POLYPROPYLENE MULTI-LAYER FILM

Abstract: A polypropylene multi-layer film comprises a substrate layer formed of crystalline polypropylene and a composition laminated on at least one side of said substrate layer. The composition comprises 70 to 95% by weight of (A) a crystalline propylene-ethylene copolymer having an ethylene content of 1.5 to 6.0% by weight and/or a crystalline propylene-α-olefin copolymer having a propylene content of 80 to 98% by weight, a butene-1 content of 2 to 20% by weight, and an ethylene content of 0 to 5% by weight, and 5 to 30% by weight of (B) a crystalline propylene-butene-1 copolymer obtained by decomposing a crystalline propylene-butene-1 copolymer having a butene-1 content of 25 to 45% by weight, an intrinsic viscosity of 2.5 dℓ/g or more (as determined in tetralin at 135°C) and a proportion of 35% by weight or more of a polymer component soluble in xylene at 20°C, and containing 1.5% by weight or less of a polymer component having a molecular weight calculated in terms of polystyrene of 10,000 or less as determined by GPC.

Description: This invention relates to a polypropylene multi-layer film having improved low-temperature heat sealing characteristics. More particularly, it relates to a polypropylene multi-layer film having an improved heat sealing property, resistance to solvent extraction and other film properties, and which is particularly suited to food packaging. The film comprises a substrate layer formed of crystalline polypropylene and, laminated thereon, a composition comprising a general purpose crystalline propylene-α-olefin copolymer having unsatisfactory low-temperature heat sealing properties and a relatively small amount of a specified crystalline propylene-butene-1 copolymer. Stretched crystalline polypropylene films have excellent mechanical strength, such as tensile strength, rigidity and low-temperature resistance, optical properties, such as gloss and transparency, and food hygienic properties such as innoxiousness and odorlessness, and hence they are widely used in packaging including food packaging. However, such a polypropylene stretched film used as a single layer has the defect that it has extremely poor heat sealing properties and, if forcibly heat sealed, undergoes thermal shrinkage, resulting in deterioration of the appearance of the product, so that heat sealing is virtually impossible. Various attempts have been made to obviate the above-mentioned defect. A widely used method is to use a multi-layer film formed by laminating on a substrate of polypropylene a resin layer having a low-temperature heat sealing property superior to that of the substrate. In such a method, the multi-layer film formed by laminating, as a resin of superior heat sealing property, polyethylene, ethylene-vinyl acetate copolymer or the like has the defect that, although it has excellent heat sealing properties, it shows deteriorated transparency and scratch resistance. On the other hand, for the purpose of obviating such a defect, there have been proposed multi-layer films having laminated thereon a propylene-ethylene copolymer having an ethylene content of about 0.5 to 5% by weight [Japanese Patent Application Kokoku (Post-Exam. Publication) No. 31478/71], propylene-ethylene-butene-1 terpolymer [Japanese Patent Application Kokai (Laid-open) No. 35487/74], and propylene-α-olefin copolymer having a content of α-olefin of 4 or more carbon atoms of 5 to 20% by weight [Japanese Patent Application Kokai No. 128781/75]. US-A-4343852 discloses a composite film wherein the surface film is made of a polymer composition comprising at least two of: a copolymer of propylene and ethylene in a weight ratio of 99. 5: 0. 5 to 90: 10; a copolymer of propylene and a C₁₋₄ α-olefin at a ratio of 70: 30 to 95: 5; and, a copolymer of butene and any other C₂₋₁₀ α-olefin in a ratio of 70: 30 to 99: 1. However, although these multi-layer films have excellent transparency and scratch resistance, their low-temperature heat sealing properties are not sufficiently good, and consequently their aptitude for high speed packaging, etc. is unsatisfactory. Accordingly, a number of attempts have been made to improve the low-temperature heat sealing property while maintaining as much as possible the good characteristics of stretched polypropylene film such as transparency and scratch resistance. For example, Japanese Patent Application Kokai No. 14223/80 discloses "a stretched composite polypropylene film which comprises a stretched crystalline polypropylene layer and a composition (A) laminated on at least one side of said layer, said composition (A) comprising 3 to 97% of an ethylene-propylene random copolymer having an ethylene content of 1 to 10% by weight, and 3 to 97% by weight of a propylene-α-olefin or propylene-α-olefin-ethylene copolymer having a propylene content of 65 to 99% by weight, a content of α-olefin of 4 to 8 carbon atoms of 1 to 30% by weight and an ethylene content of 0 to 5% by weight". Japanese Patent Application Kokai No. 58861/81 discloses "a polypropylene composite film which comprises a substrate layer formed of an isotactic polypropylene layer and a polyolefin composition laminated on at least one side of the said substrate layer, said polyolefin composition comprising 10 to 40% by weight of a propylene-butene-1 random copolymer having a propylene content of 55 to 80% by weight and a heat of crystal fusion of 20 to 80 Joule/g as determined by thermal analysis on a differential scanning calorimeter, and 90 to 60% by weight of a crystalline propylene-α-olefin random copolymer having a propylene content of 99 to 93% by weight. However, these attempts to improve the low-temperature heat sealing property by incorporation of a crystalline propylene-butene-1 copolymer all give, to the best of our knowledge, unsatisfactory products because they have unsatisfactory low-temperature heat sealing properties, or, when their low-temperature heat sealing property is at an approximately satisfactory level, they show deterioration in properties important to packaging film, such as blocking resistance and solvent resistance. Thus, there have been serious problems in that, when the amount of soft resin (which is a crystalline propylene-butene-1 copolymer) added to improve the low-temperature heat sealing property is relatively low (e.g. 30% by weight or less), although the scratch resistance, etc. of the resultant film are usually maintained at a good level, its low-temperature heat sealing property is poor; on the other hand, if the added amount of soft resin is 40% by weight or more, although the low-temperature heat sealing property is mostly satisfactory, other important properties, including scratch resistance, of the film are poor. We have now discovered a polypropylene multi-layer film which can solve the above-mentioned problems, has excellent low-temperature heat sealing properties and, moreover, has excellent packaging film properties including scratch resistance, blocking resistance and solvent resistance. Because of the problems discussed above, we have aimed to provide a product in which the amount of soft resin to be compounded is 30% by weight or less, preferably 25% by weight or less, and which has a practical heat sealing temperature (i.e. the temperature at which the seal strength per 25mm of seal width reaches 250g) of 100°C or less and which also has excellent film properties including scratch resistance, blocking resistance and solvent resistance. As a result, it has been found that the intended polypropylene multi-layer film can be obtained by using a specified crystalline propylene-butene-1 copolymer as the above-mentioned soft resin. Thus, this invention provides a polypropylene multi-layer film which comprises a substrate layer formed of crystalline polypropylene and a composition laminated on at least one side of said substrate layer, said composition comprising: (A) from 70 to 95% by weight of a crystalline propylene-ethylene copolymer having an ethylene content of from 1.5 to 6.0% by weight and/or a crystalline propylene-α-olefin copolymer having a propylene content of from 80 to 98% by weight, a butene-1 content of from 2 to 20% by weight and an ethylene content of from 0 to 5% by weight, and (B) from 5 to 30% by weight of a crystalline propylene-butene-1 copolymer which is a copolymer obtained by decomposing a crystalline propylene-butene-1 copolymer having a butene-1 content of from 25 to 45% by weight, an intrinsic viscosity of at least 2.5 dℓ/g (as determined in tetralin at 135°C) and a proportion of at least 35% by weight of a polymer component soluble in xylene at 20°C and which contains 1.5% by weight or less of a polymer component having a molecular weight calculated in terms of polystyrene of 10,000 or less as determined by GPC. The crystalline polypropylene used as the substrate is solid at ordinary conditions, and preferably contains 80% by weight or more of a boiling heptane-insoluble portion, has an intrinsic viscosity of from 1.3 to 4.2 dℓ/g, and contains at least 95% by weight of propylene in the polymer chain. Copolymers containing 5% by weight or less of ethylene and/or butene-1 can also be used. When the crystalline propylene-α-olefin copolymer (A) used in this invention is a propylene-ethylene copolymer, its ethylene content is in the range of from 1.5 to 6.0% by weight, preferably from 2.5 to 5.5% by weight. When the copolymer (A) is a propylene-ethylene-butene-1 copolymer or a propylene-butene-1 copolymer, the content of propylene ranges from 80 to 98% by weight, that of ethylene from 0 to 5% by weight and that of butene-1 from 2 to 20% by weight; preferably the propylene content is from 85 to 98% by weight, the ethylene content is from 0 to 4% by weight and the butene-1 content is from 2 to 15% by weight. More preferably, when the copolymer is a propylene-ethylene-butene-1 copolymer, the ethylene content is from 1.0 to 3.5% by weight and the butene-1 content is from 2.5 to 9.0% by weight; when it is a propylene-butene-1 copolymer, the butene-1 content is from 5 to 15% by weight. When the comonomer content is below the above-mentioned range, the improvement in heat sealing properties is insufficient, whereas when the comonomer content is above the above-mentioned range, scratch resistance, blocking resistance and solvent resistance deteriorate. The object of this invention can be achieved when the contents of propylene, ethylene and butene-1 in the crystalline propylene-α-olefin copolymer (A) are in the above-mentioned ranges for the respective copolymers. If desired, the respective copolymers of the above-mentioned comonomer content ranges may be compounded in an appropriate proportion. The crystalline propylene-α-olefin copolymer (A) preferably has a melt flow index determined according to JIS K6758 in the range of from 1 to 30, particularly from 3 to 20. The crystalline propylene-α-olefin copolymer (A) can be prepared, for example, by the method disclosed in Japanese Patent Application Kokai No. 162785/79 or 3443/80. The crystalline propylene-butene-1 copolymer (B) used in this invention is a copolymer obtained by decomposing a crystalline propylene-butene-1 copolymer which, before decomposition (hereinafter referred to as the pre-decomposition copolymer) has a butene-1 content of from 25 - 45% by weight, an intrinsic viscosity of at least 2.5 dℓ/g (as determined in tetralin at 135°C) and a proportion of a polymer component soluble in xylene at 20°C (said proportion being hereinafter referred to as CXS) of at least 35% by weight, and which contains 1.5% by weight or less of a polymer component having a molecular weight (calculated in terms of polystyrene) of 10,000 or less (this component is hereinafter referred to as the "component of MW of 10,000 or less"). Pre-decomposition copolymers having a butene-1 content of less than 25% by weight are unsuitable because they give an insufficient improvement in the low-temperature heat sealing property, whereas those having a butene-1 content exceeding 45% by weight are unsuitable because they give an insufficient improvement in the low-temperature heat sealing property or cause deterioration of scratch resistance, blocking resistance, and the like. A more preferable range of butene-1 content is from 27 to 40% by weight. The pre-decomposition copolymer should have an intrinsic viscosity of at least 2.5 dℓ/g. Those having an intrinsic viscosity of less than 2.5 dℓ/g gave an insufficient improvement in low-temperature heat sealing properties. The preferred range of intrinsic viscosity is from 2.7 to 5.5 dℓ/g. When the pre-decomposition copolymer has a CXS of less than 35% by weight it gives an insufficient improvement in low-temperature heat sealing properties. Said CXS is preferably at least 43% by weight. The extent of decomposition in obtaining the crystalline propylene-butene-1 copolymer (B) of this invention from the above-mentioned pre-decomposition polymer is preferably such that the ratio of the intrinsic viscosity before the decomposition to that after decomposition falls in the range of from 1.3:1 to 3.5:1. A ratio outside this range is unfavorable because then various problems can occur (including an insufficient improvement in low-temperature heat sealing properties, development of fish eyes on the surface of the multi-layer film, resulting in poor film appearance or, when the extent of decomposition is too large, generation of smoke and odor during the production of the multi-layer film). It is important that the amount of the component of MW of 10,000 or less in the crystalline propylene-butene-1 copolymer (B) of this invention should be no more than 1.5% by weight. When the amount exceeds 1.5% by weight, the low-temperature heat sealing property of the product becomes extremely poor. The amount of said component of MW of 10,000 or less is more preferably 1.0% by weight or less. In order to obtain a multi-layer film having a good low-temperature heat sealing property as well as the good film properties intended in this invention, the crystalline propylene-butene-1 copolymer (B) should satisfy all of the requirements mentioned above. The pre-decomposition copolymer used in this invention can be prepared by copolymerizing a mixture of propylene and α-olefin using an isospecific Ziegler-Natta catalyst. The catalyst to be used has preferably a high isospecificity. Preferred catalysts have a transition metal catalyst component which is a complex solid compound of a magnesium compound with a titanium compound or titanium trichloride having a laminar crystal structure, and a metal component which is typically an organoaluminium compound. The catalysts may also contain a known electron-donating compound as the third component. Titanium trichloride for use in such a catalyst may be prepared by reducing titanium tetrachloride with various reducing agents. Known reducing agents include metals such as aluminium and titanium, hydrogen, and organometal compounds. A typical example of titanium trichloride prepared by reduction with metals is a titanium trichloride composition containing aluminium chloride (TiCℓ₃ AA) obtained by reducing titanium tetrachloride with metallic aluminium and then activating the reduction product by grinding it in apparatus such as a ball mill or a vibrating mill. It is also possible to carry out the grinding in the presence of an ether, ketone, ester, aluminium chloride, titanium tetrachloride or the like in order to improve isospecificity, polymerization activity, and/or particle properties. Titanium trichloride which is more favorable for this invention is obtained by reducing titanium tetrachloride with an organoaluminium compound and then contacting the resultant titanium trichloride composition with an ether compound and with a halogen compound simultaneously or successively to undergo reaction. Preferred ether compounds are those represented by the general formula R¹-O-R² (R¹ and R² being each a C₁-C₁₈ alkyl group), particularly dibutyl ether or di-t-amyl ether. Halogen compounds are preferably halogens, particularly iodine, interhalogen compounds, particularly iodine trichloride, titanium halides, particularly titanium tetrachloride, and halogenated hydrocarbons, particularly carbon tetrachloride or 1,2-dichloroethane. Preferred organoaluminium compounds are those represented by the general formula AℓR 3 / nX 3-n (R³ being a hydrocarbon radical of 1 to 18 carbon atoms; X being Cℓ, Br, or I; and n being a number satisfying 3≧n>1), particularly diethylaluminium chloride or ethyaluminium sesquichloride. The methods of preparation of such titanium chloride compositions are described in detail in Japanese Patent Application Kokai Nos. 34470/72, 11986/79 and 142903/83 and U.S. Patent 4,165,298. When titanium trichloride having a laminar crystal structure is used as the transition metal compound component it is preferable to use an organo aluminium compound represented by the general formula AℓR 4 / mX 3-m (R⁴ being a C₁-C₁₈ hydrocarbon radical; X being Cℓ, Br or I; m being a number satisfying 3≧m>0) as the typical metal compound component. Organoaluminium compounds particularly favorable are those wherein R⁴ is an ethyl or isobutyl group and m satisfies 2.5≧m≧1.5. Specific examples thereof include diethylaluminium chloride, diethylaluminium bromide, diethylaluminium iodide, and mixtures thereof with triethylaluminium or ethylaluminium dichloride. When the third component described later is used in combination, organoaluminium compounds in which 3≧m≧2.5 or 1.5≧m>0 may also be favorably used for the purpose of this invention. The molar ratio of the organoaluminium compound to titanium trichloride may be selected from a wide range of from 1:1 to 1000:1. The catalyst comprising titanium trichloride and an organoaluminium compound may contain a third component known to the art. Examples of the third component include ε-caprolactam, ester compounds such as methyl methacrylate, ethyl benzoate, and methyl toluylate, phosphorous esters such as triphenyl phosphite and tributyl phosphite, and phosphoric acid derivatives such as hexamethylphosphoric triamide. The amount of the third component to be used should be experimentally determined for each individual compound because its activity varies from compound to compound. It is, however, generally equimolar or less with respect to the organoaluminium compound. When a complex solid compound of a magnesium compound with a titanium compound is used as the transition metal solid catalyst component of the catalyst, the typical metal catalyst component to be used is preferably an organoaluminium compound, particularly a compound represented by the general formula AℓR⁴ p X 3-p (R⁴ being a C₁-C₁₈ hydrocarbon radical; X being Cℓ, Br or I; p satisfying 3 ≧ p > 2). As specific examples, there may be mentioned triethylaluminium, triisobutylaluminium, or a mixture thereof with diethylaluminium chloride or diisobutylaluminium chloride. Further, the catalyst preferably contains an electron-donating compound, particularly an aromatic monocarboxylic acid ester and/or a silicon compound having a Si-OR⁵ linkage. A preferred silicon compound having a Si-OR⁵ linkage (R⁵ being a C₁-C₂₀ hydrocarbon radical) is an alkoxysilane compound of general formula R⁶ a Si(OR⁵) 4-a (R⁵ and R⁶ being each a C₁-C₂₀ hydrocarbon radical; and a being a number satisfying 0 ≦ a ≦ 3). Specific examples of the alkoxysilane compound include tetramethoxysilane, methyltrimethoxysilane, dimethyldimethoxysilane, ethyltrimethoxysilane, phenyltrimethoxysilane, tetraethoxysilane, methyltriethoxysilane, ethyltriethoxysilane, vinyltriethoxysilane, phenyltriethoxysilane, diphenyldimethoxysilane, diphenyldiethoxysilane, butyltriethoxysilane, tetrabutoxysilane, vinyltributoxysilane and diethyldiethoxysilane. The electron-donating compound is preferably used in an amount of 1 mole or less, particuarly from 0.05 to 1 mole, per mole of the organoaluminium compound. The complex solid compound of a magnesium compound with a titanium compound to be used is a so-called "supported catalyst" prepared by contacting either a titanium trichloride containing magnesium chloride obtained by reducing titanium tetrachloride with an organomagnesium compound or a solid magnesium compound with a liquid titanium compound to undergo a reaction. The solid magnesium compound preferably contains an electron-donating compound, particularly an aromatic monocarboxylic ester, an aromatic dicarboxylic diester, an ether compound, an alcohol and/or a phenol. The aromatic monocarboxylic ester may also be present at the time of the contact and reaction with the titanium compound. The complex solid compound of a magnesium compound with a titanium compound mentioned above is described in many references. Examples of catalysts favorable for this invention are described in Japanese Patent Application Kokai Nos. 119536/79, 30407/81, 59909/82, 59910/82, 59911/82, 59912/82, 59914/82, 59915/82, 59916/82 and 112982/79, U.S. Patent 4,350,802, U.S. Patent 4,483,939 and Canadian Patent 1,103,390. The pre-decomposition copolymer can be prepared by copolymerizing a mixture of propylene and α-olefin in a gas or liquid phase in the presence of the above-mentioned catalyst. In a liquid phase copolymerization, the copolymerization may be conducted after dissolving the monomers in an inert hydrocarbon solvent such as hexane and heptane, or it may be effected in a liquid phase monomer mixture. The control of the molecular weight is generally and effectively conducted by adding hydrogen to the polymerization system. Although copolymerization may be effected at any desired temperature and pressure, a temperature in the range of from 30 to 80°C is preferred. The copolymer of this invention is not necessarily a "random copolymer" in a statistically strict sense, namely a copolymer in which the chain distribution of propylene and α-olefin (which can be determined by C¹³ nuclear magnetic resonance) strictly obeys the Bernoullis' statistical rule. It may have any distribution of composition so long as it is in conformity with the definition according to this invention. The decomposition of the pre-decomposition copolymer can be conducted by known methods of decomposing polypropylene including thermal decomposition. An industrially advantageous method is, for example, to decompose the copolymer while melting and kneading it in an extruder. For efficient decomposition, it is preferable to use a radical initiator. Since odor and discoloration are particularly troublesome in film applications, aliphatic organic peroxides are preferably used. Examples of preferred aliphatic organic peroxides include 2,5-dimethyl-2,5-di(t-butylperoxy)hexane and 2,5-dimethyl-2,5-di(t-butylperoxy)hexene-3. The amount of these organic peroxide to be used is preferably from 0.005 to 1% by weight, more preferably from 0.2 to 0.08% by weight, relative to the pre-decomposition copolymer. The decomposition temperature is preferably in the range of from 180 to 300°C. The intrinsic viscosity, CXS, and the amount of the component of MW of 10,000 or less in this invention are determined according to the following methods. (1) Intrinsic viscosity Intrinsic viscosity was determined by measuring the viscosity of a completely dissolved polymer solution in tetralin at 135°C in an Ubbelohdes' viscometer in a conventional manner. A suitable antioxidant, for example about 0.2% by weight of 2,6-di-t-butyl-p-cresol, was added to the tetralin used as the solvent to prevent decomposition of the polymer during the measuring operation. (2) CXS (20°C xylene soluble portion) One gram of polymer was dissolved in 200 ml of boiling xylene. The resultant solution was gradually cooled to 50°C, and then cooled to 20°C by immersion in ice water with stirring, and allowed to stand for 3 hours to filter off the precipitated polymer. Xylene was evaporated off from the filtrate, and the residue was dried under vacuum at 60°C to recover a polymer soluble in xylene at 20°C, which was then weighed. (3) Amount of the component of MW of 10,000 or less This was determined by the use of gel permeation chromatography (GPC) in the following manner. Determination was conducted on a model 150-C ALC/GPC (Waters Associates, U.S.A.) to which two columns of Shodex (a registered trade mark) GPC AD-80M/S (Showa Denko K.K.) had been connected, using 1,2,4-trichlorobenzene containing 0.04% by weight of 2,6-di-t-butyl-p-cresol as the solvent at 140°C. The calibration curve was prepared by using nine kinds of standard polystyrenes (M W /M n = 1.01 - 1.14) having different molecular weights ranging from 2.3x10² to 6.2 x 10⁶ manufactured by Toya Soda Mfg. Co., Ltd. The amount of the component of MW of 10,000 or less in the polymer is determined by the areametric method from the molecular weight distribution curve thus obtained. Standard reference Material 706 (polystyrene of M w /M n =2.1) available from NBS (National Bureau of Standards, U.S.A.) was subjected to GPC determination in the above-mentioned manner, and was found to contain 0.5% by weight of a component of MW of 10,000 or less. The compounding ratio of the crystalline propylene-α-olefin copolymer (A) to the crystalline propylene-butene-1 copolymer (B) should be from 70 to 95% by weight of the copolymer (A) and from 5 to 30% by weight of the copolymer (B), from 10 to 25% by weight of the copolymer (B) being preferable. When the proportion of the copolymer (B) is less than 5% by weight, the desired low-temperature heat sealing property cannot be obtained, whereas, when it exceeds 30% by weight, the resultant product has deteriorated blocking resistance, scratch resistance and solvent resistance and cannot be used in practice. The method of compounding copolymer (A) and copolymer (B) is not restricted specifically so long as it give a substantially homogeneous composition. The multi-layer film thus obtained from a composition containing the crystalline propylene-butene-1 copolymer (B) obtained by decomposition has markedly improved properties as compared with a conventional multi-layer film comprising a composition using conventional copolymers. Thus, the multi-layer film of this invention has a markedly improved low-temperature heat sealing property as compared with a multi-layer film comprising a composition using a conventional copolymer having the same butene-1 content, intrinsic viscosity, melt flow index and heat of fusion (wherein the molecular weight has been controlled by a molecular weight modifier added in copolymerization). The polypropylene multi-layer film of this invention is suited to use as a packaging film particularly for food packaging, by virtue of its excellent low-temperature heat sealing property, scratch resistance, blocking resistance, solvent resistance and food hygienic properties. The composition and the film thereof of this invention can contain, as required, known additives including antioxidants, ultraviolet absorbers, lubricants, antiblocking agents, antistatic agents, anticlouding agents and nucleating agents. The polypropylene multi-layer film of this invention can be produced, for example, by the following methods. 1) Crystalline polypropylene base material and the above-mentioned composition are laminated by coextrusion, and the resultant film is stretched uniaxially or biaxially either separately or simultaneously. 2) Crystalline polypropylene base material is extruded in a molten state and uniaxially stretched in either the longitudinal or the transverse direction, and the above-mentioned composition is laminated thereon either in an extruded molten form or in a solidified film form, and the laminated film is further stretched in a different direction. The stretching of the crystalline polypropylene substrate layer of the polypropylene multi-layer film according to this invention is preferably conducted in a draw ratio in one direction within the range of from 3 to 20, more preferably from 4 to 10. The polypropylene multi-layer film of this invention can be subjected to a surface treatment such as corona discharge treatment or flame treatment in an industrially customary manner. This invention is further illustrated with reference to the following Comparative Examples and Examples. The characteristic values in the following Examples were determined according to the methods described below. 1) Haze Haze was determined according to ASTM D 2457. 2) Heat sealing property (temperature) Two portions of the laminated layer of the low-temperature heat sealing composition of the multi-layer film to be tested were superposed face to face, and pressure-bonded under a load of 2 kg/cm² for 2 seconds by means of a heat sealer heated at a prescribed temperature. The resultant film sealed in 25mm width was allowed to stand overnight and then subjected to a peeling test. The heat sealing temperature was defined as the temperature of the heat sealer at which the peeling resistance reached 250g/25mm in a peeling test conducted at a temperature of 23°C, a peeling velocity of 200mm/minute and a peeling angle of 180°C. 3) Blocking resistance Two rectangular 30 x 120mm test pieces were superposed such that rectangular 30 x 40mm portions of the side of the pieces having the composition (B) laminated thereon faced each other, a load of 500g was then placed thereon, and the test pieces were conditioned at 60°C for 3 hours. Afterwards, they were allowed to stand in an atmosphere of 23°C and 50% R.H. for 1 hour and subjected to a shear tensile test at a velocity of 200mm/minute to determine the strength necessary for peeling of the specimen. The less the strength so determined, the better the blocking resistance. 4) Scratch resistance On the side of a specimen laminated with the composition, was placed 100 cc. of No. A sea sand (15 to 25 mesh) in an area 150mm square. The whole was subjected to lateral vibration for 15 seconds by means of a rocking vibrator, and the resultant haze of the film was determined. The smaller the difference (ΔHz) of the haze thus determined from that before the test, the better the scratch resistance. 5) Solvent resistance The amount of 25°C xylene-soluble portion was determined according to FDA 177, 1520. Solvent resistance was judged good when this amount was less than 30%, and poor when the amount was 30% or more. 6) Melting point Ten milligrams of a specimen was enclosed in a sample holder for solid samples, heated at 200°C for 2 minutes, and then allowed to cool on a laboratory table at room temperature. It was allowed to stand in this condition for 1 to 2 hours, and then the specimen was tested on a differential scanning colorimeter (DSC, mfd. by Perkin Elmer Co.) in a nitrogen atmosphere at a temperature-increasing rate of 10°C/minute over a temperature range of 20°C to 180°C. The peak temperature showing the largest heat absorption in the melting diagram thus obtained was defined as No. 1 Tm, and that showing the second largest heat absorption as No. 2 Tm. 7) Heat of fusion In the melting diagram obtained in 6) above, the line of specific heat between 170° and 180°C was extrapolated linearly to the low temperature region and used as the base line to determine the melting area by a conventional method. As determined by this method, a crystalline polypropylene resin [Sumitomo Noblen (a registered trade mark) FS 2011D mfd. by Sumitomo Chem. Co. Ltd.] was found to have a heat of fusion of 91 Joule/g. 8) Boiling n-heptane isoluble portion (BHIS) This was determined according to the method described in U.S. Patent 4,168,361. EXAMPLE 1 (1) Polymerization of pre-decomposition copolymer Into a stainless steel autoclave of 100 litres internal volume equipped with a stirrer, the atmosphere in which had been replaced thoroughly by nitrogen and propylene, was charged 50 litres of purified hexane of technical grade, and the temperature was raised to 50°C. Then, 2.3kg of propylene and 7.5kg of butene-1 were charged into the autoclave, and further hydrogen was introduced thereinto to a hydrogen partial pressure in the gas phase of 0.05 kg/cm²G. Then, 30g of diethylaluminium chloride and 2.5g of titanium trichloride catalyst were charged thereinto. The titanium trichloride catalyst used was prepared according to the method described in Japanese Patent Application Kokai No. 228504/85. Copolymerization was carried out for 2 hours while propylene, butene-1, and hydrogen were being fed continuously so as to maintain the hydrogen concentration in the gas phase constant, and to give a total pressure of 3 kg/cm²G and a butene-1 content in the gas phase of 47% by weight. Thereafter, the monomers were purged, and the contents of the autoclave were transferred to a vessel equipped with a stirrer, into which 1 litre of butanol was charged and the resultant mixture was stirred at 50 to 60°C for 1 hour. Then 50 litres of water was introduced into the system, the resultant mixture was stirred at 50 to 60°C for 30 minutes and allowed to stand for 5 minutes, and the aqueous phase was separated off. This procedure was repeated two times. Then, Irganox (registered trade mark) 1076 (Ciba Geigy Co.) was added to the organic phase in an amount of about 100 ppm relative to the amount of polymer, and the organic phase was subjected to steam stripping using steam at 100°C. The polymer portion was taken out and dried overnight in a vacuum dryer at 100°C to obtain a copolymer in solid form. The procedure was repeated two times to obtain 5 kg of copolymer. The solid copolymer was comminuted in a pulverizer into powder having a size passing through a hole of 3mm diameter. The copolymer thus obtained had a butene-1 content of 34% by weight, an intrinsic viscosity of 3.3dℓ/g and 20°C xylene soluble portion (CXS) of 81% by weight. (2) Preparation of crystalline propylene-butene-1 copolymer (B) To 100 parts by weight of the pulverized copolymer obtained in (1) above, were mixed 0.1 part by weight of Sumilyzer (registered trade mark) BHT (Sumitomo Chemical Co., Ltd.), 0.1 part by weight of Irganox (registered trade mark) 1010 (Ciba Geigy Co.), 0.2 part by weight of calcium stearate and, as a decomposing agent, 0.04 part by weight of 2,5-dimethyl-2,5-di-t-butylperoxyhexane. The mixture obtained was melt-extruded through a single-screw extruder of 40mm diameter heated at 220°C, and the extruded strand was cut to obtain pellets. The residence time of the copolymer in the extruder was about 1.5 minutes. The pellets thus obtained had an intrinsic viscosity of 1.60 dℓ/g, a melt flow index of 9.5 g/10 minutes, an amount of the component of MW of 10,000 or less of 0.2% by weight, No. 1 Tm of 102°C, No. 2 Tm of 150°C, and BHIS of 16% by weight. (3) Preparation of the composition Into a mixture comprising 80% by weight of the powder of a crystalline propylene-ethylene copolymer (I) having an ethylene content of 3.1% by weight and an intrinsic viscosity of 1.70 dℓ/g, used as the crystalline propylene-α-olefin copolymer (A), and 20% by weight of the above-mentioned pellets of crystalline propylene-butene-1 copolymer (B), were added 0.1 part by weight of Sumilizer BHT (Sumitomo Chemical Co., Ltd.), 0.1 part by weight of Syloid (registered trade mark) 244 (Fuji-Davidson Co.), 0.1 part by weight of erucamide, and 0.05 part by weight of calcium stearate. The whole was mixed in a Henschel mixer and granulated through a single-screw extruder of 40mm diameter to give pellets. (4) Preparation of multi-layer film A crystalline polypropylene resin [Sumitomo Noblen (registered trade mark)] FS 2011D, melt index 2.6, (Sumitomo Chemical Co., Ltd.) was melt-extruded through a sheet extruder of 65mm bore diameter at a resin temperature of 280°C, and cooled with a cooling roll at 20°C to solidify it into a cooled sheet 0.5 mm thick. Then, the above-mentioned composition was melt-extruded through an extrusion laminator of 40mm diameter set at a resin temperature of 280°C and laminated in a thickness of 50µm on one side of the above-mentioned crystalline polypropylene sheet. The laminate thus obtained was subjected to simultaneous biaxial stretching on a small biaxial stretching machine at a stretching temperature of 150°C and draw ratio of 5 both in the longitudinal and the transverse direction to obtain a laminated film about 22 µm thick. The results of determination of the properties of the film obtained are shown in Table 1. EXAMPLE 2 (1) Polymerization of pre-decomposition copolymer The procedure described in Example 1 was repeated except that the concentrations of butene-1 and propylene and the partial pressure of hydrogen were changed, to obtain a pre-decomposition copolymer having a butene-1 content of 27% by weight, an intrinsic viscosity of 5.4 dℓ/g, and CXS of 45% by weight. (2) Preparation of crystalline propylene-butene-1 copolymer (B) Crystalline propylene-butene-1 copolymer (B) was prepared in the same manner as in Example 1 except that the amount of the decomposing agent added was changed. The copolymer (B) obtained had an intrinsic viscosity of 1.56 dℓ/g, an amount of the component of MW of 10,000 or less of 0.5% by weight, No. 1 Tm of 116°C, No. 2 Tm of 149°C, and BHIS of 13% by weight. (3) Preparation of the composition The composition was granulated into pellets in the same manner as in Example 1 except that the amount of the crystalline propylene-ethylene copolymer (I) powder was changed to 75% by weight, the crystalline propylene-butene-1 copolymer (B) was replaced by the one obtained above and its compounded amount was changed to 25% by weight. (4) Preparation of multi-layer film The same method was used as in Example 1. The results of determination of the properties of the film obtained are shown together in Table 1. EXAMPLE 3 A pre-decomposition copolymer having a butene-1 content of 37% by weight, an intrinsic viscosity of 2.75 dℓ/g and CXS of 60% by weight was obtained in the same manner as in Example 1 except that there was used a catalyst system consisting of titanium trichloride manufactured by Marubeni-Solvay Co. according to a method described in Japanese Patent Application Kokai No. 34478/72 and diethylaluminium chloride, having ε-caprolactam added thereto in a proportion of 0.2% mole relative to the diethylaluminium chloride; the butene-1 concentration, the propylene concentration, and the hydrogen partial pressure were also changed. Then, copolymer (B), the composition, and multi-layer film were prepared in the same manner as in Example 1 except that the amount of the decomposing agent added was changed. The copolymer (B) obtained above had an intrinsic viscosity of 2.07 dℓ/g, an amount of the component of MW of 10,000 or less of 0.8% by weight. No. 1 Tm of 100°C, No. 2 Tm of 139°C, and BHIS of 13% by weight. The results of determination of the properties of the film obtained are shown together in Table 1. EXAMPLE 4 (1) Polymerization of pre-decomposition copolymer A 2 litre separable flask was fitted with a stirrer, a thermometer, a dropping funnel, and a reflex condenser, and the interior was evacuated and then replaced with nitrogen. One litre of dried n-heptane was placed in the flask, and a gas mixture consisting of 68% mole of propylene and 32% mole of butene-1 was passed therethrough at a rate of 5.5 Nlitres/minute while the temperature was kept at 40°C. Then, 10 mmole of diethylaluminium chloride and further 0.3g of titanium trichloride (as used in Example 1) were introduced into the flask to initiate polymerization. Polymerization was conducted for 4 hours with stirring while the above-mentioned gas mixture was passed continuously. Then, the reaction was stopped by adding 30 ml of butanol. The reaction product was washed thoroughly with butanol, and then thrown into a large amount of methanol to precipitate a copolymer. The precipitate was dried. The above procedure was repeated four times to obtain 95g of copolymer. The copolymer was comminuted into powder in the same manner as in Example 1. The copolymer thus obtained had a butene-1 content of 38% by weight, an intrinsic viscosity of 3.6 dℓ/g, and CXS of 84% by weight. (2) Preparation of crystalline propylene-butene-1 copolymer (B) Into 100 parts by weight of the pulverised copolymer obtained in (1) above, were mixed 0.1 part by weight of Sumilizer BHT, 0.1 part by weight of Irganox 1010 (Ciba Geigy Co.), 0.2 part by weight of calcium stearate, and 0.1 part by weight of the decomposing agent used in Example 1. The mixture was kneaded for 5 minutes in a small kneader heated at 210°C. The resultant product had an intrinsic viscosity of 1.42 dℓ/g, an amount of the component of MW of 10,000 or less of 0.8% by weight, No. 1 Tm of 89°C, No. 2 Tm of 140°C, and BHIS of 8.4% by weight. (3) Preparation of the composition To a mixture comprising 85% by weight of the powder of crystalline propylene-ethylene copolymer (II) having an ethylene content of 4.7% by weight and an intrinsic viscosity of 1.64 dℓ/g, serving as the crystalline propylene-α-olefin copolymer (A), and 15% by weight of the above-mentioned copolymer (B), were added 0.1 part by weight of Sumilizer BHT, 0.2 part by weight of Syloid 244, 0.25 part by weight of oleamide and 0.05 part by weight of calcium stearate, and the mixture was kneaded for 5 minutes in a small kneader heated at 190°C. (4) Preparation of multi-layer film A crystalline polypropylene resin [Sumitomo Noblen FS 2011D] and the above-mentioned composition were each heat-formed in a press at 230°C for 10 minutes and then cooled to obtain a 500 µm thick sheet from the former and a 100 µm thick sheet from the latter. The two sheets were superposed on each other and pressed in the same manner as above to obtain a laminated sheet about 580 µm thick. The laminate thus obtained was subjected to simultaneous biaxial stretching on a small biaxial stretching machine at a stretching temperature of 150°C and a draw ratio of 5 both in the longitudinal and the transverse direction to obtain a multi-layer film about 23 µm thick. The results of determination of the properties of the film obtained are shown together in Table 1. COMPARATIVE EXAMPLE 1 A composition was prepared and a multi-layer film was prepared therefrom each in the same manner as in Example 1 except that 100% by weight of the powder of the crystalline propylene-ethylene copolymer (I) having an ethylene content of 3.1% by weight and an intrinsic viscosity of 1.70 dℓ/g was used in preparing the composition. The results of determination of the properties of the film obtained are shown together in Table 1. COMPARATIVE EXAMPLE 2 Preparation of pre-decomposition copolymer The procedure in Example 1 was repeated except that the propylene concentration, the butene-1 concentration, and the hydrogen partial pressure were changed. The catalyst system used was the same as that in Example 1. A copolymer powder having a butene-1 content of 35% by weight, an intrinsic viscosity of 1.13 dℓ/g, and CXS of 73% by weight was obtained. The copolymer powder showed an amount of the component of MW of 10,000 or less of 4.7% by weight, BHIS of 3.2% by weight, a heat of fusion of 38 Joule/g, No. 1 Tm of 104°C, and No. 2 Tm of 140°C. The copolymer powder was then used without being decomposed, to prepare a composition and multi-layer film in the same manner as in Example 1. The results of determination of the properties of the film obtained are shown together in Table 1. COMPARATIVE EXAMPLE 3 The same catalyst system as that in Example 1 was used and the procedure in Example 1 was repeated except that the butene-1 concentration, the propylene concentration, and the hydrogen partial pressure were changed, to obtain a copolymer powder having a butene-1 content of 28% by weight, a intrinsic viscosity of 1.58 dℓ/g, and CXS of 42% by weight. The copolymer powder showed an amount of the component of MW of 10,000 or less of 2.0% by weight, BHIS of 16% by weight, a heat of fusion of 51 Joule/g, No. 1 Tm of 124°C and No. 2 Tm of 143°C. The copolymer was then used without being decomposed, to prepare a composition and multi-layer film therefrom in the same manner as in Example 1. The results of determination of the properties of the film obtained are shown together in Table 1. COMPARATIVE EXAMPLE 4 A composition was prepared in the same manner as described in the section "preparation of composition" in Example 4 but by using 100% by weight of the powder of the crystalline propylene-ethylene copolymer (II) used in Example 4, and a multi-layer film was prepared therefrom in the same manner as described in the section "preparation of multi-layer film" in Example 4. The results of determination of the properties of the film obtained are shown together in Table 1. As shown in Table 1, the multi-layer film of this invention (Examples 1 to 4) is quite satisfactory in practice in haze, blocking resistance, scratch resistance, and solvent resistance, and shows a low-temperature heat sealing property of a markedly improved level. It can be seen that a multi-layer film (Comparative Examples 1 and 4) formed of conventional, well-known propylene-ethylene copolymer alone has a very poor low-temperature heat sealing property. Further, it is revealed that, even an improved version of said prior art method, namely a method wherein the copolymer (B) used is a polymer before decomposition, gives a multi-layer film (Comparative Examples 2 to 3) which is markedly poor in low-temperature heat sealing property as compared with the film according to this invention. EXAMPLES 5 AND 6, AND COMPARATIVE EXAMPLES 5 AND 6 A composition and multi-layer film were prepared in the same manner as described in Example 1 except that a terpolymer (III) having an ethylene content of 2.2% by weight, a butene-1 content of 5.7% by weight, and an intrinsic viscosity of 1.73 dℓ/g, and a propylene-butene-1 copolymer (IV) having a butene-1 content of 13% by weight and an intrinsic viscosity of 1.85 dℓ/g were used as the crystalline propylene-α-olefin copolymer (A), and the additives described in Example 4 were mixed into a composition comprising 80% by weight of said copolymer (A) and 20% by weight of the copolymer (B) used in Example 1 (Examples 5 to 6). Separately, a multi-layer film was prepared using the above-mentioned crystalline propylene-ethylene-butene-1 copolymer (III) or propylene-butene-1 copolymer (IV) (Comparative Examples 5 and 6). The results of determination of the properties of the film obtained are shown in Table 2. EXAMPLE 7 A composition and multi-layer film were prepared in the same manner as described in Example 1 except that the additives described in Example 4 were added to a composition comprising 90% by weight of a propylene-butene-1 copolymer (V) having a butene-1 content of 18% by weight and an intrinsic viscosity of 1.87 dℓ/g, used as the propylene-α-olefin copolymer (A), and 10% by weight of the copolymer (B) used in Example 1. The results of determination of the properties of the film obtained are shown together in Table 2. COMPARATIVE EXAMPLE 7 A composition and multi-layer film were prepared in the same manner as in Example 5 except for using a propylene-ethylene copolymer (VI) having an ethylene content of 0.6% by weight and an intrinsic viscosity of 1.65 dℓ/g as the crystalline propylene-α-olefin copolymer (A). The results of determination of the properties of the film obtained are shown together in Table 2. EXAMPLES 8 AND 9, AND COMPARATIVE EXAMPLE 8 Compositions and multi-layer films were prepared in the same manner as in Example 1 except that a crystalline propylene-ethylene copolymer (A) having an ethylene content of 4.7% by weight and an intrinsic viscosity of 1.64 dℓ/g, and the crystalline propylene-butene-1 copolymer (B) used in Example 1 were employed and the compounding ratio of (A) to (B) was changed. The results of determination of the properties of the film obtained are shown in Table 3. COMPARATIVE EXAMPLE 9 Polymerization was conducted in the same manner as in Example 1 except that the diethylaluminium chloride and titanium trichloride employed in Example 3 were used and the butene-1 concentration, the propylene concentration, and the hydrogen partial pressure were changed, to obtain a pre-decomposition copolymer having a butene-1 content of 27% by weight, an intrinsic viscosity of 2.01 dℓ/g and CXS of 31% by weight. Copolymer (B) was prepared in the same manner as in Example 1 except that the amount of the decomposing agent incorporated was changed. The copolymer thus obtained had an intrinsic viscosity of 1.51 dℓ/g, a melt flow index of 13g/10 minutes, an amount of the component of MW of 10,000 or less of 2.1% by weight, No. 1 Tm of 125°C, No. 2 Tm of 143°C, and BHIS of 14% by weight. Preparation of the composition and that of multi-layer film were conducted in the same manner as in Example 1. The results of determination of the properties of the film obtained are shown together in Table 3. COMPARATIVE EXAMPLE 10 Polymerization was carried out by the same method as in Example 4 except that a supported catalyst prepared according to the method described in Japanese Patent Application Kokai No. 59916/82, triethylaluminium and, as the third component, 0.22 mole of methyl toluylate per mole of triethylaluminium were used, the concentrations of butene-1 and propylene were changed, the polymerization temperature was 50°C and the polymerization time was 1 hour, to obtain a copolymer having a butene-1 content of 35% by weight, an intrinsic viscosity of 2.33 dℓ/g, and CXS of 60% by weight. The copolymer thus obtained showed an amount of the component of MW of 10,000 or less of 2.5% by weight, BHIS of 0.5% by weight, a heat of fusion of 31 Joule/g, and No. 1 Tm of 89°C. Preparation of the composition was carried out in the same manner as in Example 4 but adding the same decomposing agent as used in Example 1 to a mixture of 80% by weight of the crystalline propylene-ethylene copolymer (I) used Example 1 and 20% by weight of the above-mentioned copolymer (B). Preparation of a multi-layer film was also carried out in the same manner as in Example 4. The results of determination of the properties of the film obtained are shown together in Table 3. COMPARATIVE EXAMPLE 11 Polymerization was carried out in the same manner as in Example 4 except that the butene-1 concentration and the propylene concentration were changed and the polymerization temperature and the polymerization time were altered to 60°C and 3 hours respectively, to obtain a copolymer having a butene-1 content of 49% by weight, an intrinsic viscosity of 1.78 dℓ/g, and CXS of 85% by weight. The copolymer showed an amount of the component of MW of 10,000 or less of 4.3% by weight, BHIS of 5.5% by weight, No. 1 Tm of 75°C and No. 2 Tm of 130°C. Preparation of the composition and that of multi-layer film were conducted in the same manner as in Comparative Example 8. The results of determination of the properties of the film obtained are shown together in Table 3. Tables 2 and 3 reveal that multi-layer films according to this invention (Examples 5 to 8) keep a good balance between low-temperature heat sealing property on the one hand and haze, scratch resistance and so forth on the other hand, whereas in the Comparative Examples the two are in poor balance. That is, Comparative Examples 5 and 6, multi-layer films formed of a prior art propylene-ethylene-butene-1 terpolymer or propylene-butene-1 copolymer, give a poor low-temperature heat sealing property. Comparative Example 7 also gives a poor low-temperature heat sealing property because a propylene-ethylene copolymer of a small ethylene content (0.6% by weight) has been used therein as the copolymer (A). The multi-layer film of Comparative Example 8 has a good low-temperature heat sealing property, but is poor in blocking resistance, scratch resistance and solvent resistance because the amount of the copolymer (B) compounded is large. Comparative Examples 9 and 10 give an inferior low-temperature heat sealing property because pre-decomposition copolymers having an intrinsic viscosity of 2.01 dℓ/g and 2.33 dℓ/g, respectively, have been used. Comparative Example 11 gives a product which is poor both in the low-temperature heat sealing property and the film property because a pre-decomposition copolymer having a butene-1 content of 49% by weight has been used therein. As described in the foregoing, multi-layer film can be provided according to this invention which has extremely well balanced properties, namely excellent low-temperature heat sealing property, scratch resistance, blocking resistance, solvent resistance and so forth as compared with prior art polypropylene multi-layer film.

Claims: A polypropylene multi-layer film which comprises a substrate layer formed of crystalline polypropylene and a composition laminated on at least one side of said substrate layer, said composition comprising a crystalline propylene-ethylene copolymer having an ethylene content of from 1. 5 to 6. 0% by weight and/or a crystalline propylene-α-olefin copolymer having a propylene content of from 80 to 98% by weight, a butene-1 content of from 2 to 20% by weight, and an ethylene content of from 0 to 5% by weight, characterised in that the composition further comprises from 5 to 30% by weight of a crystalline propylenebutene-1 copolymer which is a copolymer obtained by decomposing a crystalline propylene-butene-1 copolymer having a butene-1 content of from 25 to 45% by weight, an intrinsic viscosity of at least 2. 5 dl/g (as determined in tetralin at 135°C), wherein the ratio of the intrinsic viscosity of the crystalline propylene-butene-1 copolymer before decomposition to that after decomposition is from 1. 3: 1 to 3. 5: 1, and a proportion of at least 35% by weight of a polymer component soluble in xylene at 20°C, and which contains 1. 5% by weight or less of a polymer component having a molecular weight calculated in terms of polystyrene of 10,000 or less as determined by gel permeation chromatography. A polypropylene multi-layer film according to Claim 1, wherein the crystalline polypropylene forming the substrate layer is solid under ordinary conditions, contains at least 80% by weight of a boiling n-heptane insoluble portion, has an intrinsic viscosity of from 1.3 to 4.2 dℓ/g, and contains at least 95% by weight of propylene in the polymer chain. A polypropylene multi-layer film according to Claim 1 or Claim 2, wherein the crystalline polypropylene forming the substrate layer is a copolymer containing 5% by weight or less of ethylene and/or butene-1. A polypropylene multi-layer film according to any one of the preceding Claims, wherein the crystalline propylene-ethylene copolymer (A) has an ethylene content of from 2.5 to 5.5% by weight. A polypropylene multi-layer film according to any one of Claims 1 to 3, wherein the crystalline propylene-α-olefin copolymer (A) has a propylene content of from 85 to 98% by weight, an ethylene content of from 0 to 4% by weight, and a butene-1 content of from 2 to 15% by weight. A polypropylene multi-layer film according to Claim 5, wherein the crystalline propylene-α-olefin copolymer (A) is a propylene-ethylene-butene-1 copolymer and has an ethylene content of from 1. 0 to 3. 5% by weight and a butene-1 content of from 2. 5 to 9. 0% by weight. A polypropylene multi-layer film according to Claim 5, wherein the crystalline propylene-α-olefin copolymer (A) is a propylene-butene-1 copolymer and has a butene-1 content of from 5 to 15% by weight. A polypropylene multi-layer film according to any one of the preceding Claims, wherein the crystalline propylene-butene-1 copolymer (B) before decomposition has a butene-1 content of from 27 to 40% by weight. A polypropylene multi-layer film according to any one of the preceding Claims, wherein the crystalline propylene-butene-1 copolymer (B) before decomposition has an intrinsic viscosity of from 2. 7 to 5. 5 dl/g. A polypropylene multi-layer film according to any one of the preceding Claims, wherein the amount of the component of a molecular weight of 10,000 or less in the crystalline propylene-butene-1 copolymer (B) is 1. 0% by weight or less.

Inventors: HARADA, HIROYUKI, IMA, SEIICHIRO, KAKUGO, MASAHIRO, MIYATAKE, TATSUYA
Applicants: SUMITOMO CHEMICAL COMPANY, LIMITED
Application year: 1986
Main classification: B32B27
IPC codes: C08L23, B32B27, C08L7, C08L21, C08L101