Resin formed body and resin composition
US-11905399-B2 · Feb 20, 2024 · US
US2022010113A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022010113-A1 |
| Application number | US-202117484054-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 24, 2021 |
| Priority date | Mar 27, 2019 |
| Publication date | Jan 13, 2022 |
| Grant date | — |
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A cellulose fiber-reinforced polypropylene resin formed body that is a resin formed body having respective diffraction peaks observed at positions of a scattering vector s of 1.61±0.1 nm −1 , 1.92±0.1 nm −1 , and 3.86±0.1 nm −1 in a wide-angle X-ray diffraction measurement, and is characterized by having ΔT calculated by the following formula (1) of 40.0° C. or more; and a cellulose fiber-reinforced polypropylene resin formed body that is a resin formed body having the above diffraction peaks and is characterized by having ΔT m and ΔT c expressed by the following formulae (2) and (3) and satisfying ΔT m <ΔT c ; and a producing method of these. Δ T=T m(PP Cell) −T c(PP Cell) (1) Δ T m =T m(PP) −T m(PP Cell) (2) Δ T c =T c(PP) −T c(PP Cell) (3)
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1 . A cellulose fiber-reinforced polypropylene resin formed body, which is a resin formed body having respective diffraction peaks observed at positions of a scattering vector s of 1.61±0.1 nm −1 , 1.92±0.1 nm −1 , and 3.86±0.1 nm −1 in a wide-angle X-ray diffraction measurement, and is characterized by having ΔT calculated by the following formula of 40.0° C. or more; Δ T=T m(PP Cell) −T c(PP Cell) (1) in the above-described formula, T m(PP Cell) and T c(PP Cell) , in this order, indicate a melting point and a crystallization temperature, respectively, of the above-described cellulose fiber-reinforced polypropylene resin formed body. 2 . A cellulose fiber-reinforced polypropylene resin formed body, which is a resin formed body having respective diffraction peaks observed at positions of a scattering vector s of 1.61±0.1 nm −1 , 1.92±0.1 nm −1 , and 3.86±0.1 nm −1 in a wide-angle X-ray diffraction measurement, and is characterized by having ΔT m and ΔT c expressed by the following formulae (2) and (3) and satisfying ΔT m <ΔT c : Δ T m =T m(PP) −T m(PP Cell) (2) Δ T c =T c(PP) −T c(PP Cell) (3) in the above-described formulae, T m(PP) indicates a melting point of the above-described polypropylene resin, T m(PP Cell) indicates a melting point of the above-described cellulose fiber-reinforced polypropylene resin formed body, T c(PP) indicates a crystallization temperature of the above-described polypropylene resin, and T c(PP Cell) , indicates a crystallization temperature of the above-described cellulose fiber-reinforced polypropylene resin formed body. 3 . The cellulose fiber-reinforced polypropylene resin formed body according to claim 1 , wherein a component having the diffraction peak at the position of the scattering vector s of 3.86±0.1 nm −1 has an orientation degree of more than 0.15 and less than 0.80. 4 . The cellulose fiber-reinforced polypropylene resin formed body according to claim 2 , wherein a component having the diffraction peak at the position of the scattering vector s of 3.86±0.1 nm −1 has an orientation degree of more than 0.15 and less than 0.80. 5 . The cellulose fiber-reinforced polypropylene resin formed body according to claim 1 , wherein an elongation at break at 100° C. is more than 700%. 6 . The cellulose fiber-reinforced polypropylene resin formed body according to claim 2 , wherein an elongation at break at 100° C. is more than 700%. 7 . A method for producing the cellulose fiber-reinforced polypropylene resin formed body according to claim 1 , wherein the method uses a twin-screw extruder, wherein the twin-screw extruder includes screws having a compression structure with two or more stages that at least includes a first compression portion and a second compression portion, wherein the method includes a step of adding water or maleic anhydride as a hydrophilic compound or a solution of the hydrophilic compound to a melt-kneaded product of a polypropylene resin and a cellulose fiber, at any positions from the first compression portion to the second compression portion of the screws, and conducting kneading under a pressure condition exceeding a saturated vapor pressure of the additive. 8 . A method for producing the cellulose fiber-reinforced polypropylene resin formed body according to claim 2 , wherein the method uses a twin-screw extruder, wherein the twin-screw extruder includes screws having a compression structure with two or more stages that at least includes a first compression portion and a second compression portion, wherein the method includes a step of adding water or maleic anhydride as a hydrophilic compound or a solution of the hydrophilic compound to a melt-kneaded product of a polypropylene resin and a cellulose fiber, at any positions from the first compression portion to the second compression portion of the screws, and conducting kneading under a pressure condition exceeding a saturated vapor pressure of the additive.
Cellulose; Modified cellulose · CPC title
Homopolymers or copolymers of propene · CPC title
with vegetable or animal fibrous material · CPC title
the additives only being premixed with a liquid phase · CPC title
using two or more parallel screws {or at least two parallel non-intermeshing screws}, e.g. twin screw extruders · CPC title
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