Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/18—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
  • C08L23/20—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/12—Powdering or granulating
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/20—Compounding polymers with additives, e.g. colouring
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/16—Nitrogen-containing compounds
  • C08K5/20—Carboxylic acid amides
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/04—Homopolymers or copolymers of ethene
  • C08L23/08—Copolymers of ethene
  • C08L23/0807—Copolymers of ethene with unsaturated hydrocarbons only containing four or more carbon atoms
  • C08L23/0815—Copolymers of ethene with unsaturated hydrocarbons only containing four or more carbon atoms with aliphatic 1-olefins containing one carbon-to-carbon double bond
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2323/04—Homopolymers or copolymers of ethene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2323/10—Homopolymers or copolymers of propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2323/18—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
  • C08J2323/20—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2423/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2423/04—Homopolymers or copolymers of ethene
  • C08J2423/06—Polyethene

Definitions

• the present invention relates to a polyolefin-based resin pellet and a method for producing a polyolefin-based resin pellet.
• Polyolefin-based resins are used as packaging materials for plastic bags and the like because of their durability and ease of handling, and such packaging materials are manufactured by extrusion-molding a polyolefin-based resin film.
• a characteristic required for polyolefin resin films is slipperiness, and if the slipperiness is poor, the wound films will stick to each other and will not come off, or the film will stick to the extruder and peel off when the film is extruded. Problems such as disappearance occur.
• the polyolefin-based resin film is manufactured by molding the polyolefin-based resin pellets into a film.
• Resin pellets can be obtained by melt-kneading the resin and extrusion molding.
• a lubricant that improves the slipperiness of the film can be added when the resin is melt-kneaded.
• an object of the present invention is to provide a polyolefin-based resin pellet that generates less fine powder.
• a polyolefin-based resin pellet containing a polyolefin-based resin, an erucic acid amide, and a fatty acid amide having 20 or less carbon atoms A pellet in which the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms is 100% by mass, and the content of the fatty acid amide having 20 or less carbon atoms is 1 to 6% by mass.
• the polyolefin-based resin is one or more selected from a polyethylene-based resin and a polypropylene-based resin.
• the method for producing a polyolefin-based resin pellet according to any one of [1] to [11].
• the lubricant comprises an erucic acid amide and a fatty acid amide having 20 or less carbon atoms.
• a polyolefin-based resin pellet with less generation of fine powder is provided.
• the polyolefin-based resin pellet according to the present embodiment contains a polyolefin-based resin, an erucic acid amide, and a fatty acid amide having 20 or less carbon atoms.
• the polyolefin-based resin contained in the polyolefin-based resin pellets according to the present embodiment may be any resin containing a polymer polymerized using olefins as a monomer, and is not particularly limited.
• polyethylene-based resin and polypropylene-based resin may be used. Can be mentioned.
• the polyethylene-based resin contains an ethylene-based polymer.
• ethylene-based polymers are ethylene homopolymers, copolymers of ethylene and ⁇ -olefins, and copolymers of ⁇ -olefins and ethylene substituted with alicyclic compounds.
• An example of an ethylene homopolymer is high pressure low density polyethylene (LDPE) having a density of 910 to 935 kg / m 3 in which repeating units of ethylene are randomly bonded with a branched structure by high pressure radical polymerization using a radical initiator. ..
• LDPE high pressure low density polyethylene
• copolymers of ethylene and ⁇ -olefins include linear low-density polyethylene having crystallinity, and elastomers of a copolymer of ethylene and ⁇ -olefin having low crystallinity and rubber-like elastic properties. Can be mentioned.
• the density of the linear low density polyethylene can be 900 to 940 kg / m 3
• the density of the elastomer of the copolymer of ethylene and ⁇ -olefin can be 860 to 900 kg / m 3 .
• an ⁇ -olefin is an ⁇ -olefin having 3 to 10 carbon atoms
• examples of the ⁇ -olefin having 3 to 10 carbon atoms include propylene, 1-butene, 1-pentene, 1-hexene and 4-methyl. Examples thereof include -1-pentene, 1-octene, 1-decene and 3-methyl-1-butene, preferably an ⁇ -olefin having 4 to 10 carbon atoms, and more preferably 1-butene and 1-butene. Hexene or 1-octene.
• An example of an ⁇ -olefin substituted with an alicyclic compound is vinylcyclohexane.
• the amount of the structural unit derived from ⁇ -olefin in the ethylene polymer can be 4.0 to 20% by mass.
• the copolymer of ethylene and ⁇ -olefin examples include ethylene-1-butene copolymer, ethylene-1-hexene copolymer, ethylene-1-octene copolymer, and ethylene-1-decene copolymer.
• Ethylene- (3-methyl-1-butene) copolymers which may be one type alone or a mixture of two or more types.
• the ethylene-based polymer may be a mixture of an ethylene homopolymer and a copolymer of ethylene and ⁇ -olefin.
• the melt flow rate of the ethylene polymer measured at a measurement temperature of 190 ° C. and a load of 2.16 kg can be 0.5 to 50 g / 10 minutes, and may be 1 to 30 g / 10 minutes. It is preferably 1 to 20 g / 10 minutes, and more preferably 1 to 20 g / 10 minutes.
• the ethylene polymer can be produced by a known polymerization method using a known polymerization catalyst.
• Examples of the polymerization catalyst include a homogeneous catalyst system represented by a metallocene catalyst, a Ziegler-type catalyst system, and a Ziegler-Natta-type catalyst system.
• Examples of the homogeneous catalytic system include a catalytic system composed of a transition metal compound of Group 4 of the periodic table having a cyclopentadienyl ring and an alkylaluminoxane, or a transition metal compound of Group 4 of the periodic table having a cyclopentadienyl ring.
• a transition metal compound of Group 4 of the periodic table which has a cyclopentadienyl ring in inorganic particles such as a catalytic system consisting of a compound forming an ionic complex and an organic aluminum compound, silica, and clay mineral, which reacts with the compound, and is ionic.
• a catalytic system consisting of a compound forming an ionic complex and an organic aluminum compound, silica, and clay mineral, which reacts with the compound, and is ionic.
• Examples thereof include a catalyst system obtained by supporting and modifying a catalyst component such as a compound forming the above-mentioned complex and an organic aluminum compound, and prepared by prepolymerizing ethylene or ⁇ -olefin in the presence of the above-mentioned catalyst system.
• Prepolymeration catalyst system can be mentioned.
• the high pressure method low density polyethylene can be produced by using a radical initiator as a polymerization catalyst.
• the polypropylene-based resin contains a propylene-based polymer.
• propylene-based polymers are propylene homopolymers, ethylene and / or copolymers of ⁇ -olefins having 4 to 10 carbon atoms and propylene.
• the melt flow rate measured under a measurement temperature of 230 ° C. and a load of 2.16 kg of the propylene homopolymer can be 0.1 to 50 g / 10 minutes.
• melt flow rate (MFR) measured at a measurement temperature of 230 ° C. and a 2.16 kg load of a polymer of ethylene and / or an ⁇ -olefin having 4 to 10 carbon atoms and propylene is 10 to 200 g / 10 minutes. Can be.
• the unit can be 0.1-40% by weight and the structural unit derived from propylene can be 99.9-60% by weight.
• structural unit in terms such as “structural unit derived from ethylene” means a polymerization unit of a monomer. Therefore, for example, “structural unit derived from ethylene” means a structural unit of -CH 2 CH 2- .
• Examples of the ⁇ -olefin having 4 to 10 carbon atoms include 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene, 1-octene, 1-decene and the like, preferably 1 -Butene, 1-hexene or 1-octene.
• the copolymer of ethylene and / or ⁇ -olefin having 4 to 10 carbon atoms and propylene are a random copolymer of propylene and ethylene, and a random polymer of propylene and ⁇ -olefin having 4 to 10 carbon atoms.
• examples thereof include copolymers, random copolymers of propylene and ethylene and ⁇ -olefins having 4 to 10 carbon atoms, propylene block copolymers, etc., which may be used alone or in combination of two or more. It may be a mixture.
• the propylene-based polymer may be a mixture of a propylene homopolymer, ethylene and / or an ⁇ -olefin having 4 to 10 carbon atoms, and a copolymer of propylene.
• Examples of the random copolymer of propylene and ⁇ -olefin having 4 to 10 carbon atoms include propylene-1-butene random copolymer, propylene-1-hexene random copolymer, propylene-1-octene random, and propylene.
• -1-Desen random copolymer and the like can be mentioned.
• Examples of the random copolymer of propylene, ethylene and ⁇ -olefin having 4 to 10 carbon atoms include a propylene-ethylene-1-butene copolymer, a propylene-ethylene-1-hexene copolymer, and a propylene-ethylene-. Examples thereof include 1-octene and propylene-ethylene-1-decene copolymers.
• the propylene-based polymer can be produced by a known polymerization method using a known olefin polymerization catalyst.
• Examples of the polymerization catalyst include a Cheegler-type catalyst system, a Cheegler-Natta-type catalyst system, a catalyst system composed of a transition metal compound of Group 4 of the periodic table having a cyclopentadienyl ring and an alkylaluminoxane, or a cyclopentadienyl ring.
• Periodic table of the catalyst system consisting of a transition metal compound of Group 4 and a compound that reacts with it to form an ionic complex and an organic aluminum compound, and a periodic table of inorganic particles such as silica and clay minerals having a cyclopentadienyl ring.
• Examples thereof include a catalyst system in which a catalyst component such as a Group 4 transition metal compound, a compound forming an ionic complex, and an organic aluminum compound is supported and modified, and in the presence of the above-mentioned catalyst system, ethylene or ⁇ -A prepolymerization catalyst prepared by prepolymerizing an olefin may be used.
• a catalyst component such as a Group 4 transition metal compound, a compound forming an ionic complex, and an organic aluminum compound is supported and modified
• ethylene or ⁇ -A prepolymerization catalyst prepared by prepolymerizing an olefin may be used.
• the content of the polyolefin-based resin contained in the resin pellet according to the present embodiment is preferably 98 to 99.9% by mass, with the entire resin pellet as 100% by mass, from the viewpoint of molding the pellet for various purposes. , 99.0 to 99.9% by mass, preferably.
• the resin pellet according to the present embodiment further contains an erucic acid amide and a fatty acid amide having 20 or less carbon atoms. These erucic acid amides and fatty acid amides having 20 or less carbon atoms can be added as lubricants in the production of resin pellets, and the resin pellets contain erucic acid amides and fatty acid amides having 20 or less carbon atoms from the resin pellets. The slipperiness of the produced film becomes excellent.
• the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms in the polyolefin resin pellet is preferably 200 to 10000 mass ppm, with the amount of the polyolefin resin contained in the resin pellet being 100% by mass. It is preferably about 4000 mass ppm, and more preferably 500 to 2300 mass ppm.
• the slipperiness of the film produced from the resin pellets is further improved.
• the content of the erucic acid amide in the polyolefin-based resin pellet is preferably 200 to 10000% by mass, preferably 400 to 4000% by mass, with the amount of the polyolefin-based resin contained in the resin pellet being 100% by mass. It is preferably 500 to 2300 mass ppm, and more preferably 500 to 2300 mass ppm. When the content of the erucic acid amide is in the above range, the slipperiness of the film produced from the resin pellets is further improved.
• the content of the fatty acid amide having 20 or less carbon atoms is 1 to 6% by mass, with the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms as 100% by mass. ..
• the content of the fatty acid amide having 20 or less carbon atoms is in the above range, the generation of fine powder from the resin pellets is reduced.
• the lower limit of the content of the fatty acid amide having 20 or less carbon atoms is 100% by mass of the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms. It is preferably 1.1% by mass or more, more preferably 1.2% by mass or more, and further preferably 1.3% by mass or more. From the viewpoint of reducing the generation of fine powder from the resin pellets, the upper limit of the content of the fatty acid amide having 20 or less carbon atoms is 100% by mass of the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms.
• the content of the fatty acid amide having 20 or less carbon atoms is 1 to 6% by mass, and 1.2 to 5% by mass, with the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms as 100% by mass. %, More preferably 1.5 to 4% by mass.
• the fatty acid amide having 20 or less carbon atoms may have 20 or less carbon atoms constituting the fatty acid, but more preferably 8 or more carbon atoms constituting the fatty acid, and more preferably 10 or more carbon atoms. preferable.
• the fatty acid amide having 20 or less carbon atoms may be one type of fatty acid amide or a plurality of types of fatty acid amides, but a plurality of types of fatty acid amides are preferable.
• the fatty acid amide having 20 or less carbon atoms may be an unsaturated fatty acid amide or a saturated fatty acid amide. It is preferable that the fatty acid amide having 20 or less carbon atoms contains both an unsaturated fatty acid amide and a saturated fatty acid amide from the viewpoint of suppressing the generation of fine powder of the resin pellets.
• both the unsaturated fatty acid amide and the saturated fatty acid amide are contained as the fatty acid amide having 20 or less carbon atoms, it is preferable to adjust the content ratio of the unsaturated fatty acid amide and the saturated fatty acid amide.
• the content of the unsaturated fatty acid amide in the fatty acid amide having 20 or less carbon atoms is preferably 2 to 6 with respect to the content of the saturated fatty acid amide.
• the content of the unsaturated fatty acid amide with respect to the content of the saturated fatty acid amide is more preferably 2 to 5, still more preferably 2 to 4.
• the content of unsaturated fatty acid amides relative to the content of saturated fatty acid amides can be 3-6.
• the content of the unsaturated fatty acid amide having 20 or less carbon atoms is preferably 1.0 to 6.0% by mass, with the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms as 100% by mass. , 1.0 to 4.0% by mass, more preferably 1.0 to 2.0% by mass.
• the content of the saturated fatty acid amide having 20 or less carbon atoms is preferably 0.3 to 1.0% by mass, with the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms as 100% by mass. It is more preferably 3 to 0.8% by mass, and even more preferably 0.3 to 0.5% by mass. By containing the saturated fatty acid amide having 20 or less carbon atoms in the above range, it is possible to further suppress the generation of fine powder of the resin pellets.
• unsaturated fatty acid amides having 20 or less carbon atoms examples include palmitoleic acid amides, sapienic acid amides, oleic acid amides, linoleic acid amides, gadrain acid amides, and eikosazienoic acid amides.
• the unsaturated fatty acid amide preferably contains a mono-unsaturated fatty acid amide having one double bond, and preferably contains one or more selected from oleic acid amide and gadrain acid amide.
• saturated fatty acid amides having 20 or less carbon atoms examples include caprylic acid amides, pelargonic acid amides, decanoic acid amides, palmitic acid amides, stearic acid amides, and arachidic acid amides. Among these, it is preferable to contain at least one selected from decanoic acid amide, palmitic acid amide, stearic acid amide, and arachidic acid amide.
• oleic acid amide When oleic acid amide is contained as an unsaturated fatty acid amide having 20 or less carbon atoms, the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms is 100% by mass, and the content of the oleic acid amide is 0.05 to 0. It is preferably .45% by mass, more preferably 0.2 to 0.4% by mass.
• gadrain acid amide When gadrain acid amide is contained as an unsaturated fatty acid amide having 20 or less carbon atoms, the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms is 100% by mass, and the content of gadrain acid amide is 0.5 to 5. It is preferably 0.0% by mass, more preferably 0.5 to 3.0% by mass, and even more preferably 0.5 to 1.5% by mass.
• the content of the gadrain acid amide can be 0.8 to 2.0% by mass, where the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms is 100% by mass.
• palmitic acid amide When palmitic acid amide is contained as a saturated fatty acid amide having 20 or less carbon atoms, the total amount of erucic acid amide and fatty acid amide having 20 or less carbon atoms is 100% by mass, and the content of palmitic acid amide is 0 to 0.15 mass. %, More preferably 0 to 0.1% by mass.
• the content of the palmitic acid amide can be 0.01 to 0.1% by mass, where the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms is 100% by mass.
• the content of palmitic acid amide can be 0.1% by mass or less, where the total amount of erucic acid amide and fatty acid amide having 20 or less carbon atoms is 100% by mass.
• the pellet may not contain palmitic acid amide.
• the total amount of erucic acid amide and fatty acid amide having 20 or less carbon atoms is 100% by mass, and the content of stearic acid amide is 0 to 0.20 mass. %, More preferably 0 to 0.15% by mass, and even more preferably 0 to 0.10% by mass.
• the content of the stearic acid amide can be 0.01 to 0.10% by mass, where the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms is 100% by mass.
• the content of the stearic acid amide can be 0.1% by mass or less, where the total amount of the erucic acid amide and the fatty acid amide having 20 or less carbon atoms is 100% by mass.
• arachidic acid amide When arachidic acid amide is contained as an unsaturated fatty acid amide having 20 or less carbon atoms, the total amount of erucic acid amide and fatty acid amide having 20 or less carbon atoms is 100% by mass, and the content of arachidic acid amide is 0.2 to 0. It is preferably 6.6% by mass, more preferably 0.2 to 0.5% by mass, and even more preferably 0.3 to 0.4% by mass.
• the polyolefin-based resin pellet according to the present embodiment may further contain a fatty acid amide having 22 or more carbon atoms other than the erucic acid amide, in addition to the erucic acid amide and the fatty acid amide having 20 or less carbon atoms.
• a fatty acid amide having 22 or more carbon atoms other than erucic acid amide By containing a fatty acid amide having 22 or more carbon atoms other than erucic acid amide, the slipperiness of the obtained film can be improved.
• the fatty acid amide having 22 or more carbon atoms preferably has 22 to 24 carbon atoms.
• the fatty acid amide having 22 or more carbon atoms other than the erucic acid amide may be one kind, a plurality of kinds, an unsaturated fatty acid amide, or a saturated fatty acid amide.
• the fatty acid amide having 22 or more carbon atoms other than erucic acid is preferably one or more selected from the group consisting of behenic acid amide, seracoleic acid amide and lignoceric acid amide.
• the polyolefin-based resin pellet according to the present embodiment may further contain an additive in addition to the above-mentioned polyolefin-based resin and fatty acid amide.
• additives include antioxidants, surfactants, weathering agents, antiblocking agents, antistatic agents, antifog agents, drip-free agents, pigments, fillers and the like.
• a lubricant other than the above-mentioned fatty acid amide may be contained.
• the content of the additive in the polyolefin-based resin pellet is preferably 1% by mass or less in total, with the amount of the polyolefin-based resin contained in the resin pellet being 100% by mass.
• the shape of the resin pellet according to the present embodiment is not particularly limited, but may be angular, spherical, columnar, elliptical, or polygonal, and the spherical shape suppresses the occurrence of scraping of the resin pellet. It is preferable because the generation of fine powder is reduced.
• the term "spherical” includes not only a perfect spherical shape but also a substantially spherical shape, a substantially elliptical sphere shape, and a substantially rice grain.
• the size of the resin pellets is not particularly limited, but it is preferable that the average minor axis of the resin pellets is 1 to 7 mm from the viewpoint of suppressing the occurrence of scraping of the resin pellets and the moldability of the resin pellets.
• the short diameter means the shortest diameter of the pellet.
• the average minor axis of the resin pellets is more preferably 1 to 5 mm, still more preferably 1.5 to 3.5 mm. Further, it is preferable that the average major axis of the resin pellets is 3 to 10 mm from the same viewpoint.
• the major axis means the longest diameter of the pellet.
• the average major axis of the resin pellets is more preferably 3 to 8 mm, further preferably 4 to 6 mm.
• the average weight of the resin pellets is preferably 30 to 100 mg, more preferably 30 to 80 mg, and even more preferably 40 to 60 mg.
• the average volume of the resin pellets is preferably 30 to 100 mm 3 , more preferably 30 to 80 mm 3 , and even more preferably 40 to 60 mm 3 .
• the average surface area of the resin pellets is preferably 40 to 200 mm 2 , more preferably 40 to 150 mm 2 , and even more preferably 60 to 100 mm 2 .
• the resin pellets according to the present embodiment generate less fine powder and facilitate subsequent molding processability.
• the resin pellet according to the present embodiment has a desired shape by a known molding method such as extrusion molding, injection molding, blow molding, compression molding, stretching, vacuum molding, etc., after mixing other arbitrary components as necessary. It is possible to mold into a molded product of.
• the molded product is not particularly limited, and examples thereof include films, sheets, laminated films, laminated sheets, laminated products, tubes, hoses, pipes, hollow containers, bottles, fibers, and parts having various shapes.
• the above-mentioned resin pellets can be produced by a method including, for example, a step of mixing a polyolefin resin and a lubricant to obtain a mixture, and a step of melt-extruding the obtained mixture to obtain resin pellets.
• the above-mentioned polyolefin-based resin can be used, and the lubricant mixed with the polyolefin-based resin contains the above-mentioned erucic acid amide and the fatty acid amide having 20 or less carbon atoms, and the erucic acid amide and the carbon number of carbons.
• a lubricant having a total amount of 20 or less fatty acid amides of 100% by mass and 1 to 6% by mass can be used.
• the step of mixing the polyolefin resin and the lubricant to obtain a mixture for example, a certain amount of the polyolefin resin and the lubricant are supplied to the extruder by a feeder or the like and mixed in the extruder to obtain the polyolefin resin and the lubricant. A mixture with is obtained.
• the extruder for example, a single-screw extruder, a twin-screw extruder, or the like can be used.
• the mixture of the polyolefin resin and the lubricant can be melt-kneaded if necessary.
• the temperature of the melt-kneading is preferably 140 to 300 ° C, more preferably 140 to 220 ° C.
• the other components may be supplied to the extruder to be mixed together with the polyolefin resin and lubricant to form a mixture. good.
• the obtained mixture is melt-extruded in a strand shape from the through hole of the die plate.
• Examples of the shape of the through hole of the die plate include a circle, an ellipse, a polygon, a star, a semicircle, a semi-oval, and a rectangle with rounded corners.
• the shape of the die hole is preferably circular or elliptical.
• Extrusion conditions such as extrusion speed, extrusion amount, and extrusion pressure of the mixture can be set as appropriate.
• the extruded strand-like mixture can be cooled and solidified.
• a refrigerant such as water can be used for cooling. Cooling conditions such as the temperature of the refrigerant and the flow rate of the refrigerant can be appropriately set, and the degree of cooling may be such that the extruded mixture is solidified to the extent that it can be cut.
• Pellets can be obtained by cutting the solidified strand-like mixture while cooling and solidifying the mixture in parallel with extrusion.
• a cutter such as a rotary cutter can be used.
• the resin pellets obtained by cutting can be transferred to post-processes such as drying treatment, removal of foreign substances, and packing, if necessary.
• the resin pellets can be transferred to a subsequent process through an air delivery line.
• the resin pellets In the air feeding line, from the viewpoint of suppressing the generation of fine powder, it is preferable to transfer the resin pellets at a rate of 8 to 20 tons / hour, and it is more preferable to transfer the resin pellets at a rate of 8 to 12 tons / hour.
• the air feeding line may be provided with a wind power separating device for separating the resin pellets and the fine powders to separate and remove the fine powders generated from the resin pellets.
• the resin pellet according to the present embodiment can also be produced by a method other than the above-mentioned embodiment.
• Example 1> Manufacturing of resin pellets
• Ethylene-1-butene-1-hexene copolymer manufactured by Sumitomo Chemical Co., Ltd., Sumikasen EP, melt flow rate: 1.0 g / 10 minutes, density: 919 kg / m 3 ) 80% by mass, high-pressure method low-density polyethylene ( Sumikasen, manufactured by Sumitomo Chemical Co., Ltd., melt flow rate: 4.0 g / 10 minutes, density: 923 kg / m 3 ) 20% by mass, 600% by mass of lubricant A having the composition shown in Table 1-1, antioxidant (Sumitomo) A 750 mass ppm of a simulator GP manufactured by Chemical Co., Ltd.
• Fine powder ratio fine powder mass / pellet mass
• Example 2 As shown in Table 2, in the resin pellets of Examples 1 to 4, 5 and 6, the amount of fine powder generated from the resin pellets was small. On the other hand, in Example 2 using the lubricant B having a fatty acid amide content of 20 or less carbon atoms higher than that of the lubricant D, the slipperiness of the film was superior to that of Example 4 using the lubricant D.

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• 2021
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