Particulate nucleating agent, resin composition, molded product, and production method thereof
US-10882974-B2 · Jan 5, 2021 · US
US11634559B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11634559-B2 |
| Application number | US-202117793528-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 8, 2021 |
| Priority date | Jan 20, 2020 |
| Publication date | Apr 25, 2023 |
| Grant date | Apr 25, 2023 |
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A method for producing a resin composition of the present invention is a method for producing a resin composition, the method including a step of obtaining a resin composition by heating and melt-kneading a mixture containing a particulate nucleating agent in which D50 is equal to or more than 0.1 μm and equal to or less than 300 μm and a thermoplastic resin using a twin screw extruder (100) including, inside a cylinder (10), a screw (50) having kneading discs (60), in which the step of obtaining a resin composition includes an extrusion step of extruding the mixture supplied into the twin screw extruder (100) in an ejection direction under kneading conditions in which X and Y satisfy 4.0≤X in a range of 6.0×103≤Y≤7.0×104 when a volume-based ejection amount is denoted by X (10−6·kg·h−1·mm−3), and a strain rate is denoted by Y (min−1).
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The invention claimed is: 1. A method for producing a resin composition, the method comprising: obtaining a resin composition by heating and melt-kneading a mixture containing a particulate nucleating agent in which a cumulative 50% particle size (D 50 ) in a volume-based particle size distribution is equal to or more than 0.1 μm and equal to or less than 300 μm and a thermoplastic resin using a twin screw extruder including, inside a cylinder, a screw having kneading discs, wherein the obtaining a resin composition includes extruding the mixture supplied into the twin screw extruder in an ejection direction under kneading conditions in which X and Y satisfy 4.0≤X in a range of 6.0×10 3 ≤Y≤7.0×10 4 when a volume-based ejection amount represented by Equation (I) is denoted by X (10 −6 ·kg·h −1 ·mm −3 ), and a strain rate represented by Equation (II) is denoted by Y (min −1 ), volume-based ejection amount=ejection amount (kg/h) of twin screw extruder/internal capacity (10 6 ·mm 3 ) of cylinder, and [Equation (I)] strain rate=rotation rate (min −1 ) of screw×radius (mm) of screw/width (mm) of narrow part inside cylinder. [Equation (II)] 2. The method for producing a resin composition according to claim 1 , wherein the kneading conditions in the extruding further satisfy 2.7×10 2 ≤Y/X≤1.3×10 4 . 3. The method for producing a resin composition according to claim 1 , wherein the kneading conditions in the extruding further satisfy X≤500. 4. The method for producing a resin composition according to claim 1 , wherein D1, L2, and L3 in the twin screw extruder satisfy 0.02≤(L3/D1)/(L2/D1)≤1.0 when an internal radius of the cylinder is D1 (mm), a length of the screw in an axial center direction is L2, and a total value of lengths of the kneading discs in the axial center direction is L3. 5. The method for producing a resin composition according to claim 1 , wherein the particulate nucleating agent contains a metal salt of an aromatic phosphoric acid ester represented by General Formula (1), wherein in General Formula (1), R 1 to R 4 each independently represent a hydrogen atom or a linear or branched alkyl group having 1 to 9 carbon atoms, R 5 represents a hydrogen atom or an alkyl group having 1 to 4 carbon atoms, and m represents 1 or 2, provided that when m is 1, M 1 represents a hydrogen atom, Al(OH) 2 , or an alkali metal atom, and when m is 2, M 1 represents a group 2 element, Al(OH), or Zn). 6. The method for producing a resin composition according to claim 5 , wherein the particulate nucleating agent contains a metal salt of an aromatic phosphoric acid ester represented by General Formula (1) in which M 1 is sodium and m is 1. 7. The method for producing a resin composition according to claim 1 , wherein a heating temperature in the heating and melt-kneading is equal to or higher than 150° C. and equal to or lower than 300° C. in the obtaining a resin composition. 8. The method for producing a resin composition according to claim 1 , wherein the thermoplastic resin contains a crystalline polymer. 9. The method for producing a resin composition according to claim 8 , wherein the crystalline polymer contains includes a polyolefin-based polymer. 10. The method for producing a resin composition according to claim 1 , wherein the mixture contains a filler. 11. The method for producing a resin composition according to claim 1 , wherein the mixture contains a thermoplastic elastomer. 12. The method for producing a resin composition according to claim 1 , wherein a content of the particulate nucleating agent in the mixture is equal to or more than 0.001 parts by weight and equal to or less than 10 parts by weight with respect to 100 parts by weight of the thermoplastic resin. 13. The method for producing a resin composition according to claim 1 , wherein the resin composition is obtained in a pellet shape.
Additives containing two or more different additives of the same subgroup in C08K · CPC title
Stabilisers against oxidation, heat, light, ozone · CPC title
Measuring properties of mixture, e.g. temperature or density (B29B7/724 takes precedence) · CPC title
Cyclic esters · CPC title
Fillers or reinforcements {, e.g. fibres} · CPC title
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