Liquid catalyst component, catalyst system containing said component and process for producing ethylene-alpha-olefin copolymer using said catalyst system

Abstract: A liquid catalyst component for copolymeriza­ tion of ethylene with α-olefin comprising a titanium compound represented by the following general formula: (R¹R²N) 4-(m+n) TiX m Y n wherein R¹ and R² each represents a saturated hydro­ carbon group having 8 to 30 carbon atoms; X represents halogen; Y represents an alkoxy group; m represents a number satisfying 1≦m≦3; n represents a number satisfy­ ing 0≦n≦2; and (m+n) satisfies 1≦(m+n)≦3. Said liquid catalyst component is used in combination with an organoaluminum compound as a catalyst system for copolymerization of ethylene with α-­ olefin.

Description: This invention relates a liquid catalyst component, a catalyst system containing said catalyst component for copolymerization of ethylene with α-olefins and a process for producing ethylene-α-olefin copolymers using said catalyst system, and more particularly to a process for producing ethylene-α-olefin copolymers excellent in structural randomness, weather resistance, color protection, corrosion resistance, low temperature property and dynamic property by the use of said novel catalyst system. As a general process for producing ethylene-α-olefin copolymers, the process using a catalyst consisting of a compound of a transition metal belonging to Group IV to VI of the periodic table and an organometallic compound of a metal belonging to Group I to III of the periodic table, i.e. the so-called Ziegler-Natta catalyst, is widely known. On the other hand, ethylene-α-olefin copolymers are requested to have a narrow composition distribution from the viewpoint of practical properties. Thus, in the industry, they are produced by the use of a catalyst system consisting of a vanadium compound such as VCl₃, VOCl₃ and VO(OR)₃ and an alkylaluminum halide such as Et₃Al₂Cl₃. However, although the ethylene-α-olefin copolymers produced with the above-mentioned catalyst system are narrow in composition distribution, the process is low in productivity because the catalyst has a low polymerization activity at high temperatures. Further, this process has problems that the residual vanadium and chlorine cause coloration of the resulting polymer, deteriorate its weather resistance and promote its corrosion. Accordingly, ashes must be thoroughly eliminated from the polymer in order to prevent these problems. Further, the process using the above mentioned catalyst system is disadvantageous in that, if ethylene and higher α-olefin are copolymerized with the catalyst system, the resulting copolymer is very low in molecular weight and cannot have a satisfactory mechanical strength, and in addition catalyst activity is very low. In view of the above-mentioned circumstances, a process using a catalyst system consisting of a titanium compound or a zirconium compound and an aluminum compound has been disclosed, and recently a process using a catalyst system consisting of a titanium compound or a zirconium compound and aluminoxane has been proposed. However, the ethylene-α-olefin copolymers produced with these catalyst systems have a low molecular weight, and they cannot be said to be satisfactory from the viewpoint of practical properties. On the other hand, as a process for polymerizing or copolymerizing olefins by the use of a catalyst system consisting of a compound having titanium-nitrogen bond and an organoaluminum compound, there have been disclosed a process for polymerizing ethylene with a catalyst system consisting of 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-2,030,753), a process for copolymerizing ethylene and α-olefin with a catalyst system consisting of aluminoxane and a titanium amide compound having π-allyl ligand (JP-A-62-121708), a process for polymerizing ethylene or copolymerizing ethylene and α-olefin with a catalyst system consisting of a titanium diphenylamide compound and an organoaluminum compound (EP-A-0 104 374), a process for polymerizing α-olefin or copolymerizing ethylene and α-olefin with a catalyst system consisting of a titanium amide compound having an aryl substituent and an organoaluminum compound (JP-B-42-22691), a process for homopolymerizing ethylene or α-olefin or copolymerizing ethylene and α-olefin with a catalyst system consisting of an organoaluminum compound and a lower alkyl group-containing titanium amide compound such as diethylamido-titanium trichloride [JP-B-41-5379; J. Polymer Sci., Part A-1, 241, 6 (1968)], and a process for polymerizing ethylene with a catalyst system consisting of tetrakisdiphenylamido-titanium and an organoaluminum compound (JP-B-42-11646). However, when applied to the copolymerization of ethylene and α-olefin, all the catalyst systems disclosed in the above-mentioned references are disadvantageous in the following points. Thus, the process of DE-A-2,030,753 is disadvantageous in that the resulting ethylene-α-olefin copolymer has a broad composition distribution; the process of JP-A-62-121708 is disadvantageous in that the resulting copolymer has a low molecular weight; and the processes of EP-A-0 104 374, JP-B-41-5379, JP-B-42-22691 and J. Polymer Sci., Part A-1, 241, 6 (1968) are disadvantageous in that composition distribution of the resulting copolymer is yet unsatisfactory in narrowness. Further, the process of JP-B-42-11646 is disadvantageous in that the resulting copolymer is yet unsatisfactory in narrowness of composition distribution and the catalyst is insufficient in activity. EP-A-0 271 874 discloses a process for producing crystalline vinyl aromatic polymers having a predominantly syndiotactic structure using a catalyst system comprising the product of the reaction between a titanium compound containing at least one Ti-N bond, and an organoaluminium compound containing at least one oxygen atom, bound to one aluminium atom or located between two aluminium atoms. In the above-mentioned situation, the object of this invention is to provide a process for producing an ethylene-α-olefin copolymer having a narrow composition distribution and a high molecular weight and improved in weather resistance, color protection, corrosion resistance and low temperature property by the use of a novel catalyst system. According to this invention, there is provided a liquid catalyst component comprising: a liquid catalyst component comprising a titanium compound represented by the following general formula: (R¹R²N) 4-(m+n) TiX m Y n wherein R¹ and R² each represents a saturated hydrocarbon group having 8 to 30 carbon atoms, X represents a halogen, Y represents an alkoxy group, m represents a number satisfying 1≦m≦3, n represents a number satisfying 0≦n≦2, and (m+n) satisfies 1≦(m+n)≦3; a catalyst system for copolymerization of ethylene with α-olefin comprising: (A) the above-mentioned liquid catalyst component and (B) an organoaluminum compound; as well as a process for producing an ethylene-α-olefin copolymer (hereinafter simply referred to as "copolymer") which comprises copolymerizing ethylene with an α-olefin by using said catalyst system. Owing to the use of the catalyst system of this invention, it becomes possible to produce an ethylene-α-olefin copolymer excellent in structural randomness, and an ethylene-α-olefin copolymer excellent in weather resistance, corrosion resistance, transparency, unstickiness and dynamic properties can be provided. Figure 1 is an infrared absorption spectral chart of a copolymer obtained in Example 1 of this invention; Figures 2 to 4 are infrared absorption spectral charts of copolymers obtained according to prior technique in Comparative Examples 1, 3 and 5; and Figure 5 is a flow chart diagram for facilitating to understand this invention which expresses a non-limitative typical example of the embodiment of this invention. (a) Liquid catalyst component (A) used in this invention is a secondary amide group-containing titanium compound represented by the following general formula: (R¹R²N) 4-(m+n) TiX m Y n wherein R¹ and R², which may be identical or different from each other, each represents a saturated hydrocarbon group having 8 to 30 carbon atoms, X represents a halogen, Y represents an alkoxy group, m represents a number satisfying 1≦m≦3, n represents a number satisfying 0≦n≦2, and (m+n) satisfies 1≦(m+n)≦3. If R¹ and R² each represents an unsaturated hydrocarbon group, the composition distribution of the resulting copolymer is broad. In this invention, therefore, saturated hydrocarbon groups are used as R¹ and R². Among the saturated hydrocarbon groups, aliphatic hydrocarbon groups having 8 to 30 carbon atoms are preferable, and straight chain aliphatic saturated hydrocarbon groups having 8 to 30 carbon atoms are particularly preferable because, as the carbon chain becomes closer to a straight chain, the titanium compound becomes liquid state and composition distribution of the resulting copolymer becomes narrower. As examples of the halogen represented by X in the general formula, chlorine, bromine and iodine can be referred to, among which chlorine is most preferable from the viewpoint of catalyst activity. As examples of the alkoxy group, methoxy, ethoxy, propoxy, butoxy and 2-ethylhexyloxy can be referred to. There is no limitation from the viewpoint of catalyst performance. If (m+n) in the general formula is greater than 3, free TiCl₄ exists in the titanium compound which broadens composition distribution of the resulting copolymer. If (m+n) is smaller than 1, catalyst activity is low. Accordingly, titanium compounds of which (m+n) satisfies 1≦(m+n)≦3 are used in this invention. Concrete examples of preferable titanium compounds include titanium trichloride dioctylamido, titanium dichloride bis(dioctylamido), titanium chloride tris(dioctylamido), titanium trichloride didecylamido, titanium dichloride bis(didecylamido), titanium chloride tris(didecylamido), titanium trichloride dioctadecylamido, titanium dichloride bis(dioctadecylamido), titanium chloride tris(dioctadecylamido), titanium dichloride dioctylamido ethoxide, titanium butoxide dichloride dioctylamido, titanium dichloride dioctylamido hexyloxide, titanium dichloride dioctylamido 2-ethylhexyloxide, titanium dichloride dioctylamido decyloxide, titanium dichloride didecylamido ethoxide, titanium dichloride didecylamido hexyloxide, titanium dichloride didecylamido 2-ethylhexyloxide, titanium dichloride dioctadecylamido ethoxide, titanium dichloride dioctadecylamido 2-ethylhexyloxide, titanium chloride bis(dioctylamido) hexyloxide, titanium chloride bis(dioctylamido) 2-ethylhexyloxide, titanium chloride bis(dioctylamido) decyloxide, titanium chloride bis(didecylamido) hexyloxide, titanium chloride bis(didecylamido) 2-ethylhexyloxide and titanium chloride bis(didecylamido) decyloxide. Among the above, more preferable titanium compounds are titanium trichloride dioctylamido, titanium dichloride bis(dioctylamido), titanium trichloride didecylamido, titanium dichloride bis(didecylamido), titanium trichloride dioctadecylamido and titanium dichloride bis(dioctadecylamido). As the method for synthesizing such secondary amide group-containing titanium compounds, the methods mentioned in JP-B-41-5397; JP-B-42-11646; H. Büger et al.: J. Organomet. Chem. 108 (1976), 69-84; and H.Büger et al.: J. Organomet. Chem. 20 (1969), 129-139 can be used. In this invention, the above-mentioned secondary amide group-containing titanium compounds are preferably synthesized according to the methods as mentioned above in the following manner: (i) A secondary amine compound represented by the general formula R⁵R⁶NH (wherein R⁵ and R⁶ each represents a saturated hydrocarbon group having 8 to 30 carbon atoms, preferably an aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms, more preferably a straight chain aliphatic hydrocarbon group having 8 to 30 carbon atoms in view of liquefaction of the formed titanium compound) is allowed to react with (ii) an alkyl alkali metal compound represented by the general formula R⁷M (wherein R⁷ represents a hydrocarbon group having 1 to 30 carbon atoms and M represents an alkali metal such as Li and K) to synthesize an amide compound of alkali metal, (iii) and then the amide compound of alkali metal is allowed to react with a titanium tetrahalide represented by the general formula TiX₄ (wherein X represents a halogen, preferably chlorine, bromine or iodine among which chlorine is preferable). (b) The organoaluminum compound used in this invention as catalyst component (B) is selected from known organoaluminum compounds. As its preferable examples, organoaluminum compounds represented by general formula R³ a AlM 3-a and chain-like or cyclic aluminoxanes represented by general formula can be referred to. In these formulas, R³ and R⁴ are hydrocarbon groups having 1 to 8 carbon atoms, and they may be identical or different from each other; M is hydrogen atom and/or alkoxy group; a is a number satisfying 0<a≦3, and ℓ is an integer of 1 or greater. Concrete examples of the organoaluminum compound represented by general formula R³ a AlM 3-a include trialkylaluminums such as triethylaluminum, triethylaluminum, tripropylaluminum, triisobutylaluminum and trihexylaluminum; dialkylaluminum hydrides such as dimethylaluminum hydride, diethylaluminum hydride, dipropylaluminum hydride, diisobutylaluminum hydride and dihexylaluminum hydride; 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 general formula include tetramethyldialuminoxane, tetraethyldialuminoxane, tetrabutyldialuminoxane, tetrahexyldialuminoxane, methylaluminoxane, ethylaluminoxane, butylaluminoxane and hexylaluminoxane . The amount of component (B) can be widely varied in the range of 1 to 100,000 moles per one mole of titanium atom in component (A). Preferably, however, component (B) is used in an amount ranging from 1 to 10,000 moles and more preferably from 1 to 5,000 moles, per one mole of titanium atom in component (A). (c) The monomers constituting a copolymer in this invention are ethylene and at least one kind of α-olefin(s). Concrete examples of said α-olefin include propylene, butene-1, pentene-1, hexene-1, 4-methylpentene-1, octene-1, decene-1, octadecene-1 and eicosene-1. In addition to the above-mentioned monomers, a non-conjugated diene may additionally be copolymerized for the purpose of improving the vulcanizability of copolymer. Concrete examples of said non-conjugated 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, 1,3-hexadiene, 1,6-octadiene and 6-ethyl-1,5-heptadiene. This invention is not limited by the compounds mentioned above. The copolymer of this invention can have a density so widely ranging as from 0.85 to 0.95 (g/cm³). From the viewpoint of flexibility at low temperatures, however, density of the copolymer is preferably 0.85 to 0.94, more preferably 0.85 to 0.92, and particularly preferably 0.85 to 0.90. Further, it is preferably a rubber-like random copolymer having a narrow composition distribution of which infrared absorption spectrum shows no absorption of 730 cm⁻¹ assignable to ethylene crystal chain at all. Further, the copolymer may involve two or more kinds of α-olefins and two or more kinds of non-conjugated dienes. (d) The method for supplying the catalyst components into the polymerization reactor is not critical, provided that the catalyst components must be supplied in a moisture-free state in an inert gas such as nitrogen or argon. Catalyst components (A) and (B) may be supplied either separately or after a previous mutual contact. The polymerization can be practised at a temperature ranging from -30°C to 300°C. However, the polymerization temperature is preferably -10°C to 200°C and particularly preferably 20°C to 150°C. Although pressure of the polymerization is not critical, a pressure of about 3 atmospheres to about 1,500 atmospheres is preferred from the industrial and economical points of view. As the mode of polymerization, both continuous and batch systems can be adopted. Further, a slurry polymerization using an inert hydrocarbon solvent such as propane, butane, pentane, hexane, heptane or octane, a liquid phase polymerization using no solvent, and a gas phase polymerization are all adoptable, too. Further, a chain transfer agent such as hydrogen and the like may be added for the purpose of regulating the molecular weight of the copolymer of this invention. Next, this invention will be explained in more detail by way of the following examples and comparative examples. The α-olefin content, iodine number, glass transition point and intrinsic viscosity mentioned in the examples were measured by the following methods. Thus, α-olefin content was determined from the characteristic absorption of ethylene and α-olefin by the use of infrared spectrophotometer JASCO-302 manufactured by Nippon Bunko Kogyo K. K. Iodine number was determined from the characteristic absorption of diene by the use of the same infrared spectrophotometer as above. Glass transition point (T g ) was measured by differential scanning calorimeter (SSC-5000 DSC-100, manufactured by Seiko Denshi Kogyo K. K.). Intrinsic viscosity [η] was measured in tetralin solution at 135°C with Ubbellohde viscometer. Density was measured according to JIS K-6760. In the examples and comparative examples presented below, randomness in the sequence of ethylene and α-olefin, i.e. the narrowness in the composition distribution, in copolymer was evaluated based on the existence of 730 cm⁻¹ peak (absorption due to crystalline polyethylene) in infrared absorption spectrum. That is, when the absorption at 730 cm⁻¹ was observable clearly or as a shoulder in the infrared absorption spectrum of copolymer, the composition distribution was taken as broad. When the absorption was not noticeable at all, the composition distribution was taken as narrow. Example 1 (I) Synthesis of Secondary Amino Group-Containing Titanium Compound (A) After replacing the inner atmosphere of a 300 ml flask equipped with a stirrer, a dropping funnel and a thermometer with argon gas, 3.0 ml (20 millimoles) of dioctylamine and 50 ml of hexane were charged. Then, 12.6 ml (20 millimoles) of butyllithium diluted with hexane was dropped from the dropping funnel over a period of 30 minutes, while keeping the inner temperature of the flask at 5°C. After dropping it, the mixture was additionally reacted at 5°C for 2 hours and then at 30°C for 2 hours. Subsequently, 2.2 ml (20 millimoles) of TiCl₄ diluted with hexane was dropped from the dropping funnel into the reacted mixture over a period of 30 minutes, while keeping the inner temperature of the flask at 5°C. After dropping it, the resulting mixture was additionally reacted at 5°C for one hour and then at 30°C for 2 hours. Thus, 20 millimoles (because the yield could be regarded as 100%) of a titanium compound represented by composition formula (C₈H₁₇)₂NTiCl₃ was obtained. (II) Copolymerization of Ethylene and Propylene After replacing the 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 n-heptane and 1.2 ml (5.0 millimoles) of triisobutylaluminum were charged. Then, a gas mixture of ethylene (C₂′) and propylene (C₃′) [composition of gas phase (hereinafter, all expressed in terms of ratio by volume) C₂′/C₃′ = 2/8] was blown into the solution through the blowing tube till a saturation was reached. Then, 0.25 millimole of the titanium compound obtained in (I) was added to start a polymerization. After continuing the polymerization for one hour while supplying the gas mixture at a constant temperature of 30°C, 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 consisting of 950 ml of ethanol and 50 ml of 1N hydrochloric acid and then dried in vacuum to obtain 2.2 g of an ethylene-propylene copolymer (hereinafter referred to as "EP copolymer"). The catalyst activity per one mole of titanium atom (hereinafter, simply referred to as "activity") was 8.8 x 10³ g/mol Ti. Figure 1 illustrates an infrared absorption spectrum of the polymer thus formed. In Figure 1, no absorption at 730 cm⁻¹ due to crystalline chain of ethylene (hereinafter, referred to as "IR₇₃₀") was observed, demonstrating that the polymer was a copolymer having a narrow composition distribution. In the copolymer, content (% by weight) of ethylene (hereinafter, simply referred to as "ethylene content") was 62.1%. Its intrinsic viscosity (hereinafter, simply referred to as [η]) was 2.5, density (g/cm³) (hereinafter, simply referred to as "d") was 0.879, and its glass transition point (T g ) was -59.0°C. Example 2 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that composition of gas mixture C₂′/C₃′ was equal to 5/5 and 0.5 millimoles of (C₈H₁₇)₂NTiCl₃ was used. As the result, 8.1 g of an EP copolymer was obtained. Activity was 1.6 x 10⁴ g/mole Ti. The copolymer thus formed showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. Ethylene content was 74.3%, [η] = 4.4, d = 0.873, and T g = -59.1°C. Example 3 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ as replaced with 0.44 millimole of a titanium compoud having a composition formula [(C₈H₁₇)₂N]₂TiCl₂. As the result, 2.64 g of an EP copolymer was obtained. Activity was 6.0 x 10³ g/mole Ti. The copolymer thus formed showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. Ethylene content was 51.4%, [η] = 5.4, d = 0.873, and T g = -59.0°C. Example 4 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 3, except that the triisobutylaluminum was replaced with 5 ml of n-heptane of isobutylaluminum dimethoxide (5.0 millimoles) and 0.15 millimoles of (C₈H₁₇)₂NTiCl₃ was used. As the result, 3.6 g of an EP copolymer was obtained. Activity was 2.4 x 10⁴ g/mole Ti. The copolymer thus formed showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. Ethylene content was 48.6%, [η] = 4.2, d = 0.867, and T g = -59.0°C. Example 5 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.44 millimole of a titanium compound having a composition formula [(C₈H₁₇)₂N]₂TiCl₂ and C₂′/C₃′ was equal to 5/5. As the result, 7.8 g of an EP copolymer was obtained. Activity was 1.8 x 10⁴ g/mole Ti. The copolymer thus formed showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. Ethylene content was 74.3%, [η] = 4.7, d = 0.901, and T g = -59.1°C. Example 6 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.5 millimole of a titanium compound having a composition formula (C₁₀H₂₁)₂NTiCl₃. As the result, 4.5 g of an EP copolymer was obtained. Activity was 8.9 x 10³ g/mole Ti. The copolymer thus formed showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. Ethylene content was 72.6% [η] = 2.6, d = 0.870, and T g = -59.1°C. Example 7 A copolymerization or ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.5 millimole of a titanium compound having the following composition formula: (C₈H₁₇)₂NTi[OCH₂CH(C₂H₅)C₄H₉]Cl₂ As the result, 3.4 g of an EP copolymer was obtained. Activity was 6.8 x 10³ g/mole Ti. The copolymer thus formed showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. Ethylene content was 54.7%, [η] = 2.4, d = 0.865, and T g = -59.0°C. Comparative Example 1 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.25 millimole of TiCl₄. As the result, 1.2 g of an EP copolymer was obtained. Activity was 4.5 x 10³ g/mole Ti. Figure 2 illustrates an infrared absorption spectrum of the copolymer thus formed. In Figure 2, IR₇₃₀ due to crystalline ethylene chain is clearly observed, demonstrating that the copolymer had a broad composition distribution. Ethylene content was 62.5%, and [η] was 2.7. Comparative Example 2 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.015 millimole of a titanium compound having composition formula (C₅H₅)₂TiCl₂ (Titanocenedichloride, Cp₂TiCl₂) and the triisobutylaluminum was replaced with methylaluminoxane (0.3 millimole) in 5 ml of toluene. As the result, 0.6 g of an EP copolymer was obtained. Activity was 1.2 x 10⁴ g/mole Ti. Although the polymer obtained herein showed no IR₇₃₀, its [η] was as low as 0.3. Ethylene content was 60.1%. Comparative Example 3 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.05 millimole of a titanium compound having composition formula (C₆H₅)₂NTiCl₃. As the result, 1.6 g of an EP copolymer was obtained. Activity was 3.2 x 10⁴ g/mole Ti. Figure 3 illustrates an infrared absorption spectrum of the copolymer thus obtained. In Figure 3, IR₇₃₀ due to crystalline ethylene chain is somewhat clearly observed, demonstrating that the polymer had a broad composition distribution. Ethylene content was 59.0%, and [η] was 2.8. Comparative Example 4 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.58 millimole of a titanium compound having composition formula As the result, 6.8 g of an EP copolymer was obtained. Activity was 1.2 x 10⁴ g/mole Ti. The copolymer thus obtained showed IR₇₃₀, demonstrating that it had a broad composition distribution. Ethylene content was 57.0%, and [η] was 4.8. Comparative Example 5 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.55 millimole of a titanium compound having composition formula (C₂H₅)₂NTiCl₃. As the result, 5.5 g of an EP copolymer was obtained. Activity was 9.9 x 10³ g/mole Ti. Figure 4 illustrates an infrared absorption spectrum of the copolymer thus obtained. In Figure 4, IR₇₃₀ due to crystalline ethylene chain is observed as a shoulder, demonstrating that it is a copolymer having a broad composition distribution. Ethylene content was 37.9%, [η] = 4.7, and d = 0.862. Comparative Example 6 A copolymerization of ethylene and propylene was carried out in the same manner as in Example 1 (II), except that the (C₈H₁₇)₂NTiCl₃ was replaced with 0.5 millimole of a titanium compound having composition formula (i-C₄H₉)₂NTiCl₃. As the result, 10.5 g of an EP copolymer was obtained. Activity was 2.1 x 10⁴ g/mole Ti. In its infrared absorption spectrum, the copolymer thus obtained showed IR₇₃₀ as a shoulder, demonstrating that it was a copolymer having a broad composition distribution. Ethylene content was 71.0%, [η] = 2.6, and d = 0.865. Example 8 (III) Copolymerization of Ethylene, Propylene and Non-conjugated Diene After replacing the 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 1.2 ml (5 millimoles) of triisobutylaluminum were charged. Then, after charging 12.4 ml (100 millimoles) of dicyclopentadiene as a non-conjugated diene, a gas mixture of ethylene and propylene (gas phase composition being C₂′/C₃′ = 2/8) was introduced into the solution through the blowing tube until a saturation was reached. Then, 0.19 millimole of the titanium compound having the composition formula (C₈H₁₇)₂NTiCl₃ prepared in Example 1 (I) was added to start a polymerization. Subsequently, the polymerization was continued for one hour at a constant temperature of 30°C, while supplying the same gas mixture as above, after which 20 ml of ethanol was added to stop the polymerization. The resulting copolymer was washed three times with each 1,000 ml portion of a mixture consisting of 950 ml of ethanol and 50 ml of 1N hydrochloric acid and dried in vacuum. Thus, 1.2 g of a rubbery ethylene-propylene-diene copolymer was obtained. Activity was 6.3 x 10³ g/mole Ti. The copolymer thus obtained showed no IR₇₃₀. content of this rubbery copolymer was 62.1%, its iodine number was 16.2, [η] was 3.0, and d was 0.900. Example 9 A copolymerization of ethylene, propylene and non-conjugated diene was carried out in the same manner as in Example 8, except that 13.5 ml (100 millimoles) of 5-ethylidene-2-norbornene was used as a non-conjugated diene and 0.25 millimole of the titanium compound having the composition formula (C₈H₁₇)₂NTiCl₃ prepared in Example 1 (I) was added to start a polymerization. As the result, 1.5 g of a rubbery ethylene-propylene-diene copolymer was obtained. Activity was 6.0 x 10³ g/mole Ti. The copolymer thus obtained showed no IR₇₃₀. Ethylene content was 75.5%, iodine number was 12.1, [η] = 3.8, and d = 0.875. Example 10 A copolymerization of ethylene, propylene and non-conjugated diene was carried out in the same manner as in Example 8, except that 1.2 ml (10 millimoles) of 1,5-hexadiene was used as a non-conjugated diene and 0.19 millimole of the titanium compound having the composition formula (C₈H₁₇)₂NTiCl₃ was used. As the result, 2.8 g of a rubbery ethylene-propylene-diene copolymer was obtained. Activity was 1.5 x 10⁴ g/mole Ti. The copolymer thus obtained showed no IR₇₃₀. Ethylene content was 53.0%, iodine number was 8.1, [η] = 3.1, and d = 0.902. Example 11 (IV) Copolymerization of Ethylene and Butene-1 After replacing the 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 1.2 ml (5.0 millimoles) of triisobutylaluminum were charged. Then, a gas mixture of ethylene (C₂′) and butene-1 (C₄′) (gas phase composition being C₂′/C₄′ = 1/8) was introduced into the solution through the blowing tube until a saturation was reached, after which 0.24 millimole of the titanium compound having composition formula (C₈H₁₇)₂NTiCl₃ prepared in Example 1 (I) was added to start a polymerization. Subsequently, the polymerization was continued for one hour at a constant temperature of 30°C, while supplying the gas mixture, 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 consisting of 950 ml of ethanol and 50 ml of 1N hydrochloric acid and then dried in vacuum to obtain 2.1 g of a rubbery ethylene-butene-1 copolymer. Activity was 8.8 x 10³ g/mole Ti. The copolymer thus obtained showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. Ethylene content of this rubbery copolymer was 60.5%, [η] was 3.7, d = 0.865, and T g = -69.7°C. Example 12 Copolymerization of Ethylene and Decene-1 After replacing the 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 decene-1 and 1.2 ml (5.0 millimoles) of triisobutylaluminum were charged. Then, ethylene gas was introduced into the solution through the blowing tube until a saturation was reached, after which 0.025 millimole of the titanium compound having composition formula (C₈H₁₇)₂NTiCl₃ prepared in Example 1 (I) was added to start a polymerization. Subsequently, the polymerization was continued for one hour at a constant temperature of 30°C, while supplying ethylene gas, and then 20 ml of ethanol was added to stop the reaction. The resulting polymer was washed three times with each 1,000 ml portion of a mixture consisting of 950 ml of ethanol and 50 ml of 1N hydrochloric acid and then dried in vacuum to obtain 1.87 g of a rubbery ethylene-decene-1 copolymer. Activity was 7.5 x 10⁴ g/mole Ti. The polymer thus obtained showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. The ethylene content was 67.7%, [η] was 3.7, d = 0.854, and T g = -69.5°C. Example 13 Copolymerization of Ethylene, Decene-1 and Non-conjugated Diene After replacing the inner atmosphere of a 300 ml flask equipped with a stirrer, a reflux condenser, a gas blowing tube and a thermometer with argon gas, 50 ml of decene-1, 1.23 ml (10 millimoles) of dicyclopentadiene and 1.2 ml (5.0 millimoles) of triisobutylaluminum were charged. Then, ethylene gas was introduced into the solution through the blowing tube until a saturation was reached, after which 0.025 millimole of a titanium compound having composition formula (C₈H₁₇)₂NTiCl₃ prepared in Example 1 (I) was added to start a polymerization. Subsequently, the polymerization was continued for one hour at a constant temperature of 30°C, while supplying ethylene gas, 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 mixture consisting of 950 ml of ethanol and 50 ml of 1N hydrochloric acid and then dried in vacuum to obtain 1.13 g of a rubbery ethylene-decene-1-dicyclopentadiene copolymer. Activity was 4.5 x 10⁴ g/mole Ti. The copolymer thus obtained showed no IR₇₃₀, demonstrating that it was a copolymer having a narrow composition distribution. The ethylene content was 48.4%, and iodine number was 6.2, [η] = 5.15, and d = 0.869.

Claims: Claims for the following Contracting States : BE, DE, FR, GB, IT, NL A liquid catalyst component comprising a titanium compound represented by the general formula (R¹R²N) 4-(m+n) TiX m Y n wherein R¹ and R² each represents a saturated hydrocarbon group having 8 to 30 carbon atoms, X represents a halogen, Y represents an alkoxy group, m represents a number satisfying 1≦m≦3, n represents a number satisfying 0≦n≦2, and (m+n) satisfies 1≦(m+n)≦3. A liquid catalyst component according to Claim 1, wherein the saturated hydrocarbon group having 8 to 30 carbon atoms is an aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms. A liquid catalyst component according to Claim 2, wherein the aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms is a straight chain aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms. A catalyst system for polymerization comprising (A) a liquid catalyst component according to any one of claims 1 to 3, and (B) an organoaluminum compound. A catalyst system according to Claim 4, wherein the organoaluminum compound (B) is an organoaluminum compound represented by the general formula R³ a AlM 3-a , or a chain-like or cyclic aluminoxane having a structure represented by the general formula wherein R³ and R⁴ each represents a hydrocarbon group having 1 to 8 carbon atoms, M represents hydrogen and/or an alkoxy group, a represents a number satisfying 0<a≦3, and ℓ represents an integer of 1 or greater. A catalyst system according to Claim 5, wherein the organoaluminum compound represented by the general formula R³ a AlM 3-a is a trialkylaluminum, dialkylaluminum hydride or alkylaluminum alkoxide. A catalyst system according to Claim 5, wherein the aluminoxane represented by the general formula is tetramethyldialuminoxane, tetraethyldialuminoxane, tetrabutyldialuminoxane, tetrahexyldialuminoxane, methylaluminoxane, ethylaluminoxane, butylaluminoxane or hexylaluminoxane. A catalyst system according to Claim 4, wherein the amount of component (B) is 1 to 100,000 moles per one mole of titanium atom in component (A). A process for producing an ethylene-α-olefin copolymer which comprises copolymerizing ethylene with an α-olefin by using a catalyst system according to any one of claims 4 to 8, wherein the catalyst components are supplied in a moisture-free state and in an inert gas. A process for producing an ethylene-α-olefin copolymer according to Claim 9, wherein said ethylene-α-olefin copolymer has a density of 0.85 to 0.95 (g/cm³). Claims for the following Contracting State : ES A process for preparing a liquid catalyst component comprising a titanium compound represented by the general formula (R¹R²N) 4-(m+n) TiX m Y n wherein R¹ and R² each represents a saturated hydrocarbon group having 8 to 30 carbon atoms, X represents a halogen, Y represents an alkoxy group, m represents a number satisfying 1≦m≦3, n represents a number satisfying 0≦n≦2, and (m+n) satisfies 1≦(m+n)≦3 which comprises (i) reacting a secondary amine compound, represented by the general formula R¹R²NH, wherein R¹ and R² each has the above meaning, with (ii) an alkyl alkali metal compound represented by the general formula R⁷M, wherein R⁷ represents a hydrocarbon group having 1 to 30 carbon atoms and M represents an alkali metal, to synthesize an amide compound of an alkali metal, (iii) and then reacting the amide compound of the alkali metal with a titanium tetrahalide represented by the general formula TiX₄, wherein X has the above meaning. A process according to Claim 1, wherein the saturated hydrocarbon group having 8 to 30 carbon atoms is an aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms. A process according to Claim 2, wherein the aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms is a straight chain aliphatic saturated hydrocarbon group having 8 to 30 carbon atoms. A catalyst system for polymerization comprising (A) a liquid catalyst component according to any one of claims 1 to 3, and (B) an organoaluminum compound. A catalyst system according to Claim 4, wherein the organoaluminum compound (B) is an organoaluminum compound represented by the general formula R³ a AlM 3-a , or a chain-like or cyclic aluminoxane having a structure represented by the general formula wherein R³ and R⁴ each represents a hydrocarbon group having 1 to 8 carbon atoms, M represents hydrogen and/or an alkoxy group, a represents a number satisfying 0<a≦3, and ℓ represents an integer of 1 or greater. A catalyst system according to Claim 5, wherein the organoaluminum compound represented by the general formula R³ a AlM 3-a is a trialkylaluminum, dialkylaluminum hydride or alkylaluminum alkoxide. A catalyst system according to Claim 5, wherein the aluminoxane represented by the general formula is tetramethyldialuminoxane, tetraethyldialuminoxane, tetrabutyldialuminoxane, tetrahexyldialuminoxane, methylaluminoxane, ethylaluminoxane, butylaluminoxane or hexylaluminoxane. A catalyst system according to Claim 4, wherein the amount of component (B) is 1 to 100,000 moles per one mole of titanium atom in component (A). A process for producing an ethylene-α-olefin copolymer which comprises copolymerizing ethylene with an α-olefin by using a catalyst system according to any one of claims 4 to 8, wherein the catalyst components are supplied in a moisture-free state and in an inert gas. A process for producing an ethylene-α-olefin copolymer according to Claim 9, wherein said ethylene-α-olefin copolymer has a density of 0.85 to 0.95 (g/cm³).

Inventors: EBARA TAKESHI, JYOHOUJI HIROFUMI, KAWAI KIYOSHI, MIYOSHI YOSHIHIRO, SASAKI TOSHIO, EBARA, TAKESHI, JYOHOUJI, HIROFUMI, KAWAI, KIYOSHI, MIYOSHI, YOSHIHIRO, SASAKI, TOSHIO
Applicants: SUMITOMO CHEMICAL CO, SUMITOMO CHEMICAL COMPANY, LIMITED
Application year: 1989
Main classification: C08F210
IPC codes: C08F210, C08F4