WO2020175138A1 - プロピレン系樹脂組成物および成形体 - Google Patents
プロピレン系樹脂組成物および成形体 Download PDFInfo
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- WO2020175138A1 WO2020175138A1 PCT/JP2020/005312 JP2020005312W WO2020175138A1 WO 2020175138 A1 WO2020175138 A1 WO 2020175138A1 JP 2020005312 W JP2020005312 W JP 2020005312W WO 2020175138 A1 WO2020175138 A1 WO 2020175138A1
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- propylene
- mass
- ethylene
- resin composition
- polymerization
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- 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
- C08L23/10—Homopolymers or copolymers of propene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
- B29C49/06—Injection blow-moulding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D1/00—Containers having bodies formed in one piece, e.g. by casting metallic material, by moulding plastics, by blowing vitreous material, by throwing ceramic material, by moulding pulped fibrous material, by deep-drawing operations performed on sheet material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D85/00—Containers, packaging elements or packages, specially adapted for particular articles or materials
- B65D85/50—Containers, packaging elements or packages, specially adapted for particular articles or materials for living organisms, articles or materials sensitive to changes of environment or atmospheric conditions, e.g. land animals, birds, fish, water plants, non-aquatic plants, flower bulbs, cut flowers or foliage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D85/00—Containers, packaging elements or packages, specially adapted for particular articles or materials
- B65D85/50—Containers, packaging elements or packages, specially adapted for particular articles or materials for living organisms, articles or materials sensitive to changes of environment or atmospheric conditions, e.g. land animals, birds, fish, water plants, non-aquatic plants, flower bulbs, cut flowers or foliage
- B65D85/52—Containers, packaging elements or packages, specially adapted for particular articles or materials for living organisms, articles or materials sensitive to changes of environment or atmospheric conditions, e.g. land animals, birds, fish, water plants, non-aquatic plants, flower bulbs, cut flowers or foliage for living plants; for growing bulbs
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/04—Monomers containing three or four carbon atoms
- C08F210/06—Propene
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
- B29C2049/023—Combined blow-moulding and manufacture of the preform or the parison using inherent heat of the preform, i.e. 1 step blow moulding
Definitions
- the present invention relates to a propylene resin composition, and a molded article represented by a container, which is formed from the composition.
- a propylene-based resin composition excellent in heat resistance, rigidity, and transparency may be used as a raw material for a packaging container for food such as jelly, pudding, and coffee.
- a propylene-based resin composition excellent in heat resistance, rigidity, and transparency may be used as a raw material for a packaging container for food such as jelly, pudding, and coffee.
- a propylene-based resin composition excellent in heat resistance, rigidity, and transparency may be used.
- Many since food is often handled in a cold environment during its storage and distribution, food packaging containers are not only impact resistant at room temperature, but also impact resistance at low temperature, that is, low temperature resistance. Impact resistance is required.
- a propylene-based resin composition having excellent impact resistance a composition containing a propylene-ethylene block copolymer, a nucleating agent, and a low-density polyethylene resin or a linear low-density polyethylene resin is known (for example, as a propylene-based resin composition having excellent low temperature impact resistance in Patent Document 1), a composition comprising a propylene block copolymer and an ethylene-based resin and having specific physical properties is known (for example, Patent Documents 2 and 3).
- Patent Document 4 discloses a polypropylene resin composition containing a crystalline propylene-ethylene block copolymer having a specific resin structure, a crystalline polypropylene resin, a high-density polyethylene, and optionally an elastomer. It is disclosed that a composition and a film having an excellent balance of whitening resistance, rigidity and impact resistance at low temperature can be obtained from this composition, and this composition is useful for applications such as food containers. Is described.
- Patent Document 5 discloses a propylene-based resin composition containing a specific propylene-based random block copolymer, and an injection-molded article excellent in impact resistance and the like can be obtained from this composition. Described that this can be used for food containers, etc. ⁇ 2020/175 138 2 ⁇ (: 170? 2020 /005312
- a polyethylene resin may be added to this composition for imparting functions such as impact resistance.
- Patent Document 6 a specific propylene block copolymer, a specific ethylene-olefin copolymer produced using a single-site catalyst, and a nucleating agent are specified.
- a molded product such as a food packaging container is manufactured, a propylene-based product that is excellent in rigidity, low temperature impact resistance and transparency even if it is thinner and lighter than before. Resin compositions have been proposed.
- Patent Document 1 Japanese Unexamined Patent Publication No. 20 01 _ 2 6 6 86
- Patent Document 2 JP 2 0 0 2-1 8 7 9 9 6 Publication
- Patent Document 3 JP 2 0 0 2-1 8 7 9 9 7 Publication
- Patent Document 4 JP 20000 5 _ 2 6 9 8 1 Publication
- Patent Document 5 International Publication No. 2 0 0 7/1 1 6 7 09
- Patent Document 6 International Publication No. 2 0 1 0/0 7 4 0 0 1 Summary of Invention
- the present invention provides a propylene-based resin composition capable of producing a molded product which is excellent in high-speed moldability even in the production of a thin-walled molded product and has excellent balance of rigidity and low-temperature impact resistance.
- the purpose is to
- the gist of the present invention is as follows.
- nucleating agent ⁇ 3
- n_decane The proportion of the constituent units derived from ethylene in the portion insoluble in the room temperature n_decane is 0 to 1.0% by mass.
- n_decane The proportion of the constituent units derived from ethylene in the portion soluble in room temperature n_decane is 25 to 35% by mass.
- n_ decane-soluble portion has an intrinsic viscosity [] in decalin of 130°C of 1.0 to 3.0 /9.
- the molded body of [2] above which is a body.
- a method for producing a molded article comprising the step of injection molding or injection stretch blow molding of the propylene resin composition according to the above [1].
- the propylene-based resin composition of the present invention it is possible to obtain a molded product having excellent balance in rigidity and low-temperature impact resistance with excellent high-speed moldability even when manufacturing a thin-walled molded product. it can.
- the molded product of the present invention is excellent in rigidity and low temperature impact resistance in a well-balanced manner.
- the propylene-based resin composition of the present invention satisfies 75 to 92 parts by mass of a propylene-based polymer (eighth) that satisfies the requirements (1) to (5) described later, and satisfies the following requirements (1) to (2). 8 to 25 parts by mass of ethylene-based polymer (Mitsumi) (however, the total of propylene-based polymer (8) and ethylene-based polymer (Mitsumi) is 100 parts by mass), and nucleating agent ( ⁇ ⁇ It is characterized by containing 0.02 to 1.0 parts by mass.
- the propylene-based resin composition of the present invention contains a propylene-based polymer that satisfies the requirements (81) to (85) described below. Below, "Requirements (8 1) ⁇ (8 5) ⁇ 2020/175 138 5 (: 170? 2020 /005312
- propylene-based polymer () that satisfies the formula is also simply referred to as "propylene-based polymer (8)".
- the propylene-based polymer (8) is preferably a propylene-based copolymer (so-called, containing a component mainly composed of propylene-derived structural units and a component mainly composed of propylene- and ethylene-derived structural units). Block copolymer).
- Requirement (8 1) is based on propylene polymer (8), 8 3 1//1 0-1 2 3 8 in accordance with measurement temperature 23 0 ° ⁇ , load 2.1 6 Melt flow is measured in 9 - Rate ( "! IV”.
- the following also referred to as) of Ru Oh 4 5-1 9 5 9/1 0 minutes, is that.
- the requirement (82) is that the propylene-based polymer (8) can be used at 80 to 92% by mass at room temperature n _ decane (hereinafter also referred to as " ⁇ .") and at room temperature n _ decane. It contains 8 to 20 mass% of a soluble portion (hereinafter also referred to as "mouth ⁇ "). However, the mouth The proportion of And the total of 100% and 100% by mass. Preferably the mouth. Is 82 to 88 mass% and the mouth is 12 to 18 mass%. In addition, the room temperature is specifically 25 ° ⁇ .
- the part insoluble in n _ decane ( ⁇ . [ ) is a component mainly composed of a structural unit mainly derived from propylene, and has crystallinity and high rigidity. It is considered to indicate.
- the part soluble in decane (0 ⁇ ) is usually a component mainly composed of propylene and ethylene. ⁇ It is considered that the 301 component does not show crystallinity or has low crystallinity, has a low glass transition temperature, exhibits impact resistance, and exhibits compatibility with ethylene polymer (Mitsumi). This is sometimes called a rubber component.
- the body (8) is usually a propylene-based copolymer (so-called block copolymer) having a portion insoluble in n-decane (0 _ [ ) and a portion soluble in n-decane (mouth 3 ).
- the mouth Is below the above range
- the ratio exceeds the above range
- the high-speed moldability of the propylene-based resin composition may be poor
- the rigidity (buckling strength) of the molded product obtained from the propylene-based resin composition may be poor.
- the ratio is measured by the method used in Examples described later.
- Requirement (8 3) is The proportion of ethylene-derived constitutional units is 0 to 1.0 mass%. This ratio is preferably 0- ⁇ .
- the amount of ⁇ shall be 100% by mass.
- the content of the constituent unit is 0% by mass means that the mouth is Does not contain a constitutional unit derived from ethylene, or the proportion of the constitutional unit is below the detection limit.
- the ratio of the structural units exceeds the above range, the high-speed moldability of the propylene-based resin composition may be poor, and the rigidity (buckling) of a molded product obtained from the propylene-based resin composition may be deteriorated. Strength) may be inferior.
- the ratio of the above-mentioned constitutional unit is the one measured by the method adopted in Examples described later.
- Requirement (84) is that the ratio of the structural units derived from ethylene in the above is 25 to 35 mass %. The amount of the mouth is 100% by mass. ⁇ 2020/175 138 7 ⁇ (: 170? 2020 /005312
- This proportion is preferably 27 to 35% by mass, more preferably 28 to 34% by mass.
- the molded article obtained from the propylene-based resin composition tends to have poor impact resistance. It is considered that the glass transition temperature is lowered due to the reduction of the ethylene content, the crystallinity is increased, and the absorption energy against impact is reduced.
- the ratio of the above-mentioned constitutional unit is the one measured by the method adopted in Examples described later.
- Requirement (85) is that the mouth has an intrinsic viscosity in decalin of 13.5°C (hereinafter also referred to as "intrinsic viscosity [ ⁇ ") of 1.0 to 3.0 ⁇ / 9 . It is a thing.
- the intrinsic viscosity [7? ⁇ ] is preferably 1.4 to 2.8 ⁇ /9.
- Intrinsic viscosity [7 ⁇ . When the value exceeds or is less than the above range, the impact resistance of the molded product obtained from the propylene resin composition may decrease.
- the value of the intrinsic viscosity [7] ⁇ ] is the value measured by the method adopted in Examples described later.
- the propylene-based polymer (8) is not particularly limited in its production method, but usually, propylene and ethylene are copolymerized in the presence of a metallocene compound-containing catalyst or in the presence of a Ziegler-Natta catalyst. Obtained by.
- the propylene polymer (8) is preferably obtained by copolymerizing propylene and ethylene in the presence of a Ziegler-Natta catalyst. This is because it is easy to obtain a resin having a wide molecular weight distribution and good moldability.
- metallocene compound-containing catalyst examples include metallocene compounds, organic metal compounds, organoaluminum oxy compounds and metallocene compounds. ⁇ 2020/175 138 8 ⁇ (: 170? 2020 /005312
- a metallocene catalyst composed of at least one compound selected from compounds capable of forming an ion pair in response to the reaction, and optionally a particulate carrier may be mentioned, and is preferably isotactic or syndiotactic. Mention may be made of metallocene catalysts capable of stereoregular polymerization of structure and the like.
- the metallocene compounds the crosslinkable metallocene compounds exemplified in WO 01/27 1 24, and the metallocene compounds described in [0068] to [0076] of WO201/74001 are exemplified. Preferred.
- WO 01/27 1 24 As a compound that reacts with an organometallic compound, an organoaluminumoxy compound, and a transition metal compound to form an ion pair, and as a particulate carrier that is used as necessary, WO 01/27 1 24
- the compounds disclosed in Japanese Patent Application Laid-Open No. 11_31515109 and the like can be used without limitation.
- the propylene polymer (8) can be produced by using a highly stereoregular Ziegler-Natta catalyst.
- a highly stereoregular Ziegler-Natta catalyst various known catalysts can be used.
- a catalyst composed of an organosilicon compound catalyst component having at least one group selected from the group consisting of these derivatives and the catalyst component can be used by a known method, for example, International Publication No. 201/74001. It can be produced by the method described in [0078] to [0094] of No.
- ⁇ -olefin having 2 to 8 carbon atoms can be used.
- linear olefins such as ethylene, propylene, 1-butene, 1-year-old cutene; 3-methyl-1-butene, 3-methyl-1-pentene, 3-ethyl-1-pentene, 4-methyl-1- —Pentene, 4-methyl-1-hexene, 4,4-dimethyl-1-hexene, 4,4-dimethyl 1-pentene, 4-ethyl-1-hexene, 3-ethyl-1-olefin such as olefin having a branched structure Can be used. These may be co-polymerized.
- the prepolymerization is carried out so that a polymer of about 0.1 to 100, preferably about 0.3 to 500, is produced per 19 of the solid titanium catalyst component (3). Is desirable. If the prepolymerization amount is too large, the efficiency of (co)polymer formation in the main polymerization may decrease. In the prepolymerization, the catalyst can be used at a concentration much higher than the catalyst concentration in the system in the main polymerization.
- the solid titanium catalyst component (3) (or the prepolymerization catalyst) was converted into titanium atoms per 1! More preferably, it is desirable to use it in an amount of about 0.001 to 10 mmol.
- the organic metal compound catalyst component (well) is converted to the amount of metal atoms in an amount of about 1 to 200 mol, preferably about 2 to 500 mol, per mol of titanium atom in the polymerization system. It is desirable to use it in a moderate amount.
- the amount of the organosilicon compound catalyst component ( ⁇ ) is about 0.01 to 50 mol, preferably about 0.01 to 20 mol, per mol of the metal atom of the organometallic compound catalyst component (well). It is desirable to use.
- the propylene polymer () can be obtained by co-polymerizing propylene and ethylene in the presence of the above metallocene compound-containing catalyst or in the presence of the Ziegler-Natta catalyst.
- propylene-based polymer () When the propylene-based polymer () is produced by continuous multi-stage polymerization, propylene is homopolymerized or propylene and ethylene are copolymerized in each stage. ⁇ 2020/175 138 10 ⁇ (: 170? 2020 /005312
- the polymerization may be carried out by any one of liquid phase polymerization methods such as gas phase polymerization method, solution polymerization method and suspension polymerization method, and each step may be carried out by a different method. Further, either continuous type or semi-continuous type may be used, and each stage may be divided into a plurality of polymerization vessels, for example, 2 to 10 polymerization vessels. From the industrial point of view, it is most preferable to carry out the polymerization by a continuous method, and in this case, it is preferable to divide the second and subsequent polymerizations into two or more polymerization vessels, which suppresses the generation of gel. it can.
- the polymerization medium inert hydrocarbons may be used, or liquid propylene may be used as the polymerization medium.
- the polymerization conditions in each stage are such that the polymerization temperature is in the range of about 150 to +200°C, preferably about 20 to 100°C, and the polymerization pressure is from normal pressure to
- the propylene-based polymer (8) is, for example, a reactor in which two or more polymerization vessels are connected in series, and the following two steps ([Step 1] and [Step 2]) are continuously performed. It is obtained by carrying out.
- a polymerization apparatus in which two or more reactors are connected in series may be used, and [Step 1] may be carried out in each polymerization apparatus, or two or more reactors may be used.
- [Step 2] may be carried out in each of the polymerization devices using the polymerization devices in which are connected in series.
- [Step 1] and [Step 2] are performed separately, and the polymer obtained in each is melt-kneaded using a single-screw extruder, a multi-screw extruder, a feeder, a Banbury mixer, etc.
- the polymer (8) may be produced.
- Step 1 the polymerization temperature ⁇ _ ⁇ 1 hundred ° ⁇ , a polymerization pressure of normal pressure ⁇ 5 IV! 3 gauge pressure, a step of polymerizing the ethylene propylene and optionally or not feeding ethylene, or It is the process of producing a propylene-based polymer, which is the main component of the mouth, by supplying a smaller amount of ethylene than the propylene feed amount.
- a chain transfer agent typified by hydrogen gas may be introduced to adjust the intrinsic viscosity [7?] of the polymer produced in [Step 1]. ⁇ 2020/175 138 1 1 ⁇ (: 170? 2020 /005312
- Step 2 is a step of copolymerizing propylene and ethylene at a polymerization temperature of 0 to 100° and a polymerization pressure of normal pressure to 5 IV! 3 gauge pressure.
- the propylene-ethylene copolymer rubber which is the main component of the mouth, is manufactured by increasing the ratio of ethylene feed amount to that of [Step 1].
- a chain transfer agent typified by hydrogen gas may be introduced to adjust the intrinsic viscosity [7] of the polymer produced in [Step 2].
- the propylene-based polymer (8) is obtained by continuously performing the above-mentioned [Step 1] and [Step 2], and the requirements (81) to (85) are adjusted as follows. can do.
- 1 ⁇ /1 [ ⁇ in the requirement (81) is a monomer (that is, propylene in the case of homopolymerization of propylene, propylene and ethylene in the case of copolymerization) when performing [Step 1] or [Step 2]. It can be adjusted by adjusting the ratio of the feed amount of hydrogen gas as a chain transfer agent to the feed amount of ). That is, by increasing this ratio IV! Can be increased, and by decreasing this ratio IV! Can be lowered.
- IV! can be obtained by melt-kneading the propylene-based polymer obtained by polymerization in the presence of an organic peroxide. Can be adjusted.
- the propylene-based polymer obtained by polymerization is melt-kneaded in the presence of an organic peroxide, IV! IV! becomes higher by increasing the amount of organic peroxide added when performing the melt-kneading process in the presence of organic peroxide.
- the amount of the organic peroxide is 0.01% by weight relative to 100 parts by weight of the propylene-based polymer.
- the melt-kneading treatment in the presence of the organic peroxide may be carried out after the following post-treatment step.
- the organic peroxide is not particularly limited, and conventionally known organic peroxides such as 2,5-dimethyl-2,5-di(benzoylperoxy)hexane, and 1,
- the above mouth in the requirement (2) The above ratio and the above ratio can be adjusted by adjusting the polymerization time in the above [Step 1] and [Step 2]. In other words, by increasing the ratio of the polymerization time of [Step 1] to the total polymerization time, the ratio of mouth is increased, Can be reduced. Also
- the above in the requirement (83) The ratio of the ethylene-derived structural unit to the total amount can be adjusted by adjusting the ratio of the ethylene feed amount to the propylene feed amount when performing [Step 1]. That is, by increasing the ratio of the feed amount, the ratio of the structural unit can be increased, and by decreasing the ratio of the feed amount, the ratio of the structural unit can be decreased.
- the above in requirement (eighth four)
- the ratio of the ethylene-derived structural unit to the total amount of ethylene can be adjusted by adjusting the ratio of the ethylene feed amount to the propylene feed amount when performing [Step 2]. That is, by increasing the ratio of the feed amount, the ratio of the structural unit can be increased, and by decreasing the ratio of the feed amount, the ratio of the structural unit can be decreased.
- the intrinsic viscosity [7? ⁇ ] in the requirement (85) can be adjusted by the feed amount of hydrogen gas used as a chain transfer agent when performing [Step 2].
- the intrinsic viscosity [7] ⁇ ] can be reduced by increasing the ratio of the hydrogen gas feed amount to the monomer (ie, propylene and ethylene) feed amount, and the hydrogen gas feed amount to the monomer feed amount can be reduced.
- the intrinsic viscosity [7? ⁇ ] can be increased by decreasing the ratio of.
- a propylene-based polymer () is obtained as a powder by carrying out known post-treatment steps such as a catalyst deactivation treatment step, a catalyst residue removal step, and a drying step, if necessary.
- a commercially available product may be used as the propylene polymer (8). ⁇ 2020/175 138 13 ⁇ (: 170? 2020 /005312
- the propylene-based resin composition of the present invention includes an ethylene-based polymer (Mi) that satisfies the requirements (Mis 1) to (Mis 2) described below.
- the ethylene-based polymer (Mitsumi) which satisfies the requirements (Mitsumi 1) to (Mitsumi 2) is simply referred to as “the ethylene-based polymer (Mitsumi) ".
- Examples of the ethylene-based polymer (Mitsumi) include ethylene homopolymers and ethylene
- Examples of the ⁇ -olefin include ⁇ -olefin having 3 to 20 carbon atoms, and examples thereof include propylene, 1-butene, 1-pentene, 3-methyl-1-butene, 1-hexene, 4-methyl-1-pentene. , 3-methyl-1-pentene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene, 1-eicosene and the like.
- the requirement (Min 1) is that the ethylene-based polymer (Min) is in compliance with 8 3 1 ⁇ /1 0- 1 238, measuring temperature 1 90 ° ⁇ , load 2.
- Is is 3. ⁇ _ ⁇ 50 9/1 0 minutes, is that.
- the IV! Is preferably 3. ⁇ _ ⁇ 30 9/1 0 minutes, more preferably 3. ⁇ _ ⁇ 209/1 0 minutes.
- the requirement (Mimi 2) is that the density of ethylene polymer (Mami) is That is all.
- the density is preferably 942 Ri der above, more preferably 9451 ⁇ 9/3 or more, more preferably from 955 to 9801 ⁇ 9 / Rei_1 3. ⁇ 2020/175 138 14 ⁇ (: 170? 2020 /005312
- the density of the ethylene-based polymer (Mitsumi) is less than the above range, the high-speed moldability of the propylene-based resin composition may be poor, and the molded product obtained from the propylene-based resin composition may be deteriorated.
- the rigidity (buckling strength) may be inferior.
- the density value of the ethylene-based polymer (Mitsumi) was determined by subjecting the strand obtained during IV! measurement of the ethylene-based polymer (Mitsumi) to a heat treatment at 120 ° ⁇ for 1 hour and then at room temperature for 1 hour. Measured by the density gradient tube method using a sample that has been slowly cooled to.
- the ethylene polymer (Mitsumi) can be produced by a conventionally known method.
- IV in Requirement (Minami 1)! Is a monomer (ie ethylene in the case of homopolymerization of ethylene, or ethylene in the case of copolymerization) when ethylene is polymerized (or copolymerized with ethylene and «-olefin) to produce an ethylene polymer (Mitsumi).
- the density in the requirement is defined as "- olefin feed relative to the amount of ethylene feed when ethylene is polymerized (or ethylene and ⁇ -olefin are copolymerized) to produce an ethylene polymer (Mami). It can be adjusted by adjusting the proportion of quantity. That is, by increasing this ratio, the density can be lowered, and by decreasing this ratio, the density can be increased.
- a commercially available product may be used as the ethylene polymer (Mitsumi).
- the propylene-based resin composition of the present invention contains a nucleating agent ( ⁇ ).
- the nucleating agent contained in the propylene-based resin composition of the present invention is not particularly limited, but includes sorbitol-based nucleating agent, phosphorus-based nucleating agent, carboxylic acid metal salt-based nucleating agent, polymer nucleating agent, inorganic A compound etc. are mentioned.
- the nucleating agent, sorbitol _ Le based nucleating agents, phosphorus-based nucleating agent, the polymer _ nucleating agents preferred.
- sorbitol-based nucleating agent examples include 1,2,3-trideoxy_4,6:5,7-bis- ⁇ _[(4-propylphenyl)methylene]-nonit
- phosphorus-based nucleating agent examples include sodium-bis-(4-1-butylphenyl) phosphate, potassium-bis-(4 _ 1: _ butylphenyl) phosphate, sodium-2, 2, -ethylidene-bis (4 ,
- carboxylic acid metal salt nucleating agent examples include: _ 1-butyl benzoic acid aluminum salt, hydroxydi (1-I-butyl benzoic acid) aluminum (trade name "Hashiichi Dingumihachi”), Japan Chemtech), aluminum adipate, and sodium benzoate.
- a branched ⁇ _ olefin polymer is preferably used as the polymer nucleating agent.
- branched ⁇ -olefin polymers include 3-methyl-1-butene, 3-methyl-1-pentene, 3-ethyl-1-pentene, 4-methyl-1-pentene, 4-methyl-1-hexene, 4,4. — Dimethyl-1 — hexene, 4,
- the inorganic compound include talc, mica, and calcium carbonate.
- nucleating agents may be used alone or in combination of two or more.
- the propylene-based resin composition of the present invention is excellent in rigidity of a molded article such as a container formed from the composition of the present invention by containing the nucleating agent ( ⁇ ). It is presumed that this is due to rigidity.
- the content of the nucleating agent is more than the following range, the further improving effect is small and it is not economical.
- the propylene-based resin composition of the present invention comprises the above-mentioned propylene-based polymer () 75 to 92 parts by mass, ethylene-based polymer (Mitsumi) 8 to 25 parts by mass (however, propylene-based polymer () and The total amount of the ethylene-based polymer (Mitsumi) is 100 parts by mass), and the nucleating agent ( ⁇ ) 0.02-1.0 parts by mass, and preferably a propylene-based polymer (8) 8 6 to 90 parts by mass, an ethylene polymer (Mitsumi) 10 to 14 parts by mass, and a nucleating agent ( ⁇ 0.04 to ⁇ 0.40 parts by mass are included.
- the propylene-based resin composition of the present invention contains a neutralizing agent, antioxidant, heat stabilizer, weathering agent, lubricant, and UV absorbers, antistatic agents, antiblocking agents, antifog agents, antifoam agents, dispersants, flame retardants, antibacterial agents, fluorescent brighteners, crosslinking agents, additives such as crosslinking aids; dyes, pigments, etc.
- a neutralizing agent antioxidant, heat stabilizer, weathering agent, lubricant, and UV absorbers
- other ingredients Ingredients exemplified by the colorant (hereinafter referred to as "other ingredients").
- the amount of the other components is 100 parts by mass of the total of the propylene polymer () and the ethylene polymer (M). On the other hand, it is usually 0.01 to 5 parts by mass.
- [3 ⁇ 4”) measured by the above method is preferably 50 to 1 because it has excellent fluidity during injection molding of the propylene resin composition. 4 0 9/1 0 minutes, more preferably 6 0-1 2 0 9/1 0 minutes.
- IV! of the propylene-based resin composition of the present invention is obtained by appropriately selecting the melt flow rate of the propylene-based polymer (8) or the melt flow rate of the ethylene-based polymer (M), or It can be adjusted by adjusting the blending ratio of the polymer () and the ethylene polymer (M).
- the propylene-based resin composition IV! of the present invention was prepared by dissolving each component in a kneader. ⁇ 2020/175 138 18 ⁇ (: 170? 2020 /005312
- the organic peroxide is not particularly limited, but conventionally known organic peroxides, for example, 2,5-dimethyl-2,5-di(benzoylperoxy)hexane, 1,3-bis-(1 : _Putylperoxyisopropyl) Benzene.
- the organic peroxide is 0.000 parts by weight with respect to a total of 100 parts by mass of the propylene-based polymer (8) and the ethylene ⁇ _ _ olefin copolymer (M). It is desirable to use 5 to 0.05 parts by mass.
- the propylene resin composition of the present invention is mainly Has a so-called sea-island structure in which is the continuous phase, that is, the sea, and the mouth and ethylene polymer (Mimi) are mainly the islands. Therefore, the propylene-based resin composition of the present invention can achieve both high rigidity and high low-temperature impact resistance.
- the method for producing the propylene-based resin composition of the present invention is not particularly limited.
- Examples of the production method include a method of producing a propylene-based resin composition by melt-kneading each component with a kneader.
- Examples of the kneading machine include a single-screw kneading extruder, a multi-screw kneading extruder, a kneader, a Banbury mixer, and a Henschel mixer.
- the melt-kneading conditions are not particularly limited as long as the melted resin does not deteriorate due to shearing during kneading, heating temperature, heat generated by shearing, and the like. From the viewpoint of preventing the deterioration of molten resin, it is effective to set the heating temperature appropriately and to add an antioxidant and a heat stabilizer.
- the molded article of the present invention is characterized by containing the above-mentioned propylene resin composition of the present invention. Specific examples thereof include those obtained by injection molding or injection blow molding of the propylene resin composition of the present invention.
- Examples of the molded article of the present invention include containers, home electric appliance parts, daily necessities and the like. Among them, the container is preferable from the viewpoint of impact resistance and rigidity. ⁇ 2020/175 138 19 ⁇ (: 170? 2020 /005312
- containers examples include packaging containers for liquid daily products such as hair washes, hair dressings, cosmetics, detergents and bactericides; food packaging containers for liquids such as soft drinks, water and seasonings; jelly, pudding, yogurt Food packaging containers for desserts (desert cups); packaging containers for other chemicals; packaging containers for industrial liquids.
- liquid daily products such as hair washes, hair dressings, cosmetics, detergents and bactericides
- food packaging containers for liquids such as soft drinks, water and seasonings
- packaging containers for other chemicals packaging containers for industrial liquids.
- the molded article of the present invention has excellent balance in rigidity and low temperature impact resistance
- the thickness of the body of the container is 0.3 to 2. It is preferably in the range of.
- the molded product of the present invention is excellent in low-temperature impact resistance and is excellent in moldability even if it is thin as described above.
- the method for producing a molded article of the present invention is characterized by including a step of molding the above-mentioned propylene resin composition of the present invention.
- the molding method preferably includes injection molding and injection stretch blow molding.
- an injection molding machine can be used to perform molding by the following method.
- a propylene-based resin composition is introduced into a hopper of an injection molding machine, and a resin is applied to a cylinder which is heated to about 200° to 250°°. Is sent, kneading and plasticizing into a molten state. From this, the temperature is controlled from nozzle at high pressure and high speed (maximum pressure of 50 to 2001 ⁇ 13) by cooling water or hot water to 5 to 80° ⁇ , preferably 10 to 60° ⁇ . Closed with a mold clamping mechanism ⁇ 2020/175 138 20 ⁇ (: 170? 2020 /005312
- the physical properties of the raw materials were measured by the following methods.
- N-decane was added to sample 59 of the propylene-based polymer. Add 1 4
- the solution (1) was obtained by heating and dissolving at 5°C for 30 minutes.
- the solution was left for 30 minutes to obtain a precipitate (solution (2) containing ⁇ . After that, the solution (2) was filtered with a filter cloth having a mesh size of about 15 to separate the precipitate ( ⁇ ). After the ⁇ is drying, precipitates (the mass was measured in Rei_0. the divided by precipitates (Rei_0 of mass sample weight (5 9), 11-decane-insoluble portion of ( ⁇ .) It was set as a ratio.
- the precipitate (solution (2) obtained by filtering OO) was put into about 3 times the amount of acetone as compared with solution (2), _
- the components dissolved in decane were precipitated to obtain a precipitate (/3).
- the precipitate (/3) was removed from the glass filter ( ⁇ 2, the opening was about 100 ⁇ 16
- the mass of the precipitate (/3) was measured. ⁇ 2020/175 138 21 ⁇ (: 170? 2020 /005312
- Measuring device JEOL 1-400 type nuclear magnetic resonance device
- Measurement mode Mi ⁇ 1 ⁇ /1 (Minami 1 1 6 6 1 ⁇ ⁇ 01 1 6 6 ⁇
- Pulse width 0 nuclear 45 ° (7.8 seconds)
- Pulse repetition time 5 seconds
- melt flow rate was measured according to AS TM D-1 238 (measurement temperature 1 90 °C, load 2.16 kg).
- the body density was determined.
- propylene polymers (81-1) to (8-17) were produced as propylene polymers.
- Anhydrous magnesium chloride 95.2 9 decane And 2-ethylhexyl alcohol 39 ⁇ 69 are heated at 1 30° ⁇ for 2 hours to form a homogeneous solution, and then phthalic anhydride 2 1. 3 9 is added to this solution. The mixture was stirred and mixed at 0° for 1 hour to dissolve phthalic anhydride.
- the detection of the free titanium compound was confirmed by the following method.
- the supernatant liquid (10) of the above solid catalyst component was collected by a syringe and charged into 100 (100) branches of the Schlenk which had been previously replaced with nitrogen.
- the solvent hexane was dried in a nitrogen stream and further vacuum dried for 30 minutes.
- Ion-exchanged water (401) and 50% by volume of sulfuric acid (10 I) were charged into this and stirred for 30 minutes.
- This aqueous solution was passed through filter paper for 100, and then as a masking agent for iron ( ⁇ ) ions.
- the rusco was shaken, and 20 minutes later, the absorbance at 420 n was observed using II V to detect free titanium.
- the free titanium was washed and removed and the free titanium was detected until the absorption was not observed.
- the solid titanium catalyst component (3) prepared as described above was stored as a decane slurry, and a part of this was dried for the purpose of examining the catalyst composition.
- the composition of the solid titanium catalyst component (3) thus obtained was 2.3 mass% of titanium, 61 mass% of chlorine, 19 mass% of magnesium, and 12.5 mass% of 0 I. It was
- a stainless steel autoclave with a stirrer with an internal volume of 10!_ was thoroughly dried, and after nitrogen substitution, dehydrated heptane 6!_, triethylaluminum 12.5 011110 ⁇ , dicyclopentyldimethoxysilane ⁇ .61111110 ⁇ . added. After replacing the nitrogen in the system with propylene, the hydrogen pressure in the system was increased to 0.8.
- the internal temperature was set to 30 ⁇ 2020/175 138 25 ⁇ (: 170? 2020 /005312
- a mixed gas of / (2.41_/min) was introduced.
- the internal temperature was adjusted to 60° and propylene/ethylene copolymerization was carried out for 60 minutes.
- the proportion of the constituent units derived from ethylene in is 0% by mass, The ratio of the constituent units derived from ethylene in the mixture was 31% by mass.
- the obtained propylene-based polymer (81 6) was 1 ⁇ /1 [3 ⁇ 4 was 120 9 /10 min, ⁇ . [86% by mass, mouth 1 4 wt%, [7? 3 ⁇ 1] 2.5 1/9, 0, ⁇ 0 mass% proportion of the structural unit derived from ethylene medium, The ratio of the constituent units derived from ethylene was 35% by mass.
- Polymerization was conducted in the same manner as in Production Example 1 except that hydrogen was charged in "Polymerization 1" so that the internal pressure of the system was ⁇ 0.351 ⁇ /1 3- ⁇ .
- the resulting propylene-based polymer (8 1 0 9/1 0 minutes, 0 more than 86% by weight, 0 3 1 4% by weight, [7? ⁇ ] Is 3. 0_Rei_1 1/9,
- the ratio of the constituent units derived from ethylene in the mixture was 31% by mass.
- ethylene was also introduced so that the ethylene concentration in the gas phase in the polymerization vessel was ⁇ 801 ⁇ ⁇ % (total of propylene and ethylene was 1 0001 ⁇ ⁇ %.) when propylene was introduced. Except for the above, the superposition was performed in the same manner as in Production Example 1.
- the resulting propylene polymer (81 9) was 1 ⁇ /1 [3 ⁇ 4 was 1 209 /
- Polymerization was carried out in the same manner as in Production Example 1 except that hydrogen was charged in "Polymerization 1" so that the internal pressure of the system was 0. 1 51 ⁇ /1 3-O.
- the resulting propylene-based polymer (8 0 to 86% by mass, 0 3 to 14% by mass, [7? ⁇ ] is 2.5 ⁇ 1
- the proportion of constituent units derived from ethylene in the The ratio of the constituent units derived from ethylene in the mixture was 31% by mass.
- the proportion of constituent units derived from ethylene in 0 is 0% by mass, The ratio of the constituent units derived from ethylene in the mixture was 22% by mass.
- the proportion of constituent units derived from ethylene in 0 is 0% by mass, The ratio of the constituent units derived from ethylene in the mixture was 38% by mass.
- ethylene was also introduced so that the ethylene concentration in the gas phase part in the polymerization tank was ⁇ .901 ⁇ ⁇ % (total of propylene and ethylene was 1 0001 ⁇ ⁇ %.) when propylene was introduced. Except for the above, the superposition was performed in the same manner as in Production Example 1.
- the obtained propylene-based polymer (81 17) was 1 ⁇ /1 [3 ⁇ 4 was 1 209 /10 minutes, ⁇ . [ Is 86% by mass, mouth is 14% by mass, [7 ⁇ . Is 2.56 ⁇ / 9.
- the proportion of constitutional units derived from ethylene in Okinawa is 1.6% by mass, ..
- the proportion of constitutional units derived from ethylene in Okinawa was 31% by mass.
- Nucleating agent (011) ADEKA STAB 81 1 1 (manufactured by HOMIYA 8 Co., Ltd.)
- the obtained mixture was melt-kneaded under the following conditions using a twin-screw extruder manufactured by Toshiba Machine Co., Ltd. (Chomi 1 ⁇ /135 Mi 3) to obtain a strand.
- the obtained strand was cooled with water and cut with a pelletizer to obtain a pellet (1) of a propylene-based resin composition.
- the melt flow rate (1 ⁇ /1 [3 ⁇ 4) was measured according to 8 3 1//1 mouth 1 238 (measurement temperature 230° ⁇ , load 2.1 61 ⁇ 9 ).
- the measurement was carried out using a differential scanning calorimeter (03 (3, Perkin Elmer Co., Ltd. (Diamo nd 03 ⁇ )) in accordance with “3— ⁇ 7 1 2 1”.
- the apex of the endothermic peak was defined as the crystalline melting point (x).When there are multiple endothermic peaks, the maximum endothermic peak is defined as the crystalline melting point (x).
- Sample shape Press film (230° molding, thickness 200-400
- No. 2316 Decrease temperature to 60° ⁇ at 10° ⁇ /min.
- Electric injection molding machine with a mold clamping force of 100 tons (FANUC Robot 2000 1-100 6), cylinder temperature 250 °, mold temperature 20. ⁇ , primary injection pressure 1 50 IV! 3 , injection speed Holding pressure 80 IV! 3, holding time 1.3 seconds, injection-molded pellets (1) of propylene-based resin composition, height 1 1 0, flange diameter 70, side wall thickness 0. 5 0101 containers (cups) were injection molded.
- the obtained container was evaluated as follows. The results are shown in Table 1.
- X Burr occurred on the flange surface, which is the end of the flow, a phenomenon that the end was not filled, and a sink phenomenon such as a dent on the container surface due to insufficient filling occurred.
- the condition of the obtained container was adjusted under the condition of 24 °C for 48 to 72 hours, and the container was tested using a universal testing machine (Shimadzu Corporation, 0-100 0 0 [ ⁇ Wide 250 0]). In the vertical state (with the opening facing downward), a load was applied from the top surface and the maximum load until the container was deformed was measured.
- the obtained container was conditioned for 48 to 72 hours under the condition of 24 °C and further conditioned for 24 hours or more under the environment of 51.
- a pellet of a propylene-based resin composition was prepared in the same manner as in Example 1, except that the types and amounts of the propylene-based polymer, ethylene-based polymer and nucleating agent were changed as shown in Tables 1 and 2. Was manufactured, a container was manufactured, and these were further evaluated. The results are shown in Tables 1 and 2.
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CN202080016408.1A CN113474148B (zh) | 2019-02-26 | 2020-02-12 | 丙烯系树脂组合物和成型体 |
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JPH09227735A (ja) * | 1995-12-22 | 1997-09-02 | Mitsui Petrochem Ind Ltd | ポリプロピレン系樹脂組成物 |
JP2006161033A (ja) * | 2004-11-10 | 2006-06-22 | Sumitomo Chemical Co Ltd | プロピレン系樹脂組成物およびそのフィルム |
JP2009084393A (ja) * | 2007-09-28 | 2009-04-23 | Mitsui Chemicals Inc | 飲料ボトル用キャップ |
WO2010074001A1 (ja) * | 2008-12-22 | 2010-07-01 | 株式会社プライムポリマー | プロピレン系樹脂組成物、成形体および容器 |
JP2017508035A (ja) * | 2014-02-06 | 2017-03-23 | ボレアリス エージー | 軟質及び透明衝撃コポリマー |
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JP4281157B2 (ja) | 1999-07-13 | 2009-06-17 | チッソ株式会社 | ポリプロピレン樹脂組成物 |
JP2002187996A (ja) | 2000-12-20 | 2002-07-05 | Sumitomo Chem Co Ltd | プロピレン系樹脂組成物および中空成形容器 |
JP2002187997A (ja) | 2000-12-20 | 2002-07-05 | Sumitomo Chem Co Ltd | プロピレン系樹脂組成物および中空成形容器 |
JP2005026981A (ja) | 2003-07-01 | 2005-01-27 | Seiko Epson Corp | 温度補償型圧電発振器並びに、温度補償型圧電発振器を備える携帯電話装置及び電子機器 |
JP5167120B2 (ja) | 2006-03-29 | 2013-03-21 | 三井化学株式会社 | プロピレン系ランダムブロック共重合体、該共重合体を含む樹脂組成物およびそれからなる成形体 |
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JPH09227735A (ja) * | 1995-12-22 | 1997-09-02 | Mitsui Petrochem Ind Ltd | ポリプロピレン系樹脂組成物 |
JP2006161033A (ja) * | 2004-11-10 | 2006-06-22 | Sumitomo Chemical Co Ltd | プロピレン系樹脂組成物およびそのフィルム |
JP2009084393A (ja) * | 2007-09-28 | 2009-04-23 | Mitsui Chemicals Inc | 飲料ボトル用キャップ |
WO2010074001A1 (ja) * | 2008-12-22 | 2010-07-01 | 株式会社プライムポリマー | プロピレン系樹脂組成物、成形体および容器 |
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