Process for the preparation of polypropylene random copolymer

Abstract: A Polypropylene random copolymer is obtained by copolymerizing propylene and an α-olefin or propylene, ethylene and α-olefin, using a Ziegler-Natta catalyst substantially in the absence of solvent. The content of propylene is by weight 92.3 - 75.0%, of ethylene (E) 0 - 2.7%, and of α-olefin 5.0 - 25.0%. The content (C) of 20°C xylene-soluble components in the random copolymer satisfies following conditions:- (1) ethylene content (E) less than 1.5%: C ≦ 12.0 (weight %) (2) ethylene content (E) 1.5% - 1.8%: C ≦ 42.0 - 20.0 x E (weight %) (3) ethylene content (E) 1.8% - 2.7%: C ≦ 6.0 (weight %) Film of the copolymer has a good appearance and a good balance between heat-sealability and rigidity.

Description: The present invention relates to a process for the preparation of polypropylene random copolymers and films thereof, which have an excellent appearance and an excellent balance between low-temperature heat-sealing properties and rigidity. Since polypropylene film has excellent appearance, heat-seal characteristics, heat resistance, rigidity, etc., it has been widely used in packaging fields such as food packaging and fiber packaging. Recently, to improve productivity in the packaging industry, production speed in bag-making or packaging has been increased and consequently it has been desired to develop materials having excellent higher speed bag-making properties and packaging properties, while exhibiting good sealing properties at low temperature. Accordingly, various attempts have been made to improve heat-sealing properties at low temperature, and it has been proposed to compound various kinds of low-crystalline ethylene-propylene copolymers with a polypropylene random copolymer, and to increase the content of ethylene and/or an α-olefin in a polypropylene random copolymer. However, the products so obtained still do not attain a sufficiently excellent appearance or balance between low-temperature heat-sealing properties and rigidity. If the amount of the low-crystalline polypropylene random copolymer compounded or the content of the comonomer such as ethylene, etc, in a random copolymer is increased to attain the low-temperature heat-sealing properties, the rigidity thereof is greatly decreased or the appearance is marred by whitening due to bleeding. It is known to produce polypropylene random copolymers by a solution polymerization method and a bulk polymerization method. In these polymerization methods, since the copolymerization or the post-treatment of the copolymer is conducted in a solvent, such as heptane or hexane, or a mixed medium of propylene, an α-olefin and/or ethylene, low-molecular weight polymer components which exert an influence on the blocking resistance and whitening property by bleeding, etc., are dissolved and removed, thus giving enhanced characteristics. However, on the other hand, such problems occur as that the copolymer components which are effective to provide heat-sealing properties at low temperature are dissolved and removed, and if the content of the comonomer such as an α-olefin and/or ethylene is increased, the copolymer itself is dissolved and thus cannot be produced. For these reasons, if it is intended to obtain a material capable of heat-sealing at lower temperature by these polymerization methods, a great restriction is encountered and the production of such a copolymer utilizing an industrially-useful method has not substantially been achieved. To try to achieve the above objects, it has been attempted to produce the copolymer by a so-called gas-phase polymerization method in which a solvent or an active monomer liquid is not substantially present. Such methods are described in, for example, JP-A-60-166455 and JP-A-53-26882 (the term "JP-A" as used herein means an "unexamined published Japanese patent application"), but do not, however, yield polypropylene random copolymer and film having sufficiently good appearance and balance between low-temperature heat-sealing properties and rigidity. Accordingly, an object of the present invention is to provide a polypropylene random copolymer and film thereof having an excellent appearance and balance between low-temperature heat-sealing properties and rigidity without impairment of the transparency, which is a desirable characteristic inherently possessed by polypropylene film. Such a polypropylene or polypropylene film has not been obtained by the above-described conventional techniques, but we have found that the above object of the invention can be attained by a polypropylene random copolymer wherein the copolymer compositions and the contents of 20°C xylene-soluble components are in specific ranges. According to the present invention there is provided a process for producing a polypropylene random copolymer comprising copolymerizing propylene and an α-olefin or propylene, ethylene, and α-olefin using a Ziegler-Natta catalyst comprising (A) solid catalyst components comprising magnesium, titanium and a halogen, (B) an organoaluminium compound having at least one Al-carbon bond in the molecule, and (C) a silicon compound represented by the formula wherein R 1 represents an alicyclic hydrocarbon group having 5 to 20 carbon atoms and R 2 and R 3 each represents a hydrocarbon group having 1 to 20 carbon atoms, the molar ratio of Al in component (B)/Ti in component (A) being from 1:1 to 1000:1, and the molar ratio of Si in component (C)/A1 in component (B) being from 0.02:1 to 500:1, in a gas phase at a temperature of from 20 to 150°C and a pressure of from atmospheric pressure to 40 kg/cm 2 G to obtain a polypropylene random copolymer having a propylene content of from 92.3 to 75.0% by weight, an ethylene content (E) of from 0 to 2.7% by weight, and an α-olefin content of from 5.0 to 25.0% by weight. said process gives rise to a polypropylene random copolymer wherein the content (C) of 20°C xylene-soluble components in the random copolymer satisfies the following formulae (1) to (3): in the copolymer wherein the ethylene content (E) is less than 1.5% by weight, C ≤ 12.0 (weight %); in the copolymer wherein the ethylene content (E) is from 1.5% by weight to 1.8% by weight, C ≤ 42.0 - 20.0 x E (weight %); and in the copolymer wherein the ethylene content (E) is from 1.8% by weight to 2.7% by weight, C ≤ 6.0 (weight %) A polypropylene film may be formed by melt-extruding polypropylene random copolymer obtained with the above-described process. If any one of the propylene content, the ethylene content, the α-olefin content and the content of 20°C xylene-soluble components in polypropylene random copolymer is outside the above-described ranges according to the present invention, an excellent appearance and an excellent balance between the low-temperature heat-sealing properties and rigidity cannot be attained. If the propylene content in the polypropylene random copolymer is over 92.3% by weight, the low-temperature heat-sealing property is inferior, while if the content is less than 75.0% by weight, the heat-resistance and rigidity of the copolymer are poor. If the ethylene content is over 2.7% by weight, there occur the problems that the balance between the low-temperature heat-sealing properties and the rigidity is poor, and the appearance is impaired by whitening due to bleeding. Also, if the content of the a-olefin is less than 5.0% by weight, the low-temperature heat-sealing properties are poor, while if the content thereof is over 25.0% by weight, the rigidity and the heat-resistance are poor. Furthermore, even if the propylene content, the ethylene content, and the α-olefin content are in the above-described ranges, it is important in the present invention that the content (C) of the 20°C xylene-soluble components in the polypropylene random copolymer is 12.0% by weight or less in the copolymer in which the ethylene content is less than 1.5% by weight; satisfies the following formula C ≤ 42.0 - 20.0 x E (weight %) in the copolymer in which the ethylene content (E) is from 1.5% by weight to 1.8% by weight; and is 6.0% by weight or less in the copolymer in which the ethylene content is from 1.8% by weight to 2.7% by weight. If the content of the 20°C xylene-soluble components is over the above-defined range, the copolymer and film thereof are poor in respect of appearance because of whitening due to bleeding, and of rigidity. As regards the polypropylene random copolymer it is preferred that the propylene content is from 92.5 to 78.0% by weight, the ethylene content is from 0 to 2.5% by weight, and the α-olefin content is from 5.0 to 22.0% by weight. Also, the preferred range of the content (C) of the 20°C xylene-soluble components in the polypropylene random component is 11.0% by weight or less in the copolymer where the ethylene content is less than 1.5% by weight; satisfies the following formula C ≤ 43.5 - 21.7 x E (weight %) in the copolymer in which the ethylene content (E) is from 1.5% by weight to 1.8% by weight; and is 4.5% by weight or less in the copolymer in which the ethylene content is from 1.8 to 2.7% by weight. As the α-olefin for the polypropylene random copolymer , an α-olefin having from 4 to 10 carbon atoms can be used, and butene-1 is preferably used. The polypropylene random copolymer has a melt flow rate of from 3 to 20 g/10 min, from the standpoints of transparency and high-speed workability in the production of the film. Further, the polypropylene random copolymer used generally has an intrinsic viscosity of from 1 to 3 dl/g measured at 135°C in tetralin. For the production of the polypropylene random copolymer, a Ziegler-Natta catalyst containing at least titanium, magnesium and a halogen, as essential components, is used. Accordingly, the polypropylene random copolymer is produced by the process of the present invention comprising copolymerizing a mixture of propylene and an α-olefin or a mixture of propylene, ethylene and an α-olefin by a gas phase polymerization method using a catalyst system comprising (A) solid catalyst components comprising magnesium, titanium and a halogen as the essential components, (B) an organoaluminum compound, and (C) a silicon compound represented by the formula R 1 R 2 Si(OR 3 ) 2 wherein R 1 represents an alicyclic hydrocarbon group having from 5 to 20 carbon atoms and R 2 and R 3 each represents a hydrocarbon group having from 1 to 20 carbon atoms. The solid catalyst components (A) contain titanium, magnesium and a halogen as the essential components and are generally obtained by treating with an ester compound a solid product obtained by reducing a titanium compound with an organomagnesium compound, and then treating the treated product with titanium tetrachloride. The titanium compound used to produce the solid catalyst components (A) is represented by the formula Ti(OR) b X 4-b wherein R represents a hydrocarbon group having from 1 to 20 carbon atoms, X represents a halogen atom, and b is a number satisfying the formula 0 < b ≤ 4. Examples of R are an alkyl group such as methyl, ethyl, propyl, iso-propyl, butyl, iso-butyl, amyl, iso-amyl, hexyl, heptyl, octyl, decyl or dodecyl; an aryl group such as phenyl, cresyl, xylyl or naphthyl; a cycloalkyl group such as cyclohexyl or cyclopentyl; an allyl group such as propenyl; an aralkyl group such as benzyl. A type of organomagnesium compound having a magnesium-carbon bond can optionally be used as the magnesium component. In particular, the Grignard compound represented by the formula RMgX wherein R represents a hydrocarbon group having from 1 to 20 carbon atoms and X represents a halogen atom, and the magnesium compound represented by the formula RR'Mg wherein R and R', which may be the same or different, each represents a hydrocarbon group having from 1 to 20 carbon atoms are preferably used. Examples of the Grignard compound are methylmagnesium chloride, ethylmagnesium chloride, ethylmagnesium bromide, ethylmagnesium iodide, propylmagnesium chloride, propylmagnesium bromide, butylmagnesium chloride, butylmagnesium bromide, sec-butylmagnesium chloride, sec-butylmagnesium bromide, tert-butylmagnesium chloride, tert-butylmagnesium bromide, amylmagnesium chloride, iso-amylmagnesium chloride, phenylmagnesium chloride, and phenylmagnesium bromide. Also, examples of the magnesium compound represented by RR'Mg are diethylmagnesium, dipropylmagnesium, di-iso-propylmagnesium, dibutylmagnesium, di-sec-butylmagnesium, di-tert-butylmagnesium, butyl-sec-butylmagnesium, diamylmagnesium and diphenylmagnesium. The organoaluminum compound (B) which is used in combination with the solid catalyst component (A) has at least one Al-carbon bond in the molecule. Examples of the organoaluminum compound are a trialkylaluminum such as triethylaluminum, triisobutylaluminum or trihexylaluminum; a dialkylaluminum halide such as diethylaluminum halide or diisobutylaluminum halide; a mixture of the trialkylaluminum and the dialkylaluminum halide; and an alkylaluminoxane such as tetraethyldialuminoxane or tetrabutyldialuminoxane. In these organoaluminum compounds, the trialkylaluminum, a mixture of the trialkylaluminum and the dialkylaluminum halide, and the alkylaluminoxane are preferred, and triethylaluminum, triisobutylaluminum, a mixture of triethylaluminum and diethylaluminum chloride, and tetraethyldialuminoxane are more preferred. The amount of the organoaluminum compound used can be selected in a wide range of from 1 to 1,000 moles per mole of the titanium atom in the solid catalyst, and is particularly preferably selected in the range of from 5 to 600 moles. The silicon compound (C) has the formulae: The catalyst is used such that the molar ratio of the Al atom in component (B)/the Ti atom in component (A) becomes from 1:1 to 1,000:1, and preferably from 5:1 to 600:1, and the molar ratio of the component (C)/the Al atom in component (B) becomes from 0.02:1 to 500:1, and preferably from 0.05:1 to 10:1. The polymerization is conducted at a polymerization temperature of from 20 to 150°C, and preferably from 50 to 95°C and at a polymerization pressure of from atmospheric pressure to 40 kg/cm 2 G, and preferably from 2 to 30 kg/cm 2 G, substantially in the absence of a solvent while applying propylene, ethylene, and an α-olefin together with hydrogen for controlling the molecular weight of the copolymer formed. The copolymer is melt-extruded to form a film. As a result, a film having no whitening due to bleeding (Δ haze: 0.5% or less), a heat-sealing temperature of 120°C or less, and a Young's modulus of at least 3,000 kg/cm 2 , and also having excellent appearance and balance between low-temperature heat-sealing properties and rigidity can be obtained. The film is an unstretched film having a thickness in the range of from 10 to 500 µm, and preferably from 10 to 100 µm. Also, since the film formed from the copolymer of the present invention has the preferred characteristics described above, the film is preferably used as at least one layer component in the production of multilayer films by a co-extrusion film-forming method. There is no particular restriction on the production method of the polypropylene film if the method is usually industrially applicable; for example, a method of producing a polypropylene film by a melt-extrusion molding method, such as a T-die film-forming method or a tubular film-forming method, but a T-die film-forming method wherein a high-speed film-formation is carried out by a large-scale film-forming machine is preferably used. The polypropylene random copolymer and the film thereof can be, if necessary, compounded with, for example, an antioxidant, a neutralizing agent, a lubricant, an antiblocking agent or an antistatic agent, as ordinarily used in the art. The present invention is described in more detail by reference to the following Examples and Comparative Examples, which should not be construed as limiting the scope of the invention. In addition, the measured value of each item in the specification and the Examples of the invention was measured by the following method. (1) Ethylene content and butene-1 content: Ethylene content: The ethylene content was determined by the IR spectral method described in Koobunshi Bunseki (Polymer Molecule Analysis) Handbook , page 256 [(i) Random Copolymer], published by Asakura Shoten, 1985. Butene-1 content: The butene-1 content was determined by the following equation by the IR spectral method. Butene-1 content (weight %) = 1.208K' wherein K' is the absorbance at 767 cm -1 . (2) Melt flow rate (MFR): Measured by the method of condition-14 according to JIS K7210. (3) 20°C Xylene-soluble components: After completely dissolving 1 g of each sample in 100 ml of boiling xylene, the temperature of the solution was lowered to 20°C and the solution was allowed to stand for 4 hours. Thereafter, precipitates formed were filtered away and the filtrate obtained was evaporated to dryness and dried at 70°C under reduced pressure. The weight of the residue was measured to determine the content as weight %. (4) Transparency (haze): Measured according to JIS K7105. (5) Whitening due to bleeding (Δ haze): The haze after heat-treating each sample at 60°C for 24 hours and the haze thereof before the heat- heat-treatment were measured and the difference thereof was defined as Δ haze. (6) Heat-sealing temperature: Sealed films of 25 mm in width obtained by pressing superposed films by means of a heated heat-sealer for 2 seconds by applying a load of 2 kg/cm 2 were allowed to stand overnight and thereafter the films were peeled off from each other at 23°C, at a peeling speed of 200 mm/minute, and at a peeling angle of 180°. In this case, the temperature of the heat sealer when the peeling resistance became 300 g/25 mm was employed as the heat-sealing temperature. (7) Young's modulus: Each test sample of 20 mm in width was sampled from the lengthwise direction (MD), an S-S curve was determined by a tension tester at a chuck interval of 60 mm and a tensile speed of 5 mm/min., and the initial elastic modulus was measured. Reference Example (a) Synthesis of organomagnesium compound: After replacing the atmosphere in one liter flask equipped with a stirrer, a refluxing condenser, a dropping funnel, and a thermometer with argon, 32.0 g of shaved magnesium for a Grignard reagent was placed in the flask. Then, 120 g of butyl chloride and 500 ml of dibutyl ether were charged in the dropping funnel and about 30 ml of the mixture was dropped to magnesium in the flask to initiate the reaction. After initiation of the reaction, dropping of the mixture was continued at 50°C for 4 hours and after completion of the dropping, the reaction was further continued at 60°C for one hour. The reaction mixture was cooled to room temperature and solid components formed were separated by filtration. Butylmagnesium chloride in dibutyl ether was hydrolyzed with 1N sulfuric acid and the concentration of the organomagnesium compound formed was determined by a back titration with an aqueous solution of 1N sodium hydroxide using phenolphthalein as an indicator. As a result, the concentration was 2.1 mols/liter. (b) Synthesis of solid product: After replacing the inside atmosphere of a 500 ml flask equipped with a stirrer and a dropping funnel with argon, 240 ml of hexane, 5.4 g (15.8 mmols) of tetrabutoxytitanium, and 61.4 g (295 mmols) of tetraethoxysilane were placed in the flask to form a homogeneous solution. Then, 150 ml of the organic magnesium synthesized in the above step (a) was gradually added dropwise to the solution from the dropping funnel over a period of 4 hours while maintaining the inside temperature of the flask at 5°C. Thereafter, the resulting mixture was further stirred at room temperature for one hour and solids formed were separated from liquid at room temperature, washed repeatedly three times with 240 ml of hexane, and dried under a reduced pressure to obtain 45.0 g of a light-brown solid product. The solid product obtained contained 1.7% by weight of titanium, 33.8% by weight of an ethoxy groups, and 2.9% by weight of butoxy groups. Also, in a wide angle X ray diffraction diagram of the solid product by Cu-Ka line, no clear diffraction peaks were observed, which showed that the solid product had a noncrystalline structure. (c) Synthesis of ester-treated solid: After replacing the inside atmosphere of a 100 ml flask with argon, 6.5 g of the solid product synthesized in the above step (b), 16.2 ml of toluene, and 4.3 ml (16 mmols) of diisobutyl phthalate were placed in the flask and the reaction was conducted at 95°C for one hour. After completion of the reaction, a solid product was separated from the reaction mixture and was washed three times with 33 ml of toluene. (d) Synthesis of solid catalyst (activation treatment): After completion of washing in the above step (c), 16.2 ml of toluene, 0.36 ml (1.3 mmols) of diisobutyl phthalate, 2.2 ml (13 mmols) of dibutyl ether, and 38.0 ml (346 mmols) of titanium tetrachloride were added into the flask and the reaction was conducted at 95°C for 3 hours. After the reaction was completed, solids formed were separated from the liquid at 95°C and were washed twice with 33 ml of toluene at the same temperature. Then, the treatment with the mixture of diisobutyl phthalate, dibutyl ether, and titanium tetrachloride described above was further repeated once under the same condition and the solid product was washed three times with 33 ml of hexane to obtain 5.0 g of a loess-color solid catalyst. The solid catalyst obtained contained 2.1% by weight of a titanium atom, 19.9% by weight of a magnesium atom, and 12.7% by weight of a phthalic acid ester. Example 1 (a) Catalyst component: In a 250 liter reaction vessel equipped with a stirrer was placed 150 liters of sufficiently purified hexane and after sufficiently replacing the inside atmosphere of the vessel with nitrogen, 3.2 mols of triethylaluminum (TEA), 0.32 mol of cyclohexylethyldimethoxysilane (CHEDMS), and the solid catalyst obtained in the Reference Example described above in an amount of 51.8 g calculated as the titanium atom were added to the reaction vessel. Then, 2.8 kg of propylene was continuously added thereto over a period of 2 hours while maintaining the temperature at 25°C. (b) Polymerization: The catalyst component prepared in above step (a) was supplied to a 1,000 liter polymerization bath such that the polymerization temperature became 70°C, the polymerization pressure became 14.5 kg/cm 2 G, and the average residence time became 6 hours, and while simultaneously supplying 50 mmols/hour of TEA and 5 mmols/hour of CHEDMS (Al/CHEDMS = 10/1 molar ratio), propylene and butene-1 were continuously supplied at a H 2 concentration in the polymerization bath of 0.2% to conduct a gas-phase polymerization. The copolymer obtained contained 79.9% by weight of propylene, 20.1% by weight of butene-1, and 4.0% by weight of 20°C xylene-soluble components. To 100 parts by weight of the copolymer thus obtained were added 0.1 part by weight of calcium stearate, 0.1 part by weight of Sumirizer BHT, 0.10 part by weight of Irganox 1010, 0.10 part by weight of erucic amide, and 0.15 part by weight of a fine silica powder followed by mixing with a Henschel mixer, the resulting mixture was melt-extruded to form pellets. Then, the pellets obtained were melt-extruded by a T-die film-forming machine of 50 mm in diameter at a die temperature of 250°C and cooled by a cooling roller passing therethrough cooling water of 30°C to obtain an unstretched film of 30 µm in thickness. The transparency (haze), the whitening by bleeding (Δ haze), the heat sealing temperature, and the Young's modulus of the film obtained are shown in Table 2 below. Example 2 By following the same procedure as in Example 1 except that the polymerization temperature was changed to 65°C, the propylene-butene-1 copolymer shown in Table 1 below was obtained. The evaluations were made in the same manner as in Example 1. The evaluation results obtained are shown in Table 2 below. Example 3 Three polymerization baths having inside volumes of 20 to 45 m 3 were used and a gas-phase polymerization was conducted by continuously supplying propylene, ethylene, and butene-1 in the same manner as in Example 1 except that the polymerization temperature was 80°C, the polymerization pressure was from 7 to 15 kg/cm 2 G, and the hydrogen (H 2 ) concentration was 0.25%. The copolymer obtained contained 88.6% by weight of propylene, 1.2% by weight of ethylene, 10.2% by weight of butene-1, and 3.1% by weight of 20°C xylene-soluble components. The copolymer was evaluated in the same manner as in Example 1. The evaluation results obtained are shown in Table 2 below. Examples 4 to 8 In Example 4, the same procedure as in Example 1 was followed except that the weight ratios of the monomers supplied to the polymerization bath and the H 2 concentration were changed, and in Examples 5 to 8, the same procedure as in Example 3 was followed except that the weight ratios of the monomers supplied to the polymerization baths and the H 2 concentration were changed. Also, the copolymers obtained were evaluated in the same manner as in Example 1. The analytical results of the copolymers obtained are shown in Table 1 and the evaluation results are shown in Table 2 below. Comparative Example 1 A gas-phase polymerization of propylene and ethylene was conducted under the same conditions as in Example 3 and the copolymer obtained was evaluated in the same manner as in Example 3. The evaluation results obtained are shown in Table 2 below. Comparative Example 2 Using the same polymerization baths as in Example 3, using the TiCl 3 -type solid catalyst described in JP-B-3-46001 (the term "JP-B" as used herein means an "examined published Japanese patent application"), and combining diethylaluminum chloride and methyl methacrylate as an electron donor, a gas-phase polymerization of propylene and butene-1 was conducted at a polymerization temperature of 65°C, a polymerization pressure of from 6 to 12 kg/cm 2 G and a H 2 concentration of 1.5%. The analytical results of the copolymer obtained are shown in Table 1 below and the evaluation results thereof are shown in Table 2 below. Comparative Examples 3 to 6 The same solid catalyst as used in Example 1 was used. In Comparative Examples 3, 4, and 6, using the same type of polymerization bath as used in Example 1, the same procedure as in Example 1 was followed except that the polymerization temperature was 80°C, phenyltrimethoxysilane was used as the component (c), and the phenyltrimethoxysilane was added in an amount of Al/(c) = 6.7/1 (molar ratio). Also, in Comparative Example 5, the same procedure as in Example 3 was followed except that the polymerization temperature was 70°C, the polymerization pressure was from 12 to 18 kg/cm 2 G, and the amounts of propylene, ethylene, and butene-1 supplied to the polymerization baths were changed. The copolymers obtained were evaluated in the same manner as in Example 3. The analytical results obtained of those copolymers are shown in Table 1 below and the evaluation results obtained of those copolymers are shown in Table 2 below. Prooperties of Film Haze Δ Haze Heat Sealing Temperature Young's Modulus (%) (%) (°C) (kg/cm 2 ) Example 1 1.2 0.3 109 3300 Example 2 1.1 0.3 106 3200 Example 3 2.3 0.2 118 4100 Example 4 3.0 0.4 107 3200 Example 5 2.2 0.2 120 4000 Example 6 2.1 0.2 119 4000 Example 7 1.7 0.5 114 3300 Example 8 1.9 0.5 118 3600 Comparative Example 1 2.3 1.7 127 3600 Comparative Example 2 1.3 0.3 106 2700 Comparative Example 3 1.3 0.7 103 2200 Comparative Example 4 3.5 1.8 121 3200 Comparative Example 5 1.1 0.7 114 3000 Comparative Example 6 1.8 0.9 110 2900 It can be seen from the results shown in the Tables that when the compositions of the copolymers are outside the range of the present invention (Comparative Examples 1 and 5) or even when the compositions of the copolymers are in the range of the present invention but when the content of the 20°C xylene-soluble components is outside the range of the present invention (Comparative Examples 2, 3, 4, and 6), occurrence of whitening due to bleeding is remarkable or the balance of the low-temperature heat sealing property and the rigidity is poor, and as a result, the objects of the present invention cannot be attained. Also, the balance of the heat sealing temperature and the Young's modulus of each of the copolymer films obtained in the Examples according to the present invention is the shown in the figure of the accompanying drawing together with that of each of the copolymer films obtained in the Comparative Examples. It can be seen from the results shown in the figure that each of the films of the present invention has a very excellent balance of the heat sealing temperature and the Young's modulus as compared with the films of the Comparative Examples. As described above, there can be obtained, according to the process of the present invention, films of polypropylene random copolymers whose appearance is unimpaired by whitening due to bleeding and having an excellent balance between low-temperature heat sealing properties and rigidity.

Claims: A process for producing a polypropylene random copolymer comprising copolymerizing propylene and an α-olefin or propylene, ethylene, and α-olefin using a Ziegler-Natta catalyst comprising (A) solid catalyst components comprising magnesium, titanium and a halogen, (B) an organoaluminium compound having at least one Al-carbon bond in the molecule, and (C) a silicon compound represented by any one of the following formulae: wherein the molar ratio of Al in component (B)/Ti in component (A) being from 1:1 to 1000:1, and the molar ratio of Si in component (C)/Al in component (B) being from 0.02:1 to 500:1, in a gas phase at a temperature of from 20 to 150°C and a pressure of from atmospheric pressure to 40 kgcm 2 G to obtain a polypropylene random copolymer having a propylene content of from 92.3 to 75.0 % by weight, an ethylene content (E) of from 0 to 2.7 % by weight, and an α-olefin content of from 5.0 to 25.0 % by weight, wherein, the content (C) of 20°C xylene-soluble components in the random copolymer satisfies following formulae (1) to (3); in the copolymer wherein the ethylene content (E) is less than 1.5 % by weight, C ≤ 12.0 (weight %) in the copolymer wherein the ethylene content (E) is from 1.5 % by weight to 1.8 % by weight, C ≤ 42.0 - 20.0 x E (weight %) and in the copolymer wherein the ethylene content (E) is from 1.8 % by weight to 2.7 % by weight, C ≤ 6.0 (weight %) and the copolymer obtained has a melt flow rate of from 3 to 20 g/10 min. A process as claimed in claim 1, wherein the propylene content is from 92.5 to 78.0 % by weight, the ethylene content is from 0 to 2.5 % by weight, and the α-olefin content is from 5.0 to 22.0 % by weight. A process as claimed in any preceding claim, wherein the α-olefin is an α-olefin having 4 to 10 carbon atoms. A process as claimed in any preceding claim, wherein the α-olefin is butene-1. A process as claimed in any preceding claim, wherein the solid catalyst component (A) is obtained by reducing a titanium compound with an organomagnesium compound to obtain a solid product, treating the solid product with an ester compound, and then treating the treated solid product with titanium tetrachloride. A process as claimed in any preceding claim, wherein the molar ratio of Al in component (B)/Ti in component. (A) is from 5:1 to 600:1, and the molar ratio of Si in component (C)/Al in component (B) is from 0.05:1 to 10:1. A process as claimed in any preceding claim, wherein the copolymerization is conducted at a temperature of from 50 to 95°C and a pressure of 2 to 30 kg/cm 2 G. A process as claimed in any preceding claim, wherein the copolymerization is conducted while introducing hydrogen.

Inventors: IMA SEIICHIRO, MORI JIRO, SADATOSHI HAJIME, SHIRATANI EISUKE, WAKAMATSU KAZUKI, IMA, SEIICHIRO, MORI, JIRO, SADATOSHI, HAJIME, SHIRATANI, EISUKE, WAKAMATSU, KAZUKI
Applicants: SUMITOMO CHEMICAL CO, SUMITOMO CHEMICAL COMPANY LIMITED
Application year: 1993
Main classification: C08F210
IPC codes: C08F210, C08F4, C08F2, C08F10, C08J5