Ternary catalytic system and process for the production of polydiolefins

Abstract: A catalytic system to polymerize diolefinic monomers consists of a lanthanide salt, an organometallic compound of a metal belonging to groups I, II and III of the periodic table of elements and an organometallic compound of boron. The polymers obtained are characterized in that they have a high degree of 1,4 chain units and ratio between 1.4-cis/1,4-trans units which can vary as desired, and also a narrow molecular weight distribution.

Description: The present invention relates to a ternary catalytic system obtained by the interaction of a salt of a metal , an alkyl, hydride or alkyl-hydride compound and a organometallic derivative of boron. The present invention also relates to the preparation of said catalytic system and its use in the polymerisation of diolefins, wherein the content of 1,4-cis and 1,4-trans units of the polydiolefins obtained can vary by acting on the same catalyst. The polydienes produced with this catalytic system are characterised in that they have a narrow molecular weight distribution [expressed as a ratio between the weight average molecular weight (M w ) and the number average molecular weight (M n )]. A metal belonging to the group of lanthanides, as is generally accepted in the known art, means a metal belonging to the group comprising: Scandium, having an atomic number of 21; Yttrium, having an atomic number of 39; a metal having an atomic number between than of Lanthanum (57) and Lutetium (71). These metals are part of group IIIA of the periodical table, according to the IUPAC definition prior to 1985. In addition for some of the formulae indicated in the text the following acronyms are used: TMA = Al(CH 3 ) 3 ; TEA = Al(C 2 H 5 ) 3 ; TIBA = Al(C 4 H i 9 ) 3 ; DIBAH = AlH(C 4 H i 9 ) 2 ; Nd(Ver) 3 = neodymium versatate; BPFF = B(C 6 F 5 ) 3 . In the known art, there are ample descriptions of catalytic systems with three components, based on derivatives of lanthanides (rare-earth), for the polymerisation of butadiene having a polymer with a high 1,4-cis chain units. For example German patents DE-A-1812935, DE-A-2011543, DE-A-2833721, DE-A-2830080 and International PCT patent Application WO-93-05083, describe the preparation of polybutadiene with a high degree of 1,4-cis with the use of catalytic systems based on compounds of rare- earth and aluminium trialkyls. In all cases the presence of a halogenating agent is essential, generally a derivative of boron having the general formula BR n X 3-n , of aluminium having the formula AlR n X 3-n , silicon having the general formula SiR n Cl 4-n , wherein R is an alkyl radical and X is a halogen atom such as Cl, Br or I. The type of organometallic compound of aluminium or halogen used can influence the activity of the catalyst and the molecular weight of the final polymer but the stereospecificity is not influenced in any way. The examples provided in the patents of the known art mentioned above indicate that the catalytic systems can be prepared both with the well-known technique "in situ" or preformed, with or without an ageing period, before their use in the polymerisation reaction. Interesting examples of preformed catalytic systems with an easy industrial preparation and having a high activity are those described in European patents EP-A-201962, EP-A-201979 and EP-A-207559, wherein an alkyl halide, for example t-Butylchloride, is used as halogenating agent. All of the documents of the known art quoted so far clearly demonstrate the production of polymers with a high degree of 1,4-cis units, starting from preformed catalytic systems, or systems prepared "in situ", comprising an aluminium trialkyl, a lanthanide salt and a halogenating agent. The known art also describes the use of binary catalytic systems based on lanthanide salts and aluminium trialkyls. In the latter case the stereospecificity of the final polymer greatly depends on the type of lanthanide salt. In this way, by using lanthanide halides as such or in the form of complexes with alcohols, amines, organic acids or alkylphosphates, together with aluminium trialkyls, polydiolefins are obtained, which, in the case of butadiene, have chains of monomeric units of the 1,4-cis type of over 90% (typically 95-98%). Valid examples of catalytic systems of this type are disclosed in JP-A-58 061107 (Japanese patent 8 361 107), JP-A-59 113003 (Japanese patent 84113003), US-A-4,575,538, DD-A-243034, CN-A-1036962 and SU-A-675866 respectively. When the binary system is obtained starting from an aluminium trialkyl together with an oxygenated lanthanide salt, with the rigorous exclusion of any form of halogenating agent, either organic or inorganic, the final polymer is a polybutadiene with a high content (74-90%) of 1,4-trans units. Examples of these catalytic systems are claimed in patents EP-A-091287 and JP-A-02 060907, (JP 9060907), which describe the use of binary systems based on a lanthanide carboxylate and an alkyl derivative of magnesium (MgBut 2 ) or lithium (Bu-Li) together with an aluminium trialkyl (AlEt 3 ) respectively. In both cases, apart from the use of costly components such as the alkyls of lithium or magnesium, the catalyst has a limited activity and requires long polymerisation times (24hrs) to reach industrially acceptable conversions. In addition, only plastomers with a high 1,4-trans degree can be obtained without the possibility of changing the stereospecificity of the polymer to higher values of 1,4-cis units typical of an elastomer. N.N. Chigir et al. describe (International Polymer Science and Technology, 10, 1983 N° 6 - Stereospecificity of systems based on organo-neodymium compounds and Al(iso-C4H9) 3 for the polymerisation of dienes) the stereospecificity of polydienes obtainable in the presence of lanthanide catalytic systems non containing halogen, particularly in the presence of neodymium triisopropylate or tricarboxylate in combination with tri-isobutyl Aluminium. These systems are characterised by low activity and lead to polymers containing mainly 1,4-trans units. The documents of the known art mentioned above clearly indicate that elastomeric polybutadienes with a high degree of 1,4-cis units can only be obtained with ternary or binary systems when halogen atoms in the form of organic or inorganic halogenating agents are present in the catalytic mixture, or starting from halogenated salts of lanthanides. Without these, only polymers with a high degree of 1,4-trans units (>75%) can be obtained and it is not possible to vary the relative percentage value of 1,4-trans and 1,4-cis units. Research carried out by the Applicant has, on the other hand, surprisingly discovered a ternary catalytic system, based on lanthanides, capable of supplying an elastomeric polybutadiene with varying values of 1,4-cis and 1,4-trans units as required without organic or inorganic halogenating agents, such as those indicated in the above documents; more specifically the ternary catalytic system consists of: (a) a lanthanide salt having the general formula ML 3 ; (b) an aluminium alkyl having the general formula AlR 1 3 ; (c) an organometallic derivative of boron having the general formula BR 2 3-m (C 6 H 5-n R 3 n ) m , the meaning of M, L, R 1 , R 2 and R 3 being explained in detail below. The catalytic system is formed when the three components are reacted in suitable molar ratios and under suitable experimental conditions, as will be better illustrated hereafter. In accordance with what is specified above, a first aspect of the present invention relates to a ternary catalytic system for the polymerisation of diolefinic monomers to polydiolefins having a narrow molecular weight distribution, basically consisting of: (A) a salt having the general formula ML 3 wherein M represents Sc, Y or a metal of the lanthanide group with an atomic number of between 57 and 71 and L a general anionic binder with the sole exclusion of halogen binders, (B) an alkyl, hydride or alkyl-hydride compound having general formula MeR 1 z wherein, Me is a metal belonging to groups I, II or III of the periodic table; R 1 is: an aliphatic or cycloaliphatic radical containing from 1 to 20 carbon atoms, an aromatic radical containing from 6 to 20 carbon atoms, a hydrogen atom, z is an integer from 1 to 3 equal to the value of Me, on condition that, if z is equal to 3, only one of the three R 1 groups bound to the metal can be hydrogen, (C) an organometallic derivative of boron having general formula BR 2 3-m (C 6 H 5-n R 3 n ) m wherein, R 2 is an aliphatic radical, linear or branched, containing from 1 to 20 carbon atoms; a cycloaliphatic group containing from 6 to 20 carbon atoms; an aromatic group containing from 6 to 20 carbon atoms, R 3 is a fluorine atom or CF 3 group; m is an integer between 1 and 3 n is an integer between 1 and 5. As mentioned briefly above, component (A) of the catalytic system, having general formula ML 3 , consists of an Sc, Y or lanthanide salt with an atomic number of between 57 and 71. Although the catalytic system claimed is absolutely general, for various reasons, with respect to availability, commercial price and catalytic activity, as well as the characteristics of the final polymer, the salts having general formula ML 3 where M is Nd, Pr, Dy, La, Gd and Y are preferred. The binder L is a general anionic binder with the only condition that it is not halogen. Bearing in mind what is specified above, valid, non-restrictive examples of salts of the metals claimed above are carboxylates such as naphthenate, versatate, pivalate, 2-ethylhexanoate, formiate, acetate, trifluoroacetate; alkoxides such as methylate, butylate, isopropylate, ter-butylate; phenolates; thioalkoxides; dialkylamides; bis-trimethylsilylamides; acetylacetonates and hexafluoroacetylacetonates. Component (B) of the catalytic system is represented by a hydride, alkyl or mixed derivative of a metal belonging to groups I, II or III of the periodic table of elements. Examples of this compound can be: lithium hydride, lithium-aluminium hydride, lithium butyl, lithium sec-butyl, sodium hydride, magnesium hydride, magnesium dibutyl, aluminium trimethyl, aluminium triethyl, aluminium triisobutyl, aluminium diisobutyl-monohydride, aluminium trioctyl, gallium trimethyl, gallium triethyl. For reasons of solubility, industrial availability and price, the alkyl derivatives of aluminium such as aluminium trimethyl (TMA), aluminium triethyl (TEA), aluminium triisobutyl (TIBA) and aluminium diisobutyl-monohydride (DIBAH) are preferred. Component (C) of the catalytic system consists of an organometallic derivative of boron having the general formula BR 2 3-m (C 6 H 5-n R 3 n ) m wherein R 2 is an aliphatic radical, linear or branched containing from 1 to 20 carbon atoms; a cycloaliphatic group containing from 6 to 20 carbon atoms; an aromatic group containing from 6 to 20 carbon atoms; R 3 is a fluorine atom or CF 3 group; m is an integer between 1 and 3; n is an integer between 1 and 5. Examples of this group of derivatives are: B(C 6 F 5 ) 3 , B(CH 3 )(C 6 F 5 ) 2 , B(C 2 H 5 )(C 6 F 5 ) 2 , B(C 6 H 4 F) 3 , B(C 6 H 3 F 2 ) 3 , B(C 6 H 2 F 3 ) 3 , B[C 6 H 3 (CF 3 ) 2 ] 3 , and B(C 2 H 5 )[C 6 H 3 (CF 3 ) 2 ] 2 . As specified above, the catalytic system of the present invention is prepared by mixing in suitable ratios components (A), (B) and (C), previously described, in an aliphatic, cycloaliphatic or aromatic solvent or their mixtures. This preparation can be carried out either with "in situ" or with preformation techniques. In the former case, the preparation of the catalytic system is carried out by adding, in order, component (B), the monomer to be polymerised, component (A), and, last of all, component (C), to the solvent, obtaining a limpid solution and the polymerisation is carried out in a homogeneous phase. The order of introducing the monomer, component (A) and component (B) is not binding whereas, as far as component (C) is concerned, the best results are obtained by adding this as last. In the latter case, the preformation of the catalytic system is carried out by reacting components (A), (B) and (C), in the order mentioned above, in the desired solvent, for a period of 0.5-24 hours at temperatures of between 0 and 80°C in the presence of or without small quantities of the diolefin to be polymerised. Aliphatic, cycloaliphatic or aromatic hydrocarbons can be used in the preformation reaction. The use of an aromatic solvent gives a homogeneous solution, whereas the use of an aliphatic solvent produces a partial formation of solid precipitate. The formation of the precipitate however does not negatively influence the catalytic activity as the precipitate formed during the preformation of the catalyst redissolves in the polymerisation environment forming a homogeneous phase. Experimental work has shown that the best preformation conditions are obtained by carrying out the reaction between (A), (B) and (C) in toluene, in the order specified above, at 50°C for 1 hour in the presence of or without less than 1 g of butadiene per 1 x 10 -3 moles of component (A). In the formation of the catalytic system, the molar ratios in which components (A), (B) and (C) are reacted, are of considerable importance. Research carried out by the applicant has shown that the molar ratio (B)/(A) can vary between 3 and 100 and, preferably, between 8 and 20. Values higher than 100, although they can be used, are not advisable as they do not provide any improvements in the catalytic process and the cost increases due to component (B). The molar ratio (C)/(A) can vary between 0.1 and 50 but values between 1 and 3 are preferred. As already mentioned, a further aspect of the present invention relates to the use of the catalytic system described above in a polymerisation process of conjugated diolefins monomers, (for example butadiene), this process being characterised by a high polymerisation rate and by the production, with high yields, of a polybutadiene with a varying degree of 1,4-cis and 1,4-trans units, controllable molecular weights and a narrow molecular weight distribution. More specifically, the resulting polymer of this process has percentage values of 1,4-cis and 1,4-trans units which vary from 35/63 to 98/1 respectively, whereas the percentage value of 1,2 units is generally between 0.5 and 2. In addition, the value of the weight average molecular weight (Mw) can vary between 50x10 3 and 1x10 8 and the ratio between the weight average molecular weight (Mw) and the number average molecular weight (Mn) is between 1.5 and 2.6. It can be easily confirmed that all the alkyl derivatives generate, together with compounds (A) and (C), a highly active catalytic system in the polymerisation of high polymer diolefins with a 1,4 chain units content of more than 98%. Research carried out by the Applicant has shown however that the nature of component (B) has a determining influence on the composition of the final polymer. Consequently the use of TMA produces a final polymer having a percentage of 1,4-cis/1,4-trans units of 30/70 respectively whereas the use of TIBA produces a polymer with a 98/1 ratio of the same units. The catalysts prepared with TEA and DIBAH produce polymers having intermediate ratio values between the 1,4-cis and 1,4-trans units. Other differences have been verified depending on the nature of compound (B) and relating to the activity of the catalytic system and value of final molecular weights of the polymer. It is well-known to experts in the field, however, that in a Ziegler-Natta type polymerisation, these characteristics often depend on the nature of the alkyl derivatives used for the preparation of the catalytic system and there are plenty of examples in the known art in this respect. Even if the catalytic system claimed by the applicant is active in the polymerisation of unsaturated hydrocarbon derivatives, in particular, diolefins such as 1,3-butadiene, isoprene, 1,3-pentadiene, 2,3-dimethylbutadiene, the monomer preferably used is 1,3-butadiene as the polymers of this monomer are products which are the most widely used industrially. The activity of the catalytic system depends on the nature of components (A) and (B) used and on the formation method of the catalytic system. Alkoxide derivatives therefore prove to be generally more active than carboxylate derivatives and TIBA has a similar activity to DIBAH and both are better than TMA. In general, with all the aluminium alkyls, the best activity has been obtained by preforming the catalytic system in the presence of or without small quantities of monomer and ageing for 1 hour at a temperature of 50°C. A particularly interesting feature is that the activity of preformed catalytic systems, in the presence of or without monomer, remains high even after conservation periods of the catalytic system of several weeks. The polymerisation reaction is carried out indifferently in an aliphatic solvent, n-hexane or a C 6 petroleum cutting with a boiling point of between 64 and 68°C, or in an aromatic solvent, toluene. An interesting characteristic of the catalytic system claimed in the present invention is its high activity in polymerisation with the double advantage of minimising the cost of the catalytic system and the quantity of impurities which remain in the polymer after its recovery. In fact, activities equal to 5-10 x 10 -4 moles of component (A) per Kg of diolefin polymerised are obtained with reaction times of between 0.5 and 2 hours at temperatures of between 0 and 100°C. A further aspect of the present invention relates to the polymer obtained using the above catalytic system. It consists of polybutadiene with a high 1,4 chain units content in which it is possible to vary the ratio between the 1,4-cis and 1,4-trans type units from 30/70 to 98/1 depending on the type of component (B) used. These variable cis-trans polymers form an interesting class of materials ranging from elastomers which are crystallizable under stretch, those with 1,4-Cis units >95%, to completely amorphous elastomers at room temperature, with 50% in 1,4-trans units. A common characteristic of the whole group of polymers obtained with the catalytic system claimed, and this is a further aspect of the present invention, is the low value of molecular weight distribution of the polymers intended as a ratio between the weight average molecular weight and the number average molecular weight (Mw/Mn), of between 1.5 and 2.6. This narrow distribution ensures that there are no high or low molecular weight fringes in the polymer which are always present when the Mw/Mn distribution exceeds the value of 3. In this respect, the polymerisation carried out at 0°C is to be particularly interesting, as in this case high molecular weights and a molecular weight distribution (Mw/Mn) of 1.6 are obtained. Another interesting characteristic of the polymers produced according to the present invention is the lack of any type of gel (micro or macro gel) which is often present in polybutadiene with a high 1,4-Cis chain units with a weight average molecular weight higher than 500 x 10 3 . Following this general description of the catalytic system and polymerisation process of the present invention, detailed examples of the preparation of the catalyst, polymerisation reaction and polymer obtained, are given below. These examples describe the experimental operations in order to provide a better understanding of the invention itself. Example 1 Preparation of the preformed catalyst. Procedure A. 20 cm 3 of toluene, 1.65x10 -3 moles of component (A) and 29.7x10 -3 moles of component (B) are introduced in an inert atmosphere into a 100 cm 3 graded test-tube, equipped with a lateral tap for the nitrogen flow and a magnetic anchor. The mixture is left under stirring until the solid has completely dissolved and 4.95x10 -3 moles of component (C) are then added. Using the graded scale of the test-tube, the final volume is brought to 50 cm 3 with toluene and the mixture is left to age at room temperature under stirring for the desired time. The solution of preformed catalyst thus obtained, which contains 3x10 -3 gAtoms/cm 3 of metal of component (A), is used for the polymerisation tests. Procedure B. Following the procedure of process A, a toluene solution of catalyst is prepared by introducing, in order, 0.9x10 -3 moles of component (A), 16.2x10 -3 moles of component (B) and 2.7x10 -3 moles of component (C). The solution is brought to 30 cm 3 with toluene and is maintained at 50°C for 1 h, under stirring. The concentration proves to be 3x10 -3 gAtoms/cm 3 of metal of component (A). Procedure C. 20 cm 3 of toluene, 1,15x10 -3 moles of component (A) and 20.7x10 -3 moles of component (B) are introduced in an inert atmosphere into a 100 cm 3 graded test-tube, equipped with a lateral tap for the nitrogen flow and a magnetic anchor. The mixture is left under stirring until the solid has completely dissolved and 1.2 g of liquid butadiene and 3.4x10 -3 moles of component (C) are then added, in order. Using the graded scale of the test-tube, the final volume is brought to 38 cm 3 with toluene and the preformation reaction is carried out under stirring and at room temperature for the desired time. The final solution of preformed catalyst thus obtained, which contains 3x10 -3 gAtoms/cm 3 of metal of component (A), is used for the polymerisation tests. Procedure D. Following the procedure of process A, a toluene solution of catalyst is prepared by introducing, in order, 25 cm 3 of toluene, 1.3x10 -3 moles of component (A), 23.4x10 -3 moles of component (B), 1.4 g of liquid butadiene and 3.9x10 -3 moles of component (C). The solution is brought to 43 cm 3 with toluene and is maintained at 50°C for 1 h, under stirring. The concentration proves to be 3x10 -3 gAtoms/cm 3 of metal of component (A). Example 2. The polymerisation of butadiene is described using a catalyst prepared in the presence of a monomer and without ageing ("in situ" preparation). A 200 cm 3 drinking bottle, previously heated in a muffle furnace at 140°C, is cooled to room temperature under a perfectly dry nitrogen flow, to eliminate the environmental air and humidity. The following products are charged into the bottle which is maintained under a nitrogen atmosphere and immersed in a bath at 0°C: 150 cm 3 of anhydrous hexane, 20 g of anhydrous butadiene liquid removed from an overturned cylinder with a hypodermic syringe sealed to the cylinder valve, 1 cm 3 of a hexane solution containing 3x10 -5 moles/cm 3 of Nd(OBu) 3 , 0.54 cm 3 of a 1 molar solution of Al(C 4 H 9 i ) 3 and 0.18 cm 3 of an 0.5 molar solution of B(C 6 F 5 ) 3 . The bottle is then closed with a crowned top equipped with a Teflon (R) seal, placed in a bath at 50°C and magnetically stirred for 4 hrs. The bottle is then rapidly cooled in a bath at 0 C, opened and the contents poured in 300 cm 3 of methanol containing 0.5 g of a suitable antioxidant. The coagulated polymer is collected, washed three times with methanol and then dried in a vacuum oven heated to 60°C obtaining 19 g (95% conversion) of dry polymer whose structure, upon IR analysis, proves to be 92% 1,4-cis, 7% 1,4-trans, 1.0% 1,2. Gel Permeation Chromatography analysis shows that the polymer has a Mw of 200x10 3 and Mw/Mn = 2. Examples 3-6 The influence of the type of component (B) on the stereospecificity of the polymer obtained is shown. Following the operating procedure, the concentrations and molar ratios indicated in example 2, four catalysts are prepared with the "in situ" technique, using Nd(OBu) 3 as component (A) and BPFF as component (C). The type of component (B) used, the polymerisation conditions and results obtained are shown in table 1. Example 7 Butadiene is polymerised using a preformed catalyst. A 200 cm 3 drinking bottle, previously heated in a muffle furnace at 140°C, is cooled to room temperature under a perfectly dry nitrogen flow, to eliminate the environmental air and humidity. The following products are charged into the bottle which is maintained under a nitrogen atmosphere and immersed in a bath at 0°C: 150 cm 3 of anhydrous hexane and 20 g of anhydrous butadiene. To this solution, 1 cm 3 is added of a solution containing 3x10 -3 gAtom of neodymium, preformed catalyst prepared with the procedure indicated in example 1 Procedure A using 1.1x10 -3 moles of Nd(Ver) 3 , 19.8x10 -3 moles of TIBA and 3.3x10 -3 moles of BPFF and preforming at room temperature for 24 hrs. The bottle is then closed with a crowned top equipped with a Teflon (R) seal, placed in a bath at 50°C and magnetically stirred for 1 h. After this period, the bottle is then rapidly cooled in a bath at 0°C, opened and the contents poured in 300 cm 3 of methanol containing 0.5 g of a suitable antioxidant. The coagulated polymer is collected, washed three times with methanol and then dried in a vacuum oven heated to 60°C obtaining 18.6 g (93% conversion) of dry polymer whose structure, upon IR analysis, proves to be 96% 1,4-cis, 3% 1,4-trans, 1.0% 1,2. Gel Permeation Chromatography analysis shows that the polymer has a Mw of 482x10 3 and Mw/Mn = 2. Example 8 Following the operating procedure described in example 2, a catalyst is prepared "in situ" by charging into a drinking bottle 150 cm 3 of hexane, 24 g of butadiene, 1 cm 3 of a hexane solution containing 7x10 -3 moles/cm 3 of Nd(Ver) 3 , 1.3 cm 3 of a 1 molar solution of AlH(C 4 H 9 i ) 2 and 0.42 cm 3 of an 0.5 molar solution of B(C 6 F 5 ) 3 . The polymerisation is carried out for 4 hrs at 50°C obtaining 18 g (75%) of polymer with the following analyses: 64% 1,4-cis; 34% 1,4-trans; 2% 1,2; Mw = 200x 10 3 ; Mw/Mn = 2.6. Example 9 A preformed catalyst is prepared according to the procedure described in example 1 Procedure A using as components of the catalytic system 0.7x10 -3 moles of Nd(Ver) 3 , 12.6x10 -3 moles of TMA, 2.1x10 -3 moles of BPFF and preforming for 1 hr at 50°C. Following the method indicated in example 7, 1 cm 3 of the catalyst solution previously prepared is added to 20 g of butadiene in 150 cm 3 of hexane, the polymerisation being carried out at 50°C for 1 hr. 9.0 g (45%) of dry polymer are obtained, whose structure, upon IR analysis, proves to be 32% 1,4-cis, 67% 1,4-trans, 1.0% 1,2. Gel Permeation Chromatography analysis shows that the polymer has a Mw of 332x10 3 and Mw/Mn = 2.4. Example 10 Following the operating procedure described in example 2, a catalyst is prepared "in situ" by charging into a drinking bottle 150 cm 3 of hexane, 20 g of butadiene, 1 cm 3 of a hexane solution containing 3x10 -3 moles/cm 3 of Pr(OBu) 3 , 0.54 cm 3 of a 1 molar solution of Al(CH 3 ) 3 and 0.18 cm 3 of an 0.5 molar solution of B(C 6 F 5 ) 3 . The polymerisation is carried out for 4 hrs at 50°C. 14.4 g (72%) of polymer are recovered. Examples 11-17 Three preformed catalysts are prepared by reacting, according to the procedure and ratios indicated in example 1 Procedures A and B, Nd(OBu) 3 or Pr(OBu) 3 , as components (A), with aluminium trialkyl, as component (B), and BPFF, as component (C). The polymerisation tests carried out as in example 7, show how the preformation technique considerably increases the catalyst activity and this activity remains even for long preformation periods. Components (A) and (B) used, the temperatures and preformation times, the yields and characteristics of the polymers are shown in table 2. Examples 18-22 Four preformed catalysts are prepared starting from Nd(OBu) 3 as component (A), TIBA as component (B) and BPFF as component (C). The preformation is carried out according to the procedure described in example 1 Process C and D. The polymerisation reactions were carried out as illustrated in example 7 and show how preformation in the presence of small quantities of monomer to be polymerised considerably increases the catalyst activity and this activity remains even for long preformation periods without great variations in the characteristics of the polymer. The temperatures and preformation times, the polymerisation conditions and results obtained are shown in table 3. Examples 23-28 Two preformed catalytic systems are prepared starting from Nd(Ver) 3 as component (A), TMA and TIBA as components (B) and BPFF as component (C). The catalytic systems are preformed, according to the procedure indicated in example 1 Procedures C and D, at room temperature for 24 hrs. The polymerisation tests, carried out as indicated in example 7, show the influence of the polymerisation temperature on the molecular weights of the polymers produced. The polymerisation temperatures and results obtained are shown in table 4.

Claims: Ternary catalytic system for the polymerisation of diolefinic monomers to polydiolefins having a narrow molecular weight distribution, basically consisting of: (A) a salt having the general formula ML 3 wherein M represents Sc, Y or a metal of the lanthanide group with an atomic number of between 57 and 71 and L a general anionic binder with the sole exclusion of halogen binders, (B) an alkyl, hydride or alkyl-hydride compound having general formula MeR 1 z wherein, Me is a metal belonging to groups I, II or III of the periodic table; R 1 is: an aliphatic or cycloaliphatic radical containing from 1 to 20 carbon atoms, an aromatic radical containing from 6 to 20 carbon atoms, a hydrogen atom, z is an integer from 1 to 3 equal to the value of Me, on condition that, if z is equal to 3, only one of the three R 1 groups bound to the metal can be hydrogen, (C) an organometallic derivative of boron having general formula BR 2 3-m (C 6 H 5-n R 3 n ) m wherein, R 2 is an aliphatic radical, linear or branched, containing from 1 to 20 carbon atoms; a cycloaliphatic group containing from 6 to 20 carbon atoms; an aromatic group containing from 6 to 20 carbon atoms, R 3 is a fluorine atom or CF 3 group; m is an integer between 1 and 3 n is an integer between 1 and 5. Ternary catalytic system according to claim 1, characterised in that M represents a metal such as Nd, Pr, Dy, La, Gd and Y. Ternary catalytic system according to claim 1, characterised in that the ionic binder L is a carboxylate such as naphthenate, versatate, pivalate, 2-ethyl-hexanoate, formiate, acetate, and trifluoroacetate. Ternary catalytic system according to claim 1, characterised in that the anionic binder L is an alkoxide such as methylate, butylate, ter-butylate, and isopropylate. Ternary catalytic system according to claim 1, characterised in that the anionic binder L is a phenolate, a thioalkoxide, a dialkylamide, a bistrimethylsilylamide, an acetylacetonate, and a hexafluoroacetylacetonate. Ternary catalytic system according to claim 1, characterised in that the organometallic compound (B) is: lithium hydride, lithium butyl, lithium sec-butyl, sodium hydride, magnesium hydride, magnesium dibutyl, aluminium trimethyl, aluminium triethyl, aluminium triisobutyl, aluminium diisobutyl-monohydride, aluminium trioctyl, gallium trimethyl, and gallium triethyl. Ternary catalytic system according to claim 6, characterised in that the organometallic compound (B) is aluminium trimethyl (TMA), aluminium triethyl (TEA), aluminium triisobutyl (TIBA) or aluminium diisobutyl-monohydride (DIBAH). Ternary catalytic system according to claim 1, characterised in that the compound (C) is B(C 6 F 5 ) 3' B(CH 3 )(C 6 F 5 ) 2' B(C 2 H 5 )(C 6 F 5 ) 2' B(C 6 H 4 F) 3 , B(C 6 H 3 F 2 ) 3 , B(C 6 H 2 F 3 ) 3 , B[C 6 H 3 (CF 3 ) 2 ] 3 , and B(C 2 H 5 )[C 6 H 3 (CF 3 ) 2 ] 2 . Method for the in-situ preparation of the catalytic system of claim 1, characterised in that the components and the monomer(s) are mixed in the following order: component (B), the monomer to be polymerised, component (A), and, last of all, component (C), in an aliphatic, cycloaliphatic, aromatic solvent or their mixtures; the molar ratio (B)/(A) being between 3 and 100, the molar ratio (C)/(A) being from 0.1 to 50. Method according to claim 9, characterised in that the molar ratio (B)/(A) is between 8 and 20, the molar ratio (C)/(A) is between 1 and 3. Method for the preparation of the catalytic system of claim 1 by the preformation technique, characterised in that components (A), (B) and (C) are mixed for a period of 0.5-24 hours at temperatures of between 0 and 80°C in the presence of or without small quantities of diolefin, in an aliphatic, cycloaliphatic, aromatic solvent or their mixtures, the molar ratio (B)/(A) being between 3 and 100, the molar ratio (C)/(A) being from 0.1 to 50, Method according to claim 11, characterised in that the molar ratio (B)/(A) is between 8 and 20, the molar ratio (C)/(A) is between 1 and 3. Method for the preparation of the catalytic system according to claim 1, characterised in that, components (A), (B) and (C) are mixed in toluene, in the order specified, at 50°C for 1 hour in the presence of 1 g of butadiene per 1 x 10 -3 moles of component (A). Method for the polymerisation of conjugated diolefinic monomers, characterised in that the ternary catalytic system of claim 1 is used. Method for the polymerisation of diolefinic monomers according to claim 13, characterised in that 1,3-butadiene, isoprene, 1,3-pentadiene, 2,3-dimethylbutadiene are used as diolefinic monomer. Method for the polymerisation of diolefinic monomers according to claim 13, characterised in that the polydiolefine obtained has percentage value of 1,4-cis and 1,4-trans units from 35/63 to 98/1 respectively.

Inventors: ANDREUSSI PIERO, BIAGINI PAOLO, GARBASSI FABIO, LUGLI GABRIELE, ANDREUSSI, PIERO, BIAGINI, PAOLO, GARBASSI, FABIO, LUGLI, GABRIELE
Applicants: ENICHEM ELASTOMERS, ENIRICERCHE SPA, ENICHEM ELASTOMERI S.R.L., ENIRICERCHE S.P.A.
Application year: 1995
Main classification: C08F36
IPC codes: C08F136, C08F36, C08F4