Olefin polymerization catalyst system

Abstract: An olefin polymerization catalyst system comprises an organic transition metal compound and a support, the organic transition metal compound being soluble in an inert organic solvent and the support, which is insoluble in the solvent, comprises an organic high molecular compound which contains a specific carbonyl-having group. The catalyst system polymerizes an olefin in a high activity, provides polymer with high stereoregularity, prevents adhesion or fouling of either the polymer generated in the course of polymerization or an organic aluminum oxy compound on the inner wall of a reactor, leads to high bulk density of the polymer and significantly reduced levels of fisheye and/or gel generation on the processed item. High productivity, and high quality products are attainable when using the catalyst.

Description: The invention relates to a catalyst system used for an olefin polymerization. More specifically, the invention relates to an olefin polymerization catalyst system comprising a specific transition metal compound and a specific support. In recent years, transition metal compounds which are soluble in inert organic solvents (catalyst for a homogeneous system) have been the focus of attention as olefin polymerization catalysts. Specifically, in these catalysts, so-called metallocene compounds have been well-known. The process for polymerizing olefin by using these metallocene compounds, particularly the process for stereoregularly polymerizing α-olefin has been subjected to many improvements since the report of W. Kaminsky et al. (Japan Laid-Open SHO 58-19309; Angew. Chem., 97,507 (1985)). In the slurry polymerization process for polymerizing olefin in an inert hydrocarbon by using the metallocene compound and an organic aluminum oxy compound as a catalyst, bulk polymerization process for polymerizing in a liquefied olefin monomer, or gas phase polymerization process for polymerizing in a gaseous olefin monomer, the polymer or an organic aluminum oxy compound which is formed in the course of polymerization adheres on the inner wall of the reactor, causes reduction of heat-removing capacity, further forms blocks in the reactor, and leads to troubles for the steady operation of polyolefin manufacturing facilities. Additionally, the polymer formed has a very small particle size, low bulk density, and incurs a problem of markedly lowering productivity. In order to overcome these problems, a process for polymerizing olefin in the presence of a catalyst which is prepared by supporting an organic aluminum oxy compound on silica gel, alumina and other inorganic oxides and bringing it into contact with the metallocene compound, has been described in Japan Laid-Open SHO 60-35006, 61-108610, 61-296008, 63-66206 and HEI 2-173104. These inorganic oxides generally have an acid hydroxyl group on the surface and the catalyst is supported on the support by bringing the hydroxyl group into contact with the organic aluminum oxy compounds or metallocene compounds. However, when polyolefin is prepared by using a catalyst obtained by supporting a metallocene compound and/or organic aluminum oxy compound on an inorganic oxide such as the above obtained silica gel and alumina, relatively hard inorganic materials such as silica gel support or alumina support remain in the formed item, act as a foreign matter, and result in development of fish-eyes. Such phenomenon lowers the value of the product and additionally leads to clogging of filter(s) . mounted on the molding machine, melt kneading machine and granulating machine, and renders steady operation difficult in industry. Polyolefin prepared in the presence of an olefin polymerization catalyst obtained by supporting the organic aluminum oxy compound and/or metallocene compound on the above inorganic compound support, polypropylene in particular, leads to very low stereoregularity as compared with polyolefin prepared by using a homogeneous polymerization catalyst without support. Further, properties such as stiffness, impact resistance and heat resistance are lowered and generate a large problem with quality. Activity improvement of olefin polymerization catalyst by modifying the organic aluminum oxy compound has been tried. For example, Japan Laid-Open HEI 2-78687 has disclosed a process for using a catalyst comprising metallocene compound and a benzene insoluble organic aluminum oxy compound obtained by bringing an organic aluminum oxy compound into contact with an active hydrogen containing compound. Japan Laid-Open HEI 7-53619 and 7-53620 have described a process for modifying the organic aluminum oxy compound by an organic compound such as ketoalcohol or β-diketone. Further, as to the process for modifying the organic aluminum oxy compound, Japan Laid-Open HEI 7-53620 has described a process for using a catalyst comprising a metallocene compound and the addition reaction product of an organic phosphorus compound having a specific structure and the organic aluminum oxy compound, in order to improve catalyst activity and simultaneously to prevent adhesion of formed polymer on the inner surface of the reactor. However, these processes cannot fully prevent the adhesion of polymer formed in the polymerization on the surface of the reactor. The object of the invention is to provide an olefin polymerization catalyst system which can prepare polyolefin in high activity and high stereoregularity, is free from adhesion of polymer formed in the course of the polymerization reaction or of the organic aluminum oxy compound on the inner wall of the reactor, can lead to a high bulk density of the polymer, can maintain high productivity, and improve fish eye and/or gel generation level in the product. As a result of an intensive investigation on the desired olefin polymerization catalyst system in order to solve the above objects, the present inventors have accomplished the invention. According to one aspect of the present invention, there is provided an olefin polymerization catalyst system comprising an organic transition metal compound and a support, the organic transition metal compound being soluble in an inert organic solvent selected from alkanes, aromatic hydrocarbons, ethers and halogenated hydrocarbons, the support being insoluble in the inert organic solvent, and said support being obtained by contacting a polymer, which contains a carbonyl-having group represented by the general formula [1]: wherein Q is selected from hydrogen, hydroxy, alkyl, aryl, alkoxy, aryloxy, oxycarbonyl, halogen, amino, aminocarbonyl, hydrazino or oxyanion, with an organic aluminum oxy compound and wherein said polymer is obtained by grafting or graft polymerizing a monomer, containing the carbonyl-having group on polyethylene, polypropylene, ethylene-propylene copolymer, polybutene, ethylene-butene copolymer, ethylene-propylene-butene copolymer, polyisobutene, polypentene, poly-4-methylpentene polynorborene, polybutadiene, polyisoprene, polystyrene or poly-α-methylstyrene. In another aspect, the invention also provides a support for an olefin polymerization catalyst system, wherein the support is obtained by bringing an organic aluminum oxy compound into contact with the polymer represented by general formula [1] defined above. We are aware of International patent application Wo 95/23816 (Mobil Oil Corporation) which describes an olefin polymerization catalyst system which comprises a cross-linked polymer formed by radical polymerization of divinyl benzene with styrene, and an aluminoxane disposed on the surface thereof. We are also aware of United States patent US 5362824 (Furtek et al. / Mobil Oil Corporation) which describes an olefin polymerization catalyst comprising an aluminoxane co-catalyst supported on a substrate comprising a cross-linked polymer formed by radical polymerization of divinyl benzene with styrene and p-acetoxystyrene. The olefin polymerization catalyst system of the invention will hereinafter be illustrated in detail in the following non-limitative description. In the invention, the term "soluble or insoluble in an inert organic solvent" means that an organic transition metal compound and a support have the following property. In the invention, the organic transition metal compound component and a support component are previously brought into contact with each other to prepare the catalyst and successively applied to polymerization. The term "soluble or insoluble in the inert organic solvent" means that, prior to mutual contact of these components, each component has the property of being individually soluble or insoluble in the inert organic solvent for use in the preparation of the catalyst. That is, the term means that, before contact of these two components, the organic transition metal compound is singly soluble in the inert organic solvent and the support is singly insoluble in the inert organic solvent. The inert organic solvent in the invention is alkane e.g. having 1-20 carbon atoms, aromatic hydrocarbon e.g. having 6-20 carbon atoms, ether e.g. having 2-20 carbon atoms or halogenated hydrocarbon e.g. having 1-20 carbon atoms Exemplary alkanes which can be used include methane, ethane, propane, butane, pentane, heptane, octane, isobutane, neopentane, cyclopentane, cyclohexane and decalin. Representative aromatic hydrocarbons which can be used include benzene, toluene and xylene. Specific ethers include diethyl ether, tetrahydrofuran, 1,2-dimethoxyethane and dioxane. Halogenated hydrocarbons include, for example, dichloromethane, and chloroform. These inert organic solvents can be used singly or as a mixture. The organic transition metal compound which is soluble in the inert organic solvent in the invention is, for example, a compound which includes a transition metal of the group 3 - 8 according to the periodic table on the front cover of "Chemical Dictionary, Edited by Tokyo Kagaku Dojin (1994). No particular restriction is imposed upon the transition metal compound so long as the compound can polymerize olefin by using the organic aluminum oxy compound as a co-catalyst or catalyst activating agent. Particularly preferred metallocene compound is represented by the general formula [2] or general formula [3]: wherein A 1 and A 2 are a cyclopentadienyl group, indenyl group, or fluorenyl group, one of A 1 and A 2 can be amino group, and two adjacent groups can be directly bonded to each other to form a cyclic hydrocarbon substituent; further a portion or all of the hydrogen atoms on these groups can be substituted with a substituent selected from alkyl e.g. of 1' - 20 carbon atoms, aryl e.g. of 6 - 20 carbon atoms, alkoxy e.g. of 1 - 20 carbon atoms, aryloxy e.g. of 6 - 20 carbon atoms and silicon containing alkyl e.g. of 1 - 20 carbon atoms; M is a metal selected from the group 4 in the periodic table; and X 1 and X 2 are selected from halogen, alkyl e.g. of 1 - 20 carbon atoms or anion ligand wherein A 3 and A 4 are a cyclopentadienyl group, indenyl group, or fluorenyl group, one of A 3 and A 4 can be an amino group, and two adjacent groups can be directly bonded each other to form a cyclic hydrocabon substituent; further, a portion or all of the hydrogen atoms on these groups can be substituted with a substituent selected from alkyl e.g. of 1 - 20 carbon atoms, aryl e.g. of 6 - 20 carbon atoms, alkoxy e.g. of 1 - 20 carbon atoms, aryloxy e.g. of 6 - 20 carbon atoms and silicon containing alkyl e.g. of 1 - 20 carbon atoms; A 3 and A 4 can be the same or differ from each other; M is a metal selected from the group 4 in the periodic table; Y is selected from -CR 1 R 2 -, -CR 1 R 2 -CR 3 R 4 -, or SiR 1 R 2 - wherein R 1 , R 2 , R 3 or R 4 are selected from hydrogen, alkyl e.g. of 1 - 20 carbon atoms, aryl e.g. of 6 - 20 carbon atoms, alkoxy e.g. of 1 - 20 carbon atoms, aryloxy e.g. of 6 - 20 carbon atoms or silicon containing alkyl e.g. of 1 - 20 carbon atoms, and R 1 , R 2 , R 3 , and R 4 can be the same or differ each other; X 1 and X 2 are selected from halogen, alkyl e.g. of 1 - 20 carbon atoms or anion ligand. In the above general formulas [2] and [3], the alkyl groups having 1 - 20 carbon atoms include, for example, methyl, ethyl, propyl, butyl,.isopropyl, tert-butyl, neopentyl, cyclopentyl, cyclohexyl and menthyl groups. Exemplary aryl groups having 6 - 20 carbon atoms include phenyl, tolyl and naphthyl groups. Representative alkoxy groups having 1 - 20 carbon atoms include methoxy, ethoxy, propoxy, butoxy, isopropoxy, tert-butoxy, neopentoxy, cyclopentoxy, cyclohexyloxy, and menthoxy groups. Aryloxy groups having 6 - 20 carbon atoms include, for example, phenoxy, tolyloxy, xylyloxy and naphthyloxy groups. Silicon containing alkyl groups having 1 - 20 carbon atoms include, for example, trimethylsilyl, dimethylethylsilyl, diphenylmethylsilyl, cyclohexyldimethylsilyl, triphenylsilyl, 2-(methyldiphenylsilyl)ethyl groups. Further, each other adjacent substituent can be directly bonded to form the same cyclic hydrocarbon substituent. Specifically, cyclopentane ring, cyclohexane ring, cycloheptane ring, benzene ring, naphthalene ring and derivatives of these rings are enumerated. In the above general formula [3], Y is -CR 1 R 2 -, -CR 1 R 2 -CR 3 R 4 - or -SiR 1 R 2 -. Specifically, methylene, dimethylmethylene (or isopropylidene), diphenylmethylene, diphenylethylene, 1,2-dimethylethylene, 1,1,2,2-tetramethylethylene, dimethylsilylene and diphenylsilylene group are enumerated. In the above general formulas [2] and [3], M is a metal selected from the group 4 of the periodic table and include, for example, titanium, zirconium, and hafnium. X 1 and X 2 are selected from halogen, alkyl group and anion ligand. Halogen is selected from fluorine, chlorine, bromine and iodine. Alkyl groups include, for example, methyl, ethyl, propyl and other straight alkyl groups; isopropyl and other branched alkyl groups; and cyclopropyl and other cyclic alkyl groups. Exemplary anion ligands include trimethylphosphine, triethylphosphine, triphenylphosphine, diphenylmethylphosphine and other organic phosphorus compounds; methoxy, ethoxy, n-butoxy, sec-butoxy, tert-butoxy, phenoxy, naphthoxy and other alkoxy ligands; and tetrahydrofuran, diethyl ether, dioxane, 1,2-dimethoxyethane and other ether compounds. Specific examples of metallocene compounds represented by the above general formulas [2] and [3] in the invention will be illustrated hereinafter. However, no particular restriction is imposed upon these compounds so long as the metallocene compounds can promote olefin polymerization. Exemplary metallocene compounds represented by the above general formula [2] include bis (cyclopentadienyl)-zirconium dichloride, bis(pentamethylcyclopentadienyl)zirconium) dichloride, bis(indenyl)zirconium dichloride, bis(2-methylindenyl)zirconium dichloride, bis(fluorenyl)zirconium dichloride, bis(4-t-butylfluorenyl)zirconium dichloride, pentamethylcyclopentadienyl (di-t-butylamide)zirconium dichloride, bis(cyclopentadienyl)zirconium dimethyl, bis(pentamethyl-cyclopentadienyl)zirconium dimethyl, bis(indenyl)zirconiumdimethyl, bis (2-methylindenyl)zirconium dimethyl, bis(fluorenyl)zirconium dimethyl, bis(4-t-butylfluorenyl)zirconium dimethyl, and pentamethylcyclopentadienyl(di-t-butylamide)zirconium dimethyl, and other metallocene compounds obtained by replacing zirconium of the above metallocene compounds with titanium or hafnium. Examplary metallocene compounds represented by the general formula [3] include dimethylsilylene bis(cyclopentadienyl)zirconium dichloride, dimethylsilylene bis(tetramethylcyclopentadienyl)zirconium dichloride, dimethylsilylenebis(methylcyclopentadienyl)zircnium dichloride, dimethylsilylenebis(dimethylcyclopentadienyl)zirconium dichloride, dimethylsilylene (2,4-dimethylcyclopentadienyl) (3',5'-dimethylcyclopentadienyl)zirconium dichloride, dimethylsilylene(2,3,5-trimethylcyclopentadienyl)(2',4',5'-trimethylcyclopentadienyl)zirconium dichloride, dimethylsilylenebis(t-butylcyclopentadienyl)zirconium dichloride, dimethylsilylenebis(trimethylsilylcyclopentadienyl)zirconium dichloride, dimethylsilylenebis(2-trimethylsilyl-4-t-butylcyclopentadienyl)zirconium dichloride, dimethylsilylenebis(4,5,6,7-tetrahydro indenyl)zirconium dichloride, dimethylsilylenebis(indenyl)zirconium dichloride, dimethylsilylenebis(2-methylindenyl)zirconium dichloride, dimethylsilylenebis(2,4-dimethylindenyl)zirconium dichloride, dimethylsilylenebis(2,4,7-trimethylindenyl)zirconium dichloride, dimethylsilylenebis(2-methyl-4-phenylindenyl)zirconium dichloride, dimethylsilylenebis(2-ethyl-4-phenylindenyl)zirconium dichloride, dimethylsilylenebis(benz[e]indenyl)zirconium dichloride, dimethylsilylenebis(2-methylbenz[e]indenyl)zirconium dichloride, dimethylsilylenebis(benz[f]indenyl)zirconium dichloride, dimethylsilylenebis(2-methylbenz[f]indenyl)zirconium dichloride, dimethylsilylenebis(3-methylbenz[f]indenyl)zirconium dichloride, dimethylsilylenebis(cyclopenta[cd]indenyl)zirconium dichloride, dimethylsilylenebis(cyclopentadienyl)zirconium dimethyl, dimethylsilylenebis(tetramethylcyclopentadienyl)zirconium dimethyl, dimethylsilylenebis(methylcyclopentadienyl)zirconium dimethyl, dimethylsilylenebis(dimethylcyclopentadienyl)zirconium dimethyl, dimethylsilylene(2,4-dimethylcyclopentadienyl)(3',5'-dimethylcyclopentadienyl)zirconium dimethyl, dimethylsilylene(2,3,5-trimethylcyclopentadienyl)(2',4',5'-trimethylcyclopentadienyl)zirconium dimethyl, dimethylsilylenebis(t-butylcyclopentadienyl)zirconium dimethyl, dimethylsilylenebis(trimethylsillcyclopentadienyl)zirconium dimethyl, dimethylsilylenebis(2-trimethylsilyl-4-t-butylcyclopentadienyl)zirconium dimethyl,dimethylsilylenebis(4,5,6,7-tetrahydroindenyl)zirconium dimethyl, dimethylsilylenebis(indenyl)zirconium dimethyl, dimethylsilylenebis(2-methylindenyl)zirconium dimethyl, dimethylsilylenebis(2,4-dimethylindenyl)zirconium dimethyl,dimethylsilylenebis(2,4,7-trimethylindenyl)zirconium dimethyl, dimethylsilylenebis(2-methyl-4-phenylindenyl)zirconium dimethyl, dimethylsilylenebis(2-ethyl-4-phenylindenyl)zirconium dimethyl, dimethylsilylenebis(benz[e]indenyl)zirconium dimethyl, dimethylsilylenebis(2-methylbenz[e]indenyl)zirconium dimethyl,dimethylsilylenebis(3-methylbenz[e]indenyl)zirconium dimethyl,dimethylsilylenebis(benz[f]indenyl)zirconium dimethyl, dimethylsilylenebis(2-methylbenz[f]indenyl)zirconim dimethyl, dimethylsilylenebis(3-methylbenz[f]indenyl)zirconium dimethyl, dimethylsilylenebis(cyclopenta[cd]indenyl)zirconium dimethyl, and other metallocene compounds obtained by replacing zirconium with titanium or hafnium; and further include isopropylidene(cyclopentadienyl)(fluorenyl)zirconium dichloride, isopropylidene(cyclopentadienyl)(indenyl)zirconium dichloride, isopropylidene(cyclopentadienyl)(2,7-di-t-butylfluorenyl)zirconium dichloride, isopropylidene(cyclopentadienyl)(3-methylfluorenyl)zirconium dichloride, isopropylidene(cyclopentadienyl)(4-methylfluorenyl)zirconium dichloride, isopropylidene(cyclopentadienyl)(octahydrofluorenyl)zirconium dichloride, isopropylidene(methylcyclopentadienyl)-(fluorenyl)zirconium dichloride, isopropylidene(dimethylcyclopentadienyl)(fluorenyl)zirconium dichloride, isopropylidene(tetramethylcyclopentadienyl)(fluorenyl)zirconium dichloride, or diphenylmethylene(cyclopentadienyl)(fluorenyl)zirconium dichloride, diphenylmethylene(cyclopentadienyl)(indenyl)zirconium dichloride, diphenylmethylene(cyclopentadienyl)(2,7-di-t-butylfluorenyl)zirconium dichloride, diphenylmethylene(cyclopentadienyl)(3-methylfluorenyl)zirconium dichloride, diphenylmethylene(cyclopentadienyl)(4-methylfluorenyl)zirconium dichloride, diphenylmethylene(cyclopentadienyl). (octahydrofluorenyl)zirconium dichloride, diphenylmethylene(methylcyclopentadienyl)(fluorenyl)zirconium dichloride, diphenylmethylene(dimethylcyclopentadienyl)(fluorenyl)zirconium dichloride, diphenylmethylene(tetramethylcyclopentadienyl)(fluorenyl)zirconium dichloride, or cyclohexylidene(cyclopentadienyl)(fluorenyl)zirconium dichloride, cyclohexylidene(cyclopentadienyl) (indenyl)zirconium dichloride, cyclohexylidene(cyclopentadienyl)(2,7-di-t-butylfluorenyl)zirconium dichloride, cyclohexylidene(cyclopentadienyl)(3-methylfluorenyl) zirconium dichloride, cyclohexylidene(cyclopentadienyl)(4-methylfluorenyl)zirconium dichloride, cyclohexylidene(cyclopentadienyl)(octahydrofluorenyl)zirconium dichloride, cyclohexylidene(methylcyclopentadienyl) (fluorenyl)zirconium dichloride, cyclohexylidene(dimethylcyclopentadienyl)(fluorenyl)zirconium dichloride, cyclohexylidene(tetramethylcyclopentadienyl) (fluorenyl)zirconium dichloride, or dimethylsilylene(cyclopentadienyl)(fluorenyl)zirconium dichloride, dimethylsilylene(cyclopentadienyl)(indenyl)zirconium dichloride, dimethylsilylene(cyclopentdienyl)(2,7-di-t-butylfluorenyl)zirconium dichloride, dimethylsilylene(cyclopentadienyl)(3-methylfluorenyl)zirconium dichloride, dimethylsilylene(cyclopentadienyl)(4-methylfluorenyl)zirconium dichloride, dimethylsilylene(cyclopentadienyl)(octahydrofluorenyl)zirconium dichloride, dimethylsilylene(methylcyclopentanedienyl-fluorenyl)zirconium dichloride, dimethylsilylene(dimethylcyclopentadienylfluorenyl)zirconium dichloride, dimethylsilylene(tetramethylcyclopentadienylfluorenyl)zirconium dichloride, or isopropylidene(cyclopentadienyl)(fluorenyl)zirconium dimethyl, isopropylidene(cyclopentadienyl)(indenyl)zirconium dimethyl, isopropylidene(cyclopentadienyl)(2,7-di-t-butylfluorenyl)zirconium dimethyl, cyclohexylidene(cyclopentadienyl), (fluorenyl)zirconium dimethyl, cyclohexylidene(cyclopentadienyl)(2,7-di-t-butylfluorenyl)zirconium dimethyl, dimethylsilylene(cyclopentadienyl)(fluorenyl)zirconium dimethyl, dimethylsilylene(cyclopentadienyl)(indenyl)zirconium dimethyl, and dimethylsilylene(cyclopentadienyl)(2,7-ditertbutylfluorenyl)zirconium dimethyl and other metallocene compounds obtained by replacing zirconium of the above metallocene compounds with titanium or hafnium. Exemplary metallocene compounds further include ethylenebis(indenyl)zirconium dichloride, ethylenebis-(4,5,6,7-tetrahydroindenyl)zirconium dichloride, 1,2-dimethylethylenebis(indenyl)zirconium dichloride, 1,2-dimethylethylenebis(2'-methylindenyl)zirconium dichloride, 1,2-diisopropylethylenebis(indenyl)-zirconium dichloride, 1,2-diisopropylethylenebis(2'-methylindenyl)zirconium dichloride, 1,2-dimethylethylenebis(3'-methylindenyl)zirconium dichloride, 1,2-dimethylethylenebis(4'-isoproylindenyl)zirconium dichloride, 1,2-dimethylethylenebis(4',7'-diisopropylindenyl)irconium dichloride, 1,2-dimethylethylenebis(2'-methyl-4'-isopropylindenyl) zirconium dichloride, 1,2-dimethylethylenebis(4'-cyclohexylindenyl)zirconium dichloride, 1,2-dimethylethylenebis(2'-methyl-4'-cyclohexylindenyl)zirconium dichloride, 1,2-dimethylethylenebis(4',7'-diphenyenelindenyl)zirconium dichloride, 1,2-dimethylethylenebis(2'-methyl-4'-phenylindenyl)zirconiumdichloride, 1,2-dimethylethylenebis(4'-naphthylindenyl)zirconium dichloride, 1,2-dimethylethylenebis(2'-methyl-4'-naphthylindenyl)-zirconium dichloride, 1,2-dimethylethylenebis(5'-phenylindenyl)zirconium dichloride, 1,2-dimethylethylenebis(4'-methoxyindenyl)zirconium dichloride, 1,2-dimethylethylenebis(benz[e]indenyl)zirconium dichloride, 1,2-dimethylethylenebis(2'-methylbenz[e]indenyl)zirconium dichloride, 1,2-dimethylethylenebis(3'-methylbenz[e]indenyl)zirconium dichloride, 1,2-dimethylethylenebis(benz[f] indenyl)zirconium dichloride, 1,2-dimethylethylenebis(2'-methylbenz[f]indenyl)zirconium dichloride, 1,2-dimethylethylenebis(3'-methylbenz[f]indenyl)zirconium dichloride, 1,2-dimethylethylenebis(cyclopenta[cd]indenyl)zirconium dichloride, or ethylenebis(indenyl)zirconium dimethyl, ethylenebis(4,5,6,7-tetrahydroindenyl)zirconium dimethyl, 1,2-dimethylethylenebis(2'-methyl-4'-isopropylindenyl)zirconium dimethyl, 1,2-dimethylethylenebis(4',7'-diisopropylindenyl)zirconium dimethyl, 1,2-dimethylethylenebis(2'-methyl-4'-phenylindenyl)zirconium dimethyl, 1,2-dimethylethylenebis(2'-methyl-4'-naphthylindenyl)zirconium dimethyl, 1,2-dimethylethylenebis(benz[e]indenyl)zirconium dimethyl, 1,2-dimethylethylenebis(2'-methylbenz[e]indenyl)zirconium dimethyl, and 1,2-dimethylethyenebis(3'-methylbenz[e]indenyl)zirconiumdimethyl, and other metallocene compounds obained by replacing zirconium of the above metallocene compounds with titanium or hafnium. Still further compounds include ethylene(t-butylamide)(cyclopentadienyl)zirconium dichloride, ethylene (t-butylamide)(tetramethylcyclopentadienyl)zirconium dichloride, dimethylsilylene(t-butylamide) (tetramethylcyclopentadienyl)zirconium dichloride, dimethylsilylene(t-butylamide)(indenyl)zirconium dichloride, dimethylsilylene(t-butylamide)(fluorenyl)zirconium dichloride(tetrahydrofuran), dimethylsilylene(t-butylamide) (fluorenyl)zirconium dichloride(diethyl ether), ethylene(t-butylamide)(cyclopentadienyl)zirconium dimethyl, ethylene(t-butylamide)(tetramethylcyclopentadienyl), zirconium dimethyl, dimethylsilylene(t-butylamide) (tetramethylcyclopentadienyl)zirconium dimethyl, dimethylsilylene(t-butylamide)(indenyl)zirconium dimethyl, dimethylsilylene(t-butylamide)(fluorenyl)zirconium, dimethyl(tetrahydrofuran), and dimethylsilylene(t-butylamide)(fluorenyl)zirconium diphenyl, and other metallocene compounds obtained by replacing zirconium of the above metallocene compounds with titanium or hafnium. In the polymer which is a support insoluble in the inert organic solvent of the invention and contains a carbonyl-having group represented by the general formula [1], Q is selected from hydrogen, hydroxy, alkyl, aryl, alkoxy, aryloxy, oxycarbonyl, halogen, amino, aminocarbonyl, hydrazino and oxyanion groups. The support which is insoluble in the inert hydrocarbon compound brings the organic aluminum oxy compound into contact with said polymer. Specifically, when Q contains hydrogen or oxygen in the carbonyl-having group of the general formula [1], the functional group is formyl (or aldehyde) or carboxy, respectively. When Q is alkyl or aryl, the functional group is alkyl ketone or aryl ketone, respectively. In such cases, alkyl has preferably 1 - 20 carbon atoms and specifically includes methyl, ethyl, propyl, butyl, pentyl, hexyl, isopropyl, tert-butyl, neopentyl, cyclopentyl, cyclohexyl and menthyl. Aryl has preferably 6 - 20 carbon atoms, and includes phenyl, tolyl, xylyl, naphthyl and anthryl. When Q is alkyloxy or aryloxy, the functional group is so-called ester, and is alkoxycarbonyl or aryloxycarbonyl, respectively. Alkoxy has preferably 1 - 20 carbon atoms and includes specifically methoxy, ethoxy, propoxy, butoxy, pentoxy, hexyloxy, isopropoxy, tert-butoxy, neopentoxy, cyclopentoxy, cyclohexyloxy and menthoxy. Aryloxy has preferably 6 - 20 carbon atoms and includes phenoxy, tolyloxy, xylyloxy, naphthyloxy and anthryloxy. When Q is oxycarbonyl, the functional group is carboxylic acid anhydride. When Q is halogen, the functional group is haloformyl and halogen is selected from fluorine, chlorine, bromine and iodine. When Q is amino, aminocarbonyl, or hydrazino, the functional group is respectively amide(carbamoyl), imide and hydrazide. Hydrogen on these functional groups can be substituted with, for example, methyl, ethyl, propyl, butyl, isopropyl, tert-butyl, cyclopentyl, cyclohexyl or other alkyl groups or phenyl, tolyl or other aryl groups. When Q is oxyanion, the functional group is carboxyanion and cation pair includes ammonium, sodium, potassium, calcium, magnesium, zinc and tin. The polymer which contains the carbonyl-having group represented by the formula [1] of the invention is obtained by grafting or graft polymerization of an unsaturated monomer containing the carbonyl-having group on the polymer which has no functional group, this latter polymer is polyethylene, polypropylene, ethylene propylene copolymer, polybutene, ethylene-butene copolymer, ethylene propylene butene copolymer, polyisobutene, polypentene, poly-4-methylpentene, polynorbornene, polybutadiene, polyisoprene, polystyrene or poly-α-methylstyrene, The unsaturated compound comprising the carbonyl-having group includes, for example, methacrylic acid, acrylic acid, and other acrylic acids; methyl methacrylate, 3-methacryloxypropyltrimethoxysilane, methyl acrylate and other acrylate esters; methacrylamide, acrylamide, crotonamide and other acrylamides; vinyl acetate, methyl vinyl ketone, acryloyl chloride, acrylaldehyde and other vinyl compounds; maleic anhydride, itaconic anhydride and other carboxylic acid anhydrides; maleic acid, itaconic acid and other dicarboxylic acids. No particular restriction is imposed upon the process of preparation of the polymer containing the carbonyl-having group represented by the above general formula [1]. Reaction in an organic or aqueous medium, gas phase reaction, gas/solid reaction, solventless bulk reaction, melt-kneading reaction and other any type of reaction can be applied to the preparation of the polymer. The content of the functional group in said polymer is 1 x 10 -6 - 1 x 10 -2 mol, preferably 1 x 10 -5 - 1 x 10 -3 mol per 1 g of said polymer. The support which is insoluble in the inert organic solvent in the invention is more preferably the organic polymer obtained by grafting or graftpolymerizing on polypropylene an unsaturated compound containing the carbonyl having group. The support may be more specifically a polymer obtained by grafting maleic anhydride, itaconic anhydride, methacrylic acid, acrylic acid, methyl methacrylate, 3-metharyloxypropyltrimethoxysilane or methyl acrylate, on polyethylene, polypropylene, polybutene, polyisobutene, polypentene, poly-4-methylpentene, polynorbornene, polybutadiene, polyisoprene, polystyrene, poly-α-methylstyrene and other polyolefins. The support also includes an organic polymer obtained, after such grafting or graftpolymerizing, by at least partially modifying or denaturing the functional group which is already grafted on the polymer by reactions such as esterification, amidation, haloformylation and acylation. The preferably exemplified support which is insoluble in the inert organic solvent in the invention supports the organic aluminum oxy compound on the organic polymer by bringing the organic aluminum oxy compound into contact with the organic polymer Containing the above carbonyl-having group. The organic aluminum oxy compound is maintained on the support by chemical bond with the organic polymer. Consequently, concerning the configuration of the catalyst system comprising of the organic transition material compound which is soluble in the inert organic solvent and the support which is insoluble in the inert organic solvent, it is assumed that the organic transition metal compound is maintained by way of the organic aluminum oxy compound which is supported on the organic polymer containing carbonyl-having group, and the transition metal compound is not maintained directly on the organic polymer by chemical bonding with carbonyl group of the organic polymer or by impregnation with the organic polymer. The organic aluminum oxy compound which is used in the invention is conventionally known aluminoxane wich may be represented by the general formula [4] or the general formula [5]: the general formula [5]: wherein R 5 can be the same or different and is an alkyl e.g. of 1 - 6 carbon atoms, aryl e.g. of 6-18 carbon atoms, or hydrogen, and p is an integer of 2-50, preferably 10-35. An organic aluminum compound can be mixed with the above organic aluminum oxy compound. In the invention, the process for bringing the organic aluminum oxy compound into contact with the polymer containing the carbonylhaving group and being a support insoluble in the inert organic solvent, includes the below described processes. (A) A process for bringing the organic aluminum oxy compound into contact with a polymer containing the carbonyl-having group which is dissolved in a hot, inert organic solvent (B) A process for bringing the organic aluminum oxy compound into contact with a polymer containing the carbonyl-having group which is suspended in an inert organic solvent. (C) A process for bringing the organic aluminum oxy compound into contact with a powdery a polymer containing the carbonyl-having group. The inert organic solvents used in the processes (A) and (B) are alkane, aromatic hydrocarbon, ether or halogenated hydrocarbon, preferably alkane of 1 - 20 carbon atoms, aromatic hydrocarbon of 6 - 20 carbon atoms, ether of 2 - 20 carbon atoms, and halogenated hydrocarbon of 1 - 20 carbon atoms. More specifically, these solvents include pentane, heptane, octane, isobutane, neopentane, cyclopentane, decalin and other alkanes; benzene, toluene, xylene and other aromatic hydrocarbons; diethyl ether, tetrahydrofuran, 1,2-dimethoxyethane, dioxane and other ethers; and dichloromethane, chloroform and other halogenated hydrocarbons. The inert organic solvents can be a mixture of the same. In the process (A), the polymer containing the carbonyl-having group and being insoluble at room temperature in the inert organic solvent, is dissolved in the inert organic solvent by heating to the contact temperature range of 40 - 250°C, preferably 60 - 200°C. The solution thus obtained is brought into contact with the organic aluminum oxy compound for 10 minutes to 24 hours. A powdery polymer compound which supports the organic aluminum oxy compound can be obtained from the above solution after contact treatment by, for example, the process shown below. 1 Solid component precipitates by cooling. 2 Solid component precipitates by adding a poor solvent to the solution. 3 Solution is sprayed from a nozzle into the poor solvent to precipitate the solid component. 4 The solution is sprayed with a spray drier into a solvent evaporating atmosphere to obtain powdery product. 5 Solvent is removed from the solution and the dried residue is ground by a vibration mill or ball mill. Operation temperature of 1 - 5 is lower than the melting point of the polymer. In the process (B), said polymer is suspended in the inert organic solvent and is brought into contact with the organic aluminum oxy compound at the contact temperature range of -80°C- 200°C, preferably -20°C- 150°C, for 10 minutes to 24 hours. A poor solvent is added to the suspension after contact treatment to precipitate the solid component. Alternatively, the solvent is removed from the suspension and the residue is ground by a vibration mill or ball mill. The process (C) is most simple. The polymer containing the carbonyl-having group is ground into powder substantially in the absence of solvent with a mixer or mill. In the operation, the organic aluminum oxy compound is added and brought into contact with the powdery polymer in a contact temperature range of -80°C - 200°C, preferably -20°C - 150°C for a contact time of 30 minutes to 24 hours. The obtained powder can also be suspended in a poor solvent. In the above processes (A) - (C), the proportion of the polymer containing the carbonyl-having group to the organic aluminum oxy compound is 1 x 10 -5 - 0.1 mol, preferably 1 x 10 -4 - 0.01 mol of aluminum in the organic aluminum oxy compound for 1 g of said polymer. In the present invention, the polymer which is obtained in the above processes (A) - (C), supporting the organic aluminum oxy compound, and containing carbonyl-having group is preferably washed with the inert organic solvent to remove unsupported organic aluminum oxy compound for preventing adhesion of the organic aluminum oxy compound on the inner wall of the reactor. The washing method is to suspend in the inert organic solvent the polymer which supports the organic aluminum oxy compound, or after rinsing the inert organic solvent to said polymer, washed product is obtained by filtration, decantation or centrifugation. The inert organic solvent preferably dissolves unsupported organic aluminum oxy compound and cannot dissolve the polymer which supports the organic aluminum oxy compound. No particular limitation is imposed upon the amount of washing solvent and washing cycle. Washing temperature is lower than the melting point of the polymer. In the process for polymerizing an olefin by using the catalyst system comprising the organic transition metal compound which is soluble in the inert organic solvent of the invention and the support which is insoluble in the inert organic solvent, the proportion of the polymer which supports, the organic aluminum oxy compound to the organic transition metal compound is 1 - 10000, preferably 10 - 2000 in the mol ratio of aluminum/transition metal. An olefin can be polymerized by using the catalyst system according to the invention comprising the organic transition metal catalyst and the support which supports the organic aluminum oxy compound. When an organic metal compound different from the organic aluminium oxy compound is used in combination, with the organic transition metal compound, preferable results are expected. The organic metal compounds which can be used in combination in the polymerization of olefin comprise metals selected from groups 1, 2, 12, and 13 in the periodic table. Specifically, the organic metal compound consists of lithium, sodium, potassium, beryllium, magnesium, zinc, cadmium, aluminum, gallium and alkyl of 1-20 carbon atoms. Particularly preferred is an alkylaluminum compound having 1 - 20 carbon atoms. Specific examples of alkylaluminum compound include trimethylaluminum, triethylaluminum, tri-n-propylaluminum, triisopropylaluminum, tri-n-butylaluminum, triisobutylaluminum, tri-sec-butylaluminum, dimethylaluminum chloride, diethylaluminum chloride, di-n-propylaluminum chloride, diisopropylaluminum chloride, di-n-butylaluminum chloride, diisobutylaluminum chloride, and di-sec-butylaluminum chloride. Particularly preferred compounds are trimethylaluminum, triethylaluminum, tri-n-butylaluminum, triisobutylaluminum, and tri-sec-butylaluminum. The proportion of the organic metal compound to the organic transition metal compound which is soluble in the inert organic solvent may be 1 - 10000, preferably 10 - 1000 in the mol ratio of the polymer organic transition metal compound. The proportion of the organic metal compound to the organic aluminum oxy compound supported on the polymer may be 0.01 - 100, preferably 0.1 - 10 in the mol ratio of aluminum in the polymer /organic metal compound. The invention can use an inert organic solvent for the preparation of an olefin polymerization catalyst system , when necessary. The inert organic solvent which can be preferably used are propane, butane, pentane, hexane, heptane, octane, nonane, decane, cyclopentane, cyclohexane and other alkanes; and benzene, toluene, xylene and other aromatic hydrocarbons; and a mixture of these solvents. The temperature used when preparing the catalyst from the organic transition metal catalyst and the polymer which supports organic aluminum oxy compound is - 80°C - 250°C, preferably -20°C - 200°C, and the catalyst preparation time is 10 minutes to 3 days, preferably 20 minutes to 24 hours. The catalyst system of the invention which comprises of the organic transition metal compound and support can be used after previously subjecting to polymerization or copolymerization of a small amount of an olefin. The procedure can provide the effect of improving bulk density of the generated polymer. The amount of previously polymerized or copolymerized an olefin is 0.1 - 300 g, preferably 0.5 - 100 g per 1 g of the solid catalyst. The preparation method of the solid catalyst by previously polymerizing a small amount of an olefin, can be applied to a slurry polymerization process which polymerizes olefin in an inert hydrocarbon, bulk polymerization process which polymerizes an olefin in a liquefied monomer, or gas phase polymerization process which polymerizes in a gaseous olefin monomer. Polymerization temperature is usually -100-200°C, preferably -20 - 100°C. No particular limitation is imposed upon the reaction pressure. The polymerization can be supported out batch wise, semibatch wise, and continuously. Olefins which can be polymerized by the catalyst system of the invention are α-olefins (including ethylene) e.g. of 2 - 20 carbon atoms, preferably 2 - 10 carbon atoms, and specifically include ethylene, propylene, 1-butene, 3-methyl-1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, vinylcyclohexane and styrene. Olefins further include butadiene, 1,4-pentadiene, 1,5-hexadiene, 1,4-hexadiene and other dienes having 4 - 20 carbon atoms; dicyclopentadiene, norbornene, methylnorbornene, tetracyclododecene and other cyclic olefins; and allyltrimethylsilane, vinyltrimethylsilane and other silicon containing olefins. These olefins can be used singly or as a mixture. In the invention, an olefin polymerization can be carried out by slurry polymerization, bulk polymerization and gas phase polymerization. The catalyst system of the invention can also be used for solution polymerization. Polymerization temperature is usually -100°C -200°C, preferably -20°C - 100°C. Polymerization pressure may be 1 to 80 bar (atmospheric pressure - 80 kgf/cm 2 ). Molecular weight of an olefin polymer can be controlled by using hydrogen and other molecular weight regulators. EXAMPLES The invention will be hereinafter illustrated further in detail by way of examples. However, these examples are not to be construed to limit the scope of the invention. Melting point (Tm), molecular weight distribution index (PDI), inherent viscosity ([η]), and fish eye or Gel(FE) were measured by the following methods. o Melting point (Tm): Melting point was measured with a differential scanning calorimeter (DSC) under following conditions. Apparatus: Perkin-Elmer DSC-4 Temperature rise rate: 10°C/min. Temperature falling rate: -10°C/min. or -30°C/min. o Molecular weight distribution index (PDI = Mw/Mn): Number average molecular weight (Mn) and weight average molecular weight (Mw) were measured by gel permeation chromatography under following conditions. Apparatus Waters 150 cv plus Column Shodex GPC AD-80 M/S (exclusion limit: 2 × 10 7 ) Eluent 1,3,5-trichlorobenzene Column temperature 135°C Flow rate at measurement 1.0 ml/min Sample concentration 0.2 wt/vol % Injector volume 0.200 ml Detector differential refractometer and viscometer Reference sample polystyrene standard o Inherent viscosity ([η]): Viscosity was measured at 135°C in tetralin solvent and shown in dl/g unit. o Fish eye or Gel (FE): To 100 parts by weight of polypropylene powder obtained by polymerization, 0.3 part by weight of 3,5-di-t-butyl-4-hydroxytoluene was added and mixed. The mixture was pelletized at 250'C. The pellet was successively melt-extruded with a 20 mm extruder at a resin temperature of 250'C and delivered through a down-flow T-die to obtain a film having a thickness of 40 µm. Numbers of fish-eye having a size of 100 µm or more and less than 100 µm were counted for each area of 600 cm 2 on the film. Example 1 [Preparation of organic aluminum oxy compound supported on polymer (A)] In 200 ml four necked flask sufficiently replaced with nitrogen, 5 g of maleic anhydride grafted polypropylene (maleic anhydride content: 10 wt%, 1 mmol/g), which was obtained according to the process of Japanese published patent SHO 59-14488, was suspended in 45 ml of toluene. To the suspension, 38 ml of a toluene' solution which contains 2.7 g of methylaluminoxane (manufactured by Albemarle Co. methylaluminoxane content of 8 wt%) was added and then heated with stirring at 80°C for 6 hours. The reaction mixture was cooled to room temperature, and allowed to stand. Pale yellow solid was precipitated. Supernatant was separated by decantation, 50 ml of toluene was added, and the mixture was heated at 70°C for 30 minutes, and allowed to stand at room temperature. These procedures were repeated three times. After removal of supernatant and drying in vacuo, 5.2g was obtained as pale yellow solid catalyst component(A). The solid component had 3 mmol/g as aluminum content. [Polymerization of propylene] In 50 ml two necked flask sufficiently replaced with nitrogen, 480 mg of the above-obtained pale-yellow solid catalyst component (A) was suspended in 20 ml of heptane. 1.0 mg of diphenylmethylene-(cyclopentadienyl)(fluorenyl)zirconium dichloride which was prepared according to the process of Japan Laid-Open HEI 2-274703 and 0.128 g of triisobutylaluminum were successively added to the suspension for the preparation of the catalyst. Into 5 liter stainless steel autoclave sufficiently replaced with nitrogen, successively with propylene, the above prepared catalyst was introduced. Then 1.5 kg of propylene and 2N liters of hydrogen were introduced and heated. Polymerization was carried out at 60°C for 1 hour. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. Polymer yield was 430 g. The obtained polymer had inherent viscosity [η] of 1.42 dl/g, PDI of 2.4, Tm of 133°C, and bulk density of 0.36 g/ml. The numbers of FE (fish eye or Gel) were 3 FE as 100 µm or more and 10 FE as less than 100 µm. Example 2 [Preparation of organic aluminum oxy compound supported on polymer (B)] In 1 liter four necked flask sufficiently replaced with nitrogen, 20 g of maleic anhydride grafted polypropylene (Mw: 43500, maleic anhydride content of 6.7 wt%) was suspended in 200 ml of toluene. To the suspension, 135 ml of a toluene solution of methylaluminoxane (manufactured by Albemarle Co. methylaluminoxane content of 8 wt%) was added under nitrogen, heated with stirring at 80°C for 6 hours and then cooled to 40°C. The solvent was evaporated in vacuo. To the obtained yellow-solid, 300 ml of hexane was added, washed with stirring and allowed to stand. 220 ml of supernatant was separated by inverse filtration. The residue was further washed with 400 ml of toluene and 350 ml of the solvent was removed by inverse filtration. These procedures were repeated three times and then all solvents were removed in vacuo to give 24.8 g as pale yellow solid catalyst. The solid catalyst component (B) was prepared by grinding the pale yellow solid in a ball mill. The solid component had 3.6 mmol/g as aluminum content. [Polymerization of propylene] Polymerization of propylene was carried out according to the procedure described in Example 1, but using 240 mg of the above pale yellow solid catalyst component (B) and 3N liters of hydrogen instead of 480 mg of solid catalyst component (A) and 2N liters of hydrogen. No adhesion or fouling of the polymer was observed at all on the inner wall, stirrer blade, and shaft of the autoclave. Polymer yield was 490 g. The obtained polymer had an inherent viscosity [η] of 1.22 dl/g, PDI of 2.4, Tm of 133°C, and bulk density of 0.36 g/ml. The number of FE were 8 fisheyes as 100 µm or more and 30 fisheyes less than 100 µm. Example 3 (Preparation of organic aluminum oxy compound supported on polymer (C)] In 500 ml four necked flask which was sufficiently replaced with nitrogen, 1 g of maleic anhydride grafted polypropylene (maleic anhydride content: 10 wt%, 1 mmol/g) was suspended in 400 ml of xylene. The suspension was heated at reflux until the grafted polypropylene was completely dissolved. To the boiling solution, 10 ml of a toluene solution containing 0.68 g of methylaluminoxane (manufactured by Albemarle Co., methylaluminoxane content of 8 wt.%) was added dropwise via a dropping funnel and refluxed for 4 hours. The reaction mixture was gradually cooled to room temperature over 12 hours and allowed to stand in order to precipitate pale yellow solid component. The supernatant was removed by decantation, 100 ml of toluene was added and stirred at 20°C for 30 minutes and then the mixture was allowed to stand. These washing procedures were repeated three times, the supernatant was removed and the suspension containing the solid component (C) was obtained. The solid component concentration in this suspension was 0.31 g/ml. Aluminum content was 6 mmol/g as measured this solid component which was dried in vacuo from a certain amount of suspension. [Polymerization of propylene] In 100 ml two necked flask which was sufficiently replaced with nitrogen in advance, 0.77 ml of the above suspension, 20 ml of heptane, 1.0 mg of diphenylmethylene (cyclopentadienyl)(fluorenyl)zirconium dichloride, and 0.128 g of triisobutylaluminium were added for catalyst preparation. Into 5 liter stainless steel autoclave which was replaced with a nitrogen well and then with propylene, the above catalyst was introduced, 1.5 kg of propylene and 3N liters of hydrogen were introduced. The mixture was heated at 60°C and polymerization was carried out for 1 hour while maintaining the temperature. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirring blade and shaft of the autoclave. Polymer yield was 490 g. The obtained polymer had an inherent viscosity [η] of 1.22 dl/g, PDI of 2.4, Tm of 134°C and bulk density of 0.36 g/m. The numbers of FE were 3 fisheyes as 100 µm or more and 10 fisheyes as less than 100 µm. Example 4 [Preparation of organic aluminum oxy compound supported on polymer (D)] It was performed according to the procedure described in Example 3, but removing all solvent in vacuo from the suspension after removed of the supernatant to give 1.2 g as pale yellow solid component having 6 mmol/g as aluminum content. [Polymerization of propylene] It was performed according to the procedure described in Example 3, but using 240 mg of the pale yellow solid catalyst component (D) instead of the suspension containing the solid component [C]. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirring blade and shaft of the autoclave. The polymer yield was 489.9 g. The polymer obtained had an inherent viscosity [µ] of 1.12 dl/g, PDI of 2.4, Tm of 134°C and bulk density of 0.36 g/ml. The numbers of FE were 3 fisheyes as 100 µm or more and 10 fisheyes as less than 100 µm. Example 5 [Preparation of organic aluminum oxy compound supported on polymer (E)] In 3 liter four necked flask which was sufficiently replaced with nitrogen, 4.2 g of maleic anhydride grafted polypropylene (Mw: 43500, maleic anhydride content: 6.7 wt%, 0.68 mmol/g) was suspended in 1.7 liter of xylene. The suspension was heated at 145°C and completely dissolved. 28 ml of a toluene solution of methylaluminoxane (manufactured by Albemarle Co., methylaluminoxane content of 8 wt%) was added dropwise to the solution by using a dropping funnel under nitrogen, at reflux for 4 hours, and cooled to 40°C. To the reaction mixture, 200 ml of hexane was added and stirred for 30 minutes. After allowing to stand the resultant mixture, 1.6 liter of the supernatant was removed by inverse filtration. After adding 400 ml of toluene, the resulting suspension was stirred for 30 minutes, allowed to stand, and 400 ml of supernatant was removed by inverse filtration. The toluene washing procedures were repeated 3 times. 6.0 g of a pale yellow solid was obtained by drying in vacuo. The solid catalyst component (E) was prepared by further grinding the solid product with a vibration mill. The solid component had an aluminum content of 4.7 mmol/g. [Polymerization of propylene] It was performed according to the procedure described in Example 3, but using 240 mg of the above pale yellow solid component(E) instead of the solid catalyst component (C). No adhesion or fouling of the polymer was observed all on the inner wall., stirrer blade and shaft of the autoclave. Polymer yield was 620 g. The polymer obtained had an inherent viscosity [η] of 1.29 dl/g, PDI of 2.1, Tm of 134°C and bulk density of 0.31 g/ml, The numbers of FE were 12 fisheyes as 100 µm or more and 30 fisheyes as less than 100 µm pieces. Example 6 [Preparation of (1R,2R)-1,2-dimethylethylene bis(2'-methylbenz[e]indenyl)zirconium dichloride) Trifluoromethanesulfonic anhydride (18.80 g) was added to a mixture of (2R,3R)-2,3-butanediol (ee = 99.0%) (3-00 g) and a solution of pyridine (5.25 g) in dichloromethane (100 ml)in ice bath and then stirred for 1 hour. Water was added to the reaction mixture, the organic layer was separated and dried over anhydrous magnesium sulfate. The product was passed through a silica gel column with hexane, concentrated and distilled to give (2R,3R)-2,3-butyldi(trifurate) as colorless liquid (5.31 g, 43°C/3 mmHg (about 399 Pa). Then to a solution of (2-methylbenz[e]indenyl)lithium (1.2 g) in tetrahydrofuran (hereinafter simply referred to THF) (50 ml) under nitrogen, a THF solution (10 ml) of (2R,3R)-2,3-butyldi (trifurate) (3.46 g) was added dropwise at -78°C, stirred at room temperature overnight and a saturated aqueous solution tion of ammonium chloride was added. The organic layer. was separated, dried over anhydrous magnesium sulfate and evaporated to give orange oil. This oil was passed through a silica gel column with a mixture of hexane/ethyl acetate and all solvents were removed to give a yellow solid. The solid was recrystallized from benzene to give (2R,3R)-2,3-bis(2-methylbenz[e]indenyl)butane (0.50 g) as colorless crystal. Further, a solution of the colorless crystal (310 mg) in THF (20 ml) was added dropwise at 0°C to a suspension of the excess amount of potassium hydride (95 mg) in THF (30 ml), stirred at room temperature overnight and filtrated through celite. The filtrate was added dropwise at room temperature to a suspension of zirconium tetrachloride (280 mg, 0.74 mmol) in THF (30 ml) and stirred at room temperature overnight. After removing the solvent, the residual yellow solid was extracted by Soxhlet extraction with toluene. The toluene solution was concentrated to give yellow solid (200 mg). Analytical data are listed below. 1 H-NMR (90 MHz, CDCl 3 , TMS.standard) δ; 7.67-7.86 (m, 4H), 7.35-7.58 (m, 6H), 7.00-7.29 (m, 4H), 3.48 (g, 2H), 1.26 (s, 6H), 1.24 (d, 6H). Elemental analysis; C H Calculated 66.88 4.91 Found 66.97 4.98 [Polymerization of propylene] Into 50 ml two necked flask which was sufficiently replaced with nitrogen in advance, 480 mg of the solid catalyst component (A) which was prepared in Example 1 and 20 ml of heptane were introduced and added 1.0 mg of the above obtained (1R,2R)-1,2-dimethylethylenebis,(2-methylbenz[e]indenyl)zirconium dichloride and 0.128 g of triisobutylaluminum for catalyst preparation. Into 5 litre stainless steel autoclave which was sufficiently replaced with nitrogen and successively with propylene, the above prepared catalyst was introduced and 1.5 kg of propylene was introduced. The mixture was heated and polymerization was carried out at 50°C for 1 hour. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirring blade and shaft of the autoclave. Polymer yield was 600 g. The polymer obtained had an inherent viscosity [η] of 1.58 dl/g, PDI of 2.6, Tm of 148°C and bulk density of 0.38 g/ml. The numbers of FE were 3 fisheyes as 100 µm or more and 10 fisheyes less than 100 µm. Example 7 Polymerization was performed according to the procedure described in Example 6, but using 360 mg of the solid catalyst component (E) prepared in Example 5, and polymerizing at 60°C. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirring blade and shaft of the autoclave. Polymer yield was 680 g. The obtained polymer had an inherent viscosity [η] of 1.50 dl/g, PDI of 2.3, Tm of 149°C and bulk density of 0.34 g/ml. The numbers of FE were 16 fisheyes as 100 µm or more and 40 fisheyes as less than 100 µm. Example 8 [Catalyst component prepared by previous polymerization with a small amount of propylene] In 50 ml two necked flask which was sufficiently replaced with nitrogen, 1 g of pale yellow solid catalyst component (A) prepared in Example 1 and 60 ml of heptane were suspended and then added successively 3.0 mg of diphenylmethylene(cyclopentadienyl)(fluorenyl)zirconium dichloride used in Example 1 for catalyst preparation. Propylene was introduced into the catalyst via feed tube at 25°C for 30 minutes under ambient pressure to prepare the catalyst with 2 g of polypropylene. [Polymerization of propylene] Into 5 liter stainless steel autoclave which was sufficiently replaced with nitrogen and successively with propylene, 0.128 g of triisobutylaluminum diluted in 20 ml of heptane was introduced and then 20 ml of the above catalyst slurry which was prepared by prepolymerizing propylene was introduced. Successively, 1.5 kg of propylene and 2N liters of hydrogen were introduced and then polymerized at 60°C for 1 hour. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirring blade or shaft of the autoclave. Polymer yield was 400 g. The obtained polymer had an inherent viscosity [η] of 1.40 dl/g, PDI of 2.4, Tm of 134°C and bulk density of 0.36 g/ml. The numbers of FE were 3 fisheyes as 100 µm or more and 10 fisheyes as less than 100 µm. Comparative Example 1 [Preparation of catalyst component consisting of maleic anhydride and organic aluminum oxy compound] In 300 ml four necked flask which was sufficiently replaced with nitrogen, 0.37 g (3.7 mmol) of maleic anhydride was added to 30 ml of toluene, successively, 28 ml of a toluene solution containing 2.0 g of methylaluminoxane (manufactured by Albemarle Co., methylaluminoxane content of 8 wt.%) was added, heated with stirring at 80°C for 6 hours, and cooled to room temperature. The obtained yellow reaction mixture had no solid precipitate. However, the mixture was divided into two layers, that is, a dark yellow layer and a pale yellow layer, though the interface was obscure. The pale yellow upper layer was separated, 60 ml of toluene was added, stirred for 30 minute at room temperature and allowed to stand. Such washing procedures were repeated four times. The upper layer was removed, the residue was dried in vacuo to give 1.7 g as white solid catalyst component. The solid component had 16 mmol/g as aluminum component. [Polymerization of propylene] In 50 ml two necked flask which was sufficiently replaced with nitrogen, 240 mg of the above white solid catalyst component was suspended in 20 ml of heptane. The catalyst was prepared by successively adding 1.0 mg of diphenylmethylene(cyclopentadienyl)(fluorenyl) zirconium dichloride which was used in Example 1 and 0.128 g of triisobutylaluminum. This catalyst was introduced into 5 liter stainless steel autoclave which was sufficiently replaced with nitrogen and then with propylene. Polymerization was performed according to the procedure described in Example 1. Terrible adhesion or fouling of the polymer in the polymerization was observed on the inner wall, stirrer blade and shaft of the autoclave. Polymer yield was 155 g. The polymer had an inherent viscosity [η] of 1.29 dl/g, PDI of 2.4, Tm of 130°C and bulk density of 0.20 g/ml. Comparative Example 2 [Preparation of catalyst component consisting of maleic anhydride and organic aluminum oxy compound] In 300 ml four necked flask which was sufficiently replaced with nitrogen, 0.55 g (5.5 mmol) of maleic anhydride was added to 30 ml of toluene and 2.8 ml of a toluene solution containing 2.0 g of methylaluminoxane (manufactured by Albemarle Co., methylaluminoxane content of 8 wt.%) was added. The mixture was heated with stirring at 80°C for 8 hours, cooled to room temperature and allowed to stand. The pale yellow solid was precipitated. The supernatant were removed by decantation, and 50 ml of toluene was added, heated at 70°C for 30 minutes, and allowed to stand. Such washing procedures were repeated 3 times. After removal of the supernatant, the solid was dried in vacuo to give 2.1g of pale yellow solid catalyst component. The solid component had 17 mmol/g as aluminum content. [Polymerization of propylene] In 50 ml two necked flask which was sufficiently replaced with nitrogen, 480 mg of the above pale yellow solid component was suspended in 20 ml of heptane. The catalyst was prepared by successively adding 1.0 mg of diphenylmethylene(cyclopentadienyl)(fluorenyl)zirconium dichloride used in Example 1 and 0.128 g of triisobutylaluminium Into 5 liter stainless steel autoclave which was replaced with nitrogen and then with propylene, the above prepared catalyst was introduced and 1.5 kg of propylene and 3.3 N liters of hydrogen were introduced. The temperature was elevated and polymerization was carried out at 60'C for 1 hour. Terrible adhesion or fouling of the polymer in the polymerization was observed on the inner wall, stirrer blade and shaft of the autoclave. Polymer yield was 10 g. The polymer obtained had an inherent viscosity [η] of 0.89 dl/g, PDI of 3.2, Tm of 126°C and bulk density of 0.26 g/m. Comparative Example 3 [Preparation of catalyst component consisting of organic aluminum oxy compound and silica] According to the procedure described in example concerning catalyst A (in catalyst preparation) in Japan Laid-Open SHO 61-296008, 5 g of silica : SILDEX H-121 (manufactured by Asahi glass Co.) was suspended in 25 ml of toluene. Silica was treated with aluminoxane by adding 45 ml of toluene solution of methylaluminoxane which was used in Example 1 to give 7.4g as solid catalyst component. The solid component had 6 mmol/g as aluminum content. [Polymerization of propylene] In 50 ml two necked flask which was sufficiently replaced with nitrogen, 60 mg of the above solid catalyst component was suspended in 20 ml of heptane. The catalyst was prepared by successively adding 1.0 mg of diphenylmethylene(cyclopentadienyl)(fluoroenyl)zirconium dichloride used in Example 1 and 0.128 g of triisobutylaluminum. Into 5 liter stainless steel autoclave which was sufficiently replaced with nitrogen and then with propylene, the above prepared catalyst was introduced and polymerization was carried out by the procedure described in Comparative Example 2. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. Polymer yield was 500 g. The obtained polymer had an inherent viscosity [η] of 1.38 dl/g, PDI of 2.6, Tm of 130°C and bulk density of 0.37 g/ml. The numbers of FE (fish eye) were 100 fisheyes as 100 µm or more and 6000 fisheyes as less than 100 µm. Comparative Example 4 In 50 ml two necked flask which was sufficiently replaced with nitrogen, to 23.8 ml of a toluene solution which contains 1.7 g of methylaluminoxane (manufactured by Albemarle, methylaluminoxane content of 8 wt%) in 10 ml of toluene was added. 2.0 mg of diphenylmethylene (cyclopentadienyl)(fluorenyl)zirconium dichloride to prepare the catalyst. Into 5 liter stainless steel autoclave which was sufficiently replaced with nitrogen and then with propylene, the above prepared catalyst was introduced, 1.5 kg of propylene and 3N liters of hydrogen were introduced, temperature was elevated to 60°C, and polymerization was carried out for 1 hour at 60°C. Terrible adhesion or fouling of the polymer in the polymerization was observed on the inner wall, stirring blade and shaft of the autoclave. Polymer yield was 495 g. The obtained polymer had an inherent viscosity [η] of 1.67 dl/g, PDI of 2.1, Tm of 140°C, Tm of 140°C and bulk density of 0.20 g/ml. The numbers of FE (fish eye) were 7 fisheyes as 100 µm or more and 14 fisheyes less than 100 µm. Comparative Example 5 In 50 ml two necked flask which was sufficiently replaced with nitrogen, 100 mg of solid catalyst component prepared in Comparative Example 3 was suspended in 20 ml of heptane. The catalyst was prepared by successively adding 1.0 mg of (1R, 2R)-1,2-dimethylethylenebis(2'-methylbenz[e]indenyl)zirconium dichloride used in Example 6 and 0.16 g of triisobutylaluminum. Into 5 liter stainless steel autoclave which was sufficiently replaced with nitrogen and then with propylene, the above prepared catalyst was introduced and polymerization was carried out by the procedure described in Comparative Example 3. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirring blade or shaft of the autoclave. Polymer yield was 467 g. The polymer obtained had an inherent viscosity [η] of 1.67 dl/g, PDI of 2.5, Tm of 142°C and bulk density of 0.38 g/ml. The numbers of FE were 300 fisheyes as 100 µm or more and 9000 fisheyes as less than 100 µm. Example 9 (Synthesis of isopropylidene(cyclopentadienyl) (2,7-di-tert-butylfluorenyl)zirconium dichloride] The entitled compound was prepared according to Japanese Laid-Open HEI 5-125112. Analytical data are listed below. 1 H-NMR (90 MHz, C 6 D 6 , TMS standard) δ ; 7.93-7.50 (m, 6H), 6.16 (dd, 2H), 5.58 (dd, 2H), 2.08 (s, 6H), 1.34 (s, 18H) Elemental Analysis C H Calculated 63.94 6.20 Found 64.07 6.68 [Polymerization of propylene] It was performed according to the procedure described in Example 5, but using 2.0 mg of isopropylidene(cyclopentadienyl)(2,7-di-tert-butylfluorenyl)zirconium dichloride instead of 1.0 mg of diphenylmethylene (cyclopentadienyl)(fluorenyl)zirconium dichloride. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. The polymer yield was 397 g. The obtained polymer had an inherent viscosity [η] of 0.70 dl/g, PDI of 2.3, Tm of 137°C and bulk density of 0.35 g/ml. The numbers of FE were 8 fisheyes as 100 µm or more and 40 fisheyes less than 100 µm. Example 10 [Synthesis of ethylenebis(indenyl)zirconium dichloride] The entitled compound was prepared according to the literature by Scott Collins et al in Journal of Organometallic Chemistry 342, 21 (1988). Analytical data are listed below. 1 H-NMR (90 MHz, C 6 D 6 , TMS Standard) δ; 7.33-6.70 (m, 8H), 6.41 (d, 2H), 5.73 (d, 2H), 3.05 (q, 4H) [Polymerization of propylene] It was performed according to the procedure described in Example 5, but using 2.0 mg of ethylenebis (indenyl)zirconium dichloride instead of 1.0 mg of diphenylmethylene(cyclopentadienyl)(fluorenyl)zirconium dichloride. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. The polymer yield was 97 g. The obtained polymer had an inherent viscosity [η] of 0.40 dl/g, Tm of 133°C and bulk density of 0.36 g/ml. The numbers of FE were 14 fisheyes as 100 µm or more and 50 fisheyes as less than 100 µm. Comparative Example 6 In 50 ml two necked flask which was sufficiently substituted with nitrogen, 60 mg of the solid catalyst component prepared in Comparative Example 3 was suspended in 20 ml of heptane. Successively, propylene. was polymerized by the procedure described in Comparative Example 3, but using 2.0 mg of isopropylidene(cyclopentadienyl)(2,7-di-tert-butylfluorenyl)zirconium dichloride instead of 1.0 mg of diphenylmethylene(cyclopentadienyl)(fluorenyl)zirconium dichloride. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirring blade and shaft of the autoclave. The polymer yield was 417 g. The obtained polymer had an inherent viscosity [η] of 0.93 dl/g, Tm of 133°C and bulk density of 0.38 g/ml. The numbers of FE were 200 fisheyes as 100 µm or more and 9,000 fisheyes as less than 100 µm. Comparative Example 7 Propylene was polymerized by the procedure described in Comparative Example 5, but using 2.0 mg of ethylenebis(indenyl)zirconium dichloride instead of 1.0 mg of (1R,2R)-1,2-dimethylethylenebis(2-methylbenz[e]indenyl)zirconium dichloride. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. The polymer yield was 105 g. The obtained polymer had an inherent viscosity [η] of 0.53 dl/g, Tm of 142°C and bulk density of 0.35 g/ml. The numbers of FE were 150 f isheyes as 100 µm or more and 7,000 fisheyes as less than 100 µm. Example 11 [Synthesis of rac-dimethylsilylenebis(2-methylbenz[e]-indenyl)zirconium dichloride] The entitled compound was prepared according to the literature by Udo Stehling et al., in Organometallics 13,964 (1994). Analytical data are listed below. 1 H-NMR (90 MHz, CDCl 3 , TMS standard) δ; 8.00-7.15 (m, 14H), 2.37 (s, 6H), 1.34 (s, 6H) [Polymerization of propylene] Propylene was polymerized by the procedure described in Example 10, but using 3.0 mg of rac-dimethylsilylenebis(2-methylbenz[e]indenyl)zirconiun) dichloride instead of ethylenebis(indenyl)zirconium dichloride. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner, wall, stirrer blade and shaft of the autoclave. The polymer yield was 649 g. The obtained polymer had an inherent viscosity [η] of 1.09 dl/g, Tm of 145°C and bulk density of 0.36 g/ml. The numbers of FE were 4 fisheyes as 100 µm or more and 35 fisheyes as than 100 µm. Example 12 [Synthesis of rac-dimethylsilylene(2,4-dimethylcyclopentadienyl)(3',5'-dimethylcyclopentanedienyl)zirconium dichloride] The entitled compound was prepared according to the literature by Takaya Mise et al., in Chemistry Let'ters, 1853 (1989). Analytical data are listed below. 1 H-NMR (90 MHz, CDCl 3 , TMS standard) δ: 6.43 (d, 2H), 5.27 (d, 2H), 2.28 (s, 6H), 2.05 (s, 6H), 0.77 (s, 6H), [Polymerization of propylene] Propylene was polymerized by the procedure described in Example 10, but using 2.0 mg of rac-dimethylsilylene(2,4-dimethylcyclopentadienyl((3',5'-dimethylcyclopentadienyl)zirconium dichloride instead of ethylenebis(indenyl)zirconium dichloride. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. The polymer yield was 49 g. The obtained polymer had an inherent viscosity [η] of 0.77 dl/g, Tm of 153°C and bulk density of 0.35 g/ml. The numbers of FE were 6 fisheyes as 100 µm or more and 20 fisheyes as less than 100 µm. Comparative Example 8 Propylene was polymerized by the procedure described in Comparative Example 5, but using 3.0 mg of rac-dimethylsilylbis(2-methylbenz(e)indenyl)zirconium dichloride instead of 1.0 mg of (1R, 2R)-1,2-dimethylethylene bis(2'-methylbenz[e]indenyl)zirconium dichloride. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. The polymer yield was 589 g. The obtained polymer had an inherent viscosity [η] of 1.26 dl/g, Tm of 145°C and bulk density of 0.35 g/ml. The numbers of FE were 200 fisheyes as 100 µm or more and 6,000 fish eyes as less than 100 µm. Comparative Example 9 Propylene was polymerized by the procedures described in Comparative Example 5, but using 2.0 mg of rac-dimethylsilyl(2,4-dimethylcyclopentadienyl((3',5'-dimethylcyclopentadienyl)zirconium dichloride instead of 1.0 mg of (1R,2R)-1,2-dimethylethylenebis(2'-methylbenz[e]indenyl)zirconium dichloride. No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. The polymer yield was 30 g. The obtained polymer had an inherent viscosity [η] of 1.26 dl/g,. Tm of 149°C and bulk density of 0.36 g/ml. The numbers of FE were 300 as 100 µm or more and 9,000 fisheyes as less than 100 µm. Example 13 [Preparation of organic aluminum oxy compound supported on polymer (F)] In 1 liter glass autoclave which was sufficiently replaced with nitrogen, 1.0 g of maleic anhydride grafted polypropylene (Mw: 43500, maleic anhydride content: 6.7 wt%, 0.68 mmol/g) was suspended in 400 ml of xylene, heated at 130°C and completely dissolved. 7 ml of a toluene solution containing methylaluminoxane (manufactured by Albemarle Co., methylaluminoxane content of 8 wt.%) was added via syringe under nitrogen and heated at 145°C for 4 hours. The reaction mixture was cooled to 40°C, and sprayed through a flat spray nozzle into 3 liters of hexane by nitrogen under pressure of 3 bar (3 kg/cm 2 ). The precipitate was filtered under nitrogen, rinsed successively with 400 ml of toluene, 200 ml of hexane, and then dried in vacuo to give 1.2g of pale yellow fine powdery solid. The solid component had 4.3 mmol/g as aluminum content. [Polymerization of propylene] Propylene was polymerized by the procedure described in Example 5, but using 240 mg of the above pale yellow solid catalyst component (F) instead of the solid catalyst component (E). No adhesion or fouling of the polymer in the polymerization was observed at all on the inner wall, stirrer blade and shaft of the autoclave. The polymer yield was 600 g. The obtained polymer had an inherent viscosity [η] of 1.26 dl/g, Tm of 134°C and bulk density of 0.38 g/ml. The numbers of FE were 4 fisheyes as 100 µm or more and 10 fish eyes as less than 100 µm. [Effect of the invention] By applying the catalyst system of the invention, olefin can be polymerized in high activity and polymer having high stereoregularity can be obtained. Further, adhesion or fouling of the polymer or organic aluminum oxy compound in the polymerization, is not caused on the inner wall of the reactor. The polymer has a high bulk density and the product processed articles have very few fisheyes or gel. Consequently, high productivity can be maintained, high quality product can be manufactured, and very high contribution is expected in industry.

Claims: An olefin polymerisation catalyst system comprising an organic transition metal compound and a support, the organic transition metal compound being soluble in an inert organic solvent selected from alkanes, aromatic hydrocarbons, ethers and halogenated hydrocarbons, the support being insoluble in the inert solvent, and said support being obtained by contacting a polymer, which contains a carbonyl-having group represented by the general formula [1]: wherein Q is selected from hydrogen, hydroxy, alkyl, aryl, alkoxy, aryloxy, oxycarbonyl, halogen, amino, aminocarbonyl, hydrazino or oxyanion, with an organic aluminium oxy compound, and wherein said polymer is obtained by grafting or graft polymerizing a monomer containing the carbonyl-having group on polyethylene, polypropylene, ethylene-propylene copolymer, polybutene, ethylene-butene copolymer, ethylene-propylene-butene copolymer, polyisobutene, polypentene, poly-4-methylpentene, polynorborene, polybutadiene, polyisoprene, polystyrene or poly-α-methylstyrene. An olefin polymerization catalyst system according to claim 1 wherein the support is prepared by heat-dissolving the polymer containing the carbonyl-having group represented by the formula [1] in the organic solvent and bringing it into contact with the organic aluminium oxy compound. An olefin polymerization catalyst system according to claim 1 wherein the organic aluminum oxy compound is at least one compound selected from the compounds represented by the general formula [4] or the general formula [5] wherein R 5 can be the same or different and is an alkyl e.g. of 1-6 carbon atoms, aryl e.g. of 6-18 carbon atoms, or hydrogen, and p is an integer of 2-50, preferably 10-35. An olefin polymerization catalyst system according to claim 1 wherein the unsaturated compound containing the carbonyl-having group is an unsaturated organic acid anhydride. An olefin polymerization catalyst system according to any preceding claims, comprising as a further catalyst component, an organic metal compound different from the organic aluminum oxy compound. An olefin polymerization catalyst system according to claim 5 wherein the said organic metal compound is an alkyl compound of a metal selected from the group 1, 2, 12 or 13 in the periodic table. An olefin polymerization catalyst system according to claim 6 wherein the said organic metal compound is an alkyl-metal compound selected from lithium, sodium, potassium, beryllium, magnesium, zinc, cadmium, aluminum and gallium alkylates wherein the alkyl has 1-20 carbon atoms. An olefin polymerization catalyst system according to claim 7 wherein the said organic metal compound is an alkylaluminum selected from trimethylaluminum, triethylaluminum, tri-n-propylaluminum, triisopropylaluminum, tri-n-butylaluminum, trisobutylaluminum, tri-sec-butylaluminum, dimethylaluminum chloride, diethylaluminum chloride, di-n-propylaluminum, chloride, diisopropylaluminum chloride, di-n-butylaluminum chloride, diisobutylaluminum chloride, and di-sec-butylaluminum chloride. An olefin polymerization catalyst system according to any preceding claim, wherein the organic transition metal compound is a metallocene compound. An olefin polymerization catalyst system according to claim 9 wherein the metallocene compound is a compound selected from the general formula [2] or general formula [3] wherein A 1 and A 2 are a cyclopentadienyl group, indenyl group, or fluorenyl group, one of A 1 and A 2 can be amino group, and two adjacent groups can be directly bonded to each other to form a cyclic hydrocarbon substituent; further a portion or all of the hydrogen atoms on these groups can be substituted with a substituent selected from alkyl e.g. of 1 - 20 carbon atoms, aryl e.g. of 6 - 20 carbon atoms, alkoxy e.g. of 1 - 20 carbon atoms, aryloxy e.g. of 6 - 20 carbon atoms and silicon containing alkyl e.g. of i - 20 carbon atoms; M is a metal selected from the group 4 in the periodic table; and X 1 and X 2 are selected from halogen, alkyl e.g. of 1 - 20 carbon atoms or anion ligand wherein A 3 and A 4 are a cyclopentadienyl group, indenyl group, or fluorenyl group, one of A 3 and A 4 can be an amino group, and two adjacent groups can be directly bonded each other to form a cyclic hydrocabon substituent; further, a portion or all of the hydrogen atoms on these groups can be substituted with a substituent selected from alkyl e.g. of 1 - 20 carbon atoms, aryl e.g. of 6 - 20 carbon atoms, alkoxy e.g. of 1 - 20 carbon atoms, aryloxy e.g. of 6 - 20 carbon atoms and silicon containing alkyl e.g. of 1 - 20 carbon atoms; A 3 and A 4 can be the same or differ from each other; M is a metal selected from the group 4 in the periodic table; Y is selected from -CR 1 R 2 -, -CR 1 R 2 -CR 3 R 4 -, or SiR 1 R 2 -wherein R 1 , R 2 , R 3 or R 4 are selected from hydrogen, alkyl e.g. of 1 - 20 carbon atoms, aryl e.g. of 6 - 20 carbon atoms, alkoxy e.g. of 1 - 20 carbon atoms, aryloxy e.g. of 6 - 20 carbon atoms or silicon containing alkyl e. g. or 1 - 20 carbon atoms, and R 1 , R 2 , R 3 , and R 4 can be the same or different from each other: X 1 and X 2 are selected from halogen, alkyl e·g· of 1- 20 carbon atoms or anion ligand. A support for an olefin polymerization catalyst system, the support being obtained by bringing an organic aluminum oxy compound into contact with a carrier comprising a polymer containing a carbonyl-having group represented by the general formula [1], wherein Q is selected from hydrogen, hydroxy, alkyl, aryl, alkoxy, aryloxy, oxycarbonyl, halogen, amino, aminocarbonyl hydrazino or oxyanion and wherein said polymer is obtained by grafting or graft polymerizing a monomer, containing the carbonyl-having group on polyethylene, polypropylene, ethylene-propylene copolymer, polybutene, ethylene-butene copolymer, ethylene-propylene-butene copolymer, polyisobutene, polypentene, poly-4-methylpentene polynorborene, polybutadiene, polyisoprene, polystyrene or poly-α-methylstyrene. A process of polymerizing olefins, wherein said olefins are exposed to polymerization conditions in a polymerization reactor containing the catalyst system according to any of claims 1 to 10.

Inventors: ASANUMA TADASHI, ISHII YUKIO, SUNAGA TADAHIRO, ASANUMA, TADASHI, ISHII, YUKIO, SUNAGA, TADAHIRO
Applicants: MITSUI CHEMICALS INC, MITSUI CHEMICALS, INC.
Application year: 1996
Main classification: C08F10
IPC codes: C08F4, C08F10, C08F110