyketone compounds represented by the following general formulas: wherein R⁵ to R¹⁸ each represents a hydrocarbon group having 1 to 30 carbon atoms are preferable, and aliphatic hydroxyketone compounds represented by general formulas: wherein R⁵ to R¹⁰ each represents aliphatic hydrocarbon group having 1 to 30 carbon atoms and/or hydrogen, and alicyclic hydroxyketone compounds represented by general formulas: wherein R¹¹ and R¹² each represents aliphatic hydrocarbon group having 1 to 30 carbon atoms and/or hydrogen, and E and F each represents straight or branched aliphatic hydrocarbon chain having 1 to 30 carbon atoms, are particularly preferable. As the organoaluminum compound used as catalyst component (B) of this invention, known organoaluminum compounds can be used. As preferable examples of the organoaluminum compound, organoaluminum compounds represented by general formula R²² a AlM 3-a and acyclic or cyclic aluminoxanes having a structure represented by general formula can be referred to. In these formulas, R²² and R²³, same or different from each other, each represents hydrocarbon group having 1 to 8 carbon atoms; M represents hydrogen atom and/or alkoxy group; a represents a number satisfying 0 < a ≦ 3; and b represents an integer of 2 or greater. Concrete examples of the organoaluminum compound represented by R²² a AlM 3-a include trialkylaluminums such as trimethylaluminum, triethylaluminum, tripropylaluminum, triisobutylaluminum and trihexylaluminum ; dialkylaluminum hydrides such as dimethylaluminum hydride, diethylaluminum hydride, dipropylaluminum hydride, diisobutylaluminum hydride and dihexylaluminum hydride; and alkylaluminum alkoxides such as dimethylaluminum methoxide, methylaluminum dimethoxide, diethylaluminum methoxide, ethylaluminum dimethoxide, diisobutylaluminum methoxide, isobutylaluminum dimethoxide, dihexylaluminum methoxide, hexylaluminum dimethoxide, dimethylaluminum ethoxide, methylaluminum diethoxide diethylaluminum ethoxide, ethylaluminum diethoxide, diisobutylaluminum ethoxide and isobutylaluminum diethoxide. Concrete examples of the aluminoxane represented by include tetramethyldialuminoxane, tetraethyldialuminoxane, tetrabutyldialuminoxane, tetrahexyldialuminoxane, methylaluminoxane, ethylaluminoxane, butylaluminoxane and hexylaluminoxane. Per one mole of titanium atom contained in catalyst component (A), catalyst component (B) can be used in an amount so widely ranging as 1 to 100,000 moles. Preferably, however, it is used in an amount of 1 to 10,000 moles, and more preferably in an amount of 1 to 5,000 moles. Next, the synthesis of catalyst component (A) of this invention will be mentioned. The catalyst component (A) of this invention is synthesized by reacting titanium compound (a) with compound (b) or compound (c), and removing solid substance from the reaction mixture. The method for reacting titanium compound (a) with compound (b) or compound (c) may be any of addition of compound (b) or compound (c) to titanium compound (a) and addition of titanium compound (a) to compound (b) or compound (c). Preferably, compound (a) and compound (b) or compound (c) are put to use after dissolving or diluting them with an appropriate solvent. As said solvent, aliphatic hydrocarbons such as hexane, heptane, octane, decane and the like, aromatic hydrocarbons such as toluene or xylene, alicyclic hydrocarbons such as cyclohexane, methylcyclohexane and decalin, and ether compounds such as diethyl ether, diisoamyl ether and tetrahydrofuran can be referred to. The reaction temperature is -50°C to 150°C, preferably -30°C to 120°C, and particularly 0°C to 100°C. Though the reaction time is not critical, preferable reaction time is usually about 30 minutes to about 6 hours. Compound (b) or compound (c) is used in an amount of 0.01 to 1.0, preferably 0.05 to 0.8, and particularly 0.1 to 0.6, as expressed in terms of atomic ratio of compound (b) or compound (c) to titanium atom in titanium compound (a). The catalyst components of this invention and the catalyst system of this invention are used for production of ethylene-α-olefin copolymer. Said copolymer means a copolymer constituted of ethylene and at least one α-olefin. Concrete examples of the α-olefin include propylene, butene-1, pentene-1, hexene-1, 4-methyl-pentene-1, octene-1, decene-1, octadecene-1 and eicosene-1. It is also possible in this invention to copolymerize a non-conjugated diene additionally for the purpose of improving the vulcanizability of copolymer. Concrete examples of said diene include dicyclopentadiene, tricyclopentadiene, 5-methyl-2,5-norbornadiene, 5-methylene-2-norbornene, 5-ethylidene-2-norbornene, 5-isopropenyl-2-norbornene, 5-(2'-butenyl)-2-norbornene, 1,5,9-cyclododecatriene, 6-methyl-4,7,8,9-tetrahydroindene, trans-1,2-divinylcyclobutane, 1,4-hexadiene, 4-methyl-1,4-hexadiene, 1,5-hexadiene, 1,6-octadiene and 6-methyl-1,5-heptadiene, This invention is by no means limited by the compounds mentioned above. The copolymer of this invention can have a density so widely ranging as 0.85 to 0.95 (g/cm³). From the viewpoint of flexibility at low temperature, its density is preferably 0.85 to 0.94, more preferably 0.85 to 0.92, and particularly 0.85 to 0.90. The copolymer of this invention is a rubbery random copolymer showing no absorption at 730 cm⁻¹ due to crystalline ethylene chain at all in the infrared absorption spectrum and having a narrow composition distribution. The copolymer of this invention may comprise two or more kinds of α-olefin and two or more kinds of non-conjugated diene. Next, one example of the production of the ethylene-α-olefin copolymer using the catalyst system of this invention will be mentioned. First, on the method for feeding catalyst components into polymerization reactor, there is no restriction except that the catalyst components must be fed in a moisture-free state in an inert gas such as nitrogen or argon. The catalyst components (A) and (B) may be fed either separately or after a previous mutual contact. The polymerization can be carried out over a temperature range of -30°C to 300°C. Preferably, however, temperature of the polymerisation is -10°C to 200°C, and particularly 20°C to 150°C. Though the pressure of polymerization is not critical, a pressure of about 3 atmospheres to 1,500 atmospheres is preferable from the viewpoint of industrial practicability and economical reason. The polymerization can be carried out by any of continuous process and batch process. A slurry polymerization using an inert hydrocarbon solvent such as propane, butane, pentane, hexane, heptane and octane, a liquid phase polymerization using no solvent, and a gas phase polymerization are also possible. Further, a chain transfer agent such as hydrogen and the like may be added for the purpose of regulating molecular weight of the copolymer of this invention. Next, this invention will be illustrated in more detail by way of the following examples and comparative examples. In the examples, content of α-olefin, iodine number and intrinsic viscosity were measured by the following methods. Thus, content of α-olefin was determined from the characteristic absorptions of ethylene and α-olefin by the use of infrared spectrophotometer JASCO A-302 manufactured by Nihon Bunko Kogyo K.K. Iodine number was determined from the characteristic absorption of diene by the use of the same infrared spectrophotometer as mentioned above. Intrinsic viscosity [η] was measured at 135°C in tetralin with Ubbelohde viscometer. Titanium content in the catalyst component was measured by atomic absorption analysis. Example 1 (i) Synthesis of Catalyst Component (A) After replacing inner atmosphere of a 300 ml flask equipped with a stirrer, a dropping funnel, a reflux condenser and a thermometer with argon gas, 23.8 ml of a hexane solution containing 5 mmoles of a titanium compound represented by (C₈H₁₇)₂N-TiCl₃ was charged. Then, 0.39 g (2.5 mmoles) of benzoylacetone dissolved in 10 ml of hexane was dropped from the dropping funnel into the flask over a period of 30 minutes while maintaining the temperature of the solution in flask at 75°C. After completing the dropping, the resulting mixture was further reacted at 75°C for 6 hours. From the mixture obtained by the above-mentioned reaction, the resulting solid substance was removed. Thus, 33.8 ml of a hexane solution containing catalyst component (A) was obtained. The quantity of titanium atom contained in the hexane solution was 0.075 mmole/ml, as determined by atomic absorption analysis. (ii) Copolymerization of Ethylene with Propylene After replacing inner atmosphere of a 300 ml flask equipped with a stirrer, a reflux condenser, a gas blowing tube and a thermometer with argon gas, 200 ml of heptane and 5.0 ml (5 mmoles) of triisobutylaluminum were charged. Then, a mixture of ethylene and propylene gas (composition of gas phase: C₂′/C₃′ = 2/8; composition of gas phase is expressed in terms of ratio by volume, hereinafter the same) was introduced into the solution through the gas blowing tube until a saturation was reached, after which 3.6 ml of the hexane solution containing catalyst component (A) obtained in (i) (Ti atom: 0.25 mmole) was added to start polymerization. Thereafter, feeding of the gas mixture was continued while maintaining the temperature at 30°C to carry out the polymerization. After one hour, 20 ml of ethanol was added to stop the polymerization. The copolymer thus formed was three times washed with each 1,000 ml portion of a mixture comprising 950 ml of ethanol and 50 ml of 1 N hydrochloric acid, and then it was dried in vacuum to obtain 5.95 g of an ethylene-propylene copolymer (hereinafter referred to as "EP copolymer"). Catalyst activity per one hour per one mole of Ti atom (hereinafter, simply referred to as "activity") was 2.4 x 10⁴ g/mole-Ti. In the infrared absorption spectrum of the EP copolymer thus obtained, no absorption peak of 730 cm⁻¹ assignable to crystalline ethylene chain (hereinafter referred to as "IR₇₃₀") was observable, demonstrating that the EP copolymer had a narrow composition distribution. Propylene content in the copolymer was 33.3% by weight, and its intrinsic viscosity (hereinafter referred to as [η]) was 3.0. Example 2: Copolymerization of Ethylene with Butene-1 A copolymerization of ethylene with butene-1 was carried out under the same conditions as in Example 1 (ii), except that a mixture of ethylene and propylene gas was replaced with a mixture of ethylene and butene-1 gas (C₂′/C₄′ = 2/8) and the hexane solution containing catalyst component (A) was used in an amount of 1.8 ml (Ti atom: 0.125 mmole). As the result, 5.3 g of an ethylene-butene-1 copolymer (hereinafter referred to as EB copolymer) was obtained. Activity was 4.2 x 10⁴ g/mole-Ti. In the EB copolymer thus obtained, no IR₇₃₀ was noticeable, demonstrating narrowness of composition distribution. Butene-1 content was 40.7%, and [η] was 3.7. Example 3: Copolymerization of Ethylene with Hexene-1 After replacing inner atmosphere of a 300 ml flask equipped with a stirrer, a reflux condenser, a gas blowing tube and a thermometer with argon gas, 200 ml of hexene-1 and 5.0 ml (5 mmoles) of triisobutylaluminum were charged into the flask. Then, ethylene gas was introduced into the solution through the blowing tube at a rate of 375 ml/min. until saturation was reached, after which 0.036 ml of the hexane solution containing catalyst component (A) obtained in Example 1 (i) (Ti atom: 0.0025 mmole) was added thereto to start a polymerization. Thereafter, polymerization was continued for one hour, while continuing feeding of the gas at a constant temperature of 30°C, after which 20 ml of ethanol was added to stop the polymerization. The resulting polymer was three times washed with each 1,000 ml portion of a mixture comprising 950 ml of ethanol and 50 ml of 1 N hydrochloric acid and then dried in vacuum to obtain 1.9 g of an ethylene-hexene-1 copolymer (hereinafter referred to as EH copolymer). Activity was 7.7 x 10⁵ g/mole-Ti. The EH copolymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. Its hexene-1 content was 49.3%, and its [η] was 6.9. Example 4: Copolymerization of Ethylene with Decene-1 A copolymerization of ethylene with decene-1 was carried out under the same conditions as in Example 3, except that the hexene-1 was replaced with 200 ml of decene-1. As the result, 0.7 g of an ethylene-decene-1 copolymer (hereinafter referred to as ED copolymer) was obtained. Activity was 2.6 x 10⁵ g/mole-Ti. The ED copolymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. Its decene-1 content was 57.3%, and its [η] was 6.3. Example 5 Ethylene and propylene were copolymerized under the same conditions as in Example 1, except that, in the synthesis of catalyst component (A) of Example 1 (i), the benzoylacetone was replaced with 2.5 mmoles of ethyl 3-oxobutanate. As the result, 1.3 g of EP copolymer was obtained. Activity was 1.5 x 10⁴ g/mole-Ti. The EP copolymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. Its propylene content was 31.2%, and its [η] was 3.1. Example 6 Ethylene and propylene were copolymerized under the same conditions as in Example 1, except that, in the synthesis of catalyst component (A) of Example 1 (i), the benzoylacetone was replaced with 2.5 mmoles of dibenzoylmethane. As the result, 3.8 g of EP copolymer was obtained. Activity was 1.5 x 10⁴ g/mole-Ti. The EP copolymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. its propylene content was 29.3%, and its [η] was 3.2. Example 7 A copolymerization of ethylene with propylene was carried out in the same manner as in Example 1, except that, in the ethylene-propylene copolymerization of Example 1 (ii), the triisobutylaluminum was replaced with 5 mmoles of di-isobutylaluminum methoxide and the hexane solution containing catalyst component (A) was used in an amount of 0.72 ml (Ti atom: 0.05 mmole). As the result, 5.7 g of EP copolymer was obtained. Activity was 1.1 x 10⁵ g/mole-Ti. The EP copolymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. Its propylene content was 32.1%, and its [η] was 3.4. Example 8 A copolymerization of ethylene with propylene was carried out in the same manner as in Example 1, except that, in the ethylene-propylene copolymerization of Example 1 (ii), the triisobutylaluminum was replaced with 6.7 mmoles of methylaluminoxane and the hexane solution containing catalyst component (A) was used in an amount of 0.014 ml (Ti atom: 0.001 mmole). As the result, 0.14 g of EP copolymer was obtained. Activity was 1.0 x 10⁵ g/mole Ti. The EP copolymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. Its propylene content was 33.1%, and its [η] was 3.2. Example 9 A copolymerization of ethylene with propylene was carried out in the same manner as in Example 1 (ii), except that catalyst component (A) was synthesized in the same manner as in Example 1 (i) by using a titanium compound represented by (C₁₀H₂₁)₂NTiCl₃ in place of the titanium compound (C₈H₁₇)₂NTiCl₃ and 3.6 ml of a hexane solution containing the resulting catalyst component (A) (Ti atom: 0.25 mmole) was used in the same manner as in Example 1 (ii). As the result, 3.0 g of EP copolymer was obtained. Activity was 1.1 x 10⁴ g/mole-Ti. The EP copolymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. Its propylene content was 30.6%, and its [η] was 3.0. Example 10: Copolymerization of Ethylene with Propylene and Dicyclopentadiene After replacing inner atmosphere of a 300 ml flask equipped with a stirrer, a reflux condenser, a gas blowing tube and a thermometer with argon gas, 200 ml of heptane, 1.24 ml (10 mmoles) of dicyclopentadiene and 5.0 ml (5 mmoles) of triisobutylaluminum were charged. Then, a mixture of ethylene and propylene gas (C₂′/C₃′ = 2/8) was introduced into the solution through the gas blowing tube until saturation was reached. The, 3.6 ml of a hexane solution containing catalyst component (A) (Ti atom: 0.25 mmole) was added to start a polymerization reaction. Then, polymerization was carried out for one hour while continuing the feeding of the gas mixture at a constant temperature of 30°C, after which 20 ml of ethanol was added to stop the polymerization. The resulting polymer was washed thrice with each 1,000 ml portion of a mixture comprising 950 ml of ethanol and 50 ml of 1 N hydrochloric acid and then dried in vacuum to obtain 3.0 g of an ethylene-propylene- dicyclopentadiene copolymer (EPDM). Activity was 4.2 x 10⁴ g/mole-Ti. Its propylene content was 27.0%, [η] was 3.1, and iodine number was 12.0 (g/100 g). Comparative Example 1: Copolymerization by the Use of Titanium Tetrachloride Ethylene and propylene were copolymerized in the same manner as in Example 1 (ii), except that, as catalyst component (A), 0.5 mmole of titanium tetrachloride was used in place of the (C₈H₁₇)₂NTiCl₃. As the result, 2.3 g of EP copolymer was obtained. Activity was 4,500 g/mole Ti. The EP copolymer thus obtained showed IR₇₃₀, demonstrating broadness of its composition distribution. Its propylene content was 37.5%, and its [η] was 2.7. Comparative Example 2 Ethylene and propylene were copolymerized in the same manner as in Example 1 (ii), except that 0.5 mmole of titanocene dichloride (Cp₂TiCl₂) was used as catalyst component (A) in place of (C₈H₁₇)₂NTiCl₃ and 25 mmoles of aluminoxane was used in place of the triisobutylaluminum. As the result, 0.6 g of EP copolymer was obtained. Activity was 12,000 g/mole-Ti. Although the copolymer thus obtained showed no IR₇₃₀, its propylene content was 39.9%, and its [η] was 0.29, demonstrating that this copolymer had a very low molecular weight. Example 11 (i) Synthesis of Catalyst Component (A) After replacing inner atmosphere of a 300 ml flask equipped with a stirrer, a dropping funnel, a reflux condenser and a thermometer with argon gas, 45.6 ml of a hexane solution containing 10 mmoles of a titanium compound represented by composition formula (C₈H₁₇)₂N-TiCl₃ was charged into the flask. Then, 10 ml of a hexane solution containing 0.42 ml (4 mmoles) of 3-methyl-3-hydroxybutanone was dropped from the dropping funnel into the solution over a period of 30 minutes while maintaining temperature of the solution in the flask at 75°C. After dropping it, the resulting mixture was further reacted for 6 hours at 75°C. Then, solid substance was removed from the reaction mixture. Thus, 72 ml of a hexane solution containing catalyst component (A) was obtained. The separation of solid substance from the solution was carried out by using a cylindrical filter. Concentration of titanium atom in the hexane solution was revealed as 0.046 mmole/ml by atomic absorption analysis. (ii) Copolymerization of Ethylene with Propylene After replacing inner atmosphere of a 300 ml flask equipped with a stirrer, a reflux condenser, a gas blowing tube and a thermometer with argon gas, 200 ml of heptane and 2.0 ml (2 mmoles) of triisobutylaluminum were charged. Then, a mixture of ethylene and propylene gas (C₂′/C₃′ = 2/8) was introduced into the solution through the gas blowing tube until saturation was reached, after which 4.35 ml of the hexane solution containing catalyst component (A) obtained in (i) (Ti atom: 0.2 mmole) was added to start a polymerization reaction. Thereafter, polymerization was carried out for 10 minutes while feeding the gas mixture at a constant temperature of 30°C, and then 20 ml of ethanol was added to stop the polymerization. The resulting polymer was washed three times with each 1,000 ml portion of a mixture comprising 950 ml of ethanol and 50 ml of 1 N hydrochloric acid and then dried in vacuum to obtain 3.45 g of an EP copolymer. Activity was 1.0 x 10⁵ g/mole-Ti. The EP copolymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. Its propylene content was 33.3% by weight, and its [η] was 3.0. During the polymerization, a polymer insoluble in the solvent used in polymerization was deposited. Its weight fraction (hereinafter referred to as HIP (%)) was 0.1%. However, no adhesion to stirring wheel was observed. Example 12 Ethylene and propylene were copolymerized under the same conditions as in Example 11, except that the 3-methyl-3-hydroxybutanone was replaced with 6.51 ml (0.2 mmole) of 3-methyl-4-hydroxybutanone in Example 11 (i). As the result, 2.59 g of EP copolymer was obtained. Activity was 4.6 x 10⁴ g/mole-Ti. The polymer thus obtained showed no IR₇₃₀, demonstrating narrowness of its composition distribution. Its propylene content was 40.7%, and its [η] was 3.7. During the copolymerization, deposition of HIP was observed in a quantity of 1.5%. However, no adhesion to stirring wheel was observed. Comparative Example 3: Copolymerization by the Use of Titanium Tetrachloride Ethylene and propylene were copolymerized in the same manner as in Example 11, except that 0.5 mmole of titanium tetrachloride was used as catalyst component (A) in place of the (C₈H₁₇)₂NTiCl₃ in Example 11 (ii). As the result, 2.3 g of EP copolymer was obtained. Activity was 4,500 g/mole-Ti. The copolymer thus obtained showed IR₇₃₀, demonstrating broadness of its composition distribution. Its propylene content was 37.5%, and its [η] was 2.7. Comparative Example 4 Ethylene and propylene were copolymerized in the same manner as in Example 11, except that 0.5 mmole of titanocene dichloride (Cp₂TiCl₂) was used as catalyst component (A) in place of (C₈H₁₇)₂NTiCl₃ and 25 mmoles of aluminoxane was used in place of the triisobutylaluminum in Example 11 (ii). As the result, 0.6 g of EP copolymer was obtained. Activity was 12,000 g/mole-Ti. Although the EP copolymer thus obtained showed no IR₇₃₀, its propylene content was 39.9%, and its [η] was 0.29, demonstrating that it was a copolymer having a very low molecular weight.

Claims: A liquid catalyst component (A) for use in the production of ethylene-α-olefin copolymers obtained by reacting: (a) a titanium compound represented by the following general formula: (R¹R²N) 4-(m+n) TiX m Y n wherein R¹ and R², same or different from each other, each represents a hydrocarbon group having 1 to 30 carbon atoms; X represents a halogen; Y represents an alkoxy group; m represents a number satisfying 1 ≦ m ≦ 3; and n represents a number satisfying 0 ≦ n < 3, provided that (m+n) satisfies 1 ≦ (m+n) ≦ 3; with (b) at least one compound selected from the compounds represented by the following general formula: wherein R³ and R⁴, same or different, each represents a hydrocarbon group having 1 to 30 carbon atoms and/or an alkoxy group having 1 to 30 carbon atoms; or by reacting: (a) with (c) at least one compound selected from the group consisting of hydroxyaldehydes and ketoalcohols having both carbonyl group and hydroxyl group in their molecule which are represented by the following general formulas (I) to (VI): wherein R⁵ to R¹⁸ each represents a hydrocarbon group having 1 to 30 carbon atoms and/or hydrogen; E, F and G each represents a straight or branched hydrocarbon chain having 1 to 30 carbon atoms, provided that said hydrocarbon chain may optionally have an unsaturated bond; g, h, i and j each represents a number of 1 to 4; and k and ℓ each represents a number of 0 to 2, and, after the reaction of (a) with (b) or (c), removing the resulting solid substance from the reaction mixture, said liquid catalyst component being free from the components (b) or (c). A liquid catalyst component according to Claim 1, wherein R¹ and R² in the formula of the titanium compound each represents a saturated hydrocarbon group having 1 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein R¹ and R² in the formula of the titanium compound each represents an aliphatic saturated hydrocarbon group having 1 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein R¹ and R² in the formula of the titanium compound each represents a straight chain aliphatic saturated hydrocarbon group having 1 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein R¹ and R² in the formula of the titanium compound each represents a hydrocarbon group having 8 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein R¹ and R² in the formula of the titanium compound each represents a saturated hydrocarbon group having 8 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein R¹ and R² in the formula of the titanium compound each represents an aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein R¹ and R² in the formula of the titanium compound each represents a straight chain aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein the compound (b) is a β-diketone compound, β-keto acid compound or malonic diester compound. A liquid catalyst component according to Claim 9, wherein the compound (b) is a β-diketone compound. A liquid catalyst component according to Claim 1, wherein the compound (c) is a hydroxyketone compound represented by the general formulas (I)-(IV) in which R⁵ to R¹⁸ each represents a hydrocarbon group having 1 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein the compound (c) is an aliphatic hydroxyketone compound represented by the general formula (I) or (II) in which R⁵ to R¹⁰ each represents an aliphatic hydrocarbon group having 1 to 30 carbon atoms and/or hydrogen. A liquid catalyst component according to Claim 1, wherein the compound (c) is an alicyclic hydroxyketone compound represented by the general formula (III) or (IV) wherein R⁹ and R¹⁰ each represents an aliphatic hydrocarbon group having 1 to 30 carbon atoms and/or hydrogen, and E and F each represents a straight or branched aliphatic hydrocarbon chain having 1 to 30 carbon atoms. A liquid catalyst component according to Claim 1, wherein the reaction of the titanium compound (a) with the compound (b) or compound (c) is carried out at -50 to 150°C for 30 min. to 6 hours. A liquid catalyst component according to Claim 1, wherein an amount of the compound (b) or compound (c) is 0.01 to 1.0 mole per one mole of titanium atom contained in the titanium compound (a). A catalyst system for use in the production of ethylene-α-olefin copolymers comprising: (A) a liquid catalyst component according to any one of claims 1 to 15; and (B) an organoaluminum compound. A catalyst system according to Claim 16, wherein the organoaluminum compound (B) is an organoaluminum compound represented by the general formula R²² a AlM 3-a or acyclic or cyclic aluminoxane having a structure represented by general formula [Al(R²³)-O] b , in which R²² and R²³, same or different from each other, each represents a hydrocarbon group having 1 to 8 carbon atoms; M represents a hydrogen atom and/or an alkoxy group; a represents a number satisfying 0 < a ≦ 3; and b represents an integer of 2 or greater. A catalyst system according ot Claim 16, wherein the amount of the component (B) is 1 to 100,000 moles per one mole of titanium atom contained in component (A). A process for producing ethylene-α-olefin copolymers which comprises copolymerizing ethylene with at least one α-olefin in the presence of a catalyst system according to any one of claims 16 to 18 at a temperature of -30°C to 300°C under a pressure of about 3 atmospheres to 1,500 atmospheres. A process according to Claim 19, wherein the α-olefin is propylene, butene-1, pentene-1, hexene-1, 4-methylpentene-1, octene-1, decene-1, octadecene-1 or eicocene-1. A process according to Claim 19, wherein a non-conjugated diene is copolymerized. A process according to Claim 19, wherein the density of the ethylene-α-olefin copolymer is 0.85-0.95 g/cm³.

Inventors: JOHOJI HIROFUMI, KAWAI KIYOSHI, SASAKI TOSHIO, SHIRAISHI HIROYUKI, JOHOJI, HIROFUMI, KAWAI, KIYOSHI, SASAKI, TOSHIO, SHIRAISHI, HIROYUKI
Applicants: SUMITOMO CHEMICAL CO, SUMITOMO CHEMICAL COMPANY, LIMITED
Application year: 1990
Main classification: C08F4
IPC codes: C08F4, C08F210