HOT-MELT ADHESIVE

Abstract: A random copolymer of a C₄ to C₁₂ α-olefin with an aromatic vinyl monomer, wherein the α-olefin content is 50 to 98 mole % and the softening point is 40 to 150 °C, is useful as a hot-melt adhesive and excellent in adhesion, processability and environmental aging resistance such as thermal aging resistance. The copolymer can be used as a hot-melt adhesive or a heat sealant when combined with 70 to 10 wt% of a tackifier.

Description: The present invention relates to a hot-melt adhesive comprising a random copolymer of an α-olefin which is butene-1, pentene-1, hexene-1, heptene-1, octene-1, nonene-1, decene-1 or undecene-1, with an aromatic vinyl monomer, which has excellent adhesiveness, workability and environmental aging resistances such as thermal aging resistance, and which can be used in various fields such as packaging, bookmaking, pouchmaking, woodworking, can manufacturing, construction and sanitary uses. The present invention also relates to a composition comprising the above-mentioned copolymer and a tackifier, which can be used as a hot-melt adhesive or a heat sealant. Recently, hot-melt adhesives have been increasingly used in various fields since they have superior coating properties, safety, cleanness for working atmosphere and energy saving properties over prior art solvent type adhesives. Compositions including a base polymer such as natural rubber, ethylene-vinyl acetate copolymer or a styrene-butadiene-styrene block copolymer have been used as prior art hot-melt adhesives and heat-sealing adders. However, since the compositions including a base polymer such as natural rubber, a styrene-butadiene-styrene block copolymer or a styrene-isoprene-styrene copolymer have a lot of double bonds, they have poor thermal resistance stability and have problems that oxidation, decomposition and coloring do not only occur on application, but also the bonding performance changes with time after bonding. An ethylene-vinyl acetate copolymer based composition has a poor adhesiveness to polyolefin resins such as polyethylene and polypropylene. For the prior art hot-melt adhesive, it is generally necessary to compound a tackifier into a base polymer. A single-component resin for an adhesive having both performances of the base polymer and the tackifier has been demanded for simplicity of steps and preventing variations of products on compounding. US-A-3,757,000 describes a copolymer of styrene and isobutylene which can be used in a hot melt resin or pressure sensitive adhesive. The copolymer is prepared using a primary catalyst of an alkyl aluminium dihalide and co-catalyst of water, an alkyl halide, a hydrogen halide or an alcohol. JP-A-50/158642 describes a resin obtained from 20-80 pts styrene and 20-80 pts of a 4-5C fraction containing more than 15 wt% olefins. The resin is prepared using a catalyst of Et₂AlCl. The present inventors have found from an intensive study to provide a resin for an adhesive which has excellent adhesiveness, workability and environmental aging resistances such as thermal aging resistance that a random copolymer including a given α-olefin and a given aromatic vinyl monomer is excellent in the aforementioned characteristics. The present invention aims to overcome the above-mentioned problems which the prior art has encountered, and to provide a hot-melt adhesive comprising an α-olefin aromatic vinyl monomer copolymer which has excellent adhesiveness, workability and environmental aging resistance. The present invention provides a hot-melt adhesive which comprises a random copolymer of an α-olefin which is butene-1, pentene-1, hexene-1, heptene-1, octene-1, nonene-1, decene-1 or undecene-1, and an aromatic vinyl monomer, said α-olefin units being contained in an amount of 50 to 98% by mol, and the aromatic vinyl monomer units being contained in an amount of 50 to 2% by mol, in the copolymer, said copolymer having an intrinsic viscosity {η} of 0.01 to 7 dl/g, as measured at 135°C in decalin, a melting viscosity of 1,000 to 100,000 centipoise at 200°C and a softening point of 50 to 150°C, and containing substantially no olefinic bonds in the polymer chain. The present invention also provides a polyolefin composition, comprising: {A} 30 to 90% by weight of an α-olefin based random copolymer including units derived from an α-olefin which is butene-1, pentene-1, hexene-1, heptene-1, octene-1, nonene-1, decene-1 or undecene-1, and units derived from an aromatic vinyl monomer, said copolymer containing substantially no olefinic double bonds in the polymer chain; (1) the units derived from the α-olein being present in an amount of 50 to 96% by mol and the units derived from the aromatic vinyl monomer being present in an amount of 4 to 50% by mol; and (ii) the intrinsic viscosity {η} as measured at 135°C in decalin being 0.01 to 7 dl/g; and {B} 70 to 10% by weight of a tackifier. The present invention further provides an adhesive-bonded structure comprising a plurality of matrices selected from metals, plastic resins and papers and an adhesive interposed between the matrices for bonding them with each other, wherein the adhesive comprises {A} 30 to 90% by weight of an α-olefin based random copolymer including units derived from an α-olefin which is butene-1, pentene-1, hexene-1, heptene-1, octene-1, nonene-1, decene-1 or undecene-1, and units derived an aromatic vinyl monomer, said copolymer containing substantially no olefinic double bonds in the polymer chain; (i) the units derived from an α-olefin being present in an amount of 50 to 96% by mol, and the units derived from an aromatic vinyl monomer being present in an amount of 4 to 50% by mol; and (ii) the intrinsic viscosity {η} measured at 135°C in decalin being 0.01 to 7 dl/g, and {B} 70 to 10% by weight of a tackifier. In accordance with the present invention, by performing a random copolymerization between the above α-olefin and an aromatic vinyl monomer while maintaining the content of the α-olefin to 50 to 98% by mol, the softening point can be maintained to from 40 to 150°C, which is suitable for a hot-melt adhesive and the adhesive power to various substrates can be remarkably enhanced while environmental aging resistances such as thermal aging resistance can be remarkably improved. It is thought that the improvement in environmental aging resistance in the present invention is due to the fact that substantially all the main chains of the polymer are formed of single bonds between carbon atoms and that no olefinic double bonds between ethylene-carbon atoms are present in the main chains and in the side chains. In the random copolymer of the present invention, alkyl side chains based on the above α-olefin and aryl (phenyl) side chains based on the aromatic vinyl group co-exist randomly. The combination of these side chains provides an excellent adhesive power to a substrate and melt flow properties suitable for a hot-melt. The α-olefin may be used alone or a combination of two or more α-olefins. Examples of the aromatic vinyl monomer are styrene, alkyl substituted styrene such as α-methylstyrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, o-ethylstyrene, m-methylstyrene, p-ethylstyrene, propylene styrene, butylstyrene; halogen substituted styrene such as chlorostyrene and bromostyrene; and vinylnaphthalene such as 1-vinylnaphthalene, 2-vinylnaphthalene, and 1-vinyl-4-methylnaphthalene. Among these styrene and vinyltoluene (methylstyrene) are preferable. The aromatic vinyl monomers may be used alone or a combination thereof may be used. The α-olefin-aromatic vinyl random copolymer may be provided by copolymerization of the above mentioned monomers with the other copolymerizable monomers such as ethylene and propylene which is contained in such an amount that the object of the present invention is accomplished, generally at not higher than 30% by mol, particularly not higher than 10% by mol per the total amount of both monomers. In the α-olefin-aromatic vinyl random copolymer, the unit derived from the α-olefin is present in an amount of 50 to 98% by mol, preferably 60 to 96% by mol, and the unit derived from the aromatic vinyl monomer is present in an amount of 2 to 50% by mol, preferably 4 to 40% by mol. The intrinsic viscosity {η} of the random copolymer measured in decalin at 135°C is from 0.01 to 7 dl/g, preferably 0.1 to 5 dl/g. This characteristic value is a measure representative of the molar weight of the α-olefin random copolymer and serves to provide a random copolymer having the above-mentioned excellent properties in combination with the other characteristics. The melting viscosity of the α-olefin-aromatic vinyl random copolymer at 200°C is from 1,000 to 100,000 centipoise, preferably 2,000 to 80,000 centipoise. This characteristics value is a measure of the coating properties when the hot-melt adhesive of the present invention is used. The softening point of the α-olefin/aromatic vinyl random copolymer measured by the ring and ball method is from 50 to 150°C, more preferably from 70 to 130°C. This characteristic value is a measure of the maximum temperature when the hot-melt adhesive of the present invention is used. The α-olefin/aromatic vinyl random copolymer can, for example, be obtained by copolymerizing an α-olefin with an aromatic vinyl monomer in the presence of an olefin polymerizing catalyst. The olefin polymerizing catalyst which is preferably used on copolymerization comprises a solid titanium catalyst component (a), an organic aluminium compound catalyst component (b), and an electron donor component (c) which is added if necessary. The solid titanium catalyst component (a) contains as essential components, magnesium, titanium, halogen and an electron donor. The atomic ratio of magnesium/titanium is higher than 1, preferably 3 to 50, more preferably 6 to 30. The atomic ratio of halogen/titanium is higher than 1, preferably 4 to 100, more preferably 6 to 40. The molar ratio of the electron donor/titanium is preferably 0.1 to 10, more preferably 0.2 to 6. The specific surface area of the solid titanium catalyst component (a) is preferably no less than 3m²/g, more preferably about 40 to 1000m²/g, even more preferably about 100 to 800m²/g. A titanium compound cannot usually be separated from titanium catalyst component (a) by simple means such as washing with hexane at ambient temperature. The X-ray spectrum of the catalyst component (a) shows that a magnesium compound is in the crystalline state or, preferably, in the very crystalline state in comparison with that of commercially available usual magnesium dihalide independently of the kind of a starting magnesium compound which is used for the catalyst preparation. The titanium catalyst component (a) may contain other elements, metals and functional groups apart from the essential components and may be diluted with an organic diluent. The solid state titanium catalyst component (a) is prepared by contacting the magnesium compound, the titanium compound and the electron donor (if necessary) with each other. On preparation of the solid titanium catalyst component (a), other reaction agents such as compounds of silicon, phosphorous and aluminium may be used if necessary. Such a solid titanium catalyst component (a) can be prepared according to any of methods disclosed in the specifications of Japanese Unexamined Patent Publications Nos. Sho 50-108385, 50-126590, 51-20297, 51-28189, 51-64586, 51-92885, 51-136625, 52-87489, 52-100596, 51-147688, 52-104593, 53-2580, 53-40093, 53-40094, 55-135102, 55-135103, 55-152710, 56-811, 56-11908, 56-18606, 58-83006, 58-138705, 58-138706, 58-138707, 58-138708, 58-138709, 58-138710, 58-138715, 60-23404, 61-21109, 61-37802 and 61-37803. A method of manufacturing the solid state titanium catalyst component (a) will now be described. Magnesium compounds can be used for preparing the solid titanium catalyst component (a). The magnesium compounds include magnesium compounds having a reducing power or having no reducing power. The magnesium compounds having a reducing power may be an organic magnesium compound represented by, for example, the formula X n MgR 2-n wherein 0≦n<2, R represents a hydrogen atom or an alkyl group, an aryl group or cycloalkyl group having 1 to 20 carbon atoms and, if n=0, each R may be the same or different, and X represents a halogen. Specifically, the organic magnesium compounds having a reducing power include dimethyl magnesium, diethyl magnesium, dipropyl magnesium, dibutyl magnesium, diamyl magnesium, dihexyl magnesium, didecyl magnesium, ethyl magnesium chloride, propyl magnesium chloride, butyl magnesium chloride, hexyl magnesium chloride, amyl magnesium chloride, butyl ethoxy magnesium, ethyl butyl magnesium, octyl butyl magnesium, and butyl magnesium hydride. The magnesium compounds can be used alone or may form a complex compound with an organic aluminium compound. These magnesium compounds may be liquid or solid. Specific examples of the magnesium compounds having no reducing power include magnesium halides such as magnesium chloride, magnesium bromide, magnesium iodide, and magnesium fluoride; alkoxy magnesium halides such as methoxy magnesium chloride, ethoxy magnesium chloride, isopropoxy magnesium chloride, butoxy magnesium chloride, and octoxy magnesium chloride; alkoxy magnesium halides such as phenoxy magnesium chloride, and methyl phenoxy magnesium chloride; alkoxy magnesium such as ethoxy magnesium, isopropoxy magnesium, butoxy magnesium, n-octoxy magnesium, and 2-ethyl hexoxy magnesium; and carboxylates of magnesium such as magnesium laurate, and magnesium stearate. These magnesium compounds having no reducing power may be compounds derived from the above-mentioned magnesium compounds having a reducing power or derived on preparation of the catalyst component. For deriving a magnesium compound having no reducing power from a magnesium compound having a reducing power, it will suffice to contact a magnesium compound having a reducing power with a polysiloxane compound, a halogen containing compound such as a silane compound containing a halogen, an aluminium compound containing a halogen, an ester and alcohol or compound having an OH group or an active carbon-oxygen bond. The magnesium compound may be a complex compound between the above-mentioned magnesium compound and another metal or a mixture of the above-mentioned magnesium compound with a double compound or other metal compound. The magnesium compounds may be a mixture of two or more of the above-mentioned compounds and may be used in the form of a liquid or solid. If the compound is solid, it may be liquified by using alcohols, carboxylic acids, aldehydes, amines or metal acid esters. Among these, magnesium compounds having no reducing power are preferable and magnesium compounds containing a halogen are more preferable. Among these, magnesium chloride, alkoxy magnesium chloride or aryloxy magnesium chloride are preferably used. There are various quadrivalent titanium compounds used for preparation of the solid titanium catalyst component (a). Usually a quadrivalent titanium compound represented by the formula Ti(OR) g X 4-g wherein R denotes a hydrocarbon group, X denotes a halogen atom and 0≦g≦4 is used. Specific examples of the quadrivalent titanium compound include titanium tetrahalides such as TiCℓ₄, TiBr₄ and TiI₄; alkoxy titanium trihalides such as Ti(OCH₃)Cℓ₃, Ti(OC₂H₅)Cℓ₃, Ti(On-C₄H₉)Cℓ₃, Ti(OC₂H₅)Br₃, Ti(O-iso-C₄H₉)Br₃; dialkoxy titanium dihalides such as Ti(OCH₃)₂Cℓ₂, Ti(OC₂H₅)₂Cℓ₂, Ti(On-C₄H₉)₂Cℓ₂, Ti(OC₂H₅)₂Br₂; trialkoxy titanium monohalides such as Ti(OCH₃)₃Cℓ, Ti(OC₂H₅)₃Cℓ, Ti(On-C₄H₉)₃Cℓ, Ti(OC₂H₅)₃Br; and tetralkoxy titanium such as Ti(OCH₃)₄, Ti(OC₂H₅)₄, Ti(On-C₄H₉)₄, Ti(O-iso-C₄H₉)₄, Ti(O-2-ethylhexyl)₄. Among these, titanium tetrahalides and alkoxy titanium trihalides are preferable. In particular, the use of alkoxy titanium trihalides is preferable. These titanium compounds may be used alone or a combination of two or more compounds may be used. The titanium compounds may be diluted with a hydrocarbon or a hydrocarbon halide. On preparation of the solid titanium catalyst component (a), an electron donor may be used according to need. As such an electron donor, oxygen containing electron donors such as an alcohol, phenol, ketone, aldehyde, carboxylic acid, ester of an organic acid or inorganic acid, ether, acid amide, acid anhydride, alkoxysilane and electron donors containing nitrogen such as ammonia, amine, nitrile, and isocyanate may be used. Specific examples of the electron donor include: alcohols having 1 to 18 carbon atoms such as methanol, ethanol, propanol, pentanol, hexanol, octanol, dodecanol, octadecyl alcohol, benzyl alcohol, phenylethyl alcohol, cumil alcohol, and isopropylbenzyl alcohol; phenols having 6 to 20 carbon atoms which may contain a lower alkyl group, such as phenol, cresol, xylenol, ethyl phenol, propyl phenol, nonyl phenol, cumil phenol, and naphthol; ketones having 3 to 15 carbon atoms such as acetone, methyl ethyl ketone, methyl isobutyl ketone, acetophenone, benzophenone, cyclohexane, and banzoquionone; aldehydes having 2 to 15 carbon atoms such as acetaldehyde, propionaldehyde, octylaldehyde, penzaldehyde, tolualdehyde, and naphtaldehyde; organic esters having 1 to 18 carbon atoms such as methyl formate, methyl acetate, ethyl acetate, vinyl acetate, propyl acetate, octyl acetate, cyclohexyl acetate, ethyl propionate, methyl butyrate, ethyl valerate, methyl chloroacetate, ethyl dichloroacetate, methyl methacrylate, ethyl crotonate, ethyl cyclohexanecaboxylate, methyl benzoate, ethyl benzoate, propyl benzoate, butyl benzoate, octyl benzoate, cyclohexyl benzoate, phenyl benzoate, benzyl benzoate, methyl toluylate, ethyl toluylate amyl toluylate, ethyl ethylbenzoate, methyl anisate, ethyl anisate, ethyl ethoxybenzoate, γ-butylolactone δ-valerolactone, coumarin, phthalide, and ethylene carbonate; acid halides such as acetyl chloride, benzoyl chloride, chloride toluylate, and chloride anisate; ethers having 2 to 20 carbon atoms such as methyl ether, ethyl ether, isopropyl ether, butyl ether, amyl ether, tetrahydrofuran, anisole, and diphenyl ether; acid amides such as N,N-dimethylamide acetate; N,N-diethylamide benzoate and N,N-dimethylamide toluylate; amines such as methylamine, ethylamine, diethylamine, trimethylamine, triethylamine, tributylamine, piperidine, tribenzylamine, aniline, pyridine, picoline, and tetramethylethyrenediamine; nitriles such as acetonitrile, benzonitrile, and trinitrile; organic phosphorus compounds having a P-O-C bond such as trimethyl phosphite, and tirethyl phosphite; and alkoxysilanes such as ethyl silicate and diphenyl dimethoxysilane. Preferable examples of the organic esters are polyvalent carboxylates. An example of such a polyvalent carboxylate is a compound having a skeleton represented by the general formula: wherein R¹ represents a substituted or unsubstituted hydrocarbon group, R², R⁵ and R⁶ represent hydrogen atoms or substituted or unsubstituted hydrocarbon groups, and R³ and R⁴ represent hydrogen atoms or substituted or unsubstituted hydrocarbon groups, preferably at least one of R₃ and R⁴ being a substituted or unsubstituted hydrocarbon group. R³ and R⁴ may be coupled with each other, and if the hydrocarbon groups, R¹ to R⁶ are substituted, the substituent contains different atoms such as N, O, S and has a group such as C-O-C, COOR, COOH, OH, SO₃H, -C-N-C-, and NH₂. Specific examples of such a polyvalent carboxylate include aliphatic polycaboxylates such as diethyl succinate, dibutyl succinate, diethyl methylsuccinate, α-diisobutyl methylglutalate, diethyl methylmalonate, diethyl isopropylmalonate, diethyl butylmalonate, diethyl phenylmalonate, diethyl diethylmalonate, diethyl phenylmalonate, diethyl diethylmalonate, diethyl dibuthylmalonate, monoctyl maleate, dioctyl maleate, dibutyl maleate, dibutyl butylmaleate, diethyl butylmaleate, β-diisopropyl methylglutalate, dialryl ethylsuccinate, di-2-ethylhexyl fumarate, diethyl itaconate, and dioctyl citraconate; aliphatic polycarboxylates such as 1,2-diethyl cyclohexanecarboxylate, carboxylate, 1,2-diisobutyl cyclohexanecarboxylate, diethyl tetrahydrophthalate, and diethyl nazicate; aromatic polycarboxylates such as monoethyl phthalate, dimethyl phthalate, methylethyl phthalate, monoisobutyl phthalate, diethyl phthalate, ethylisobutyl phthalate, di-n-propyl phthalate, diisopropyl phthalate, di-n-butyl phthalate, diisobutyl phthalate, di-n-heptyl phthalate, di-2-ethylhexyl phthalate, di-n-octyl phthalate, dineopentyl phthalate, didecyl phthalate, benzylbutyl phthalate, diphenyl phthalate, benzylbutyl phthalate, diphenyl phthalate, diethyl naphthalenedicarboxylate, dibutyl naphthalenedicarboxylate, triethyl trimellitate, dibutyl trimellitate and different ring polycarboxylates such as 3,4-furan dicarboxylic acid. Other examples of the polyvalent such carboxylates include esters of long chain dicarboxylates such as diethyl adipate, diisobutyl adipate, diisopropyl sebasate, di-n-butyl sebasate, di-n-octyl sebasate, di-e-ethylhexyl sebasate. Among these compounds, use of a carboxylate is preferable. Use of a polyvalent carboxylate, particularly phthalates is more preferable. The electron donor which is preferably contained in the solid titanium catalyst component (a) has no active electrons as is similar to organic or inorganic esters, alkoxysilane compounds, aryloxysilane compounds, ethers, ketones, tertiary alcohols, acid halides, and acid anhydrides. As the electron donor, organic esters, alkoxysilane compounds and aryloxysilane compounds are preferable. Among them, a more preferable donor is an ester of an aromatic monocarboxylic acid with an alcohol having 1 to 8 carbon atoms and an ester of a dicarboxylic acid such as malonic acid, substituted malonic acid, substituted succinic acid, maleic acid, substituted maleic acid, 1,2-cyclohexylcarboxylic acid and phthalic acid with an alcohol having more than one carbon atom. The electron donor is not necessarily be used as a starting material and may be produced in the course of preparation of the solid titanium catalyst component. The solid titanium catalyst component may be prepared by contacting the above-mentioned magnesium compounds, the titanium compounds and the electron doner, and a carrier compound and reaction accelerator which are added if necessary with each other. The carrier compound includes Al₂O₃, SiO₂, B₂O₃, MgO, CaO, TiO₂, ZnO, ZnO₂, SnO₂, BaO, ThO and a resin such as a styrene-divinylbenzene copolymer. Among them, Al₂O₃, SiO₂ and the styrene-divinylbenzene copolymer are preferable. As a reaction accelerator, organic and inorganic compounds containing, for example, silicon, phosphorus, or aluminium may be used. The solid titanium catalyst component (a) is prepared by contacting the magnesium compounds, the titanium compound, and the electron donor if necessary and further the carrier compound if necessary with each other. The method of preparing the solid titanium catalyst component (a) is not particularly restricted. Several preparing methods will now be briefly described: (1) A magnesium compound, an electron donor and a titanium compound are contacted with each other in the desired order to react with each other. For the reaction, each component may be preliminarily processed with the electron donor and/or a reaction accelerator such as an organic aluminium compound and a silicon compound containing a halogen. The electron donor is used at least one time in this method. (2) A liquid magnesium compound having no reducing power is reacted with a liquid titanium compound in the presence of an electron donor to precipitate a solid magnesium-titanium double compound. (3) The reaction product obtained by method (2) is further reacted with a titanium compound. (4) The reaction product obtained by method (1) or (2) is further reacted with an electron donor or a titanium compound. (5) A solid material obtained by pulverizing a magnesium compound, an electron donor and a titanium compound is processed with any one of a halogen, a halogen compound and an aromatic hydrocarbon. This method may include a step for pulverizing only the magnesium compound, a complex compound including the magnesium compound and the electron donor or the magnesium compound and a titanium compound. After pulverizing, the pulverized material may be preliminarily processed with a reaction accelerator and then processed with, for example, a halogen. The reaction accelerator may include an organic aluminium compound or a silicon compound containing a halogen. (6) The compound obtained by methods (1) to (4) is processed with a halogen, a halogen compound or an aromatic hydrocarbon. (7) The reaction product which is obtained by contacting a metal oxide, an organic magnesium compound and a halogen containing compound is contacted with an electron donor and a titanium compound. (8) A magnesium compound such as a magnesium salt of organic acid, alkoxymagnesium or aryloxymagnesium is reacted with an electron donor, a titanium compound and/or a halogen containing hydrocarbon. (9) A hydrocarbon solution containing at least a magnesium compound and an alkoxy titanium; a titanium compound; an electron donor and a halogen containing compound such as a halogen containing silicon compound added if necessary are reacted with each other. (10) A liquid magnesium compound having no reducing power is reacted with an organic aluminium compound to precipitate a solid magnesium-aluminum double compound, which is then reacted with an electron donor and a titanium compound. When the solid titanium catalyst component (a) is prepared by such a method, the amounts of the magnesium compound, the titanium compound and the electron donor added according to need are different depending upon the kind, the contact conditions and the order of contact. For 1 mole of magnesium, the electron donor preferably is used in an amount of 0.01 to 5 moles, particularly preferably 0.1 to 1 mole, and the liquid titanium compound is preferably used in an amount of 0.1 to 1000 moles, particularly preferably 1 to 200 moles. The temperature at which these compounds are contacted with each other is usually -70°C to 200°C, preferably 10°C to 150°C. The solid titanium catalyst component (a) obtained by the above mentioned methods may be purified by being sufficiently washed with a liquid inactive hydrocarbon. Examples of the inactive hydrocarbons which may be used for this end include: aliphatic hydrocarbons such as n-pentene, isopentene; n-hexene, isohexene, n-heptane, n-octane, isooctane, n-decane, n-dodcane, kerosene, and fluid paraffin; cycloaliphatic hydrocarbons such as cyclopentene, methylcyclopentene, cyclohexane, and methylcyclohexane; aromatic hydrocarbons such as benzene, toluene, xylene, and cymene; and hydrocarbon halides such as chlorobenzene, dichloroethane and a mixture thereof. The olefin polymerization catalyst used for manufacturing the α-olefin random copolymer used in the present invention comprises the above mentioned solid titanium catalyst component (a) and the organic aluminium compound catalyst component (b). The organic aluminium compound catalyst component (a) may include, for example, (1) an organic compound represented by the general formula R¹ m A (OR²) n H p X q wherein R¹ and R² represent hydrocarbon groups generally having 1 to 15 carbon atoms, preferably 1 to 4 carbon atoms, which may be the same or different, X represents a halogen atom, 0<m<3, 0≦n<3, 0≦p<3, and 0≦q<3 provided that m+n+p+q=3 ; and (2) a complex alkylated compound between a group I metal and aluminium, represented by the general formula M¹AℓR¹₄ wherein M¹ represents Li, Na or K and R¹ is the same as above. Examples of the organic aluminium compound (1) include: a compound represented by the general formula R¹ m Aℓ(OR²) 3-m wherein R¹ and R² are same as above and m is preferably 1.5≦m≦3; a compound represented by the general formula R¹ m AℓX 3-m wherein R¹ is the same as above, X represents a halogen atom, and m is preferably 0<m<3; and a compound represented by the general formula R¹ m Aℓ(OR²) n X q wherein R¹ and R² are the same as above, X represents a halogen atom, 0<m≦3, 0≦n<3, 0≦q<3, and m+n+q=3 . Specific examples of the aluminium compound (1) include: trialkyl aluminium such as triethyl aluminium and tributyl aluminium; trialkenyl aluminium such as triisoprenyl aluminium; dialkyl aluminium alkoxide such as diethyl aluminum ethoxide and dibutyl aluminium butoxide; alkyl aluminium sesquialkoxide such as ethyl aluminium sesquiethoxide, and butyl aluminium sesquibutoxide; partially alkoxylated alkyl aluminium having an average composition represented by the formula R¹ 2.5 Aℓ(OR²) 0.5 ; dialkyl aluminium halide such as diethyl aluminium chloride, dibutyl aluminium chloride and diethyl aluminium bromide; alkyl aluminium sesquihalide such as ethyl aluminium sesquichloride, butyl aluminium sesquichloride and ethyl aluminium sesquibromide; partially halogenated alkyl aluminium such as ethyl aluminium dichloride, propyl aluminium dichloride and butyl aluminium dibromide; dialkyl aluminium hydride such as diethyl aluminium hydride and dibutyl aluminium hydride; alkyl aluminium dihydride such as ethyl aluminium dihydride, propyl aluminium dihydride and another partially hydrogenated alkyl aluminium; and partially alkoxylated and halogenated alkyl aluminium such as ethyl aluminium ethoxychloride, butyl aluminium butoxychloride and ethyl aluminium ethoxybromide. The compound analogous to compound (1) may include an organic aluminium compound having two or more aluminium atoms which are bonded to each other through an oxygen or nitrogen atom. Such an organic compound includes, for example, (C₂H₅)₂AℓOAℓ(C₂H₅)₂, (C₄H₉)₂AℓOAℓ(C₄H₉)₂, and methyl aluminoxane. A compound included in (2) includes, for example, LiA (C₂H₅)₄ and LiA (C₇H₁₅)₄. Among the compounds of (1) and (2), trialkyl aluminium or alkyl aluminium which is bonded with the above mentioned two or more aluminium compounds is preferable. The olefin polymerizing catalyst used for manufacturing the α-olefin random copolymer {A} constituting the polyolefin composition of the present invention comprises the solid titanium catalyst component (a), the organic aluminium compound catalyst component (b) and the electron donor (c) if necessary. The electron donor (c) includes amines, amides, ethers, ketones, nitriles, phosphines, stibines, arcines, phosphoramids, esters, thioethers, thioesters, acid anhydrides, acid halides, aldehydes, alcolates, alkoxy (aryloxy) silanes, organic acids, amides and salts of metals which belong to groups I to IV of the periodic Table. The salts may be formed by a reaction between an organic acid and an organic metal compound. Specific examples of the electron donor (c) include the electron donor used for the preparation of the above mentioned titanium component (a). An excellent result is obtained when organic acid ester, the alkoxy (aryloxy) silane compound, ether, ketone, acid anhydride or amide, for example, is used as the electron donor (c). Particularly if the electron donor in the solid titanium catalyst component (a) is a monocarboxylate, it is preferable that an alkyl ester of an aromatic carboxylic acid be used as the electron donor (c). If the electron donor in the solid titanium catalyst component (a) is an ester between the dicarboxylic acid which has been mentioned as a preferable compound and an alcohol having two or more carbon atoms, it is preferable that an organic silicon compound represented by the following general formula be used as the electron donor (c): R n Si(OR') 4-n wherein R and R' represent hydrocarbon groups and 0<n<4. Specific examples of the organic silicon compound represented by the general formula set forth above include trimethylmethoxysiloxane, trimethylethoxysilane, dimethyldimethoxysilane, dimethyldiethoxysilane, diisopropyldimethoxysilane, t-butylmethyldimethoxysilane, t-amylmethyldiethoxysilane, diphenyldimethoxysilane, phenylmethyldimethoxysilane, diphenyldiethoxysilane, bis o-triledimethoxysilane, bis m-triledimethoxysilane, bis p-triledimethoxysilane, bis p-trilediethoxysilane, bisethylphenyldimethoxysilane, dicyclohexyldimethoxysilane, cyclohexylmethyldimethoxysilane, cyclohexylmethyldiethoxysilane, ethyltrimethoxysilane, ethyltriethoxysilane, vinyltrimethoxysilane, methyltrimethoxysilane, n-propyltriethoxysilane, decyltrimethoxysilane, decyltriethoxysilane, phenyltrimethoxysilane, γ-chloropropyltrimethoxysilane, methyltriethoxysilane, ethyltriethoxysilane, vinyltriethoxysilane, t-butyltriethoxysilane, n-butyltriethoxysilane, isobutyltriethoxysilane, phenyltriethoxysilane, γ-aminopropyltriethoxysilane, chlorotriethoxysilane, ethyltriisopropoxysilane, vinyltributoxysilane, cyclohexyltrimethoxysilane, cyclohexyltriethoxysilane, 2-norbornanetrimethoxysilane, 2-norbornanetriethoxysilane, 2-norbornanemethyl-dimethoxysilane, ethyl silicate, butyl silicate, trimethylphenoxysilane, methyltriallyloxysilane, vinyltris (β-methoxyethoxysilane), vinyltriacetoxy-silane, dimethyltetraethoxydisiloxane; cyclopentyltrimethoxysilane, 2-methylcyclopentyltrimethoxysilane, 2,3-dimethylcyclopentyltrimethoxysilane, cyclopentyltriethoxysilane; dicyclopentyldimethoxysilane, bis(2-methylcyclopentyl)dimethoxysilane, bis(2,3-dimethylcyclopentyl)dimethoxysilane, dicyclopentyldiethoxysilane; and tricyclopentylmethoxysilane, tricyclopentylethoxysilane, dicyclopentylmethylmethoxysilane, dicyclopentylethylmethoxysilane, hexenyltrimethoxysilane, dicyclopentylmethylethoxysilane, cyclopentyldimethylmethoxysilane, cyclopentyldiethylmethoxysilane, and cyclopentyldimethylethoxysilane. Among them, it is preferable to use ethyltriethoxysilane, n-propyltriethoxysilane, t-butyltriethoxysilane, vinyltriethoxysilane, phenyltriethoxysilane, vinyltributoxysilane, diphenyldimethoxysilane, phenylmethyldimethoxysilane, bis p-triledimethoxysilane, p-trilemethyldimethoxysilane, dicyclohexyldimethoxysilane, cyclohexylmethyldimethoxysilane, 2-norbornanetriethoxysilane, 2-norbornanemethyldimethoxysilane, phenyltriethoxysilane, dicyclopentyldimethoxysilane, hexenyltrimethoxysilane, cyclopentyltriethoxysilane, tricyclopentylmethoxysilane, and cyclopentyldimethylmethoxysilane. Two or more of these organic silicon compounds may be mixed and used. The olefin polymerizing catalyst used for copolymerization may be a catalyst formed from a metallocene component (d) and an aluminoxane component (e). The metallocene component (d) may be represented by the general formula: wherein M represents zirconium, titanium, or hafnium, L represents a ligand having a cycloalkadienyl skeletal structure, wherein the two L groups may be bonded to each other via an alkylene group, a substituted alkylene group or a silylene group, and X and Y represent hydrocarbon groups having 1 to 12 carbon atoms, alkoxy groups, aryloxy groups, halogens or hydrogen atoms. Examples of the ligand having a cycloalkadienyl skeletal structure include alkyl substituted cyclopentadienyl groups such as a cyclopentadienyl group, a methylcyclopentadienyl group, a pentamethylcyclopentadienyl group, an indenyl group, and a fluorenyl group. The alkylene group includes a methylene group, an ethylene group, and a propylene group. The substituted alkylene group includes an isopropylidene group. The substituted silylene group includes dimethylsilylene and diphenylsilylene groups. X and Y represent hydrocarbon groups having 1 to 12 carbon atoms, alkoxy groups, aryloxy groups, halogen and hydrogen atoms. Examples of the hydrocarbon groups having 1 to 12 carbon atoms include an alkyl group, a cycloalkyl group, an aryl group, and an aralkyl group. Specifically the alkyl group includes a methyl group, an ethyl group, a propyl group, a isopropyl group, and a butyl group. Examples of the cycloalkyl groups includes α cyclopentyl group and a cyclohexyl group. The aryl group includes a phenyl group, and a trile group. The aralkyl group includes a benzyl group and a neophyl group. The alkoxy group includes a methoxy group, an ethoxy group and a butoxy group. The aryloxy group includes a phenoxy group. The halogen includes fluorine, chlorine, bromine and iodine. Specific examples of the transition metal compounds including a ligand having a cycloalkadienyl skeletal structure in which M is zirconium, include: bis(cyclopentadienyl)zirconium chloride, bis(cyclopentadienyl)zirconium dibromide, bis(cyclopentadienyl)methyl zirconium monochloride, bis(cyclopentadienyl)ethyl zirconium monochloride, bis(methylcyclopentadienyl)zirconium dichloride, bis(indenyl)zirconium dichloride, bis(cyclopentadienyl)zirconium diemthyl, bis(cyclopentadienyl)zirconium methoxychloride, bis(cyclopentadienyl)zirconium ethoxychloride, ethylene bis(indenyl)dimethyl zirconium, ethylene bis(indenyl)zirconium dichloride, ethylene bis(4,5,6,7-tetrahydro-1-indenyl)zirconium dichloride, dimethylsilylene bis(cyclopentadienyl)zirconium dichloride, dimethylsilylene bis(indenyl)zirconium dichloride, and dimethylsilylene bis(methylcyclopentadienyl)zirconium dichloride. In the above mentioned zirconium compounds, compounds in which the zirconium is substituted by titanium or hafnium may be used. The aluminoxane component (e) may be produced by the following methods: (1) A hydrocarbon solvent suspension of a compound containing adsorption water or salts containing water of crystallization, such as magnesium chloride hydrate, copper sulfate hydrate, aluminium sulfate hydrate, nickel sulfate hydrate and cerium chloride hydrate is added with an organic aluminium compound such as trialkyl aluminium so that they react with each other, and the component (e) is recovered in the form of a hydrocarbon solution. (2) Water, ice or water vapor is directly acted upon an organic aluminium compound such as trialkyl aluminium in a solvent such as benzene, toluene, ethyl ether or tetrahydrofuran and the component (e) is recovered in the form of a hydrocarbon solution. The aluminoxane may contain a small amount of organic metal component. The aluminoxane may be disolved in a solvent again after a solvent or unreacted organic aluminium compound is removed from the recovered aluminoxane solution by distillation. The organic aluminium compounds used for the preparation of the aluminoxane include the compounds which have been exemplarily described as the organic aluminium compound catalyst component (b). Among them, trialkylaluminium is preferably used. The above mentioned organic aluminium compounds may be used alone or in combination. The solvent used for a solution of the aluminoxane includes aromatic hydrocarbons such as benzene, toluene, xylene, cumene, and cymene, aliphatic hydrocarbons such as pentane, hexane, heptane, octane, decane, dodecane, hexadecane, octadecane; cycloalphatic hydrocarbons such as cyclopentane, cyclohexane, cyclooctane, methylcyclopentane; petroleum fractions such as gasoline, kerosene and gas oil, and hydrocarbon solvents such as halides particularly chlorides and bromides of the above mentioned aromatic hydrocarbons, aliphatic hydrocarbons and cycloaliphatic hydrocarbons. Furthermore ethers such as ethyl ether and tetrahydrofuran may be used. Among the solvents, aromatic hydrocarbons are particularly preferable. Specific examples of the inactive hydrocarbon medium used include: aliphatic hydrocarbons such as propane, butane, pentane, hexane, heptane, octane, decane, dodecane, and kerosene; cycloaliphatic hydrocarbons such as cyclopentane, cyclohexane, and methylcyclopentane; and aromatic hydrocarbons such as benzene, toluene, and xylene; hydrocarbon halides such as ethylene chloride and chlorobenzene and the mixture thereof. Liquid -olefin or aromatic vinyl monomer may also be used at a polymerization reaction temperature which will be described hereafter. Preferable usage of each catalyst component in a polymerization system is as follows: The titanium atoms are in the component (a) is in an amount of about 0.0001 to 1.0 mm mol per 1 of reaction volume. The metal atoms are in the component (b) in an amount of about 1 to 500 mols per 1 mol of the titanium atoms in the component (a). The component (c) is in an amount of 0.001 to about 10 mols, preferably about 0.01 to about 2 mols, particularly preferably about 0.05 to about 1 mol, per 1 mol of the metal atoms in the component (b). The polymerization temperature may be approximately selected and is preferably up to about 200°C, more preferably about 5o to 180°C. The pressure may be appropriately selected. It is preferable that polymerization be performed at atmospheric pressure or about 50kg/cm². The polymerization may be performed in any of the batch, semi-continuous and continuous methods. The molecular weight may be adjusted to some extent by changing the polymerization temperature and usage ratios of the catalyst components. It is most effective to add hydrogen to the polymerization system. In one embodiment of the present invention, the α-olefin random copolymer is used as it is as an adhesive. In another embodiment of the present invention, 30 to 90% by weight, preferably 35 to 90% by weight, particularly preferably 40 to 90% by weight of the α-olefin random copolymer is compounded with 70 to 10% by weight, preferably 65 to 10% by weight, particularly preferably 60 to 10% by weight, of the tackifier {B}. As the tackifier, various tackifier resins which are usually used for hot-melt binders and self-adhesives may be used. Depending upon a source of monomers to be polymerized, the tackifier resins include: aliphatic hydrocarbon resins mainly manufactured from C₄ fraction, C₅ fraction obtained by decomposition of, for example, petroleum or naphtha, and a mixture thereof or a fraction thereof, for example, isoprene and 1,3-pentadiene in the C₅ fraction as the main raw material; aromatic hydrocarbon resins manufactured mainly from styrene derivatives and indenes in C₉ fraction obtained by decomposition of, for example, petroleum and naphtha; aliphatic/aromatic copolymer hydrocarbon resins which are obtained by copolymerization of any of the C₄ and C₅ fraction with the C₅ fraction; cycloaliphatic hydrocarbon resins which are obtained by hydrogenaling an aromatic hydrocarbon; synthesized terpene hydrocarbon resins having a structure containing aliphatic, cycloaliphatic and aromatic hydrocarbons; terpene hydrocarbon resins manufactured from α, β-pinene in terpene oil; cumarone indene hydrocarbon resins manufactured from indene and styrenes in coal tar naphtha; low molecular weight styrene resins; and rosin resins such as rosins and rosin esters. In the present invention, a composition mainly including the above mentioned α-olefin random copolymer or this copolymer may be compounded with various additives according to need. For example, if the composition is used as an adhesive, the composition may be added with softening agents such as dioctyl phthalate, dibutyl phthalate, machine oil, process oil and polybutene; waxes having a melting point of 40 to 65°C, such as petroleum parafin wax, polyolefin wax, microwax; fillers such as calcium carbonate, zinc white, titanium oxide, and silica; and antioxidents such as phenol or bisphenol organic compounds and metallic soap. In order to prepare the hot-melt adhesive composition, a mixture of the α-olefin random copolymer {A}, the tackifier {B} if necessary and the above mentioned various additives if necessary is agitated while heating so that an uniform melt is prepared. The melt is formed into granules, flakes, pellets and bars according to the use application while being cooled. The hot-melt adhesive composition will be used for melting or application again. For example, if it will be used for bonding the corners of molded parts, a bar-shaped composition will be loaded into a welding gun and then used. In order to prepare a pressure-sensitive adhesive, a mixture including the α-olefin random copolymer {A}, the tackifier {B} and the above mentioned various additives added according to needs may be usually kneaded on a roller or alternatively dissolved in an appropriate solvent. The present invention provides a hot-melt adhesive which is useful for various substrates such as metal, plastics or paper. Various surface treated steel plates or foils and light metal plates or foils, such as aluminium, are used as the metal substrate. The surface treated steel plates or foils may be subjected to one or more plating treatments such as zinc plating, tin plating, nickel plating, nickel-tin plating or aluminium plating, forming treatment such as electrolytic chromic acid treatment, and chemical treatments such as chronic acid treatment, phosphoric acid treatment and zirconium treatment. As light metal plates or foils, aluminium alloy plates or foils may be used as well as pure aluminium plate or foils. They may be coated with thermoplastic coating materials and/or thermosetting coating materials which are known per se. As a plastic substrate, molded articles or films made of various plastics are used. The plastic resins include, for example, olefin resins such as polyethylene, polypropylene, ethylene-propylene copolymer, ethylene-vinyl acetate copolymer, and ionomer; polyesters such as polyethylene terephthalate, polybutylene terephthalate, polyethylene terephthalate, polyethylene isophthalate; polyamides such as nylon 6, nylon 6,6, nylon 6-nylon 6,6 copolymer; polyhexamethylene isophthamide and polyhexamethylene terephthamide; polycarbonates; vinyl chloride resins and vinylidene chloride resins. The plastics substrate may be unstretched or molecular-oriented by monoaxial or biaxial stretching. The paper substrate may include glassine paper, pure white roll paper, imitation paper, other packaging paper and kraft paper. Furthermore, synthesized pulp paper, and mixed screened paper between the synthetic pulp and cellulose paper, mixed screened paper between the above mentioned papers and inorganic fibers may also be used. The hot-melt adhesive of the present invention may be, of course, used for bonding laminates comprising one or more of the above mentioned substrates. The hot-melt adhesive of the present invention may be used for sealing and bonding between a container and a lid, for bonding a plurality of members themselves for integration and for laminating of the above mentioned substrates themselves by utilizing its excellent performance. The adhesion structure may be freely designed. A non-strippable adhesion structure can be provided by using the hot-melt adhesive or a readily strippable adhesion structure may be provided by mixing another olefin resin. The above mentioned various substrates may be coated with the hot-melt adhesive composition on one side or both sides to provide pressure-sensitive tapes. For any use applications, the composition of the present invention has advantages that it has excellent in adhesion properties, thermal stability resistance, heat resistance, weather resistance and color shade, that it develops no odor on preparation of the composition and in use and that it is excellent in preservation of flavor of contents and sanitary characteristics when used as a packaging material. The present invention will be further described in the following Examples. Examples The α-olefin random copolymer used in the following Example 1 was synthesized as follows: (Synthesis (1) of α-olefin random copolymer) (Preparation of solid titanium catalyst component (a)) 95.2g of anhydrous magnesium chloride, 442ml of decane and 390.6g of 2-ethylhexyl alcohol were heated at 130°C for 2 hours for reaction to obtain a uniform solution. 21.3g of phthalic anhydride was added to the solution and mixed by being agitated at 130°C for one hour so that the phthalic anhydride was dissolved in uniform solution. After the thus obtained uniform solution was cooled to room temperature, a total of 75ml of the uniform solution was drop charged into 200ml of titanium over one hour. After completion of charging, the temperature of the mixture liquid was elevated to 110°C, at which the mixture liquid was added with 5.22g of diisobutyl phthalate and was maintained at the same temperature while being agitated for two hours. After completion of the 2 hour reaction, a solid portion was collected by thermal filtration. After the solid portion was suspended in 275ml of titanium tetrachloride solution again, a heating reaction was performed at 110°C for 2 hours again. After termination of the reaction, the solid portion was collected again by thermal filtration and was sufficiently washed with decane and hexane at 110°C until no free titanium compound in the solution was detected. The solid titanium catalyst component (a) which had been prepared by the above mentioned procedure was preserved as a decantation slurry. A part of the slurry was dried for the purpose of analyzing the catalyst composition. The component of the obtained titanium catalyst component (a) comprised 2.5% by weight of titanium, 63.2% by weight of chlorine, 20.7% by weight of magnesium and 12.5% by weight of diisobutyl butanephthalate. (Polymerization) 800ml of toluene and 200ml of styrene were charged into a 2 of polymerizer having agitating blades. After nitrogen bubbling was conducted for 15 minutes, 10 mm mol of tri-isobutyl aluminium and 1 mm mol of trimethylmethoxysilane were charged. Thereafter the bubbling was ceased and butyne-1 and hydrogen were continuously introduced to the polymerizer at a rate of 150 per hour, respectively. The solution was elevated in temperature to 60°C and was added with titanium catalytic component having 0.2 mm mol, calculated in terms of titanium atom, to commence polymerization. The polymerization was conducted at 60°C for 30 minutes. The polymerization proceeded in a solution state. The polymerization was stopped by adding isobutyl alcohol. The polymer was precipitated in a large amount of methanol and was vacuum dried for one day and night so that 96g of polymer was obtained. The polymer contained 90.2% by mol of butyne-1 and the intrinsic viscosity of the polymer which was measured in decaline at 135°C was 0.45 d /g. (Synthesis (2) of α-olefin random copolymer) The copolymer of butene-1 and styrene which was used in Examples 2, 3, 4, 5 and 6 was synthesized by changing styrene and butene-1 which were used in (Synthesis (1) of α-olefin random copolymer). (Synthesis (3) of α-olefin random copolymer) The random copolymer of butene-1 and p-methyl styrene which was used in Example 7 was synthesized by using an appropriate amount of p-methylene in lieu of styrene in (Synthesis (1) of α-olefin random copolymer). (Synthesis (4) of α-olefin random copolymer) The polybutene-1 used in comparative Example 1 was synthesized without using styrene. (Synthesis (5) of α-olefin random copolymer) The propylene-styrene random copolymer used in comparative Example 2 was synthesized by using propylene in lieu of butene-1 and using an appropriate amount of styrene and propylene in (Synthesis (1) of α-olefin random copolymer). Example 1 Butene-1 styrene random copolymer containing 90.2% by mol of butene-1 and having a viscosity (7 B ) of 7100 centipoise measured at 200°C by means of Brookfield viscometer and a softening point (R&B softening point) of 105°C measured by the ring and ball method was melted and uniformly applied upon a polyethylene terephtalate plate as the α-olefin random copolymer and was naturally allowed to cool. The coating thickness was 56 µm. A biaxially oriented film of polypropylene was superposed thereon and was heat sealed to the polyethylene terephthalate plate under conditions of 120°C, 3kg/cm² and ten seconds to obtain a specimen for evaluating the bond strength. Evaluation of the bonding strength of the specimen was conducted by the method as follows: (T-peel Test) Peeling speed: 30 cm/minute. (Shear Adhesive Failure Temperature (SAFT) measurement) Temperature elevation speed: 25°C/hour load: 500g The results of the test were shown in Table 1. In Table 1, 7 B represents the viscosity which was measured at 200°C by means of a Brookfield viscometer and 7 E represents the viscosity measured at 200°C by means of an Emiller viscometer. The R&B softening point represents the softening point measured by the ring and ball method, PET and OPP represent biaxially oriented films of polyethylene and polypropylene, respectively. Examples 2 and 3 The procedures of Example 1 were repeated in the same manner except that the α-olefin aromatic vinyl random copolymer or a bond base was changed as shown in Table 1. The results are shown in Table 1. Comparative Example 1 The procedures of Example 1 were repeated in the same manner except that polybutene-1 was used in lieu of the α-olefin aromatic vinyl random copolymer. The results are shown in Table 1. Comparative Example 2 The procedures of Example 1 were repeated in the same manner except that polypropylene was used as the α-olefin in lieu of butene-1. The results are shown in Table 1. Example 4 50% by weight of butene-1 styrene random copolymer which is an α-olefin random copolymer containing 90.1% by mol of butene-1 and having an intrinsic viscosity of 0.50 measured at 135°C in decaline and 50% by weight of Alkono P-100 manufactured by Arakawa Kagaku Co., Ltd., a hydrogenated styrene resin (hydrogenation factor 100%) used as a tackifier were melted and mixed with each other at 200°C for two hours. The obtained mixture was uniformly applied upon a polyethylene terephthalate plate in a molten state and was naturally allowed to cool. The application thickness was 56 mm. A biaxially oriented film of polypropylene was superposed thereon and heat sealed at 120°C under a pressure of 3kg/cm² for 10 seconds to obtain a specimen for evaluating the bond strength. A T-peel test was conducted at a measured temperature of 20°C and a peeling speed of 30 cm/min. for evaluating the bond strength of the specimen. The results are shown in Table 2. Examples 5 to 7 The procedures of Example 4 were repeated in the same manner except that a aromatic vinyl monomer and α-olefin content are changed as shown in Table 2. The results are shown in Table 2.

Claims: A hot-melt adhesive which comprises a random copolymer of an α-olefin which is butene-1, pentene-1, hexene-1, heptene-1, octene-1, nonene-1, decene-1 undecene-1, and an aromatic vinyl monomer, said α-olefin units being contained in an amount of 50 to 98% by mol, and the aromatic vinyl monomer units being contained in an amount of 50 to 2% by mol, in the copolymer, said copolymer having an intrinsic viscosity {η} of 0.01 to 7 dl/g, as measured at 135°C in decalin, a melting viscosity of 1,000 to 100,000 centipoise at 200°C and a softening point of 50 to 150°C, and containing substantially no olefinic bonds in the polymer chain. A hot-melt adhesive as defined in claim 1 in which 60 to 96% by mol of α-olefin units and 4 to 40% by mol of aromatic vinyl units are contained. A hot-melt adhesive as defined in claim 1 or 2 in which the α-olefin is butene-1. A hot-melt adhesive as defined in any one of claims 1 to 3 in which the aromatic vinyl monomer is styrene. A polyolefin composition, comprising: {A} 30 to 90% by weight of an α-olefin based random copolymer including units derived from an α-olefin which is butene-1, pentene-1, hexene-1, heptene-1, octene-1, nonene-1, decene-1 undecene-1, and units derived from an aromatic vinyl monomer, said copolymer containing substantially no olefinic double bonds in the polymer chain; (1) the units derived from the α-olein being present in an amount of 50 to 96% by mol and the units derived from the aromatic vinyl monomer being present in an amount of 4 to 50% by mol; and (ii) the intrinsic viscosity {η} as measured at 135°C in decalin being 0.01 to 7 dl/g; and {B} 70 to 10% by weight of a tackifier. An adhesive-bonded structure comprising a plurality of matrices selected from metals, plastic resins and papers and an adhesive interposed between the matrices for bonding them with each other, wherein the adhesive comprises {A} 30 to 90% by weight of an α-olefin based random copolymer including units derived from an α-olefin which is butene-1, pentene-1, hexene-1, heptene-1, octene-1, nonene-1, decene-1 or undecene-1, and units derived an aromatic vinyl monomer, said copolymer containing substantially no olefinic double bonds in the polymer chain; (i) the units derived from an α-olefin being present in an amount of 50 to 96% by mol, and the units derived from an aromatic vinyl monomer being present in an amount of 4 to 50% by mol; and (ii) the intrinsic viscosity {η} measured at 135°C in decalin being 0.01 to 7 dl/g, and {B} 70 to 10% by weight of a tackifier. A hot-melt adhesive as defined in any one of claims 1 to 4 in which the copolymer further contains an ethylene and/or a propylene unit as a copolymerizable monomer unit in an amount of not higher than 30% by mol, based on the total weight of the α-olefin monomer and the aromatic vinyl monomer. A polyolefin composition as defined in claim 5 in which the copolymer further contains an ethylene and/or a propylene unit as a copolymerizable monomer unit in an amount of not higher than 30% by mol, based on the total weight of the α-olefin monomer and the aromatic vinyl monomer. An adhesive-bonded structure as defined in claim 6 in which the copolymer further contains an ethylene and/or a propylene unit as a copolymerizable monomer unit in an amount of not higher than 30% by mol, based on the total weight of the α-olefin monomer and the aromatic vinyl monomer.

Inventors: KAWASAKI MASAAKI MITSUI PETROC, KITANI HIROAKI MITSUI PETROCHE, MINAMI SHUJI MITSUI PETROCHEMI, YOSHITAKE JUNICHI MITSUI PETRO, KAWASAKI, MASAAKI MITSUI PETROCHEMICAL IND., LTD.,, KITANI, HIROAKI MITSUI PETROCHEMICAL IND., LTD.,, MINAMI, SHUJI MITSUI PETROCHEMICAL IND., LTD.,, YOSHITAKE, JUNICHI MITSUI PETROCHEMICAL IND., LTD.
Applicants: MITSUI PETROCHEMICAL IND, MITSUI PETROCHEMICAL INDUSTRIES, LTD.
Application year: 1991
Main classification: C09J123
IPC codes: C09J123