CATALYSTS FOR THE POLYMERIZATION OF OLEFINS

Abstract: Supported components (component (c)) and the corre­ sponding catalysts for polymerizing olefins, comprising the product of the reaction among : (a) a metallorganic Al compound; (b) an electron-donor compound reactive towards MgCl₂ but not capable of forming complexes with AlEt₃ in standard conditions; (c) a solid including a halogenated tetravalent titanium compound and an electron-donor compound, supported on titanium trichloride or tribromide or on vanadium trichloride or tribromide having a surface area of at least 100m²/g, the electron-donor compound being characterized in that it is extractable with AlEt₃ (under standard conditions) for at least 70% by moles.

Description: This invention relates to supported catalyst components for the polymerization of olefins CH₂=CHR, in which R is hydrogen or an alkyl with 1―4 carbon atoms or an aryl, and of mixtures of such olefins with one another and/or with ethylene, and to the catalysts prepared from such components. It is known how to use TiCl₃ in the various crystalline forms (alpha, beta, gamma and delta) as component of Ziegler-Natta catalysts for the stereoregular polymerization of olefins. The TiCl₃ utilized in these catalysts is generally prepared by reduction of TiCl₄ with Al and subsequent activation, by means of grinding, of the solid obtained (TiCl₃ ARA). The reduction of TiCl₄ may be also accomplished by means of hydrogen: the solid obtained is then activated by grinding (TiCl₃ HRA). Known are also catalysts which comprises a titanium compound containing at least a Ti-Cl bond and an electron-donor, which are supported on activated magnesium halides. The catalysts supported on magnesium halides are characterized by a particularly high activity, which considerably exceeds the one of the catalysts prepared from TiCl₃. From FR―A―2 320 957 catalysts are known comprising a solid component obtained by copulverizing a magnesium and/or a manganese halide and a trivalent titanium compound, as for instance TiCl₃, with an aromatic hydrocarbon and a tetravalent titanium compound, as for instance a titanium tetrahalide in such proportions as to have the titanium compounds supported on the magnesium and/or manganese halides. These catalyst components, as well as the final catalysts obtained from them, do not comprise electron donor compounds and are suitable for the polymerization of ethylene and more generally for the non-stereoregular polymerization of olefins. It has now surprisingly been found that it is possible to obtain highly active and stereospecific catalyst systems starting from catalytic components comprising a tetravalent titanium compound containing at least a Ti-Cl bond and an electron-donor compound corresponding to a particular test (Test A) supported on Ti or V trichloride or tribromide having particular surface area characteristics. The catalysts are prepared by reacting the supported component with aluminium-trialkyl compound and with an electron-donor compound corresponding to Test B specified hereinbelow. Test A: The electron-donor compound (EDA) is extractable with AlEt₃ for at least 70% by moles from the solid catalytic component under the following reaction conditions: into a 5-liter flask there are introduced 4 liters of deaerated and anhydrous n-heptane containing 20 m · moles of Al(C₂H₅)₃. The temperature is brought to 70°C and about 1 g of solid catalytic component is introduced, whereafter the whole is allowed to react under the stirring for 15 minutes. It is quickly cooled down to 0°C and, by filtration, a solid is isolated, which is then dried under vacuum at 25°C and analyzed. Test B: The electron-donor (EDB) is reactive towards MgCl₂, but it is not capable of forming complexes with Al(C₂H₅)₃ under standard conditions. The test for determining the complexing capability of the electron-donor with AlEt₃ is carried out by using a Metrohom potentiograph, mod. E 536, equipped with a titration bench E 535, an automatic burette E 552, a magnetic stirrer E 549 and a titration cell EA 880. A combined electrode EA 281 (Pt/Ag/KCl 3M) is utilized. As titration agent there is used a 0.5 M hexane solution of Al-triethyl, which is added to a 0.5 M benzene solution of the compound being tested. It is operated at room temperature and in a nitrogen atmosphere. The reactivity test of the electron-donor compound EDA with MgCl₂ is carried out under the following conditions: into a 500-cm³ flask there are introduced, in a nitrogen atmosphere, 2 g of MgCl₂ (21 m · moles) suspended in 200 cm³ of toluene and 3.5 m · moles of the electron-donor compound being tested. It is allowed to react at 25°C during 1 hour, the solid is filtered and it is washed with 200 cm³ of toluene and then with 200 cm³ of n-heptane. The solid is isolated, dried and analyzed. As MgCl₂ it is employed the product obtained from MgCl₂ · 2.5 C₂H₅-OH by reaction with Al-triethyl, according to the following modalities: into a 3000-ml flask there are introduced 2340 cm³ of a 0.83 M hexane solution of Al(C₂H₅)₃; while keeping the temperature below 10°C there are added, in small doses, 136 g of MgCl₂ · 2.5 C₂H₅-OH. At the end of such addition, it was heated to 70°C, keeping such temperature during 4 hours; then it is filtered and the solid is repeatedly washed with n-heptane, whereafter it is dried under a 26.6―66.5 Pa (0.2―0.5 Torr) vacuum. The surface area of the obtained MgCl₂ is of 618 m²/g and the pores volume is of 0.532 cm³/g. The titanium or vanadium trihalide utilized for preparing the compounds of the present invention must have a surface area of at least 100 m²/g after treatment with AlEt₃ under standard conditions. The standard conditions for the treatment with AlEt₃ are the same as indicated in test A for the extraction of electron-donor EDA. The average dimension of the crystallites is generally below 30 nm (300Å) and preferably ranges from 6 to 25 nm (60 to 250Å). It is calculated by means of known methods and in particular, in the case of TiCl₃, by measuring the width, at half height, of the reflection (110)+(108) which appears―in the X-ray spectrum at an interplane distance of 0.177 nm (1.77Å) and by applicating the Sherrer equation: D(110)= K · 1542 · 57.3 (B-b)cosv wherein: K=a constant, which in the specific case of TiCl₃ is equal to 1.84; B=width (in degrees), at half height, of the reflection (110); b=instrumental broadening; v=Bragg angle. The presence, in the starting titanium trihalide lattice, of Al halides in amounts equal to Al contents higher than 0.5―1% by weight badly affects the catalyst activity. By substituting, in these catalyst components, a portion of TiCl₃ or VCl₃ by MgCl₂ in order to have a supports mixture on which a tetravalent titanium compound and an electron-donor compound corresponding to test A can be deposited, it is possible to obtain catalysts endowed with an even higher activity. The catalysts of the invention comprise the product of the reaction among at least the following components: (a) an Al-alkyl compound, preferably an Al-trialkyl or a compound containing two or more Al atoms bound to one another through oxygen or nitrogen atoms or through SO₄ or SO₃ groups; (b) an electron-donor compound (or a Lewis base) EDB which, under the standard measuring conditions, as mentioned hereinbefore, is reactive with MgCl₂, but does not form complexes with Al-triethyl; (c) a solid comprising a tetravalent titanium halogenated compound and an electron-donor compound EDA supported on titanium or vanadium trichloride or tribromide, the solid component or the starting trichloride having a surface area of at least 100 m²/g after treatment with AlEt₃ under standard conditions, the electron-donor compound being extractable with AlEt₃ for at least 70% by moles from the solid. Tetravalent Ti halogenated compound and electron-donor compound EDA supported on Ti or V trichloride or tribromide means the compounds and/or the reaction products thereof interreacted with the supports and/or physically fixed on same. The Al-alkyl compounds of component (a) include the Al-trialkyls, such as for example AlEt₃, Al(i-Bu)₃, Al(i-C₃H₇)₃, AlEt₂H, and compounds containing two or more Al atoms bound to one another by means of hetero-atoms, such as: (C₂H₄)₂Al―O―Al(C₂H₅)₂, As already mentioned herein, Al-alkyl compounds in which Al atoms are bound by means of groups such as SO₄ or SO₃ are suitable as well. The Al-alkyl compounds are employable in admixture with Al-alkyl halides, such as AlEt₂Cl. Compound (b) is selected in particular from compounds of general formula: R m SiY n X p wherein: R is an alkyl, alkenyl, aryl, aryl-alkyl or cycloalkyl with 1―20 carbon atoms; Y is a ―OR′, ―OCOR′, ―NR′₂ radical in which R′, either like or unlike R, has the same meaning as R; X is an atom of halogen or of hydrogen or a group ―OCOR″ or ―NR″₂ in which R″, like or unlike R′, is defined as R′; m, n, p are integers, which respectively range: m from 0 to 3, n from .1 to 4 and p from 0 to 1; m+n+p is equal to 4. Preferred silicon compounds are: phenyl - alkoxy - silanes such as phenyl - triethoxy- or phenyl - trimethoxy - silane, diphenyl - dimethoxy and diphenyl - diethoxy - silane, monochloro - phenyl - diethoxy - silane; alkyl - alkoxy - silanes such as ethyl - triethoxy - silane, ethyl - triisopropoxy - silane. In the catalysts according to the present invention the silicon compound is present in the combined form in the solid product of the reaction among the various components which form the catalyst, in a molar ratio between the silicon compound and the Ti halogen compound higher than 0.05 and generally ranging from 0.1 to 5. Other compounds (b) which have proved suitable are: 2,2,6,6 - tetramethylpiperidine, 2,2,5,5 - tetramethylpyrrolidine, 2,2,6,6 - tetramethylpiperidide - Al - diethyl, di(m - methyl - phenyl) - amine, 2,2,6,6 - tetramethyl - tetrahydro - γ - pyrone, Al - dichloromonophenoxy. The electron-donor compound as is defined in (b) does not exhibit, at the equivalence point of the potentiometric titration with Al-triethyl conducted under the standard conditions indicated hereinbelow, any appreciable variation or wave of potential. Conversely, such modification is very sharp in the case of titration with amines such as isoquinoline and is very appreciable in the case of esters such as ethyl para-toluate. Component (c) is preparable according to various methods. One of such methods consists in co-grinding TCl₃ or VCl₃ and the electron-donor compound and in subsequently reacting, in hot conditions, the ground product with an excess of TiCl₄. Another method consists in decomposing an adduct TiCl₃ · nROH or VCl₃ · nROH (where 1 ≦n≦6 and R is an alkyl radical having 2―8 carbon atoms) with an excess of SiCl₄ in the presence of the electron-donor and in treating the resulting solid, in hot conditions, with an excess of TCl₄. When also MgCl₂ is contained in component (c), TCl₃ or VCl₃, MgCl₂ and the electron-donor compound are ground together and the reaction product is treated in hot conditions with an excess of TCl₄. The MgCl₂-containing TiCl₃ may be prepared also in other manners, one of which consisting in reducing TiCl₄ with MgR₂ or MgRCl (wherein R is a hydrocarbon radical containing 1 to 20 carbon atoms). By treating this product with the electron-donor and with TCl₄ it is possible to obtain a catalyst component according to the invention. In component (c) the molar ratio between Mg dihalide and total Ti is lower than 1 and the molar ratio between total titanium and electron-donor compound ranges from 0.1 to 50. Electron-donor compound EDA is selected among the following classes of compounds: 1) mono- and polyesters of saturated polycarboxylic acid in which at least one of the ester carbonyl groups is bound to a tertiary or quaternary carbon atom or to a linear or ramified chain with at least 4 carbon atoms; 2) mono- and polyesters of unsaturated polycarboxylic acids in which two carboxylic groups are bound to vicinal carbon atoms forming a double bond and in which at least one of the hydrocarbyl radicals R of groups COOR is a saturated or unsaturated ramified radical with 3―20 carbon atoms, or it is an aryl or arylalkyl radical with 6―20 C; 3) mono- and diesters of aromatic dicarboxylic acids with the COOH groups in ortho position, in which at least one of the hydrocarbyl radicals R contains from 2 to 20 C; 4) mono- and polyesters of aromatic hydroxy-compounds containing at least two hydroxyl groups in ortho position, or esters of hydroxyacids containing at least a hydroxyl group in ortho position with respect to the carboxyl group; 5) esters of saturated or unsaturated carboxylic acids RCOOR′ in which at least one of the hydrocarbyl radicals R and R′ is a saturated or unsaturated ramified radical with 3 up to 20 C or it is an arylalkyl radical with 7―20 C or it is an acyl radical with 3 up to 20 C bound to the carbonyl of the ester group either directly or through a methylene group and in which radical R′, if linear, is a hydrocarbyl radical containing from 1 to 20 C; 6) esters of the carbonic acid of formula: in which at least one of the hydrocarbyl radicals R, which may be equal or different, is a radical with 3 up to 20 C; 7) silicon compounds containing at least a Si-OR or SiOCOR or Si-NR₂ bond, in which R is a hydrocarbyl radical with 1 to 20 C. Representative esters are: Class 1 Diethyl - diisobutyl - malonate, diethyl - n - butyl - malonate, diethyl - di - n - butyl - malonate, diethyl - phenyl - malonate, diethyl - 1,2 - cyclohexane - dicarboxylate, dioctyl - sebacate, diisobutyl - adipate. Class 2 Di - 2 - ethylhexyl - maleate, diisobutyl - maleate, diisobutyl - 3,4 - furandicarboxylate, di - 2 - ethylhexyl - fumarate, 2 - ethylhexyl - monomaleate. Class 3 Diisobutyl - 2,3 - naphthalene - dicarboxylate, di - n - propyl-, di - n - butyl-, diisobutyl-, di - n - heptyl-, di - 2 - ethylhexyl-, di - n - octyl-, di - neopentyl - phthalate, monobutyl ester and mono-isobutyl ester of phthalic acid, ethyl - isobutyl - phthalate, ethyl - n - butyl - phthalate. Class 4 2,3 - diacetoxynaphthalene, 1,2 - diacetoxybenzene, 1 - methyl - 2,3 - diacetoxybenzene, ethyl benzoylsalicylate, methyl acetyl - salicylate. Class 5 Ethylene glycol-pivalate, 1,4 - butadiol - pivalate, benzyl- and isobutyl-pivalate, n - propyl - pivalate, ethyl - diphenyl - acetate, isobutyl - methacrylate, isobutyl - acrylate, ethyl - benzoyl - acetate, isobutyl - pivalate, isobutyl - trans - 3 - methoxy - 2 - butenoate. Class 6 Diphenyl-carbonate. Preferred esters are: esters of maleic acid, pivalic acid, methacrylic acid, carbonic acid and phthalic acid, in particular the alkyl, aryl and cycloalkylesters of said acids. As previously mentioned herein, the surface area of the solid component and of the starting Ti or V trichloride exceeds 100 m²/g. The area is measured after treatment with AlEt₃ in standard conditions. Preferably, the surface area is higher than 150―200 m²/g. The average dimensions of the crystallites are generally below 30 nm (300Å); preferably they are lower than 25 nm (250Å) and range for example from 23 to 6 nm (230 to 60Å). Components (a), (b) and (c) are reacted with one another in any order; however, components (a) and (b) are premixed before being brought into contact with component (c). Such pre-contact can take place also in the presence of the monomer. Component (c) can be premixed with component (a) and/or with component (b). Premixing of (a) and (b) occurs at temperatures usually ranging from room temperature to the temperature employed during the polymerization. The pre-reaction of (c) and (b) may be conducted even at higher temperatures. Compound (b) can be also incorporated and reacted with said component (c). Component (b) is reacted in a molar ratio with respect to the Ti tetravalent halogenated compound supported on component (c) of at least 1, and in a molar ratio with respect to the Al-alkyl compound employed as component (a) lower than 20 and preferably ranging from 0.05 to 1. Ratios higher than 1 are employable with compounds (b) which do not complex or only slightly complex the Al-triethyl even under conditions promoting such formation. The catalysts according to the invention are utilized for polymerizing olefins according to known methods, i.e. when the polymerization is conducted in a liquid phase, either in the presence or in the absence of an inert hydrocarbon solvent, or in a gas phase, or also when, for example, a polymerization step in the liquid phase is combined with a polymerization step in gas phase. Generally, the temperature ranges from 40° to 160°C, but preferably from 60° to 90°C, operating both at atmospheric pressure and at a higher pressure. As a molecular weight regulator it is possible to use hydrogen or another known regulator. The catalysts are particularly suited to the polymerization of ethylene, propylene, butene-1, styrene and 4-methyl-pentene-1. The catalysts are also useful to polymerize, according to known methods, mixtures of propylene and ethylene in order to prepare, for example, modified propylenes having an improved impact resistance at low temperatures (the so-called block copolymers of propylene and ethylene), or to obtain statistic crystalline copolymers of propylene with minor proportions of ethylene. Polymerization-in-suspension of propylene A suspension consisting of 1,000 ml of anhydrous and deaerated n-heptane, of 5 millimoles of aluminium triethyl, of the desired amount of electron-donor and of the solid catalytic component is introduced into a stainless steel autoclave having a 3000 ml capacity, equipped with an anchor-type magnetic stirrer and thermometer, thermoregulated at 60°C, whereinto propylene is made to flow. Subsequently, hydrogen is introduced at a pressure of 19.6 kPa (0.2 atmospheres), whereafter it is rapidly heated to 70°C while simultaneously feeding propylene up to a total pressure of 686.5 kPa (7 atmospheres). Such pressure is kept constant all through the polymerization by going on feeding the monomer. After 4 hours the polymerization is stopped and the polymer is isolated by filtration and it is dried. The polymer amount dissolved in the filtrate is isolated, weighed and summed to the polymer soluble in boiling n-heptane for the calculation of the isotacticity index (l.l.). The results of the polymerization tests are reported on the Table. Polymerization of propylene in liquid monomer A proper amount of the catalytic complex prepared in the examples and 50 ml of anhydrous and deaerated n-heptane are introduced; together with 5 m · moles of Al(C₂H₅)₃ and 1 m · mole of phenyltriethoxysilane, under a dry argon pressure, into a stainless steel 2-liter autoclave, equipped with an anchor-type stirrer, heated to 70°C and containing hydrogen for a partial pressure of 19.6 kPa (0.2 atm.) and 500 g of anhydrous propylene. After 4 hours the reaction is stopped, the non-polymerized propylene is discharged, and from the autoclave the polymer is extracted, which is then dried and weighed. The results of this polymerization test are reported on the Table (test 1*). Example 1 Into a jar of a vibrating mill having a total volume of 1 liter and containing 3 kg of steel balls of 16 mm diameter there were introduced, in a nitrogen atmosphere, 45 g of TiCl₃ and 7.7 ml of diisobutylphthalate; it was ground during 70 hours at room temperature. 10 g of the resulting solid were suspended in 100 ml of TiCl₄ and the whole was allowed to react, under stirring, at 100°C during 2 hours. After such period of time, TiCl₄ was removed by filtration and an equal amount thereof was added, allowing to react for further 2 hours at 120°C; TiCl₄ was removed by filtration, and washings with n-heptane at 90°C were carried out until disappearance of the chlorine ions in the filtrate. After isolation and drying under vacuum, the solid exhibited, on analysis, the following composition: Ti= 25.1 % DIBF = 4.1 %. The surface area of the catalyst component was of 212 m²/g (B.E.T.) and the crystallite dimension was of 23 nm (230Å) (D( 110)). The polymerization tests carried out by using this catalyst component, and the properties of the resulting polymer are indicated on the Table. Example 2 Example 1 was repeated by using, instead of diisobutylphthalate, 4.5 ml of isobutyl pivalate. The solid, after isolation and drying under vacuum, exhibited on analysis the following composition: Ti= 26.7% IBP= 4.5%. The surface area of the catalyst component was of 151 m²/g and the size of the crystallites was of 15 nm (150Å) (D(110)). The polymerization test carried out using this catalyst component and the properties of the resulting polymer are reported on the Table. Example 3 Into a 250 cc test tube there were introduced 42 g of VCl₃ · 3C₂H₅OH and 200 ml of SiCl₄; it was reacted at reflux during 48 hours. The solid obtained after filtration and washing with n-heptane was suspended at 60°C in 100 ml of n-heptane containing 15 m · moles of diisobutyl - phthalate; it was allowed to react during 2 hours at the same temperature, then the solid was isolated by filtration and was suspended in 150 ml of TiCl₄ under stirring at 100°C for two hours. After such period of time, TiCl₄ was removed by filtration and an equal amount thereof was added allowing to react for further 2 hours at 120°C; TiCl₄ was removed by filtration, and washings with n-heptane at 90°C were carried out until disappearance of the chlorine ions from the filtrate. The isolated and vacuum-dried solid exhibited on analysis the following composition: Ti= 4.2% V= 20.4% DIBF= 4%. The surface area of the catalyst component was of 162 m²/g and the dimension of the crystallites was of 19 nm (190Å) (D(110)). The polymerization test conducted by using this catalyst component as well as the properties of the polymer so obtained are reported on the Table. Example 4 Example 1 was repeated by subjecting to reaction with TiCl₄ 10 g of the product obtained by co-grinding 12.6 g of MgCl₂, 20.51 g of TiCl₃HR and 7.4 ml of diisobutyl - phthalate. The solid dried under vacuum exhibited on analysis the following composition: Ti= 8.15% Mg= 11.2% DIBF= 4.24% Surface area=208 m²/g Crystallite size=6.5 nm (65Å) (D(110)). The polymerization test carried out by using this catalyst component, and the properties of the resulting polymer are reported on the Table. Example 5 Example 1 was repeated by subjecting to reaction with TiCl₄ 10 g of the product obtained by co-grinding 11.6 g of MgCl₂, 34 g of TiCl₃HR and 10 ml of diisobutylphthalate. The solid dried under vacuum exhibited on analysis the following composition: Ti= 11.8% Mg= 6.7% DIBF= 4.6% Surface area=232 m²/g Crystallite dimension=11 nm (110Å) (D(110)). The polymerization test carried out by using this catalyst component, as well as the properties of the polymer obtained are reported on the Table. Example 1 (comparative test) The polymerization test of example 1 was repeated with the exception that ethyl p · toluate (EPT) was utilized instead of phenyltriethoxysilane. The molar ratio between Al-triethyl and EPT was equal to 3.3. Polymerization conditions and properties of the polymer are reported on the Table. Example 2 (comparative test) The preparation of the catalyst component of example 1 was repeated with the exception that TiCl₃ ARA was employed instead of TiCl₃ HR. The surface area of the solid after treatment with TiCl₄ was of 52 m²/g. The results of the polymerization test and the properties of the obtained polymer are reported on the Table.

Claims: 1. Catalyst components for the polymerization of olefins comprising a tetravalent titanium halogenated compound and an electron-donor compound EDA, which are supported on titanium or vanadium trichloride or tribromide having a surface area of at least 100 m²/g, the electron-donor compound being characterized in that it is extractable with AlEt₃ for at least 70% by moles, the test of extractability being carried out at 70°C for 15 minutes with a 0.005 molar solution of AlEt₃ in n-heptane containing 250 mg/l of the catalyst component under stirring after which the resulting mixture is quickly cooled down to 0°C and, by filtration, a solid is isolated, which is then dried under vacuum at 25°C and analyzed; and being selected among the following classes of compounds: 1) nono- and polyesters of saturated polycarboxylic acids in which at least one of the ester carbonyl groups is bound to a tertiary of quaternary carbon atom or to a linear or ramified chain with at least 4 carbon atoms; 2) mono- and polyesters of unsaturated polycarboxylic acids in which two carboxylic groups are bound to vicinal carbon atoms forming a double bond and in which at least one of the hydrocarbyl radicals R of groups COOR is a saturated or unsaturated ramified radical with 3-20 carbon atoms, or it is an aryl or arylalxyl radical with 6-20 C; 3) mono- and diesters of aromatic dicarboxylic acids with the COOH groups in ortho position, in which at least one of the Iydrocarbyl radicals R contains from 2 to 20 C; 4) mono- and polyesters of aromatic hydroxy-compounds containing at least two hydroxyl groups in ortho position, or esters of hydroxyacids containing at least a hydroxyl group in ortho position with respect to the carboxyl group; 5) esters of saturated or unsaturated carboxylic acids RCOOR′ in which at least one of the hydrocarbyl radicals R and R′ is a saturated or unsaturated ramified radical with 3 up to 20 C or it is an arylalkyl radical with 7-20 C or it is an acyl radical with 3 up to 20 C bound to the carbonyl of the ester group either directly or through a methylene group and in which radical R′, if linear, is a hydrocarbyl radical containing from 1 to 20 C; 6) esters of the carbonic acid of formula: in which at least one of the hydrocarbyl radicals R, which may be equal or different, is a radical with 3 up to 20 C; 7) silicon compounds containing at least a Si-OR or SiOCOR or Si-NR₂ bond, in which R is a hydrocarbyl radical with 1 to 20 C. 2. The catalyst components according to claim 1, in which the support is titanium trichloride. 3. The catalyst components according to claims 1 and 2, in which compound EDA is selected from the alkyl, aryl and cycloalkyl esters of the maleic, pivalic, methacrylic, carbonic and phthalic acids. 4. The catalyst components according to claim 3, in which the tetravalent titanium halogenated compound is TiCl₄. 5. Catalysts for the polymerization of olefins comprising the product of the reaction among the following components: a) an Al-alkyl compound, b) an electron-donor compound EDB which is reactive with MgCl₂, but does not form complexes with the Al-alkyl, the test of reactivity with MgCl₂ and the test for the complexation with Al-alkyl being carried out as described in the Test B described in the description, c) a component as is described in the preceding claims. 6. The catalysts according to claim 5, in which component a) is an Al-trialkyl such as AlEt₃, Al(i-Bu)₃, Al(i-C₃H₇)₃, AlEt₂H or a compound containing two or more Al atoms bound to one another through atoms of oxygen or of nitrogen or groups SO₄ or SO₃, such as (C₂H₅)₂Al―O―Al(C₂H₅)₂, 7. The catalysts according to claim 5, in which component b) is selected from the compounds of general formula R m SiY n X p wherein: R is an alkyl, alkenyl, aryl, aryl-alkyl or a cycloalkyl with 1-20 carbon atoms; Y is a radical ―OR′, ―OCOR′, ―NR′₂ in which R′, ehther like or unlike R, has the same meaning as R; X is an atom of halogen or of hydrogen or a group ―OCOR″ or ―NR″₂ in which R″, like or unlike R′, has the same meaning as R′; m, n, p are integers ranging: m from 0 to 3, n from 1 to 4 and p from 0 to 1; m+n+p being equal to 4. 8. The catalysts according to claim 7, in which component b) is selected from the following compounds: phenyl - alkoxy - silanes such as phenyl - trimethoxy- or phenyl - trimethoxy - silane, diphenyl - dimethoxy- and diphenyl - diethoxy - silane, monochlorophenyl - diethoxy - silane; alkyl - alkoxy - silanes such as ethyl - triethoxy - silane, ethyl - triiso - propoxy - silane. 9. The catalysts according to claim 5, in which component b) is selected from the following compounds: 2,2,6,6 - tetramethylpiperidine, 2,2,5,5 - tetramethylpyrrolidine, 2,2,6,6 - tetramethylpiperidide - Al - diethyl, di(m - methyl - phenyl) - amine, 2,2,6,6 - tetramethyl - tetrahydro - γ - pyrone, Al - dichloro - monophenoxy. 10. A process for polymerizing olefins of formula CH₂=CHR, in which R is hydrogen or an alkyl with 1 to 4 carbon atoms or an aryl, and mixtures of such olefins with one another and/or with ethylene, in the presence of catalysts as are defined in the preceding claims 5 through 9. 11. The process according to claim 10, in which propylene is polymerized in the presence of catalysts as are defined in the preceding claims 5 through 9. 12. The process according to claim 11, in which propylene is polymerized in liquid phase.

Inventors: ALBIZZATI, ENRICO
Applicants: HIMONT INCORPORATED
Application year: 1985
Main classification: C08F10
IPC codes: C08F4, C08F10