ALKYL-METAL COCATALYST

Abstract: A catalyst system for alphaolefin type polymerizations, including at least one metal alkyl compound having the for­ mula R‴₃ Min combination with a Group IVA-VIII transition metal chloride or bromide on a support and a hindered and an unhindered Lewis base wherein R‴ is C₁ to C₂₀ primary, branched primary, secondary or tertiary alkyl, cycloalkyl, alkenyl or aralkyl group, or a hydride, M is aluminium, gallium or indium. The improved catalyst system provides polymers having increased isotactic stereoregularity as well as lower catalyst residue.

Description: The present invention relates to unique and novel catalyst systems for the conventional alpha olefin type polymerization at significantly improved polymerization activity, wherein the resultant polymers have a high degree of isotactic stereoregularity. An object of my present invention is to provide improved catalyst systems having a major increase in polymerization acitvity while being able to control over a wide range the polymer crystallinity, e.g., isotacticity. It is well known in the art to use an alkyl metal compound of Groups I-III in combination with a transition metal compound of Groups IV rVIII as a catalyst system for olefinic polymerization. While nearly all of the alkyl metal compounds are effective for the polymerization of ethylene, only a few are effective for the preparation of isotactic polymers of propylene and higher alpha olefins and only Et2AlCl, AlEt3 and i Bu2AlH have any important commercial utility. A major cost involved in the polymerization of the alpha olefins is the cost of the catalyst components. Therefore, the cost of the manufacture of the polymer can be effectively reduced by the use of catalyst systems having a higher polymerization activity. A further concern is the ability to produce polymers having a minimum amount of catalyst residues thereby eliminating a costly deashing operation. A still further concern is the ability to produce polymers having a high degree of isotactic stereoregularity thereby ,enabling the manufacturer to eliminate or reduce the costly operation involving the removal and separation of atactic polymer from the isotactic polymer. The improved catalyst system of the present invention provides a means for the manufacturer to obtain these desirable reali zations. The improved catalyst systems of the present invention which are employed in alpha olefin polymerizations tlude a Group IVA-VIII transition metal chloride or bromide on a support, one or more Unhindered Lewis bases, at least one metal alkyl compound at least one of which is a metal trialkyl compound of Al, Ga or In, and at least one hindered Lewis base. The Group IVA to VIII transition metal chloride or 'bromide herein ab.breviated to transition metal halide is in the form of solid crystalline compounds, solid solutions or compositions with other metal salts or supported on the surface of a wide range of solid supports. For highest stereospecificity it is desirable to have the transition metal halide, or its support composition, in the layer lattice structure with very small crystallites, high surface area, or sufficient defects or foreign components to facilitate high dispersion during polymerization. The transition metal halide may also contain various additives such as Lewis bases, pi bases, polymers or organic or inorganic modifiers. Vanadium and titanium halides such as VC13, VBr3, Tics3, TiC14, TiBr3 or TiBr4 are preferred, most preferably TiC13 or TiC14 and mixtures thereof. The most preferred TiC13 compounds are those which contain TiC14 edge sites on a layer lattice support such as alpha, delta, or gamma TiC13 or various structures and modifications of TiC13, MgC12 or other inorganic compounds having similar layer lattice structures. The most preferred TiC14 compounds are those supported on chloride layer lattice compounds such as'MgC12. Other anions. may be also present, such as other halides pseudo-halides, alkoxides, hydroxides, oxides or carboxylates, etc., .' providing that sufficient chloride is available for isospecific site formation. Mixed salts or -double salts such as K2TiC16 or MgTiC16 can be employed alone or in combination with electron donor compounds. The most preferred transition metal compound is TiC14 containing MgC12 especially in the presence of Lewis bases (electron donor compounds). The Lewis bases can be employed in combination with the trialkyl metal compound or with the transition metal halide or with both components as long as they do not cause excessive cleavage of metalcarbon bonds or loss of active sites. A wide variety of both unhindered and hindered Lewis bases may be used including such types as tertiary amines, esters, phosphines, phosphine oxides, phosphates (alkyl, aryl)?, phosphites, hexaalkyl phosphoric triamides, dimethyl sulfoxide, dimethyl formamide, secondary amines, ethers, epoxides, ketones, saturated and unsaturated heterocycles, or cyclic ethers and mixtures thereof. Typical but nonlimiting examples are diethyl ether, dibutyl ether, tetrahydrofuran, ethyl acetate, methyl p-toluate, ethyl p-anisate, ethyl benzoate, phenyl acetate, amyl acetate, methyl octanoate acetophenone, benzophenone, triethyl amine, tributyl-amine, dimethyl decylamine, pyridine, N-methylpiperidine, 2,2,6 ,6-tetramethylpiperidine and the like. Although unhindered Lewis bases are preferred in the preparation of the supported transition metal catalyst component, hindered Lewis bases are preferably used in combination with the trialkyl metal cocatalyst. Hindered Lewis bases are those whose complexing ability toward the cocatalyst is hindered sufficiently by steric and/or electronic effects to cause appreciable dissociation of the trialkyl metal-Lewis base complex under polymerization conditions. Although a wide range of mole ratios may be used, dissociation measures on a 1:1 complex is normally in the range of 5-95%, preferably greater than about 10% and less than 90%. Steric hindrance is achieved by bulky substituents around the heteroatom which reduces the accessibility of the base functionality to the Lewis acid, that is, the trialkyl metal compound. Electronic hindering (weakening) is obtained by placing electron withdrawing substituents on the heteroatom to reduce the electron density on the basic heteroatom. Aromatic substituents are especially useful because they are relatively unreactive toward other catalyst components. Hindered Lewis bases derived from piperidines, pyrrolidines, ketones, tetrahydrofuran, secondary and tertiary aromatic amines and tertiary aliphatic amines are preferred, with the hindered nitrogen bases being most preferred. Non-limiting examples of sterically hindered bases include 2,2,6,6-tetramethyl-piperidine, 2,2,5,5-tetramethyl pyrrolidine; 2,2,5,5-tetramethyltetrahydrofuran; di-tert-butylketone,; 2,6-diisopropylpiperidine; ortho-tolyl t-butylketone, methyl 2,6-ditert-butylphenylketone, diisopropylethylamine, t-butyldimethylamine; 6-methyl-2-isopropyl pyridine, and the like. Electronically hindered Lewis bases include diphenylamine, di-ortho-tolylamine, N,N-diethylaniline, di-ortho-tolylketone, and the like. Since aromatic substituents are also bulky, some of the electronically hindered bases also have a steric contribution to the hindrance, Especially preferred hindered amines are 2,2,6 ,6-tetramethyl-piperidine; 2,2,5 ,5-tetramethyl- pyrrolidine and the diarylamines. Completely hindered bases, such as 2,6-di-tertiary-butylpyridine, and the like, which complex the alkyl metal cocatalyst too weakly, are ineffective for improving stereospecificity and are excluded from this invention. Unhindered Lewis bases have fewer and smaller substituents than hindered bases adjacent to the heteroatom such that their complexes with the trialkyl metal cocatalyst are too strong to permit sufficient dissociation under polymerization conditions to activate the catalyst or improve stereospecificity. Examples of conventional, unhindered, Lewis bases include di-n-alkyl ethers, n-alkyl esters of alkyl or aryl carboxylic acids, di-n-alkyl ketones, diaryl ketones unsubstituted in the ortho positions, secondary and tertiary n-alkyl amines, piperidines containing less than three methyl groups or the equivalent steric bulk in the 2 and 6 positions, pyridines containing less than two t-butyl groups or the equivalent steric bulk in the 2 and 6 positions, and the like. Non-limiting examples of unhindered Lewis bases include dibutyl ether, ethyl acetate, ethyl p-anisate, ethyl benzoate, benzophenone, tributyl amine, 2-isopropylpyridine, 2,6-diethylpyridine, 2,6-dimethylpiperidine, 2,5-dimethyltetrahydrofuran, and all related compounds containing less steric hindrance than the above examples. Obviously a somewhat less hindered base may be used in combination with a more hindered alkyl metal compound to achieve the desired dissociation. Salts of Group IA-IIIB metals may also be employed with the catalysts if they are partially or wholly solubilized by reaction with the alkyl metal components. Preferred are the carboxylates, alkoxides and aryloxides of Groups IIA-IIIB metals, more preferably magnesium and aluminum. Non-limiting examples include Mg(OOCR")2, R"OMgOOCR", ClMgOR", Mg(OR")2, R112AlOOCC6H5, RA1(00CR") R"2AlOR", and the like, where R" is a hydrocarbyl group. Most preferred are the alkoxide and carboxylate salts of magnesium and aluminum prepared in situ by reacting the organometal compounds with R"OH or carboxylic acids in hydrogen solvents. Sterically hindered alkoxides and aryloxides are especially preferred, where R" = t-butyl, t-amyl, l,l-diethylpropyl, l,l-diethylbenzyl, 2,6-di-tert-butylphenyl, l,l-diphenylpropyl, triphenylmethyl, and the like. I The trialkyl metal compounds useful in this invention have the formula R''' M wherein M = Al, Ga or 3 In, and R''' is a C1-C20 primary, secondary or tertiary alkyl, branched primary alkyl, cycloalkyl, alkenyl or aralkyl group or hydride or/ mixture thereof, more preferably at least one alkyl group having at least two carbon atoms, and most preferably having 2 to 4 carbon atoms. Preferred cocatalysts contain 1-2 secondary or tertiary hydrocarbyl groups. The salt of the Group IA-IIIB meSel is used at a molar ratio of 1 to 50 to 50 to 1 moles of the salt of Group IA-IIIB metal per mole of the trialkylaluminum compound R"3Al, preferably 1 to 10 to 10 to 1 moles when the oxygen-containing group is alkoxide or aryloxide, and most preferably less than 1 to 1 when these groups are hindered. Wzen the group is carboxylate, the ratio is 0.1 to 1, preferably 0.1 to 0.5 carboxylate groups per mole of the trialkyl metal compound. The use of these Group IA-IIIB metal salts is preferably with the supported titanium catalyst systems as embodied in this invention. The conventional trialkyl metal cocatalysts (R"'3M) useful in this invention include AlEt3, Al n-Pr3, Al n-Bu3, Al iBu3, Al trihexyl, Al tridecyl, Al iBu2H, Al-tri-isoprenyl, Al tribenzyl GaEt3, Ga n-Bu3, InEt3, and mixtures thereof containing more than one type of R''' group or more than one metal. The preferred cocatalysts of the present invention have the general formula RnMR'3 n wherein M = Al, Ga or In, R is a secondary or tertiary hydrocarbyl group selected from the group consisting of a C3-C20 secondary or tertiary alkyl, cycloalkyl, alkenyl or aralkyl group, R' is selected from the group consisting of C1-C20 primary alkyl, alkenyl or aralkyl or hydride; and n = 1-3, prefferably 1-2, and most preferably n = 2. Preferably R' is C2-C10 primary alkyl or aralkyl, or hydride with.the restriction that not more than one hydride group may be Present; most preferably R' is C2-C4 primary alkyl. The R group is preferably - a C4-C16 secondary or tertiary alkyl group or cycloalkyl group and is most preferably one which is not readily susceptible to elimination or displacement by monomer during polymerization. In addition to the simple secondary alkyl groups, other groups are also effective in which the aluminum is attached to a secondary or tertiary carbon atom, h.(., cyclohexyl, cyclooctyl, tert-butyl, tert-amyl, s-norbornyl, and the like. The most preferred compositions have the formula R AlR1 n in which the secondary and tertiary alkyl n groups contain 4-10 carbons and n = 2. Mixtures of the cocatalysts of this invention with conventional alkyl metal cocatalysts also yields improved results. Suitable non-limiting examples of preferred cocatalysts include i-Pr2AlEt, s-BuAlEt2, s-Bu2AlEt, t-BuAlEt2, t-Bu2AlEt, s-Bu3Al, 1,l-dimethylheptyl AlEt2, s-Bu2Aln-C16H33, t Bu2AlCH2C6H5, s-Bu(t-Bu)AlN-Bu, cyclohexyl2AlEt, s-pentyl Ali-Bu2, t-Bu2AlMe, t-Bu2Aln C8H171 (2-ethylcyclopentyl)2- AlEt, 2-(3-ethylnorbornyl) AlEt2, 2-norbornyl Ali-Bu2, (2-norbornyl)2, Ali-Bu, acenaphthyl Ali-Bu2, cyclooctyl (i-Bu) A1H, 3-ethyl-5ethylidinenorbornyl AlEt2, 9-i-bu-9-alumino-3 , 3, 1-bi- cyclononane, s-Bu2AlH, t-Bu2AlH, t-Bu2InEt, s-Bu2-GaEt, neopentyl AlEt2, neopentyl2 AlEt and the like. The most preferred compounds include those in the above list which have the formula R1-2AlR' 1' especially those having the formula R2AlR'. One method of preparing these secondary alkyl aluminum compounds is to react internal olefins with AliBu3 or i-Bu AlH to add A1-H across the double bond 3 2 to form alkyl aluminum compounds. When the double bond is in a strained ring compound. A1R3 may be used to add A1-R across the double bond and obtain preferred compounds which are very resistant to displacement or elimination. Strained ring olefins include cyclopentene, norbornene, norbornadiene, ethylidine norbornene, dicyclopentadiene, and the like. This method is preferred because of raw material availability and simplicity of reaction, although this invention is not limited by the method of synthesis. Other methods include the direct synthesis from the reactive metals and the secondary or tertiary halides, the various organometallic synthesis involving ligand exchange between Al, Ga or In compounds and secondary or tertiary alkyl metal compounds of more electropositive metals such as Groups IA and IIA, and the reaction of the metals with the alkyl mercury compounds. Particularly useful is the general reaction of secondary or tertiary alkyl lithium compounds with R'MX2 or R'2MX because it takes place readily in dilute hydrocarbon solutions. Although di-secondary alkyl aluminum compounds are preferred to mono-secondary alkyl compounds, the mono-alkyl types become more effective the greater the steric bulk of the group as long as it does not interfere with active site formation or lead to decomposition under reaction conditions. For the alkyl metal cocatalysts of this invention,the most preferred transition metal compounds contain TiC14 supported on MgC12 and one or more Lewis bases. The concentration of the transition metal in the polymerization zone is 0.001 to 5mM, preferably less than O.lmM. The molar ratio of the trialkyl metal compound to the transition metal compound is 0.5:1 to 200:1 or hiqher, more preferably 5:1 to 100:1. The molar ratio the 'inhindere oS Lewis base to organometal compound can vary widely but is preferably 0.1:1 to 1:1. However, the hindered Lewis bases may be added in greater than equimolar amounts, from 0.1 to 1 to 10 to 1 moles per mole of organometal compound, to obtain higher stereospecificity without a major loss of activity which would occur with unhindered bases. Surprisingly, it has been found that the Group the IA-IIIB salts may be omitted when / hindered Lewis base is used together with the trialkyl metal cocatalyst. Both high activity and high stereospecificity are obtained when the Lewis base is sufficiently hindered to prevent poisoning the stereospecific catalyst sites. In such cases, an excess of the hindered base over the alkyl metal cocatalyst still produces high activity, whereas an excess of the less hindered bases completely kills the catalyst. The desired steric hindrance is the same as defined above for dissociation from the trialkyl metal compound. The catalyst system of the invention enables the process for making alpha olefin polymers having a high degree of isotactic stereoregularity to be carried out at a temperature of 250 to 1500C, more preferably about 400 to 800C, at pressures of 1 atm. to 50 atm. The reaction time for polymerization is 0.1 to 10 hours, more preferably 0.5 to 3 hours. Due to the high catalyst activity, shorter times and temperatures below 800C can be readily employed. The reaction solvent for the system can be any inert paraffinic, naphthenic or aromatic hydrocarbon such as benzene, toluene, xylene, propane, butane, pentane, hexane, heptane, cyclohexane, and mixtures thereof. Preferably, excess liquid monomer is used as solvent. Gas phase polymerizations may also be carried out with or without minor amounts of solvent. Typical, but non-limiting examples of C2-C20 alpha olefinic monomers employed in the present invention for the manufacture of homo-, co- and terpolymers are ethylene, propylene, butene-l, pentene-l, hexene-l, octadecene-l, 3-methylbutene-l, styrene, ethylidene norbornene, 1,5-hexadiene and the like and mixtures thereof. Isotactic polymerization of propylene and higher olefins is especially preferred, including block copolymerizations with ethylene. The trialkyl metal compound and the supported transition metal compound can be added separately to the reactor or premixed before addition to the reactor, but are preferably added separately. In the case of the formation of R2MR', the metal di- or trihalide compounds which are used are a metal halide consisting of R'MX2,1X3 or a mixture thereof, wherein M is group consisting of Al, Ga, or In, R' is a C1 to C20 primary alkyl, alkenyl or aralkyl group or hydride; X is chloride, bromide or a monovalent anion which cannot initiate polymerization of olefinic monomers, wherein the anion is alkoxide, phenoxide, thioalkoxide, carboxylate, etc. or a fixture thereof. Typical but nonlimiting examples are ethyl aluminum dichloride, aluminum trichloride, ethyl aluminum dibromide, ethyl chloroaluminum bromide, octayl aluminum dichloride, ethyl indium dichloride, butyl aluminum dichloride, benzyl aluminum dichloride, ethyl chloroaluminum butoxide and mixtures thereof. Mixtures of metal halide compounds can be readily employed. The C2 to C4 alkyl aluminum dihalides are most preferred for high stereospecificity and the monoalkylaluminum dichlorides are most preferred. The diorganomagnesium compound with whih.,-R2MX2 or MX3 is reacted has the general formula lig wherein R can be the same or different and is a C3 to C20, secondary or tertiary alkyl, cycloalkyl, aralkyl or alkenyl group'. Typical, but non-limiting examples are (s-Bu)2Mg, (t-Bu)2-Mg or (i-Pr);Mg. Mixtures of diorganomagnesium compounds can be readily employed providing at least one secondary or tertiary group is present. The most preferred organic groups are secondary and tertiary alkyl groups, e.g. t-Bu or s-Bu. The molar ratio of the alkyl metal halide compound (R'MX2) to the diorganomagnesium compound is 0.5:1 to 2:1, more preferably 0.7:1, and most preferably about 1:1. For the MX3 compound the ratio is 1:1 to 1:3, most preferably 2:3. The molar ratio of the metal halide compound or the diorganomagnesium compound to the transition metal compound is less than 200:1 or higher and more preferably less than 100:1. The metal halide compound and diorganomagnesium compound can be added separately to the reactor containing the transition metal compound but are preferably premixed before the addition to the reactor. Employing either the metal halide compound or the diorganomagnesium compound alone with the transition metal compound does not provide the improved catalyst efficiency and stereospecificity as envisaged in this application. In order to attain this, it is necessary to employ both the metal halide compound and diorganomagnesium compound in combination with the transition metal compound in the critical proportions as previously defined. The concentration of the transition metal in the polymerization zone is 0.001 to 5mM, preferably less than 0.lmM. In the case of the formation of RMR'2 the metal alkyl compounds which are used are metal alkyl compounds. - consisting of R'2MX or R'3M EMI11.1 mixtures thereof, wherein M is A1, Ga or In, R' is a EMI11.2 C1 C1 to C20 primary alkyl, alkenyl tr aralkylAor hydride; ;¯, X is & monovalent anion which cannot initiate polymerization of olefins, such as F, C1, Br, OR", SR" or OOCR", wherein R" is & BR< - C1 to C20 alkyl, branched alkyl, cycloalkyl, aryl, naphthenic, aralkyl or alkenyl group , X is more preferably C1 or Br and most preferably C1. Typical, but non-limiting examples are diethyl aluminum chloride, aluminum triethyl, diethylaluminum bromide, diethylaluminum benzoate, diisobutylaluminum hydride, dioctylaluminum chloride, diethylgallium butoxide, diethylindium neodecanoate, triethylindium, dibenzylaluminum chloride and mixtures thereof. Mixtures of metal alkyl compounds can be readily employed. The C2 to C4 alkyl aluminum compounds are preferred for high stereospecificity, and the dialkyl aluminum chlorides are most preferred. The mono-organomagnesium compound with which R' 1 2 or R r is reacted has the general formula RMgX where R is & BR< C to C20 secondary or tertiary alkyl, cycloalkyl, aralkyl or alkenyl group. X is an anion which cannot initiate polymerization of olefins, such as C1, Br, OR", SR" ar OOCR", wherein R" is a C1 to C20 alkyl, branched alkyl, cycloalkyl, naphthenic, aryl, aralkyl, allyl out alkenyl group 4. Typical, but non-limiting examples are s-BuMgCl, t-BuMgC1, s-BuMgOOCC6H5, r or s-BuMgOC15H31, and mixtures thereof. Mixtures of organomagnesium compounds can be readily employed. The most preferred X groups are OR" and OOCR" and the most preferred R groups are secondary or tertiary alkyls. The molar ratio of the organomagnesium RMgX compound to the metal alkyl compound (R'2MX or R'3M) is 2 to 1 to 1 to 2, most preferably 1 to 1. The molar ratio of the metal alkyl compound or the organomagnesium compound to the transition metal compound is less than 200 to 1 or higher and more preferably less than 100 to 1. The metal alkyl compound (R'2MX or R'3M) and organomagnesium compound RMgX can be added separately to the reactor containing the transition metal compound but are preferably premixed before the addition to the reactor. Employing either the metal alkyl compound or the organomagnesium compound alone with the transition metal compound does not provide the improved catalyst efficiency and stereospecificity as envisaged in this application. In order to attain this, it is desirable to employ both the metal alkyl compound and organomagnesium compound in combination with the transition metal compound =., the proportions previously defined. The concentration of the transition metal in the polymerization zone is 0.001 to 5mM, preferably less than 0.lmM. Example 1 An aluminum alkyl compound containing both secbutyl and ethyl groups was prepared by mixing equimolar amounts of (sec-butyl)201g 0.16Et2O and ethyl aluminum dichloride in heptane, heating to 650C, 15 min., separating the magnesium chloride solids and vacuum stripping the clear solution. N4R analysis indicated the composition sBu2AlEt 0.45Et2O. Metals analysis showed that only 0.50% Mg was present in this fraction. The above liquid alkyl aluminum compound (0.2g) was used as cocatalyst with 0.2g catalyst prepared by reacting anhydrous MgC12 (5 moles) with TiC14 C6H5COOEt (1 mole) in a ball mill 4 days, followed by a neat TiC14 treat at 800C, 2 hours, washed with heptane and vacuum dried. The catalyst contained 2.68% Ti. Propylene was polymerized in 500 ml n-heptane at 650C, 1 hour at 765 to 770mm. Polymerization rate was 130 g/g catalyst/hour and the polymer insoluble in boiling heptane = 97.6%. Example 2 Three alkyl aluminum compounds containing secbutyl groups were prepared by reacting the proper stoi chiometrid amounts of sec-butyl lithium in heptane with either ethyl aluminum dichloride or diethylaluminum chloride, heating to boiling, filtering the insoluble LiCl, and vacuum stripping the clear solutions. Nearly theoretical yields were obtain of s-BuEtAlCl (A), s-Bu2EtAl (B) and s-BuEt Al tC). Compositions were established by ÚH and 13C NMR and by G.C. analysis of the alkyl fragments. Polymerizations were carried out as in Example 1 using 1 mmole aluminum alkyl compound and 0.2 g of the supported TiC14 catalyst. The results summarized in Table I are compared to those obtained using the control ethyl aluminum compounds. In all three runs with sec-butyl alkyls, both activity and stereospecificity (heptane insolubles) were higher than those obtained with the conventional ethyl aluminum compounds. The trialkyls were far superior to the dialkyl aluminum chlorides and the di-sec-butyl aluminum ethyl was clearly superior to the mono-sec-butyl aluminum diethyl compound. TABLE I Rate Run Al Alkyl g/g/ Cat/hr. % HI A Et2AlCl control 48.9 68.0 B s-Bu1.07EtAlCl0.93 64.6 79.1 C Et3Al control 344 83.1 D s-BuEt2Al 380 90.3 E s-Bu2EtAl 357 93.0 Example 3 Sec-alkyl aluminum hydrides also give improved results compared to the closely related primary alkyl aluminum hydride (i-Bu2AlH), following the procedure of Example 2. TABLE II Run Al Alkyl Rate % HI N i-Bu2AlH control 456 83.1 O s-Bu2.6AlH0.4 462 85.8 P* AlEt3 control 241 82.3 Q* iBu3Al control 264 89.3 R* s-BU2 6AlHO.4 284 90.7 S* s-BU2 3AlHo.7 223 9,0.1 * Another catalyst preparation was used. It was made by ball milling 5 moles MgCl2 with 1 mole ethylbenzoate for one day, adding 1 mole TiC14 and milling 3 days, then treating with neat TiC14 at 800C, 2 hours, washing with heptane and vacuum dried. The catalyst contained 3.44% Ti. Run 0 using sec-butyl groups gave higher activity and stereospecificity than Run N using the closely related, but primary, isobutyl groups. Improved results are also seen versus the AlEt3 control using the same supported titanium catalyst (Example 2, Run by. Runs R and S show substantially higher heptane insolubles using two different sec-butyl aluminum hydrides compared to control Runs P and Q using AlEt3 and iBu3Al with the same catalyst. Example 4 The procedure of Example 3, Run P, was followed except that magnesium benzoate was used as a cocatalyst modifier. The magnesium salt was made in situ by reacting a hydrocarbon solution of (n + s-Bu)2Mg with two moles of benzoic acid. The salt slurry was reacted with the alkyl metal cocatalyst in 500 ml n-heptane at 25 to 65"C to obtain a soluble product before the catalyst was added. TABLE III Mmoles Mmoles Run Al Cpd Mg (O0C) 2 Rate % HI A(Control) 1 AlEt3 -- 241 82.3 B 1 AlEt3 0.25 210 93.0 C 1 AlEt3 0.50 0 - D(Control) 1 t-Bu2A1Et -- 248 93.8 E 1 t-Bu2AlEt 0.25 125 97.7 When used in small amounts relative to the aluminum trialkyl cocatalyst, the magnesium benzoate sharply increased stereospecificity as measured by the percent boiling heptane insolubles (Runs B and E vs. A and D). Adtivity decreased somewhat, but the results for both rate and % HI were superior to those of conventional TiC13 catalysts (Example 3 Runs N, P and Q). At a ratio of 0.5 Mg(OOC)2 to AlEt3, the catalyst was inactive The modifier was effective with both types of aluminum trialkyls, but it gave the highest stereospecificity with the novel trialkyl aluminum cocatalysts of this invention. Example 5 The procedure of Example 3, Run P, was followed except that dialkyl aluminum alkoxides were used as cocatalyst modifiers. TABLE IV Run Mmoles A1R3 Mmoles Al Alkoxide Rate % HI V 0.8 t-Bu2AlEt 0.2 t-Bu2AlOCMeEt0, 196 .94.2 W 0.8 t-Bu2A1Et 0.2 t-Bu2AlOCEt02 191 94.6 X* 1 AlEt3 -- 506 81.6 Y* 1 AlEt3 10 Et2AlOC15H3l 113 95.5 * Another catalyst preparation was used (contained 3.16% Ti). Comparison of Runs V and W with control run D, Example 4, shows that the alkoxide additives increased stereospecificity as measured by heptane insolubles. This was also true for Run Y versus its control (Run X). In this case, a large excess of alkoxide was used relative to the A1R3. These results are opposite to those using unsupported TiC13 catalysts in which it is known that dialkyl aluminum alkoxide cocatalysts produce low heptane insoluble products. Example 6 The procedure of Example 5 was followed using another catalyst preparation having 3.38% Ti and using a hindered Lewis base in place of the Al alkoxide. TABLE V Mmoles Run A1ET 'moles Hindered Base Rate % HI E 1 2 Tetramethyl THF (1) 277 94.1 F 1 1 Tetramethylpiperidine (2) 402 95.5 G 1 2 i Pr2NEt 289 95.3 H 1 1 Di-orthotolylamine 309 93.4 Mmoles Unhindered Base Control 1 1 MeOt-Bu 129 91.3 Control 1 1 Met-BuNH 11 95.5 Control 1 1.06 Et3N 38 97.0 Control 1 1 2,6-Di-t-butylpyridine 487 84.8 Control 1 481 81.8 (1) 2,2,5, 5-tetramethyltetrahydrofuran. (2) 2,2,6,6-tetramethylpiperidine. Comparison with the Control Run without a hindered base shows that the hindered bases (Runs E-H) gave both high activity and high HI, whereas the control runs with unhindered bases -gave improved HI but with a serious loss of activity. The completely hindered 2,6-di-t-butylpyridine had little effect on either rate or HI. EXAMPLE 7 The procedure of Example 6 was followed except that the catalyst preparation of Example 5, Run X, was used. TABLE VÏ Mmoles Run AlR3 Mmoles Hindered Base Rate % HI I 1 ALERT3 1 Diphenylamine 233 95.6 J 1 AlET3 2 Tetramethylpiperidine 292 97.1 K 1 sBu2A1ET 1 Tetramethylpiperidine 302 95.0 L 1 i Bu3Al 1 Tetramethylpiperidine 423 97.1 Mmoles Unhindered Base Control 1 sBu2AlEt 1 2,6-Dimethylpiperidine 4 ' 85.4 Control 1 AlEt3 1 Ethylpbenzoate 0 - Control 5 AlEt3 4 Tetrahydrofuran 100 83.0 Comparison with Control Run X of Example 5 shows that the hindered bases gave both high activity and high HI, whereas the unhindered bases gave both low activity and HI. EXAMPLE 8 The procedrue of Example 6 was followed using various alkyl metal compounds, Lewis bases and base concentrations. TABLE VII Mmoles Run AlR3 Mmoles Hindered Base Rate % HI M 1 AlEt3 0.2 Tetramethylpiperidine 441 94.7 N 1 AlEt3 1 t-Bu(i-Pr)NH 279 95.4 O 1 AliBu3 1 i-Pr2NMe 367 94.0 P 1 AliBu3 0.2 C6H5CH2(t-Bu)NH 407 94.6 Q 1 AlsecBu3 1 Tetramethylpiperidine 291 96.7 Control 1 AliBu3 500 89.7 Control 1 AlsecBu3 461 91.6 Comparison with the control runs (AlEt3 control in Example 6) shows that the hindered bases gave major increases in isotacticity, as measured by the percent heptane insoluble, with only a minor loss of activity. EXAMPLE 8 Polymerization was carried out in liquid propylene using a mixture of an unhindered base plus a hindered base. A l-liter reactor was charged with AlEt3, 2,2,6,6-tetramethylpiperidine (TMPip) (hindered base) and ethylbenzoate (EB) (unhindered base) in a few ml n-heptane. Liquid propylene (500 ml at about 70C) was added rapidly and the temperature was increased rapidly to 650C., the catalyst was added and the temperature was maintained at 650C. TABLE VIII t Cocatalyst,mmoles Time Rate Run mg. AlEt3 TMPiP EB min. g/g Cat/hr. %HI R 15 0.3 0.9 0.01 30 11500 95.0 S 10 0.2 0 0.02 30 18300 87.9 T 15 0.3 0.9 0 30 13800 92.4 Control 10 0.2 0 0 27 20600 68.6 Run R contained both hindered and unhindered bases added with the cocatalyst and gave outstanding results compared to S or T, in which one of the bases was omitted. All three experiments gave greatly improved stereospecificity (% HI) compared to the control run in which no bases were added with the-cocatalyst. The catalyst component, contained about 18 trot. % ethylbenzoate but this was ineffective for producing high HI as shown by the control run. The results in Run R were surpising since they show that the use of the two types of Lewis bases gave significantly better results than would be expected based on the results from each base alone.

Claims: CLAIMS: 1. A catalyst composition which comprises a mixture: (a) at least one alkyl metal compound having the formula R"'3M, wherein M = Al, Ga or In, R1 is a C1 to C20 primary branched primary, secondary or tertiary alkyl, cycloalkyl, alkenyl or aralkyl group, hydride or a mixture thereof; (b) a Group IVA to VIII transition metal chloride or bromide on a layer lattice support, the molar ratio of said R'' to said transition metal chloride or bromide being about 0.-5:1 to 200:1, and (c) at least one unhindered Lewis base, said Lewis base not causing excessive cleavage of metal-carbon bonds or loss of active sites under polymerization conditions; and (d) at least one hindered Lewis base. 2. A composition according to claim 1 wherein said support is MgC12. 3. A composition according to either of claims 1 and 2 wherein said transition metal chloride or bromide is TiC13, TiBr3 or TiBr4 or a mixture thereof. 4. A composition according to either of claims 1 and 2 wherein said transition metal chloride or bromide is TiC14. 5. A composition according to any one of the preceding claims wherein said hindered Lewis base is a piperidine, a pyrrolidine, - a ketone, a tetrahydrofuran, a secondary or tertiary aromatic amine, a tertiary aliphatic amine ora.mixture thereof. 6. A composition according to claim 5 wherein said hindered Lewis base is 2,2,6,-tetramethylpiperidine, 2,2,5,5-tetramethyl-pyrrolidine, 2,2,5, 5-tetramethyltetrahydrofuran, di-tert-butylketone or 2-6-diisopropylpiperidine or a mixture thereof. 7. A composition according to any one of claims 1 to 4 wherein said hindered Lewis base is orthotolyl t-butylketone, methyl 2,6-di-tertbutyl-phenylketone, diisopropylethylamine, t-butyldimethylamine, or 6methyl-2-isopropylpyridine, or a mixture thereof. 8. A compstion according to any one of claims 1 to 4 wherein said hindered Lewis base is diphenylamine, di-ortho-tolylamine, N-N-diethylaniline, di-ortho-tolylketone or a mixture thereof. 9. A composition according to any one of the preceding claims wherein said R1 ''3M contains at least one of said alkyl groups having 2 to 4 carbon atoms. 10. A composition according to any one of the preceding claims which also contains a salt of a Group IA to IIB metal.

Inventors: LANGER, ARTHUR WALTER, JR.
Applicants: EXXON RESEARCH AND ENGINEERING COMPANY
Application year: 1981
Main classification: C08F10
IPC codes: C08F10, C08F4