CATALYST FOR PRODUCING ATACTIC POLYPROPYLENE, AND PROCEDURE FOR PREPARING SUCH CATALYST

Abstract: Atactic polypropylene is produced by slurry-polymerizing propylene with the aid of a Ziegler-Natta catalyst system wherein the carrier is a chlorinated organic magnesium compound. The catalyst system is prepared in that the above-obtained solid component is refluxed with hot TiCl4 solution, and the product thus obtained is fed together with trialkylaluminium under slurry conditions into propylene in order to obtain an atactic polymer.

Description: Catalyst for producing atactic polypropylene, and procedure for preparing such catalyst The present invention concerns a Ziegler-Natta catalyst with the aid of which mainly atactic polypropylene can be produced very simply, and a procedure for preparing a catalyst of this kind. In the patent literature numerous examples are known of the producing of isotactic polypropylene using catalysts with MgCl2 carrier. The starting material may be directly M Cl2 or an organo- magnesium compound treated with a chlorinating agent (e.g. alkyl chlorides, HC1, CCI , etc.) and which may have the form MgClR or MgCl2 has been activated to a catalytically active crystal form either mechanically, by grinding, or chemically, by first treating it with an alcohol and then with a titanium compound. Since the desired product was an isotactic polypropylene, an agent improving steteroselectivity (a so-called internal donor) has invariably been added to the catalyst in one of its preparation steps, for instance ethylbenzoate (EtOBz). Activation of the catalyst with an aluminium- alkyl or aluminiumchloroalkyl compound yields an active Ziegler- Natta catalyst, which in order to achieve a good isotacticity index (> 98%) furthermore requires that in the aluminium treatment another electron donor (a so-called external donor) is used. These donor and activation steps complicate the catalyst preparation, and it is not possible with catalysts of this type to prepare a catalyst producing mainly atactic polypropylene. Using ground gCl2*TiCl4 catalyst in producing atactic polypropylene is known in the art (Angew. Makromol. Chem. 120 (1984) 73-90). A value about 20% is then achieved for the isotacticity. The reference GB 1,335,887 (Montecatini Edison, filed Oct. 29, 1970) also dis- closes a MgCl2*TiCl catalyst prepared by grinding and with iso¬ tacticity 28.5% (heptane extraction method) and activity about- 1 2 kg polymer per g of catalyst are achieved. Catalyst producing atactic polypropylene has also been prepared in said reference by grinding gCl2 together with 3TiCl3*AlCl3, but the activity remained low in that case. Additives (EtOBz, BUNH2 have also been added at 5 grinding, but the isotacticity index went higher if this was done (to 44%, see JP 59/43008 A2, Toyo Soda Mfg Co). Mg-alkyl compounds have also been used for starting materials in preparing catalysts for atactic polypropylene. There are few -|Q examples, to be sure, and no activities equal to those in the present invention have been reached in any o e of them. In these examples, TiCl was reduced with the aid of an Mg alkyl or of Grinard's reagent to a TiCl3-based catalyst. When TiCl4 is reacted with magnesiumdialkyl or alkylmagnesiumhalide compounds, catalysts -|5 containing TiCl3 are obtained, their activity falling short of that of Mg chloride carrier catalysts. There are no examples of chlorinating an Mg dialkyl to gCl in such a case. In the reference DE 2751807 (Veba-Chemie AG, 1979) , a catalyst 20 has been prepared in a rather complicated way, starting from Mg chips which were treated with ethylbromide in ether solution, whereby MgEtBr was obtained, of which EtMg is formed in accordance with Schlenk's equilibrium equation. This was titanized with TiCl4_ Catalyst activated by the catalyst component thus obtained and by 25 DEAC (diethylaluminium chloride) produced "substantially atactic" polypropylene (isotacticity index < 20%) as little as 0.5-1.5 kg per g of cat. The dibutylmagnesium/trie h laluminium complex has reacted with 30 titanium tetrachloride, according to the reference BE 883 637 = US 4,276,191 (Standard Oil Co., 1980). Polymerizing with DEAC produced highly atactic polymer, but the activity was only 128 g polypropylene per g of cat. 35 In the reference US 3,933,934 (Naphtachimie, 1978), TiCl 4 was reduced with the aid of metallic Mg, iodine and n-butyl-chloride, 1 thereby obtaining a mixture of MgCl2 and TiCl3. With this catalyst highly atactic polypropylene was obtained (heptane-soluble fraction 96-99%), but the activity was low, on order of less than 1 kg polymer per g of cat. 5 Reacting TiCl4 with magnesium alcoholates or with magnesium hydroxide has been applied in preparing catalysts appropriate for producing amorphous polyolefines, in the reference US 3,951,935 (Hoechst AG, 1976). SiCl has also been used as additive. The -|0 activities are low, about 400 g polymer per mmol, owing to the reaction products of alcoholate and TiCl4, titaniumchloroalkoxides. The polymerizing catalyst of the present invention is formed with a chlorine-containing compound, which must not contain titanium, l5 of a chlorinated organic magnesium compound which has been treated with TiCl4 solution, and this component constitutes together with a cocatalyst an active catalyst system for producing atactic poly¬ propylene. Preparation of the polymerizing catalyst of the invention is commenced by chlorinating an organic magnesium compound which 0 has been dissolved in an anhydrous solvent, for instance in a hydrocarbon. Treatment of this solution with a suitable chlorinating agent is easiest to perform by bubbling gaseous chlorinating agent through the solution, for instance chlorine or hydrogen chloride gas. Chlorination of the Mg compound is also feasible with a liquid 5 chlorinating agent, such as carbon tetrachloride, chloroform, dichloromethane, alkylchlorides (e.g. butylchloride) , etc. The product thus obtained is washed several times with dry, that is anhydrous, solvent, which is advantageously the same hydrocarbon as said solvent for the magnesium compound. This chlorinated magne- 0 sium compound, which may be called carrier, is next treated with TiCl by refluxing the solution of the carrier compound with liquid TiCl4 during several hours, e.g. 2-4 hrs, at elevated temperature, about 80-100°C. The product thus obtained has usually the following elemental contents (only the most important contents have been 5 measured): Mg «= 15-21% by weight, Ti = 2-10% by weight, Cl - 30- 85% by weight. 1 The catalyst initiating and maintaining polymerization consists of a component constituted by the carrier and the Ti compound, and a cocatalyst, for which trialkylaluminium is advantageously used when producing tactic polypropylene. 5 The polymerizing proper may be carried out under various polymerizing conditions with this catalyst, but slurry conditions have been found to be best, that is, catalyst and monomer are added to a suitable solvent, and the polymer, which is insoluble ■JQ in said fluid, forms as a slurry therein. The following observations can be made when comparing the present invention with the references cited in the foregoing and with polypropylene catalyst patents on the whole:- 15 (a) in the patents, polypropylene is understood to be the usually desired isotactic polymer (which contains heptane-soluble polymer less than 10-20%); 20 ( ) no donor whatsoever is used in the catalyst of the invention; (c) although the use of MgCl2, and partly also the use of Mg alkyls, towards producing atactic polypropylene is known in the art, we are not aware of any patent in which the carrier is expressly 25 prepared for producing atactic polypropylene by chlorinating a magnesiumalkyl compound for catalyst carrier in the way described above and by subsequently reacting the carrier with a titanium compound. That is, the chlorinating compound is not a compound containing titanium, e.g. TiC^, which involves formation of TiCl3, 30 whereby the activity is lowered; (d) there is no need to grind the carrier in order to make a good catalyst, as has been done when starting out with gCl2! the procedure is therefore quite simple. The catalyst is prepared in 35 one single reactor, and only two reaction steps (chlorinating and titanizing) are required in the process. 1 Atactic polypropylene is a simple amorphous polyolefine. It has surfactant properties owing to its amorphous state, and its uses are based precisely on this circumstance. It may indeed be used, for instance, to make hot melt glues, to make lamination glues, to c fill cables, as an addition to bitumen or to replace it completely in roofing materials, as adhesive component in anticorrosives, in wall-to-wall carpeting, in acoustic lagging, and in various crystals and sealing compounds. It also serves as cementing substance and as moisture protection in road construction materials and traffic ■|0 lane markings. It may be used as an inexpensive filler and/or modifier substance in elastomers. Atactic polypropylene may be added to plaster of Paris to make it waterproof. It is usable in laminations for foodstuff packaging ■ |5 because it is non-toxic and thus meets the provisions concerning foodstuff packages. Modified with maleic acid anhydride, atactic polypropylene is usable as additive in lubricating oils. Atactic polypropylene 0 grafted with polybutadiene, with the aid of peroxides, is suitable for producing films, tubing, sections, laminations or fibres. Atactic polyolefines, and consequently atactic polypropylene as well, may be used in self-adhesive tapes, in moisture-resistant 5 thermal and electric insulating materials, in inks, as oil absorbent, and in cold-pressing objects. The catalyst was prepared as described in the examples following below. 0 EXAMPLE 1 100 ml BOMAG (butyloctylmagnesium, 20% heptane solution, Schering AG) were added into a one-litre glass reactor fitted with mixer, 5 thermometer and reflux condenser. All transfers and treatments took place under pure nitrogen (99.999%). 100 ml heptane, dried on "I molecular screens, were added. Dry chlorine gas was bubbled through the mix during 30 min. while the temperature was 20-32°C. The brown precipitate thus obtained was washed four times with dry heptane, allowed to settle, and the heptane was siphoned off. The - solid catalyst carrier was treated with 100 ml heptane and 100 ml TiCl during 2 hours at 80-100°C. The catalyst thus obtained was washed with heptane five times while warm, the precipitate was allowed to settle, the heptane was removed by siphoning, followed by drying in a nitrogen flow. The solid catalyst contained: Mg 10 16.5% by weight, Ti 4.5% by weight, and Cl 60.0% by weight. EXAMPLE 2 150 ml BOMAG and 300 ml dry heptane were added into a one-litre ■jt j reactor. The mix was treated with dry HC1 gas during 30 min. , cooling the reactor on an ice/water bath. The temperature kept between 20 and 30°C. A light yellow precipitate formed, through which nitrogen was conducted during 30 min. 300 ml heptane were added, the material was allowed to settle, the solution was siphoned 20 °ffi and the catalyst carrier was washed four times as described. 100 ml TiCl4 and 100 ml heptane were added into reactor; titanium treatment was carried out during 2 hours at 100°C. 10 ml heptane were added, settling was allowed, the solution was siphoned off, and the catalyst was washed five times with hot heptane. The product 25 was ultimately dried in vacuum and in nitrogen flow. The solid catalyst contained: Mg 10.2% by weight, Ti 2.3% by weight, and Cl 80.0% by weight. EXAMPLE 3 30 150 ml BOMAG and 300 ml dry heptane were added into a one-litre reactor. 40 ml CCI4, dissolved in 40 ml heptane, were slowly added from a dropping funnel. The reactor was cooled on an ice bath, the temperature keeping within 10-35°C. A light brown precipitate was 35 obtained, which was washed four times with 300 ml heptane. The catalyst carrier was treated with 100 ml TiCl4 and 100 ml heptane 1 at 100°C during 2 hours. The reddish brown catalyst thus obtained was washed four times with hot heptane and dried in vacuum and in nitrogen flow. The solid catalyst contained: Mg 21.0% by weight, Ti 2.1% by weight, and Cl 62% by weight. 5 EXAMPLE 4 115 ml DBM (14% dibutylmagnesium/Isopar E solution, Lithco Europe Ltd) and 300 ml heptane were added into a one-litre reactor. -|Q Chlorine gas was conducted through the solution during 20 min. at 20-30°C. The yellow precipitate thus obtained was nitrogenated during 30 min. 600 ml heptane were added, and settling was allowed. The solution was siphoned off and 50 ml TiCl4 and 50 ml heptane were added upon the catalyst carrier. The temperature was raised "|5 to 92°C and kept at this height 2 hours. The catalyst thus obtained was washed four times with 300 ml heptane while hot. Drying in vacuum and in nitrogen flow followed. The solid catalyst contained: Mg 17.1% by weight, Ti 5.5% by weight, and Cl 59.8% by weight. 0 EXAMPLE 5 Into a one-litre reactor, 100 ml heptane and 14.9 g Mg(0Et)2 were added. HC1 was bubbled through the suspension at 20-80°C during 2 hours, whereby the colour turned light brown. 100 ml TiCl4 were 5 added to the suspension, and the mixture was kept at 98°C for 2 hours. Settling was allowed, the solution was siphoned off, and washing with hot heptane was performed four times. The product was dried with nitrogen. The solid catalyst contained: Mg 15.4% by weight, Ti 8.9% by weight, and Cl 58% by weight. 0 POLYMERIZING Propylene was polymerized with the aid of a combination of the Mg/Ti components as in Examples 1 to 5 and triisobutylaluminium, 5 in slurry conditions, as follows. 630 ml heptane were placed in a two-litre reactor. A syringe was used to add 20 ml aluminiumalkyl 1 diluted in heptane, whereupon a special feeder funnel was used to add the catalyst, flushing with 50 ml heptane (total volume: 700 ml) . For aluminium alkyl, triisobutylaluminium was used, with Al/Ti ratio = 100. The mixing was adjusted to 500 rpm. Hydrogen 5 was added, and polymerizing was performed by feeding gaseous monomer continuously. Polymerizing was done during 3 hours at 70°C. On concluded polymerizing, the solvent was evaporated from the product in a three-litre decanting glass, which was left to stand about 10 hours in a fume cupboard. Evaporation was then continued with ■ "10 slow and cautious heating (about 4 hours) until the polymer was completely molten. Careful agitation was applied, and the product was poured into an aluminium mould. The gain was weighed. The isotacticity was measured on the polymer which had been comminuted to pieces 3-5 mm in diameter, by extracting the product (about 3 g -J5 of it) during 6 hours with boiling heptane. The results recorded in the polymerizing tests are presented in Table 1 below. 20 TABLE 1 Polymerizing tests with the catalysts of the Examples Example Propylene Hydrogen Activity Isotacticity 25 press., bar press., bar kg PP/g cat. % 1 8 3.6 7.8 22 2 8 3 5.2 28 3 8 3 5.7 37 4 8 3 4.0 25 30 5 8 3 4.0 38 35

Claims: 1 Claims 1. A catalyst for producing atactic polypropylene, characterized in that it consists of a transition metal component with a carrier 5 which is an organic Mg compound chlorinated with a chlorine- containing compound containing no titanium and titanized with TiCl4 and of a trialkylaluminium cocatalyst, without any electron- donating compound whatsoever. -|0 2. Catalyst according to claim 1, characterized in that the organic magnesium compound is dialkylmagnesium, advantageously butyloctyl¬ magnesium or dibutylmagnesium. 3. Catalyst according to claim 1, characterized in that the "15 chlorinating compound is CI2 gas. 4. Catalyst according to claim 1, characterized in that the chlorinating compound is hydrogen chloride HC1. 0 5. Catalyst according to claim 1, characterized in that the chlorinating compound is carbon tetrachloride CCI4. 6. Catalyst according to claim 4, characterized in that the organic magnesium compound is magnesium methanolate g(OC2Hg)2- 5 7. Procedure for preparing a catalyst suitable for use in producing atactic polypropylene, characterized in that an organic Mg compound, which has been dissolved in an anhydrous liquid hydrocarbon, is chlorinated with a compound containing chlorine and containing no 0 titanium, and the carrier compound thus obtained is treated, with reflux, with liquid TiCl4, and the transition metal component thus obtained is combined with trialkylaluminium, without presence of any electron-donor compound whatsoever. 5 8. Procedure according to claim 7, characterized in that the organic Mg compound is dialkylmagnesium, advantageously butyloctylmagnesium 1 or dibutylmagnesium. 9. Procedure according to claim 8 , characterized in that the chlorinating compound is CI2 gas . 5 10. Procedure according to claim 8, characterized in that the chlorinating compound is hydrogen chloride HC1. 11. Procedure according to claim 8, characterized in that the ■ JO chlorinating compound is carbon tetrachloride CCI4. 12. Procedure according to claim 10, characterized in that the organic Mg compound is magnesium metanolate Mg 0C2H5)2- ■ J5 13. Procedure according to any one of claims 8-12, characterized in that titanizing is carried out at a temperature about 80-100°C. 14. Procedure according to any one of claims 8-13, characterized in that the titanizing time is about 2-4 hours. 20 25 30 35

Inventors: LEINONEN TIMO, SORMUNEN PEKKA, LEINONEN, TIMO, SORMUNEN, PEKKA
Applicants: NESTE OY
Application year: 1988
Main classification: C08F4
IPC codes: C08F4, C08F10, C08F110