JPH08174698A - Manufacture of fiber-reinforced thermoplastic resin foam - Google Patents
Manufacture of fiber-reinforced thermoplastic resin foamInfo
- Publication number
- JPH08174698A JPH08174698A JP6322170A JP32217094A JPH08174698A JP H08174698 A JPH08174698 A JP H08174698A JP 6322170 A JP6322170 A JP 6322170A JP 32217094 A JP32217094 A JP 32217094A JP H08174698 A JPH08174698 A JP H08174698A
- Authority
- JP
- Japan
- Prior art keywords
- thermoplastic resin
- fiber
- hollow body
- reinforced thermoplastic
- foaming
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920005992 thermoplastic resin Polymers 0.000 title claims abstract description 200
- 239000006260 foam Substances 0.000 title claims abstract description 50
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 238000005187 foaming Methods 0.000 claims abstract description 34
- 238000007493 shaping process Methods 0.000 claims abstract description 31
- 239000004088 foaming agent Substances 0.000 claims abstract description 22
- 230000002093 peripheral effect Effects 0.000 claims abstract description 10
- 238000003892 spreading Methods 0.000 claims abstract description 9
- 239000011342 resin composition Substances 0.000 claims description 44
- 239000002131 composite material Substances 0.000 claims description 15
- 230000001276 controlling effect Effects 0.000 claims description 10
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 229920000915 polyvinyl chloride Polymers 0.000 abstract description 12
- 239000004800 polyvinyl chloride Substances 0.000 abstract description 12
- 239000011521 glass Substances 0.000 abstract description 2
- 239000000835 fiber Substances 0.000 description 46
- 239000010410 layer Substances 0.000 description 31
- 238000000034 method Methods 0.000 description 27
- -1 polyethylene Polymers 0.000 description 27
- 238000001125 extrusion Methods 0.000 description 23
- 229920005989 resin Polymers 0.000 description 14
- 239000011347 resin Substances 0.000 description 14
- 239000004698 Polyethylene Substances 0.000 description 13
- 229920000573 polyethylene Polymers 0.000 description 13
- 238000001816 cooling Methods 0.000 description 12
- 239000012783 reinforcing fiber Substances 0.000 description 12
- 230000033228 biological regulation Effects 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 10
- 239000012792 core layer Substances 0.000 description 10
- 239000007789 gas Substances 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 238000005452 bending Methods 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 5
- 239000004793 Polystyrene Substances 0.000 description 5
- 229920001577 copolymer Polymers 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- 229920002223 polystyrene Polymers 0.000 description 5
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 description 4
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 4
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 4
- 229920001893 acrylonitrile styrene Polymers 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- SCUZVMOVTVSBLE-UHFFFAOYSA-N prop-2-enenitrile;styrene Chemical compound C=CC#N.C=CC1=CC=CC=C1 SCUZVMOVTVSBLE-UHFFFAOYSA-N 0.000 description 4
- 230000003014 reinforcing effect Effects 0.000 description 4
- 229920003002 synthetic resin Polymers 0.000 description 4
- 239000000057 synthetic resin Substances 0.000 description 4
- 229920000049 Carbon (fiber) Polymers 0.000 description 3
- 239000004801 Chlorinated PVC Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 239000004917 carbon fiber Substances 0.000 description 3
- 229920000457 chlorinated polyvinyl chloride Polymers 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 235000014113 dietary fatty acids Nutrition 0.000 description 3
- HDERJYVLTPVNRI-UHFFFAOYSA-N ethene;ethenyl acetate Chemical group C=C.CC(=O)OC=C HDERJYVLTPVNRI-UHFFFAOYSA-N 0.000 description 3
- 229920001038 ethylene copolymer Polymers 0.000 description 3
- 239000000194 fatty acid Substances 0.000 description 3
- 229930195729 fatty acid Natural products 0.000 description 3
- 239000003365 glass fiber Substances 0.000 description 3
- 238000004898 kneading Methods 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 3
- 229920005670 poly(ethylene-vinyl chloride) Polymers 0.000 description 3
- 229920001187 thermosetting polymer Polymers 0.000 description 3
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- 239000004156 Azodicarbonamide Substances 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- 239000004952 Polyamide Substances 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 2
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 2
- 235000019399 azodicarbonamide Nutrition 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 2
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 2
- AYOHIQLKSOJJQH-UHFFFAOYSA-N dibutyltin Chemical compound CCCC[Sn]CCCC AYOHIQLKSOJJQH-UHFFFAOYSA-N 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000000088 plastic resin Substances 0.000 description 2
- 238000013001 point bending Methods 0.000 description 2
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 229920001707 polybutylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000004926 polymethyl methacrylate Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000000344 soap Substances 0.000 description 2
- CZGWDPMDAIPURF-UHFFFAOYSA-N (4,6-dihydrazinyl-1,3,5-triazin-2-yl)hydrazine Chemical compound NNC1=NC(NN)=NC(NN)=N1 CZGWDPMDAIPURF-UHFFFAOYSA-N 0.000 description 1
- ZBBLRPRYYSJUCZ-GRHBHMESSA-L (z)-but-2-enedioate;dibutyltin(2+) Chemical compound [O-]C(=O)\C=C/C([O-])=O.CCCC[Sn+2]CCCC ZBBLRPRYYSJUCZ-GRHBHMESSA-L 0.000 description 1
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 1
- FRCHKSNAZZFGCA-UHFFFAOYSA-N 1,1-dichloro-1-fluoroethane Chemical compound CC(F)(Cl)Cl FRCHKSNAZZFGCA-UHFFFAOYSA-N 0.000 description 1
- OHMHBGPWCHTMQE-UHFFFAOYSA-N 2,2-dichloro-1,1,1-trifluoroethane Chemical compound FC(F)(F)C(Cl)Cl OHMHBGPWCHTMQE-UHFFFAOYSA-N 0.000 description 1
- ICGLPKIVTVWCFT-UHFFFAOYSA-N 4-methylbenzenesulfonohydrazide Chemical compound CC1=CC=C(S(=O)(=O)NN)C=C1 ICGLPKIVTVWCFT-UHFFFAOYSA-N 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 1
- 239000004604 Blowing Agent Substances 0.000 description 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 description 1
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 description 1
- 239000004709 Chlorinated polyethylene Substances 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 1
- 239000006057 Non-nutritive feed additive Substances 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004696 Poly ether ether ketone Substances 0.000 description 1
- 239000004695 Polyether sulfone Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 239000004734 Polyphenylene sulfide Substances 0.000 description 1
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 229920006231 aramid fiber Polymers 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 235000009120 camo Nutrition 0.000 description 1
- 235000005607 chanvre indien Nutrition 0.000 description 1
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 1
- HGAZMNJKRQFZKS-UHFFFAOYSA-N chloroethene;ethenyl acetate Chemical compound ClC=C.CC(=O)OC=C HGAZMNJKRQFZKS-UHFFFAOYSA-N 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- UQLDLKMNUJERMK-UHFFFAOYSA-L di(octadecanoyloxy)lead Chemical compound [Pb+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O UQLDLKMNUJERMK-UHFFFAOYSA-L 0.000 description 1
- RFAIKXASDCRKEP-UHFFFAOYSA-N dioctyl(sulfanylidene)tin Chemical compound CCCCCCCC[Sn](=S)CCCCCCCC RFAIKXASDCRKEP-UHFFFAOYSA-N 0.000 description 1
- BRWZYZWZBMGMMG-UHFFFAOYSA-J dodecanoate tin(4+) Chemical compound [Sn+4].CCCCCCCCCCCC([O-])=O.CCCCCCCCCCCC([O-])=O.CCCCCCCCCCCC([O-])=O.CCCCCCCCCCCC([O-])=O BRWZYZWZBMGMMG-UHFFFAOYSA-J 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 239000011487 hemp Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- OCWMFVJKFWXKNZ-UHFFFAOYSA-L lead(2+);oxygen(2-);sulfate Chemical compound [O-2].[O-2].[O-2].[Pb+2].[Pb+2].[Pb+2].[Pb+2].[O-]S([O-])(=O)=O OCWMFVJKFWXKNZ-UHFFFAOYSA-L 0.000 description 1
- UMKARVFXJJITLN-UHFFFAOYSA-N lead;phosphorous acid Chemical compound [Pb].OP(O)O UMKARVFXJJITLN-UHFFFAOYSA-N 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229940049920 malate Drugs 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N malic acid Chemical compound OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 229940050176 methyl chloride Drugs 0.000 description 1
- 125000000325 methylidene group Chemical group [H]C([H])=* 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 229920002530 polyetherether ketone Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 229920006380 polyphenylene oxide Polymers 0.000 description 1
- 229920000069 polyphenylene sulfide Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 229920002725 thermoplastic elastomer Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、熱可塑性樹脂発泡芯層
と、繊維強化熱可塑性樹脂表皮層とからなる繊維強化熱
可塑性樹脂発泡体の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a fiber reinforced thermoplastic resin foam comprising a thermoplastic resin foam core layer and a fiber reinforced thermoplastic resin skin layer.
【0002】[0002]
【従来の技術】従来、熱可塑性樹脂発泡芯層と、繊維強
化合成樹脂表皮層とからなる長尺の合成樹脂複合発泡体
の製造方法としては、断面異形形状を有する熱可塑性樹
脂発泡体を連続的に一方向に移送しつつ、その外面に熱
硬化性樹脂を含浸させた連続繊維を供給し、加熱して引
抜成形する方法が知られている(特開平4−33963
5号公報参照)。2. Description of the Related Art Conventionally, as a method for producing a long synthetic resin composite foam comprising a thermoplastic resin foam core layer and a fiber reinforced synthetic resin skin layer, a thermoplastic resin foam having an irregular cross-sectional shape is continuously produced. A method is known in which continuous fibers impregnated with a thermosetting resin are supplied to the outer surface of the fiber while being transported in one direction, and the fiber is heated to be pultruded (Japanese Patent Laid-Open No. 4-33963).
(See Japanese Patent Publication No. 5).
【0003】[0003]
【発明が解決しようとする課題】従来の上記成形方法で
は、予め断面異形形状の発泡成形体を用意する必要があ
り、非常に煩雑であった。また、連続繊維に含浸させた
熱硬化性樹脂は低粘度であるため、均一な肉厚の繊維強
化合成樹脂表皮層が得られず、複合発泡体に均一な機械
的強度を得ることが不可能であった。In the conventional molding method described above, it was necessary to prepare in advance a foamed molded article having an irregular cross-section, which was very complicated. In addition, since the thermosetting resin impregnated into the continuous fiber has a low viscosity, it is not possible to obtain a fiber-reinforced synthetic resin skin layer with a uniform thickness, and it is impossible to obtain uniform mechanical strength in the composite foam. Met.
【0004】この問題を解決する方法として、繊維強化
熱可塑性樹脂シートを連続的に中空状体に賦形し、中空
状体内に発泡性熱可塑性樹脂組成物を供給して発泡さ
せ、発泡圧により所望の断面形状に賦形する方法が考え
られる。しかし、この製造方法では、繊維強化熱可塑性
樹脂中空状体の断面形状と製品である繊維強化熱可塑性
樹脂発泡体の断面形状が大きく異なる場合、中空状体は
部分的に大きく延ばされ、局部的に薄くなったり、破れ
たりして、製品強度にばらつきが生じるという欠点があ
る。この欠点を解消する方法としては、繊維強化熱可塑
性樹脂シートを中空状体に賦形する際、予め製品形状に
賦形し、製品形状の中空状体内部に発泡性熱可塑性樹脂
組成物を供給して発泡させる方法が考えられるが、複雑
な断面形状に賦形することは困難であるし、仮りに賦形
できたとしても、発泡性熱可塑性樹脂組成物を複雑な断
面形状の中空状体内に供給することは困難である。As a method for solving this problem, a fiber-reinforced thermoplastic resin sheet is continuously shaped into a hollow body, and a foamable thermoplastic resin composition is supplied into the hollow body to cause foaming, and a foaming pressure is applied. A method of shaping into a desired cross-sectional shape can be considered. However, in this manufacturing method, when the cross-sectional shape of the fiber-reinforced thermoplastic resin hollow body and the cross-sectional shape of the fiber-reinforced thermoplastic resin foam, which is the product, are greatly different, the hollow body is partially greatly extended, However, there is a drawback in that the strength of the product varies due to the fact that the product becomes thin or breaks. As a method of eliminating this drawback, when the fiber-reinforced thermoplastic resin sheet is shaped into a hollow body, it is shaped into a product shape in advance, and the foamable thermoplastic resin composition is supplied inside the hollow body of the product shape. However, it is difficult to shape it into a complicated cross-sectional shape, and even if it can be shaped, the expandable thermoplastic resin composition will have a hollow body with a complicated cross-sectional shape. Is difficult to supply.
【0005】本発明の目的は、均一な厚さの繊維強化熱
可塑性樹脂表皮層を有し、もって均一な機械的強度を有
しかつ所望断面形状が得られる繊維強化熱可塑性樹脂発
泡体の製造方法を提供することにある。The object of the present invention is to produce a fiber-reinforced thermoplastic resin foam having a fiber-reinforced thermoplastic resin skin layer having a uniform thickness and thus having a uniform mechanical strength and a desired cross-sectional shape. To provide a method.
【0006】[0006]
【課題を解決するための手段】請求項1の発明による繊
維強化熱可塑性樹脂発泡体の製造方法は、繊維強化熱可
塑性樹脂シートを連続的に中空状体に賦形する工程と、
中空状体内部に熱可塑性樹脂及び発泡剤からなる発泡性
熱可塑性樹脂組成物を発泡させながら連続的に供給し、
その発泡圧により中空状体を規制しつつ周方向に略均一
に展延させる工程と、展延した中空状体を、その外周長
を略一定に保ちつつ変形させて所定の断面形状に賦形す
る工程とを含むことを特徴とするものである。A method for producing a fiber-reinforced thermoplastic resin foam according to the present invention comprises a step of continuously shaping a fiber-reinforced thermoplastic resin sheet into a hollow body,
Continuously supplying while foaming a foamable thermoplastic resin composition comprising a thermoplastic resin and a foaming agent inside the hollow body,
A step of controlling the hollow body by the foaming pressure to spread it substantially uniformly in the circumferential direction, and deforming the expanded hollow body while keeping the outer peripheral length substantially constant to shape it into a predetermined cross-sectional shape. And a step of performing.
【0007】請求項2の発明による繊維強化熱可塑性樹
脂発泡体の製造方法は、繊維強化熱可塑性樹脂シートを
連続的に中空状体に賦形する工程と、中空状体内部に熱
可塑性樹脂及び発泡剤からなる発泡性熱可塑性樹脂組成
物を連続的に供給する工程と、発泡性熱可塑性樹脂組成
物を発泡させ、その発泡圧により中空状体を規制しつつ
周方向に略均一に展延させる工程と、展延した中空状体
を、その外周長を略一定に保ちつつ変形させて所定の断
面形状に賦形する工程とを含むことを特徴とするもので
ある。The method for producing a fiber-reinforced thermoplastic resin foam according to the second aspect of the present invention comprises a step of continuously forming a fiber-reinforced thermoplastic resin sheet into a hollow body, and a thermoplastic resin inside the hollow body, A step of continuously supplying a foamable thermoplastic resin composition comprising a foaming agent, foaming the foamable thermoplastic resin composition, and spreading the foam substantially uniformly in the circumferential direction while controlling the hollow body by the foaming pressure. And a step of deforming the expanded hollow body while keeping the outer peripheral length thereof substantially constant and shaping it into a predetermined cross-sectional shape.
【0008】請求項3の発明による繊維強化熱可塑性樹
脂発泡体の製造方法は、繊維強化熱可塑性樹脂層及び、
熱可塑性樹脂及び発泡剤からなる発泡性熱可塑性樹脂組
成物層を有する複合シートを、繊維強化熱可塑性樹脂層
が外面となるようにして連続的に中空状体に賦形する工
程と、発泡性熱可塑性樹脂組成物を発泡させ、その発泡
圧により中空状体を規制しつつ周方向に略均一に展延さ
せる工程と、展延した中空状体を、その外周長を略一定
に保ちつつ変形させて所定の断面形状に賦形する工程と
を含むことを特徴とするものである。A method for producing a fiber-reinforced thermoplastic resin foam according to the present invention is a fiber-reinforced thermoplastic resin layer,
A step of continuously shaping a composite sheet having a foamable thermoplastic resin composition layer composed of a thermoplastic resin and a foaming agent into a hollow body so that the fiber-reinforced thermoplastic resin layer is the outer surface; A step of foaming a thermoplastic resin composition and controlling the hollow body by the foaming pressure to spread the hollow body substantially uniformly in the circumferential direction, and deforming the expanded hollow body while keeping the outer peripheral length substantially constant. And a step of shaping into a predetermined cross-sectional shape.
【0009】繊維強化熱可塑性樹脂シートに用いられる
熱可塑性樹脂の具体例としては、ポリエチレン、ポリプ
ロピレン、ポリ塩化ビニル、塩素化ポリ塩化ビニル、ポ
リスチレン、ポリアミド、ポリエチレンテレフタレー
ト、ポリブチレンテレフタレート、ポリカーボネート、
ポリフッ化ビニリデン、ポリフェニレンサルファイド、
ポリフェニレンオキサイド、ポリエーテルスルホン、ポ
リエーテルエーテルケトン、ポリメチルメタクリレート
等があげられる。また、上記熱可塑性樹脂の単量体から
なる共重合体や、上記熱可塑性樹脂のグラフト樹脂やブ
レンド樹脂、例えばエチレン−塩化ビニル共重合体、酢
酸ビニル−エチレン共重合体、酢酸ビニル−塩化ビニル
共重合体、アクリロニトリル−ブタジエン−スチレン共
重合体、アクリロニトリル−スチレン共重合体、シラン
変性ポリエチレン、アクリル酸変性ポリプロピレン、マ
レイン酸変性ポリエチレンなども使用可能である。ま
た、熱可塑性エラストマーや架橋された熱可塑性樹脂も
使用可能である。成形温度を考慮すると、120〜25
0℃で成形可能である、ポリエチレン、ポリプロピレ
ン、ポリ塩化ビニル、ポリスチレン、塩素化ポリ塩化ビ
ニル、エチレン−塩化ビニル共重合体、酢酸ビニル−エ
チレン共重合体、酢酸ビニル−塩化ビニル共重合体、ア
クリロニトリル−ブタジエン−スチレン共重合体、アク
リロニトリル−スチレン共重合体が好ましい。Specific examples of the thermoplastic resin used for the fiber-reinforced thermoplastic resin sheet include polyethylene, polypropylene, polyvinyl chloride, chlorinated polyvinyl chloride, polystyrene, polyamide, polyethylene terephthalate, polybutylene terephthalate, polycarbonate,
Polyvinylidene fluoride, polyphenylene sulfide,
Examples thereof include polyphenylene oxide, polyether sulfone, polyether ether ketone, polymethyl methacrylate and the like. Further, a copolymer composed of the above-mentioned thermoplastic resin monomer, a graft resin or a blend resin of the above-mentioned thermoplastic resin, for example, an ethylene-vinyl chloride copolymer, a vinyl acetate-ethylene copolymer, a vinyl acetate-vinyl chloride. Copolymers, acrylonitrile-butadiene-styrene copolymers, acrylonitrile-styrene copolymers, silane-modified polyethylene, acrylic acid-modified polypropylene, maleic acid-modified polyethylene and the like can also be used. Further, a thermoplastic elastomer or a crosslinked thermoplastic resin can also be used. Considering the molding temperature, 120-25
Polyethylene, polypropylene, polyvinyl chloride, polystyrene, chlorinated polyvinyl chloride, ethylene-vinyl chloride copolymer, vinyl acetate-ethylene copolymer, vinyl acetate-vinyl chloride copolymer, acrylonitrile, which can be molded at 0 ° C. -Butadiene-styrene copolymer and acrylonitrile-styrene copolymer are preferable.
【0010】本発明で使用する熱可塑性樹脂は、単独で
使用されても併用されてもよく、物性を損なわない範囲
で、ジブチル錫マレートポリマー、ジブチル錫ビス(モ
ノアルキルマレート)などの有機錫マレート系、ジブチ
ル錫ラウレート、モノブチル錫脂肪酸塩などの有機錫ラ
ウレート系、ジオクチル錫サルファイド、ジブチル錫3
メルカプトロピオネートなどの有機錫メルカプト系、三
塩基性硫酸鉛、塩基性亜流酸鉛などの鉛塩、ステアリン
酸カルシウム、ステアリン酸鉛などの金属石鹸といった
熱安定剤、脂肪酸エステルワックス、低分子量ポリエチ
レンワックス、金属石鹸、多価アルコール、脂肪族アル
コール、脂肪酸アミノなどの滑剤、アクリル系樹脂、オ
レフィン系樹脂などの加工助剤、ジブチルフタレート、
ジオクチルフタレートなどの可塑剤、酸化防止剤、紫外
線吸収剤、改質剤、着色剤のような添加剤、及びタル
ク、マイカ、炭酸カルシウム、木粉、繊維強化熱硬化性
樹脂粉砕粉などの充填材が配合されてもよい。The thermoplastic resin used in the present invention may be used alone or in combination, and may be an organic material such as dibutyltin maleate polymer or dibutyltin bis (monoalkylmalate) as long as the physical properties are not impaired. Tin malate type, dibutyl tin laurate, organic tin laurate type such as monobutyl tin fatty acid salt, dioctyl tin sulfide, dibutyl tin 3
Organic tin mercapto type such as mercaptopionate, lead salt such as tribasic lead sulfate and basic lead phosphite, heat stabilizer such as metal soap such as calcium stearate and lead stearate, fatty acid ester wax, low molecular weight polyethylene wax Lubricants such as metal soaps, polyhydric alcohols, aliphatic alcohols and fatty acid aminos, processing aids such as acrylic resins and olefin resins, dibutyl phthalate,
Plasticizers such as dioctyl phthalate, antioxidants, UV absorbers, modifiers, additives such as colorants, and fillers such as talc, mica, calcium carbonate, wood powder, fiber-reinforced thermosetting resin ground powder. May be blended.
【0011】繊維強化熱可塑性樹脂シートに用いられる
繊維としては、本発明の製造工程において加えられる熱
により溶融軟化及び炭化しないものが使用可能であり、
具体的には、ガラス繊維;炭素繊維;シリコン・チタン
・炭素繊維;ボロン繊維;金属繊維;アラミド繊維、ポ
リエステル繊維、ポリアミド繊維などの有機繊維、絹、
綿、麻などの天然繊維をあげることができるが、強度、
コストを考慮すると、ガラス繊維、炭素繊維が好まし
い。フィラメントの直径は1〜100μm、特に3〜2
3μmが好ましい。フィラメントの直径が、1μmより
小さい場合は、繊維による補強効果は小さい。また、1
00μmより大きい場合は、熱可塑性樹脂と繊維の接触
面積が、同種類の同重量である小径の繊維と比較して小
さくなるため、熱可塑性樹脂と繊維の密着性が低下し、
繊維による補強効果は小さい。As the fibers used in the fiber-reinforced thermoplastic resin sheet, those which are not melt-softened or carbonized by the heat applied in the manufacturing process of the present invention can be used.
Specifically, glass fiber; carbon fiber; silicon / titanium / carbon fiber; boron fiber; metal fiber; aramid fiber, polyester fiber, organic fiber such as polyamide fiber, silk,
Natural fibers such as cotton and hemp can be mentioned, but strength,
Considering cost, glass fiber and carbon fiber are preferable. The diameter of the filament is 1 to 100 μm, especially 3 to 2
3 μm is preferable. When the diameter of the filament is smaller than 1 μm, the reinforcing effect of the fiber is small. Also, 1
When it is larger than 00 μm, the contact area between the thermoplastic resin and the fiber is smaller than that of the same kind and the same diameter of the small diameter fiber, so that the adhesion between the thermoplastic resin and the fiber is lowered,
The reinforcing effect of fibers is small.
【0012】繊維強化熱可塑性樹脂シート中の繊維の含
有量は、5〜80重量%、特に10〜50重量%の範囲
が好ましい。含有量が5重量%より少ないと補強効果は
小さく、80重量%より多いと繊維どうしを結合する樹
脂が少ないため得られる繊維強化熱可塑性樹脂発泡体の
繊維強化熱可塑性樹脂表皮層は弱いものになる。The fiber content in the fiber reinforced thermoplastic resin sheet is preferably in the range of 5 to 80% by weight, particularly 10 to 50% by weight. If the content is less than 5% by weight, the reinforcing effect is small, and if the content is more than 80% by weight, the amount of resin that binds the fibers to each other is small, and thus the fiber-reinforced thermoplastic resin foam has a weak fiber-reinforced thermoplastic skin layer. Become.
【0013】繊維強化熱可塑性樹脂シート中の繊維は、
3mm以上のものが用いられ、10mm以上が好まし
く、連続繊維であることがより好ましい。繊維が長いほ
ど繊維強化熱可塑性樹脂発泡体の強度は強くなり、繊維
長が3mmより短いと補強効果は小さい。また、中空状
体を規制しつつ周方向に均一に展延させるには、繊維特
に連続繊維が中空状体の長手方向になるように配向して
いることが好ましい。The fibers in the fiber reinforced thermoplastic resin sheet are
Those having a diameter of 3 mm or more are used, preferably 10 mm or more, and more preferably continuous fibers. The longer the fiber, the stronger the strength of the fiber-reinforced thermoplastic resin foam, and if the fiber length is shorter than 3 mm, the reinforcing effect is small. Further, in order to uniformly extend the hollow body in the circumferential direction while controlling the hollow body, it is preferable that the fibers, particularly the continuous fibers, are oriented in the longitudinal direction of the hollow body.
【0014】請求項1及び2の発明における繊維強化熱
可塑性樹脂シートは、例えばつぎのようにして製造され
る。すなわち、強化繊維束を開繊して一方向に引き揃え
た後、これらに熱可塑性樹脂フィルムを重ねて加熱ピン
チロール間を通過させ、溶融熱可塑性樹脂を強化繊維相
互間に浸入させ、つぎに冷却ロール間を通過させて冷却
し、繊維強化熱可塑性樹脂シートを得る。The fiber-reinforced thermoplastic resin sheet according to the first and second aspects of the invention is manufactured, for example, as follows. That is, after opening the reinforcing fiber bundle and aligning in one direction, superimposing a thermoplastic resin film on these and passing them between heating pinch rolls, allowing the molten thermoplastic resin to penetrate between the reinforcing fibers, and then The fiber-reinforced thermoplastic resin sheet is obtained by passing between cooling rolls and cooling.
【0015】同繊維強化熱可塑性樹脂シートは、またつ
ぎのようにしても製造することができる。すなわち、一
方向に引き揃えた連続強化繊維束を、粉体状熱可塑性樹
脂の流動床を通過させて開繊しながら強化繊維に粉体状
熱可塑性樹脂を付着させて帯状となした後、加熱ピンチ
ロール間を通過させ、熱可塑性樹脂を溶融させて強化繊
維相互間に浸入させ、つぎに冷却ロール間を通過させて
冷却し、繊維強化熱可塑性樹脂シートを得る。The fiber-reinforced thermoplastic resin sheet can also be manufactured in the following manner. That is, the continuous reinforcing fiber bundle aligned in one direction, after passing through a fluidized bed of the powdery thermoplastic resin and opening the fiber-shaped thermoplastic resin to the reinforcing fiber while opening, The fiber-reinforced thermoplastic resin sheet is obtained by passing between heating pinch rolls, melting the thermoplastic resin to penetrate between the reinforcing fibers, and then passing between cooling rolls for cooling.
【0016】繊維がランダムな状態で配されている繊維
強化熱可塑性樹脂シートを製造するには、上記のように
して得られた粉体状熱可塑性樹脂が付着した強化繊維
を、ロータリーカッターで細断し、細断された強化繊維
を集積し、加熱下で加圧して、細断強化繊維に熱可塑性
樹脂を含浸させ、その後冷却させることにより、繊維強
化熱可塑性樹脂シートを得る。In order to produce a fiber-reinforced thermoplastic resin sheet in which fibers are randomly arranged, the reinforcing fibers to which the powdery thermoplastic resin obtained as described above is attached are finely cut with a rotary cutter. A fiber-reinforced thermoplastic resin sheet is obtained by accumulating chopped and chopped reinforcing fibers, pressurizing them under heating to impregnate the chopped reinforcing fibers with a thermoplastic resin, and then cooling.
【0017】繊維強化熱可塑性樹脂シートの厚みは、
0.1〜10mmが好ましく、0.3〜2mmがより好
ましい。厚みが0.1mmより薄いと、繊維強化熱可塑
性樹脂シートの強度は弱く、10mmより厚いと、中空
状体への賦形が困難となる。The thickness of the fiber reinforced thermoplastic resin sheet is
0.1-10 mm is preferable and 0.3-2 mm is more preferable. If the thickness is thinner than 0.1 mm, the strength of the fiber-reinforced thermoplastic resin sheet is weak, and if it is thicker than 10 mm, shaping into a hollow body becomes difficult.
【0018】発泡性熱可塑性樹脂組成物に用いられる熱
可塑性樹脂としては、繊維強化熱可塑性樹脂シートに用
いられる熱可塑性樹脂と同様のものが使用可能である
が、繊維強化熱可塑性樹脂シートに用いられる熱可塑性
樹脂と熱融着可能である熱可塑性樹脂を用いることは、
得られる繊維強化熱可塑性樹脂発泡体の曲げ強度が向上
し、好ましい。具体的には、同じ種類の熱可塑性樹脂
(同じ単量体より重合された熱可塑性樹脂)同士を用い
ることが好ましい。異なる種類の熱可塑性樹脂を使用す
る場合の組合せとしては、例えば、ポリエチレンとポリ
プロピレン、ポリエチレンと酢酸ビニル−エチレン共重
合体、ポリエチレンと塩素化ポリエチレン、ポリスチレ
ンとアクリロニトリル−ブタジエン−スチレン共重合
体、ポリスチレンとアクリロニトリル−スチレン共重合
体、ポリ塩化ビニルと塩素化ポリ塩化ビニル、ポリ塩化
ビニルとエチレン−塩化ビニル共重合体、ポリ塩化ビニ
ルと酢酸ビニル−塩化ビニル共重合体、ポリ塩化ビニル
とポリメチルメタクリレート、ポリ塩化ビニルとアクリ
ロニトリル−ブタジエン−スチレン共重合体、ポリブチ
レンテレフタレートとポリエチレンテレフタレート、ア
クリロニトリル−ブタジエン−スチレン共重合体とアク
リロニトリル−スチレン共重合体などがあげられる。ま
た、熱可塑性樹脂と変性した同じ種類の熱可塑性樹脂の
組合せも使用できる。この例としては、ポリエチレンと
シラン変性ポリエチレン、ポリエチレンとアクリル酸変
性ポリプロピレン、ポリエチレンとマレイン酸変性ポリ
エチレンなどがあげられる。The thermoplastic resin used in the expandable thermoplastic resin composition may be the same as the thermoplastic resin used in the fiber reinforced thermoplastic resin sheet, but it is used in the fiber reinforced thermoplastic resin sheet. The use of a thermoplastic resin capable of heat fusion with the thermoplastic resin
The bending strength of the obtained fiber-reinforced thermoplastic resin foam is improved, which is preferable. Specifically, it is preferable to use thermoplastic resins of the same type (thermoplastic resins polymerized from the same monomer). As combinations when using different types of thermoplastic resins, for example, polyethylene and polypropylene, polyethylene and vinyl acetate-ethylene copolymer, polyethylene and chlorinated polyethylene, polystyrene and acrylonitrile-butadiene-styrene copolymer, polystyrene and polystyrene. Acrylonitrile-styrene copolymer, polyvinyl chloride and chlorinated polyvinyl chloride, polyvinyl chloride and ethylene-vinyl chloride copolymer, polyvinyl chloride and vinyl acetate-vinyl chloride copolymer, polyvinyl chloride and polymethyl methacrylate, Polyvinyl chloride and acrylonitrile-butadiene-styrene copolymer, polybutylene terephthalate and polyethylene terephthalate, acrylonitrile-butadiene-styrene copolymer and acrylonitrile-styrene copolymer, etc. It is below. Also, a combination of the thermoplastic resin and the same type of modified thermoplastic resin can be used. Examples thereof include polyethylene and silane-modified polyethylene, polyethylene and acrylic acid-modified polypropylene, polyethylene and maleic acid-modified polyethylene, and the like.
【0019】発泡性熱可塑性樹脂組成物に用いられる発
泡剤としては、発泡させながら供給する場合(請求項1
の発明)、熱により化学分解してガスを生成する分解型
発泡剤と、揮発性液体のガス化を利用する物理型発泡剤
が使用できる。また、熱可塑性樹脂を溶融温度以上で混
練しながら二酸化炭素や窒素などのガスを圧入し、熱可
塑性樹脂に分散させ、圧力を開放して発泡させてもよ
い。The foaming agent used in the expandable thermoplastic resin composition is supplied while foaming (claim 1
Invention), a decomposition-type foaming agent that chemically decomposes to generate gas, and a physical-type foaming agent that utilizes gasification of a volatile liquid can be used. Alternatively, while kneading the thermoplastic resin at a melting temperature or higher, a gas such as carbon dioxide or nitrogen may be injected under pressure to disperse the thermoplastic resin, and the pressure may be released for foaming.
【0020】供給した後に発泡させる場合(請求項2及
び3の発明)、分解型発泡剤又は熱可塑性樹脂に揮発性
液体や二酸化炭素や窒素などを発泡剤として溶け込ませ
て分散させた、いわゆる発泡ビーズが使用できる。When foaming after supply (inventions of claims 2 and 3), so-called foaming, in which a volatile liquid, carbon dioxide, nitrogen or the like is dissolved as a foaming agent in a decomposable foaming agent or a thermoplastic resin and dispersed. Beads can be used.
【0021】分解型発泡剤の具体例としては、アゾジカ
ルボンアミド、アゾビスイソブチロニトリル、N,N’
−ジニトロソペンタメチレンテトラミン、pp’−オキ
シビスベンゼンスルホニルヒドラジド、アゾジカルボン
酸バリウム、トリヒドラジノトリアジン、p−トルエン
スルホニルヒドラジド、重炭酸ナトリウム、炭酸アンモ
ニウム等があげられる。物理型発泡剤の具体例として
は、プロパン、ブタン、ペンタン、ヘキサン、ヘプタン
などの脂肪族炭化水素、塩化メチル、二酸化メチレンな
どの塩素化脂肪族炭化水素、1,1−ジクロロ−1−フ
ルオロエタン、2,2−ジクロロ−1,1,1−トリフ
ルオロエタン、1,1,1,2−テトラフルオロエタン
などのフロンガスなどがあげられる。発泡剤の種類によ
って発生するガス量は異なるので、配合量は適宜調整し
なければならないが、熱可塑性樹脂100重量部に対し
て、1〜20重量部の範囲で配合するのが好ましい。発
泡剤の配合量が少なすぎると、発泡体は得られず、また
発泡剤の配合量が多すぎると、セルが破泡して緻密なセ
ルが得られず、得られる繊維強化熱可塑性樹脂発泡体の
曲げ強度が低下する。例えば、アゾジカルボンアミドを
用いて10倍の熱可塑性樹脂発泡体を製造する場合、5
〜7.5重量部混合するのが適当である。Specific examples of the decomposition type foaming agent include azodicarbonamide, azobisisobutyronitrile, N, N '.
-Dinitrosopentamethylenetetramine, pp'-oxybisbenzenesulfonyl hydrazide, barium azodicarboxylate, trihydrazinotriazine, p-toluenesulfonyl hydrazide, sodium bicarbonate, ammonium carbonate and the like. Specific examples of the physical type blowing agent include aliphatic hydrocarbons such as propane, butane, pentane, hexane and heptane, chlorinated aliphatic hydrocarbons such as methyl chloride and methylene dioxide, 1,1-dichloro-1-fluoroethane. , 2,2-dichloro-1,1,1-trifluoroethane, 1,1,1,2-tetrafluoroethane, and other chlorofluorocarbon gas. The amount of gas generated varies depending on the type of the foaming agent, so the amount to be blended must be adjusted appropriately, but it is preferably blended in the range of 1 to 20 parts by weight with respect to 100 parts by weight of the thermoplastic resin. If the blending amount of the foaming agent is too small, a foam cannot be obtained, and if the blending amount of the foaming agent is too large, the cells are broken and a dense cell cannot be obtained, resulting in the fiber-reinforced thermoplastic resin foaming. The bending strength of the body decreases. For example, when a 10-fold thermoplastic resin foam is produced using azodicarbonamide,
It is suitable to mix up to 7.5 parts by weight.
【0022】発泡性熱可塑性樹脂組成物から形成される
発泡芯層の発泡倍率としては、要求される強度や比重、
使用する熱可塑性樹脂の種類などにより適宜選択される
が、1.2〜20倍が好ましく、2〜10倍が特に好ま
しい。発泡倍率が1.2倍未満であると、発泡させるこ
とによる軽量性が低下し、発泡倍率が20倍を超える
と、強度が低下する。The expansion ratio of the foam core layer formed from the expandable thermoplastic resin composition is required strength and specific gravity,
It is appropriately selected depending on the type of thermoplastic resin used, but is preferably 1.2 to 20 times, and particularly preferably 2 to 10 times. When the expansion ratio is less than 1.2 times, the lightness due to foaming is reduced, and when the expansion ratio exceeds 20 times, the strength is reduced.
【0023】請求項3の発明における複合シートは、例
えばつぎのようにして製造される。すなわち、上記方法
で得られた繊維強化熱可塑性樹脂シートの片面に予め製
造された発泡性熱可塑性樹脂組成物シートを加熱融着さ
せるか、又は同繊維強化熱可塑性樹脂シートの片面に未
発泡の発泡性熱可塑性樹脂組成物をシート状に押し出し
て積層することにより、複合シートを得る。The composite sheet according to the invention of claim 3 is manufactured, for example, as follows. That is, the foamable thermoplastic resin composition sheet previously produced on one side of the fiber-reinforced thermoplastic resin sheet obtained by the above method is heat-fused, or the one side of the fiber-reinforced thermoplastic resin sheet is unfoamed. A composite sheet is obtained by extruding the expandable thermoplastic resin composition into a sheet shape and laminating it.
【0024】繊維強化熱可塑性樹脂シートは、単層であ
っても、複数層であってもよい。また、複合シートの場
合、これは繊維強化熱可塑性樹脂層及び発泡性熱可塑性
樹脂組成物層のいずれかが複数層であってもよい。The fiber-reinforced thermoplastic resin sheet may be a single layer or a plurality of layers. Further, in the case of the composite sheet, this may be a plurality of layers of either the fiber reinforced thermoplastic resin layer or the expandable thermoplastic resin composition layer.
【0025】本発明において中空状体には、1枚の繊維
強化熱可塑性樹脂シート又は複合シートの縁部同士を突
き合わせ又は重なり合わせて賦形されたものの他、縁部
同士に若干の隙間が生じている場合も含まれる。In the present invention, the hollow body is formed by abutting or overlapping edges of one fiber-reinforced thermoplastic resin sheet or composite sheet, and a slight gap is formed between the edges. It is also included.
【0026】また、繊維強化熱可塑性樹脂シート及び複
合シートの中空状体への賦形は、シート1枚のみで行な
ってもよいし、複数枚のシートをその幅方向に一部重な
るように並べて行なってもよい。The fiber-reinforced thermoplastic resin sheet and the composite sheet may be shaped into a hollow body by only one sheet, or a plurality of sheets may be arranged so as to partially overlap each other in the width direction. You may do it.
【0027】繊維強化熱可塑性樹脂シート及び複合シー
トを中空状体に賦形する方法としては、シートを合成樹
脂製又は金属製シューや同ロールなどで徐々に曲げてい
く方法があげられ、曲げる際、シートの割れや裂けを防
ぐため、遠赤外線ヒーターや熱風ブロアーで加熱し、熱
可塑性樹脂を軟化状態としながら賦形を行なうことが好
ましい。さらに、シートが徐々に曲げられ、中空状体に
賦形されるような通路を有する金型内に前記シートを通
過させて中空状体に賦形してもよい。As a method for shaping the fiber-reinforced thermoplastic resin sheet and the composite sheet into a hollow body, there is a method of gradually bending the sheet with a synthetic resin or metal shoe or the same roll. In order to prevent the sheet from cracking or tearing, it is preferable that the sheet is heated with a far infrared heater or a hot air blower to perform shaping while the thermoplastic resin is in a softened state. Furthermore, the sheet may be gradually bent and shaped into a hollow body by passing the sheet through a mold having a passage that is shaped into the hollow body.
【0028】ここで軟化状態とは、JIS−K−720
6に準じて測定されたビカット軟化温度以上に、熱可塑
性樹脂が加熱された状態を指す。Here, the softened state means JIS-K-720.
A state in which the thermoplastic resin is heated to a temperature equal to or higher than the Vicat softening temperature measured according to 6.
【0029】請求項1の発明において、賦形した中空状
体内部に発泡性熱可塑性樹脂組成物を発泡させながら連
続的に供給する場合は、押出機内で発泡性熱可塑性樹脂
組成物をガス発生温度以上で混練し、発生したガスを熱
可塑性樹脂に分散させ、発泡性熱可塑性樹脂組成物の溶
融温度以上に温度調節した押出口より中空状体内部に押
し出す。また、熱可塑性樹脂を押出機で溶融温度以上に
混練しながら二酸化炭素や窒素などのガスを圧入し、熱
可塑性樹脂に分散させ、熱可塑性樹脂の溶融温度以上に
温度調節した押出口より中空状体内部に押し出してもよ
い。In the invention of claim 1, when the expandable thermoplastic resin composition is continuously supplied while being foamed inside the shaped hollow body, the expandable thermoplastic resin composition is gas-generated in the extruder. The mixture is kneaded at a temperature or higher, the generated gas is dispersed in a thermoplastic resin, and the gas is extruded into the hollow body through an extrusion port whose temperature is adjusted to the melting temperature or higher of the foamable thermoplastic resin composition. Also, while kneading the thermoplastic resin in the extruder at a temperature higher than the melting temperature, gas such as carbon dioxide or nitrogen is injected under pressure to disperse it in the thermoplastic resin, and it is hollow from the extrusion port whose temperature is adjusted to the melting temperature of the thermoplastic resin or higher. It may be pushed out inside the body.
【0030】請求項2の発明において、中空状体内部に
発泡性熱可塑性樹脂を連続的に供給する方法としては、
熱可塑性樹脂の溶融温度以上かつ発泡剤の分解温度以下
で押出機で溶融混練し押し出す方法や、予め製造した発
泡剤を含有するシート状、ペレット状若しくは棒状の熱
可塑性樹脂組成物又は発泡ビーズを、中空状体内部に連
続的に供給する方法があげられる。In the invention of claim 2, as a method for continuously supplying the foamable thermoplastic resin into the hollow body,
A method of melt-kneading and extruding with an extruder at a melting temperature of a thermoplastic resin or more and a decomposition temperature of a foaming agent or less, and a sheet-shaped, pellet-shaped or rod-shaped thermoplastic resin composition or foamed beads containing a foaming agent produced in advance. The method of continuously supplying the inside of the hollow body can be mentioned.
【0031】請求項2及び3の発明において、発泡性熱
可塑性樹脂組成物を発泡させる方法としては、中空状体
を発泡剤の発泡温度以上に加熱された金型に挿入する方
法や、同中空状体内部に発泡剤の発泡温度以上に加熱さ
れた熱風を吹き込む方法があげられる。In the inventions of claims 2 and 3, as a method of foaming the expandable thermoplastic resin composition, a method of inserting a hollow body into a mold heated to a temperature higher than the foaming temperature of the foaming agent, or the same hollow There is a method of blowing hot air heated above the foaming temperature of the foaming agent into the inside of the body.
【0032】本発明において「発泡温度」とは熱分解型
発泡剤の場合には、その分解温度を、物理型発泡剤の場
合にはその沸点をいう。In the present invention, the "foaming temperature" means the decomposition temperature in the case of a thermal decomposition type foaming agent, and the boiling point in the case of a physical type foaming agent.
【0033】中空状体を周方向に均一に展延させる際
は、繊維強化熱可塑性樹脂シートを構成する熱可塑性樹
脂を軟化状態とすることがあり、又中空状体の展延後の
断面形状は、円形、楕円形、多角形であることが好まし
く、真円形が最も好ましい。なお、多角形の場合は角数
が多いほど好ましい。When the hollow body is evenly spread in the circumferential direction, the thermoplastic resin forming the fiber reinforced thermoplastic resin sheet may be in a softened state, and the cross-sectional shape of the hollow body after spreading Is preferably a circle, an ellipse, or a polygon, and a perfect circle is most preferable. In the case of a polygon, it is preferable that the number of corners is large.
【0034】中空状体を周方向に均一に展延させる方法
としては、金型内面が前方に向かって広がった規制金型
内に中空状体を挿入し、発泡性熱可塑性樹脂組成物の発
泡圧で中空状体を金型内面に押しあてつつ通過させる方
法や、中空状体の周囲から加熱して発泡性熱可塑性樹脂
組成物を発泡させながら中空状体の外周面をロール又は
シユーで周方向に均一に延ばすように規制しつつ展延さ
せる方法があげられる。規制金型内で中空状体を展延さ
せる場合は、中空状体外部からの真空引きや中空状体内
部に別途圧力を加える場合は、規制部材内部に給気用配
管を施し、中空状体内部に気体を供給できるような規制
部材構造とし、内部からの圧空により中空状体の展延を
補助してもよい。As a method for uniformly spreading the hollow body in the circumferential direction, the hollow body is inserted into a regulation mold in which the inner surface of the mold spreads forward, and the foamable thermoplastic resin composition is foamed. A method in which the hollow body is pressed against the inner surface of the mold so as to pass therethrough, or the outer peripheral surface of the hollow body is surrounded by rolls or shoes while heating the periphery of the hollow body to foam the expandable thermoplastic resin composition. There is a method of spreading while controlling so as to uniformly spread in the direction. When expanding the hollow body in the regulation mold, when vacuuming from the outside of the hollow body or when separately applying pressure to the inside of the hollow body, provide air supply piping inside the regulation member and A restricting member structure that allows gas to be supplied to the inside may be used, and the expansion of the hollow body may be assisted by compressed air from the inside.
【0035】中空状体を軟化状態にする方法としては、
中空状体の外形を規制する金型や治具を、ヒーターで熱
可塑性樹脂の軟化温度以上に加熱する方法があげられ
る。また、中空状体内に供給された発泡性熱可塑性樹脂
組成物自体の熱により加熱する方法もあげられる。As a method for making the hollow body soft,
There is a method of heating a mold or a jig that regulates the outer shape of the hollow body with a heater to a temperature not lower than the softening temperature of the thermoplastic resin. In addition, a method of heating with the heat of the expandable thermoplastic resin composition itself supplied into the hollow body is also included.
【0036】本発明において、発泡圧とは、発泡性熱可
塑性樹脂組成物より生じる発泡圧のみならず、つぎの圧
力も含まれる。すなわち、発泡性熱可塑性樹脂組成物の
発泡圧のみでは、中空状体を規制部材に押し付けるだけ
の圧力が得られない場合、別途中空状体内部から圧力を
加え又は中空状体外部から真空圧を付加するが、このよ
うな場合は、その圧力を発泡性熱可塑性樹脂組成物の発
泡圧に付加した圧力をいう。In the present invention, the foaming pressure includes not only the foaming pressure generated from the foamable thermoplastic resin composition but also the following pressures. That is, if the foaming pressure of the expandable thermoplastic resin composition alone does not provide sufficient pressure to press the hollow body against the regulating member, a separate pressure is applied from inside the hollow body or a vacuum pressure is applied from outside the hollow body. In this case, the pressure is added to the foaming pressure of the expandable thermoplastic resin composition.
【0037】中空状体の周方向への展延の程度は、熱可
塑性樹脂の種類、中空状体の肉厚、展延時の温度によっ
て異なるが、繊維強化熱可塑性樹脂表皮層の厚みが、
0.1mm以上になるようにすることが好ましい。0.
1mm未満であると、強度は弱くなり、また、最終断面
形状に賦形する際、繊維強化熱可塑性樹脂中空状体が破
れるおそれがある。The degree of circumferential spreading of the hollow body depends on the type of thermoplastic resin, the wall thickness of the hollow body, and the temperature at the time of spreading, but the thickness of the fiber-reinforced thermoplastic resin skin layer is
It is preferable that the thickness is 0.1 mm or more. 0.
When it is less than 1 mm, the strength becomes weak and the fiber-reinforced thermoplastic resin hollow body may be broken when the final cross-sectional shape is formed.
【0038】本発明では、展延した中空状体を、その外
周長を略一定に保ちつつ変形させて所定の断面形状に賦
形する。この際所定断面形状に賦形する方法は、その外
周長が略一定であれば特に限定されず、例えば、入口形
状が展延された中空状体と同形状であり、出口形状が所
定断面形状であり、金型内面形状が出口形状へと漸次変
化する金型に中空状体を挿入し、金型により外部から規
制しつつ賦形する方法や、前記金型の代わりに、ロール
やシューを用いた賦形方法があげられる。In the present invention, the expanded hollow body is deformed while keeping its outer peripheral length substantially constant and shaped into a predetermined cross-sectional shape. At this time, the method of shaping into a predetermined cross-sectional shape is not particularly limited as long as the outer peripheral length thereof is substantially constant. For example, the shape of the inlet is the same as the expanded hollow body, and the shape of the outlet is the predetermined cross-sectional shape. That is, a hollow body is inserted into a mold in which the inner surface shape of the mold gradually changes to an outlet shape, a method of shaping while controlling from the outside by the mold, or a roll or shoe instead of the mold. The shaping method used may be mentioned.
【0039】展延した中空状体を所定断面形状に賦形す
る際、中空状体を構成する熱可塑性樹脂の軟化温度以上
に保持しておく必要があるが、かかる温度に保持する方
法は、特に限定されず、前記金型、ロール又はシュー等
に加熱機能をもたせ、金型等を加熱する方法等があげら
れる。When shaping the expanded hollow body into a predetermined cross-sectional shape, it is necessary to keep the temperature above the softening temperature of the thermoplastic resin forming the hollow body. The method is not particularly limited, and examples thereof include a method in which the mold, roll, shoe, or the like has a heating function to heat the mold or the like.
【0040】最後に、本発明による繊維強化熱可塑性樹
脂発泡体の製造に用いられる装置の1例を、図1および
2を参照してつぎに説明する。なお、下記の説明におい
て、「前」とは図1の右方を指す。繊維強化熱可塑性樹
脂発泡体の製造装置は、巻き戻しロール(1) を有する繊
維強化熱可塑性樹脂シート繰出機と、その前方に配置せ
られかつ一側方の押出機(2) と連結せられた押出金型
(3) と、押出金型(3) の前に連続状に配置せられた規制
金型(4) と、規制金型(4) の前に連続状に配置せられた
賦形金型(5) と、賦形金型(5) の前方に連続状に配置せ
られ冷却金型(6) と、冷却金型(6) の前方に配置せられ
た引取機(7) とを備えている。Finally, an example of the apparatus used for producing the fiber-reinforced thermoplastic resin foam according to the present invention will be described below with reference to FIGS. 1 and 2. In the following description, “front” refers to the right side of FIG. 1. The fiber reinforced thermoplastic resin foam manufacturing equipment is equipped with a rewind roll (1) and a fiber reinforced thermoplastic resin sheet feeding machine, which is arranged in front of it and is connected to an extruder (2) on one side. Extrusion mold
(3), the regulation die (4) continuously arranged in front of the extrusion die (3), and the shaping die (4) continuously arranged in front of the regulation die (4). 5), a cooling mold (6) continuously arranged in front of the shaping mold (5), and a take-up machine (7) arranged in front of the cooling mold (6). There is.
【0041】押出金型(3) は、通常U字状の入口と、環
状出口とを有しており、入口から出口にかけて、U字状
に変形されて押出金型(3) に挿入された繊維強化熱可塑
性樹脂シート(A1)の両縁を徐々に接近させて最後に両縁
を突き合わせ、又は重ね合せ中空状体となすような通路
(8) が形成されている。押出機(2) は、シート(A1)が完
全に中空状になる手前の位置で押出金型(3) の内コア
(9) と連結せられている。内コア(9) には、この連結部
から押出金型(3) の前端に至るまで直径5mmの円形樹
脂通路(10)が設けられている。そして、内コア(9) に
は、その後端から前端まで貫通する熱風供給路(11)が設
けられており、熱風供給路(11)の後端に図示しない加熱
装置に連結された熱風導管が接続されている。The extrusion die (3) usually has a U-shaped inlet and an annular outlet, and is deformed into a U-shape from the inlet to the outlet and inserted into the extrusion die (3). A passage in which both edges of the fiber reinforced thermoplastic resin sheet (A1) are gradually brought close to each other and finally the both edges are abutted or overlapped to form a hollow body.
(8) is formed. The extruder (2) is located inside the core of the extrusion die (3) before the sheet (A1) becomes completely hollow.
It is linked to (9). The inner core (9) is provided with a circular resin passage (10) having a diameter of 5 mm from this connecting portion to the front end of the extrusion die (3). Then, the inner core (9) is provided with a hot air supply passage (11) penetrating from the rear end to the front end, and a hot air conduit connected to a heating device (not shown) is provided at the rear end of the hot air supply passage (11). It is connected.
【0042】規制金型(4) の内面は、入口側で押出金型
(3) の通路(8) と同じ形状となっているが、出口側では
より大きな相似形状となっている。そして、入口から出
口にかけて金型内面の形状が次第に大きくなるように変
化している。すなわち、金型内面は前方に向かって広が
ったテーパ状となっている。賦形金型(5) の内面は、入
口側で規制金型(4) の出口形状の大きさに合致している
が、出口側では、所定形状、例えば図2に示すような正
方形となっている。そして、入口から出口において次第
に出口形状となるように変化している。冷却金型(6) の
内面は、賦形金型(5) の出口形状の大きさに合致してい
る。なお、規制金型(4) 及び賦形金型(5) はヒーターを
備えており、適当な温度に加熱されるようになってい
る。The inner surface of the regulation die (4) is an extrusion die on the inlet side.
It has the same shape as the passage (8) of (3), but has a larger similar shape on the outlet side. The shape of the inner surface of the mold gradually changes from the entrance to the exit. That is, the inner surface of the mold has a tapered shape that widens forward. The inner surface of the shaping die (5) matches the size of the outlet shape of the regulation die (4) on the inlet side, but on the outlet side it has a predetermined shape, for example, a square as shown in FIG. ing. Then, the shape is gradually changed from the entrance to the exit so as to form the exit shape. The inner surface of the cooling die (6) matches the size of the outlet shape of the shaping die (5). The regulation mold (4) and the shaping mold (5) are equipped with a heater so that they can be heated to an appropriate temperature.
【0043】[0043]
【作用】本発明は、中空状体に賦形した繊維強化熱可塑
性樹脂の内部で発泡性熱可塑性樹脂組成物を発泡させ、
その発泡圧により中空状体を規制しつつ周方向に略均一
に展延させ、展延した中空状体を、その外周長を略一定
に保ちつつ変形させて所定の断面形状に賦形するもので
あるから、均一な厚さの繊維強化熱可塑性樹脂表皮層が
得られ、かつ製品の断面形状も所望のものとなしうる。According to the present invention, the expandable thermoplastic resin composition is foamed inside the fiber-reinforced thermoplastic resin shaped into a hollow body,
By controlling the foaming pressure to expand the hollow body substantially uniformly in the circumferential direction, and deforming the expanded hollow body while maintaining its outer peripheral length substantially constant to shape it into a predetermined cross-sectional shape. Therefore, the fiber-reinforced thermoplastic resin skin layer having a uniform thickness can be obtained, and the cross-sectional shape of the product can be desired.
【0044】繊維強化熱可塑性樹脂層及び発泡性熱可塑
性樹脂組成物層を有する積層シートを、繊維強化熱可塑
性樹脂層が外面となるようにして連続的に中空状体に賦
形し、つぎに内側の発泡性熱可塑性樹脂組成物を発泡さ
せる請求項3の発明では、繊維強化熱可塑性樹脂表皮層
と熱可塑性樹脂発泡芯層との界面に、発泡性熱可塑性樹
脂組成物から生じたガスが進入してボイドが発生するこ
とを防止することができる。A laminated sheet having a fiber-reinforced thermoplastic resin layer and a foamable thermoplastic resin composition layer is continuously shaped into a hollow body so that the fiber-reinforced thermoplastic resin layer is the outer surface, and then In the invention of claim 3 in which the foamable thermoplastic resin composition on the inside is foamed, gas generated from the foamable thermoplastic resin composition is present at the interface between the fiber-reinforced thermoplastic resin skin layer and the thermoplastic resin foam core layer. It is possible to prevent the entry of voids.
【0045】[0045]
【実施例】本発明の実施例を比較例と対比して説明す
る。 実施例1 一方向に揃えた連続強化繊維束4本を、粉体状熱可塑性
樹脂の流動床中を通過させて開繊させながら強化繊維に
粉体状熱可塑性樹脂を付着させて帯状となした後、22
0℃に加熱されたピンチロール間を10kg/cm2 で
加圧加熱しながら通過させ、熱可塑性樹脂を溶融させて
強化繊維相互間に浸入させ、つぎに冷却ピンチロール間
を通過させて冷却し、厚み0.4mm、幅100mm、
繊維含有率23.3重量%の繊維強化熱可塑性樹脂シー
トを得た。EXAMPLES Examples of the present invention will be described in comparison with comparative examples. Example 1 Four continuous reinforcing fiber bundles aligned in one direction are passed through a fluidized bed of a powdery thermoplastic resin to open the fibers, and the powdery thermoplastic resin is attached to the reinforcing fibers to form a band. After doing, 22
Pass through the pinch rolls heated to 0 ° C. while heating under pressure at 10 kg / cm 2 , melt the thermoplastic resin and infiltrate between the reinforcing fibers, and then pass through the cooling pinch rolls to cool. , Thickness 0.4mm, width 100mm,
A fiber reinforced thermoplastic resin sheet having a fiber content of 23.3% by weight was obtained.
【0046】図1〜2に示す装置を用いて繊維強化熱可
塑性樹脂発泡体を製造するのであるが、まず、上記繊維
強化熱可塑性樹脂シート(A1)を繰出機に移し、つぎに、
繰出機の巻き戻しロール(1) から巻き戻された繊維強化
熱可塑性樹脂シート(A1)を200℃に温度調節された押
出金型(3) に挿入し、同金型(3) 内で連続的に中空体に
賦形することにより断面直径31.8mmの真円形の中
空体(A2)となし、賦形された中空体(A2)を180℃に加
熱された規制金型(4) 内に導くとともに、規制金型(4)
内を通過中の中空体(A2)内に押出金型(3) の樹脂通路(1
0)の押出口から発泡性熱可塑性樹脂組成物を発泡させな
がら連続的に押し出して供給し、発泡圧により軟化状態
の中空体(A2)を規制金型(4) の前方に向けて広がったテ
ーパ状内面に押し当ててそわせ、次第に周方向に均一に
展延させ、断面直径47.7mmの真円形となし、つぎ
に展延した中空体(A3)を180℃の賦形金型(5) に導
き、その外周長を一定に保ちつつ変形させて、図2に示
すように、所定の断面形状である一辺37.5mmの正
方形に賦形し、その後冷却金型(6) を通過させて冷却
し、引取機(7) により引き取って熱可塑性樹脂発泡芯層
(B) と繊維強化熱可塑性樹脂表皮層(A4)とを有する断面
が1辺37.5mmの正方形である繊維補強熱可塑性樹
脂発泡体(C) を得た。A fiber-reinforced thermoplastic resin foam is manufactured using the apparatus shown in FIGS. 1 and 2. First, the fiber-reinforced thermoplastic resin sheet (A1) is transferred to a feeding machine, and then,
Insert the fiber reinforced thermoplastic resin sheet (A1) unwound from the unwinding roll (1) of the feeding machine into the extrusion die (3) whose temperature is adjusted to 200 ° C, and continuously in the die (3). The shape of the hollow body (A2) with a cross-sectional diameter of 31.8 mm is achieved by shaping it into a hollow body (A2), and the shaped hollow body (A2) is heated to 180 ° C inside the regulation mold (4). Guide to and regulate molds (4)
Inside the hollow body (A2) passing through the inside, the resin passageway (1) of the extrusion die (3)
The foamable thermoplastic resin composition was continuously extruded and supplied from the extrusion port of (0) while being foamed, and the hollow body (A2) in a softened state was expanded toward the front of the regulation mold (4) by the foaming pressure. Push it against the tapered inner surface and gradually spread it evenly in the circumferential direction to form a true circle with a cross-sectional diameter of 47.7 mm. Then, expand the hollow body (A3) with a shaping mold at 180 ° C ( 5), deform it while keeping the outer circumference constant, and shape it into a square with a side of 37.5 mm, which has a predetermined cross-sectional shape, and then pass through the cooling mold (6), as shown in FIG. Let it cool, then take it off with a take-off machine (7) to form the thermoplastic resin foam core layer.
A fiber-reinforced thermoplastic resin foam (C) having a cross section of (B) and the fiber-reinforced thermoplastic resin skin layer (A4) was a square having a side of 37.5 mm was obtained.
【0047】この実施例において、連続強化繊維として
は、ガラス繊維(日東紡績ガラスロービング、4400
g/km、繊維径23μm)を、粉体状熱可塑性樹脂と
しては、ポリ塩化ビニルに表1の配合を行なったもの
を、発泡性熱可塑性樹脂としては、ポリ塩化ビニルに表
2の配合を行なったものをそれぞれ用いた。なお、配合
はスーパーミキサーを用いて樹脂温度が100度になる
まで行なった。In this example, the continuous reinforcing fibers were glass fibers (Nitto Spinning Glass Roving, 4400).
g / km, fiber diameter 23 μm), as the powdery thermoplastic resin, polyvinyl chloride compounded in Table 1 is used, and as the foamable thermoplastic resin, polyvinyl chloride compounded in Table 2 is used. What was done was used respectively. The blending was performed using a super mixer until the resin temperature reached 100 degrees.
【0048】[0048]
【表1】 [Table 1]
【0049】[0049]
【表2】 [Table 2]
【0050】実施例2 押出金型の調節温度を170℃としたこと、押出金型の
樹脂通路の押出口から発泡性熱可塑性樹脂組成物を発泡
させずに押し出し、押し出し後発泡させたこと以外は実
施例1と同様にして断面正方形の繊維強化熱可塑性樹脂
発泡体を得た。 実施例3 実施例1の繊維強化熱可塑性樹脂シートの代わりに、繊
維強化熱可塑性樹脂層及び発泡性熱可塑性樹脂組成物層
を有する複合シートを用い、同複合シートを繊維強化熱
可塑性樹脂層が外面となるようにして中空体に賦形する
こと、実施例2の押し出された発泡性熱可塑性樹脂組成
物の代わりに、賦形された中空体の内側の発泡性熱可塑
性樹脂組成物を発泡させること、前記複合シートが、表
2の配合を行なったポリ塩化ビニルを、押出機から17
0℃に温度調節されたシート成形金型を通過させ、発泡
させずに押し出しながら実施例1の繊維強化熱可塑性樹
脂シートに積層したものであること以外は実施例2と同
様にして断面正方形の繊維強化熱可塑性樹脂発泡体を得
た。Example 2 Except that the controlling temperature of the extrusion die was 170 ° C., the expandable thermoplastic resin composition was extruded from the extrusion opening of the resin passage of the extrusion die without foaming, and foamed after extrusion. A fiber-reinforced thermoplastic resin foam having a square cross section was obtained in the same manner as in Example 1. Example 3 Instead of the fiber-reinforced thermoplastic resin sheet of Example 1, a composite sheet having a fiber-reinforced thermoplastic resin layer and a foamable thermoplastic resin composition layer was used, and the fiber-reinforced thermoplastic resin layer was used as the composite sheet. Forming into a hollow body so that it becomes the outer surface, and instead of the extruded expandable thermoplastic resin composition of Example 2, foam the expandable thermoplastic resin composition inside the formed hollow body. Then, the composite sheet was prepared by mixing the polyvinyl chloride compounded in Table 2 with an extruder.
A sheet having a square cross section was obtained in the same manner as in Example 2 except that the sheet was passed through a sheet forming mold whose temperature was adjusted to 0 ° C. and was extruded without foaming and laminated on the fiber-reinforced thermoplastic resin sheet of Example 1. A fiber reinforced thermoplastic resin foam was obtained.
【0051】比較例1 実施例1で用いた装置のうち、規制金型及び賦形金型を
除き、代わりに規制金型及び賦形金型の位置に、31.
8mmの真円形入口から1辺37.5mmの正方形出口
まで徐々に変化された金型内面を有する賦形金型を配置
し、繰出機の巻き戻しロールから巻き戻された繊維強化
熱可塑性樹脂シートを200℃に温度調節された押出金
型に挿入し、同金型内で連続的に中空状に賦形すること
により中空体となし、賦形された中空体を180℃に加
熱された賦形金型内に導くとともに、賦形金型内を通過
中の中空体内に押出金型の樹脂通路の押出口から発泡性
熱可塑性樹脂組成物を発泡させながら連続的に押し出し
て供給し、発泡圧により軟化状態の中空体を賦形金型の
内面に押し当ててそわせ、図2に示すように正方形に賦
形し、その後冷却金型を通過させて冷却し、引取機によ
り引き取って熱可塑性樹脂発泡芯層と繊維強化熱可塑性
樹脂表皮層とを有する1辺が37.5mmである断面正
方形の繊維強化熱可塑性樹脂発泡体を得た。Comparative Example 1 In the apparatus used in Example 1, except for the restriction mold and the shaping mold, 31.
A fiber-reinforced thermoplastic resin sheet in which a shaping mold having a mold inner surface gradually changed from a true circular inlet of 8 mm to a square outlet of 37.5 mm on a side is arranged and unwound from a rewinding roll of a feeding machine. Was inserted into an extrusion mold whose temperature was adjusted to 200 ° C., and a hollow body was formed by continuously forming a hollow body in the mold, and the shaped hollow body was heated to 180 ° C. The foamable thermoplastic resin composition is continuously extruded and fed from the extrusion port of the resin passage of the extrusion die into the hollow body passing through the shaping die while being guided into the shaping die and foamed. The softened hollow body is pressed against the inner surface of the shaping mold by pressure, shaped into a square as shown in FIG. 2, then passed through a cooling mold to cool, and then taken up by a take-up machine to generate heat. Has a plastic resin foam core layer and a fiber-reinforced thermoplastic resin skin layer That one side was obtained fiber-reinforced thermoplastic resin foam square cross section is 37.5 mm.
【0052】比較例2 押出金型の温度を170℃、賦形金型の温度を220℃
としたこと、押出金型の樹脂通路の押出口から発泡性熱
可塑性樹脂組成物を発泡させずに押し出し、押し出し後
発泡させたこと以外は比較例1と同様にして断面正方形
の繊維強化熱可塑性樹脂発泡体を得た。Comparative Example 2 The temperature of the extrusion die was 170 ° C. and the temperature of the shaping die was 220 ° C.
In the same manner as in Comparative Example 1 except that the expandable thermoplastic resin composition was extruded from the extrusion opening of the resin passage of the extrusion die without foaming and was extruded and then foamed, the fiber-reinforced thermoplastic resin having a square cross section was used. A resin foam was obtained.
【0053】比較例3 実施例3の複合シートを用い、同複合シートを繊維強化
熱可塑性樹脂層が外面となるようにして中空体に賦形す
ること、比較例2の押出された発泡性熱可塑性樹脂組成
物の代わりに賦形せられた中空体の内側の発泡性熱可塑
性樹脂組成物を発泡させること以外比較例2と同様にし
て断面正方形の繊維強化熱可塑性樹脂発泡体を得た。Comparative Example 3 Using the composite sheet of Example 3, the composite sheet was shaped into a hollow body so that the fiber reinforced thermoplastic resin layer was on the outer surface, and the extruded foamable heat of Comparative Example 2 was used. A fiber-reinforced thermoplastic resin foam having a square cross section was obtained in the same manner as in Comparative Example 2 except that the expandable thermoplastic resin composition inside the shaped hollow body was foamed instead of the plastic resin composition.
【0054】各実施例及び比較例で得られた製品におけ
る発泡芯層の発泡倍率は3.5倍であった。各実施例及
び各比較例の製品の端面を観察すると、繊維強化熱可塑
性樹脂表皮層の厚みは、各実施例のものでは均一であっ
たのに比べ、比較例のものではばらつきがあり、薄い部
分があった。The expansion ratio of the foam core layer in the products obtained in each of the examples and comparative examples was 3.5. When observing the end faces of the products of each example and each comparative example, the thickness of the fiber-reinforced thermoplastic resin skin layer was uniform in each of the examples, but varied in the comparative examples and thin. There was a part.
【0055】上記各繊維強化熱可塑性樹脂発泡体の繊維
強化熱可塑性樹脂表皮層の厚みをつぎの3点で測定し、
その結果を表3に示す。 イ点…頂点から0.5mmの箇所 ロ点…一辺の中心箇所 ハ点…イ点とロ点間の中心箇所The thickness of the fiber-reinforced thermoplastic resin skin layer of each of the fiber-reinforced thermoplastic resin foams was measured at the following three points,
Table 3 shows the results. Point a: 0.5 mm from the apex Point b: central point on one side C point: central point between points a and b
【表3】 以上の結果より、本発明の製造方法で得られた繊維強化
熱可塑性樹脂発泡体では、繊維強化熱可塑性樹脂表皮層
の厚みにばらつきがないことは明らかである。上記得ら
れた任意の20の繊維強化熱可塑性樹脂発泡体について
3点曲げ試験を行ない、その平均曲げ強度及びその標準
偏差を表4に示す。[Table 3] From the above results, it is clear that the fiber-reinforced thermoplastic resin foam obtained by the production method of the present invention has no variation in the thickness of the fiber-reinforced thermoplastic resin skin layer. A 20-point fiber-reinforced thermoplastic resin foam obtained above was subjected to a 3-point bending test, and its average bending strength and its standard deviation are shown in Table 4.
【0056】3点曲げ試験結果は、支点間距離:120
0mm、試験速度:20mm/分とした。The result of the three-point bending test is: distance between fulcrums: 120
The test speed was 0 mm and the test speed was 20 mm / min.
【表4】 以上の結果より、本発明の製造方法で得られた繊維強化
熱可塑性樹脂発泡体では、曲げ強度にばらつきがないこ
とは明らかである。[Table 4] From the above results, it is clear that the fiber-reinforced thermoplastic resin foam obtained by the production method of the present invention has no variation in bending strength.
【0057】[0057]
【発明の効果】本発明によれば、均一な厚さの繊維強化
熱可塑性樹脂表皮層が得られるから、製造された繊維強
化樹脂発泡体は、均一な曲げ強度を有し、しかもその断
面形状を複雑なものを含め所望のものとなすことができ
る。とくに、請求項3の発明によれば、上記の外に、さ
らに繊維強化熱可塑性樹脂表皮層と熱可塑性樹脂発泡芯
層との界面に発泡性樹脂組成物から発生したガスが浸入
し、ボイドが生じるのを防止することができるため、繊
維強化熱可塑性樹脂表皮層と熱可塑性樹脂発泡芯層との
融着性が優れた繊維強化熱可塑性樹脂発泡体を得ること
ができる。According to the present invention, since a fiber-reinforced thermoplastic resin skin layer having a uniform thickness can be obtained, the produced fiber-reinforced resin foam has a uniform bending strength and a cross-sectional shape thereof. Can be as complex or as desired. In particular, according to the invention of claim 3, in addition to the above, gas generated from the foamable resin composition penetrates into the interface between the fiber-reinforced thermoplastic resin skin layer and the thermoplastic resin foam core layer, and voids are generated. Since it can be prevented from occurring, it is possible to obtain a fiber-reinforced thermoplastic resin foam having excellent fusion bonding property between the fiber-reinforced thermoplastic resin skin layer and the thermoplastic resin foam core layer.
【図面の簡単な説明】[Brief description of drawings]
【図1】本発明の方法の実施に用いられる繊維強化熱可
塑性樹脂発泡体の製造装置の1例を示す一部切り欠き平
面図である。FIG. 1 is a partially cutaway plan view showing an example of an apparatus for producing a fiber-reinforced thermoplastic resin foam used for carrying out the method of the present invention.
【図2】図1のII−II線にそう拡大断面図である。FIG. 2 is an enlarged sectional view taken along line II-II of FIG.
(3) :押出金型 (4) :規制金型 (5) :賦形金型 (6) :冷却金型 (A1):繊維強化熱可塑性樹脂シート (A2):中空体 (A3):展延した中空体 (A4):繊維強化熱可塑性樹脂表皮層 (B) :熱可塑性樹脂発泡芯層 (C) :繊維強化熱可塑性樹脂発泡体 (3): Extrusion die (4): Controlling die (5): Forming die (6): Cooling die (A1): Fiber reinforced thermoplastic resin sheet (A2): Hollow body (A3): Expansion Expanded hollow body (A4): Fiber-reinforced thermoplastic resin skin layer (B): Thermoplastic resin foam core layer (C): Fiber-reinforced thermoplastic resin foam
フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29K 105:04 105:06 B29L 9:00 Continuation of front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location B29K 105: 04 105: 06 B29L 9:00
Claims (3)
中空状体に賦形する工程と、中空状体内部に熱可塑性樹
脂及び発泡剤からなる発泡性熱可塑性樹脂組成物を発泡
させながら連続的に供給し、その発泡圧により中空状体
を規制しつつ周方向に略均一に展延させる工程と、展延
した中空状体を、その外周長を略一定に保ちつつ変形さ
せて所定の断面形状に賦形する工程とを含むことを特徴
とする繊維強化熱可塑性樹脂発泡体の製造方法。1. A step of continuously shaping a fiber-reinforced thermoplastic resin sheet into a hollow body, and continuously forming a foamable thermoplastic resin composition containing a thermoplastic resin and a foaming agent inside the hollow body. Of the hollow body is controlled by the foaming pressure and is spread substantially uniformly in the circumferential direction, and the spread hollow body is deformed while keeping the outer circumference substantially constant. And a step of shaping the fiber-reinforced thermoplastic resin foam into a cross-sectional shape.
中空状体に賦形する工程と、中空状体内部に熱可塑性樹
脂及び発泡剤からなる発泡性熱可塑性樹脂組成物を連続
的に供給する工程と、発泡性熱可塑性樹脂組成物を発泡
させ、その発泡圧により中空状体を規制しつつ周方向に
略均一に展延させる工程と、展延した中空状体を、その
外周長を略一定に保ちつつ変形させて所定の断面形状に
賦形する工程とを含むことを特徴とする繊維強化熱可塑
性樹脂発泡体の製造方法。2. A step of continuously shaping a fiber-reinforced thermoplastic resin sheet into a hollow body, and continuously supplying a foamable thermoplastic resin composition containing a thermoplastic resin and a foaming agent inside the hollow body. And the step of foaming the expandable thermoplastic resin composition, and substantially uniformly spreading in the circumferential direction while controlling the hollow body by the foaming pressure, and the expanded hollow body, the outer peripheral length A method for producing a fiber-reinforced thermoplastic resin foam, comprising the step of deforming while maintaining substantially constant and shaping into a predetermined cross-sectional shape.
樹脂及び発泡剤からなる発泡性熱可塑性樹脂組成物層を
有する複合シートを、繊維強化熱可塑性樹脂層が外面と
なるようにして連続的に中空状体に賦形する工程と、発
泡性熱可塑性樹脂組成物を発泡させ、その発泡圧により
中空状体を規制しつつ周方向に略均一に展延させる工程
と、展延した中空状体を、その外周長を略一定に保ちつ
つ変形させて所定の断面形状に賦形する工程とを含むこ
とを特徴とする繊維強化熱可塑性樹脂発泡体の製造方
法。3. A composite sheet having a fiber-reinforced thermoplastic resin layer and a foamable thermoplastic resin composition layer comprising a thermoplastic resin and a foaming agent is continuously prepared with the fiber-reinforced thermoplastic resin layer being the outer surface. A step of forming a hollow body into a hollow body, a step of foaming the expandable thermoplastic resin composition, and a step of spreading the foamable thermoplastic resin composition substantially uniformly in the circumferential direction while regulating the hollow body by the foaming pressure; And a step of deforming the body into a predetermined cross-sectional shape while keeping the outer peripheral length of the body substantially constant, and manufacturing the fiber-reinforced thermoplastic resin foam.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6322170A JPH08174698A (en) | 1994-12-26 | 1994-12-26 | Manufacture of fiber-reinforced thermoplastic resin foam |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6322170A JPH08174698A (en) | 1994-12-26 | 1994-12-26 | Manufacture of fiber-reinforced thermoplastic resin foam |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08174698A true JPH08174698A (en) | 1996-07-09 |
Family
ID=18140723
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6322170A Pending JPH08174698A (en) | 1994-12-26 | 1994-12-26 | Manufacture of fiber-reinforced thermoplastic resin foam |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08174698A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014208420A (en) * | 2013-03-29 | 2014-11-06 | 積水化成品工業株式会社 | Method for producing fiber reinforced composite and fiber reinforced composite |
-
1994
- 1994-12-26 JP JP6322170A patent/JPH08174698A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014208420A (en) * | 2013-03-29 | 2014-11-06 | 積水化成品工業株式会社 | Method for producing fiber reinforced composite and fiber reinforced composite |
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