JP2000263624A - Manufacture of extrusion foamed composite, and foamed composite - Google Patents
Manufacture of extrusion foamed composite, and foamed compositeInfo
- Publication number
- JP2000263624A JP2000263624A JP11073506A JP7350699A JP2000263624A JP 2000263624 A JP2000263624 A JP 2000263624A JP 11073506 A JP11073506 A JP 11073506A JP 7350699 A JP7350699 A JP 7350699A JP 2000263624 A JP2000263624 A JP 2000263624A
- Authority
- JP
- Japan
- Prior art keywords
- core material
- resin
- die
- foaming
- skin
- 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.)
- Granted
Links
- 239000002131 composite material Substances 0.000 title claims abstract description 71
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 18
- 238000001125 extrusion Methods 0.000 title claims abstract description 10
- 239000011162 core material Substances 0.000 claims abstract description 163
- 239000000463 material Substances 0.000 claims abstract description 106
- 239000006260 foam Substances 0.000 claims abstract description 97
- 229920005989 resin Polymers 0.000 claims abstract description 93
- 239000011347 resin Substances 0.000 claims abstract description 93
- 238000005187 foaming Methods 0.000 claims abstract description 61
- 238000001816 cooling Methods 0.000 claims abstract description 21
- 238000000034 method Methods 0.000 claims abstract description 21
- 238000004513 sizing Methods 0.000 claims abstract description 16
- 238000000576 coating method Methods 0.000 claims abstract description 3
- 239000011248 coating agent Substances 0.000 claims abstract 2
- 229920005992 thermoplastic resin Polymers 0.000 claims description 41
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 26
- 239000004088 foaming agent Substances 0.000 claims description 21
- 229920002725 thermoplastic elastomer Polymers 0.000 claims description 11
- 239000002667 nucleating agent Substances 0.000 claims description 9
- 229920005990 polystyrene resin Polymers 0.000 claims description 9
- FACXGONDLDSNOE-UHFFFAOYSA-N buta-1,3-diene;styrene Chemical group C=CC=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 FACXGONDLDSNOE-UHFFFAOYSA-N 0.000 claims description 8
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 claims description 8
- 229920001935 styrene-ethylene-butadiene-styrene Polymers 0.000 claims description 7
- 150000001336 alkenes Chemical class 0.000 claims description 6
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 6
- 239000006261 foam material Substances 0.000 claims description 3
- 239000010410 layer Substances 0.000 description 22
- 210000004027 cell Anatomy 0.000 description 10
- 230000000694 effects Effects 0.000 description 10
- 210000000497 foam cell Anatomy 0.000 description 9
- 230000004927 fusion Effects 0.000 description 9
- -1 for example Substances 0.000 description 8
- 238000000465 moulding Methods 0.000 description 7
- 239000000126 substance Substances 0.000 description 5
- 239000004743 Polypropylene Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 229920001155 polypropylene Polymers 0.000 description 4
- 239000000454 talc Substances 0.000 description 4
- 229910052623 talc Inorganic materials 0.000 description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004604 Blowing Agent 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
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000010097 foam moulding Methods 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 239000013585 weight reducing agent Substances 0.000 description 2
- DEIGXXQKDWULML-UHFFFAOYSA-N 1,2,5,6,9,10-hexabromocyclododecane Chemical compound BrC1CCC(Br)C(Br)CCC(Br)C(Br)CCC1Br DEIGXXQKDWULML-UHFFFAOYSA-N 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 239000004156 Azodicarbonamide Substances 0.000 description 1
- PMPVIKIVABFJJI-UHFFFAOYSA-N Cyclobutane Chemical compound C1CCC1 PMPVIKIVABFJJI-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 1
- 235000019399 azodicarbonamide Nutrition 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000012792 core layer Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 description 1
- 238000007731 hot pressing Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- FTQWRYSLUYAIRQ-UHFFFAOYSA-N n-[(octadecanoylamino)methyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCNC(=O)CCCCCCCCCCCCCCCCC FTQWRYSLUYAIRQ-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920005668 polycarbonate resin Polymers 0.000 description 1
- 239000004431 polycarbonate resin Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012508 resin bead Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910001868 water Inorganic materials 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Molding Of Porous Articles (AREA)
Abstract
Description
【0001】[0001]
【技術分野】本発明は,土木,建材等の分野,例えばコ
ンクリート型枠,壁材,床材,天井材,棚材等に使用さ
れる発泡複合体,即ち発泡状態にある芯材(発泡芯材)
に表皮材を被覆してなる発泡複合体及びその製造方法に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a foam composite used in the fields of civil engineering and construction materials, for example, concrete forms, walls, floors, ceilings, shelves, etc. Material)
And a method for producing the same.
【0002】[0002]
【従来技術】従来より,発泡剤を含有させた熱可塑性樹
脂を押出機から押し出し,発泡させて芯材とし,該芯材
の外周に表皮材を被覆して,発泡複合体とする方法が知
られている。押し出し発泡は連続的に発泡体を製造する
ことができるので生産量,製造コスト面で有利で有り,
広く行われている。2. Description of the Related Art Conventionally, there has been known a method in which a thermoplastic resin containing a foaming agent is extruded from an extruder, foamed to form a core material, and a skin material is coated on the outer periphery of the core material to form a foamed composite. Have been. Extrusion foaming is advantageous in terms of production volume and production cost because foam can be produced continuously.
Widely used.
【0003】ところが,押し出し発泡によって,厚みの
大きい芯材を所望の形状どおりに作ること,またその芯
材に表皮材を被覆することは困難である。それは,発泡
剤を含んだ芯材用発泡性樹脂を正確に板状等の形状に押
し出しても,押し出された芯材用発泡性樹脂は押出機の
ダイスを出た直後に発泡する。そのため,押し出し物
は,三次元的に膨れて,目的とする形状から大きく変形
湾曲するからである。従って,こうして得られた発泡芯
材を所望の形状にするには,切削や熱プレスによってそ
の形状を矯正し,使用することになる。そのため発泡複
合体の製造工程が煩雑であると共に材料に無駄が多い。However, it is difficult to form a thick core material into a desired shape by extrusion foaming and to cover the core material with a skin material. That is, even if the foaming resin for the core material containing the foaming agent is accurately extruded into a plate shape or the like, the extruded foamable resin for the core material foams immediately after exiting the die of the extruder. Therefore, the extruded material swells three-dimensionally and largely deforms and curves from the desired shape. Therefore, in order to make the foam core material thus obtained into a desired shape, the shape is corrected by cutting or hot pressing and used. Therefore, the manufacturing process of the foamed composite is complicated, and the material is wasteful.
【0004】このような煩雑と無駄を解消するために,
予め成形した発泡プラスチックの長尺体を押出機に入
れ,ダイスを用いて表皮材を被覆し,所望の形状にし,
複合体の表面強度,曲げ強度を改善する方法(例えば特
開平8−336876号公報)がある。しかしながら,
この方法は,予め成形した発泡体を用いるため工程が2
工程になり製造コストが高くなる欠点がある。In order to eliminate such complexity and waste,
A long body of foamed plastic molded in advance is put into an extruder, and the skin material is covered with a die to obtain a desired shape.
There is a method for improving the surface strength and bending strength of a composite (for example, Japanese Patent Application Laid-Open No. 8-336876). However,
This method requires two steps because a preformed foam is used.
There is a disadvantage that the process becomes a process and the production cost increases.
【0005】また,特開平4−282237号公報にお
いては,発泡体の表面にスキン層を得るために,発泡体
を押し出しホーミングダイで低温に冷却する,スキン層
付き発泡体の製造方法が示されている。しかし,この方
法では,スキン層が非常に薄く0.5mm以上の肉厚の
スキン層を得ることは困難である。Japanese Patent Application Laid-Open No. 4-282237 discloses a method for producing a foam with a skin layer, in which the foam is extruded and cooled to a low temperature with a homing die in order to obtain a skin layer on the surface of the foam. ing. However, in this method, it is difficult to obtain a skin layer having a very small skin layer and a thickness of 0.5 mm or more.
【0006】更に,特開平2−194922号公報にお
いては,内部が発泡樹脂層でその外周全体を非発泡樹脂
層で被覆する方法が示されている。しかし,この方法で
は芯材である発泡体と表皮材がダイス内で合流するため
に,発泡樹脂の温度が被覆する表皮材の温度近くに上昇
する。そのため,発泡樹脂の溶融粘度も下がりダイス内
の樹脂圧力も低下し,目標密度0.14〜0.02g/
l(リットル)という高発泡倍率の芯材を得ようとして
も,発泡体のセルの均一性,独立性が不充分となり,発
泡複合体として満足のいくものが得られない。また,押
出し発泡複合体には,軽量であると共に,その使用時に
おける強度確保のため剛性が高いことも要求される。Further, Japanese Patent Application Laid-Open No. 2-194922 discloses a method in which the inside is covered with a foamed resin layer and the entire outer periphery is covered with a non-foamed resin layer. However, in this method, the temperature of the foamed resin rises close to the temperature of the skin material to be coated, because the foam material as the core material and the skin material merge in the die. As a result, the melt viscosity of the foamed resin also decreases, and the resin pressure in the die also decreases, resulting in a target density of 0.14 to 0.02 g /
Even if an attempt is made to obtain a core material having a high expansion ratio of 1 (liter), the uniformity and independence of the cells of the foam become insufficient, and a satisfactory foam composite cannot be obtained. In addition, the extruded foam composite is required to be lightweight and have high rigidity in order to secure strength during use.
【0007】[0007]
【解決しようとする課題】本発明はかかる従来の問題点
に鑑みてなされたもので,発泡セルの均一性,独立気泡
性が良好で,高発泡倍率の芯材を有し,かつ軽量で剛性
の高い,押出し発泡複合体及びその製造方法を提供しよ
うとするものである。DISCLOSURE OF THE INVENTION The present invention has been made in view of the above-mentioned conventional problems, and has uniformity of foam cells, good closed cell properties, a core material having a high expansion ratio, light weight and rigidity. An extruded foam composite having a high hardness and a method for producing the same are provided.
【0008】[0008]
【課題の解決手段】請求項1の発明は,発泡剤を含有さ
せた熱可塑性樹脂よりなる芯材用発泡性樹脂を第1押出
機の第1ダイスから押し出し,一方非発泡熱可塑性樹脂
又は低発泡性熱可塑性樹脂よりなる表皮材を第2押出機
の第2ダイスから押し出し,両押出機の先端に設けた上
記第1ダイス及び第2ダイスの外部において,上記芯材
用発泡性樹脂からなる芯材の外周に上記表皮材を被覆し
てなる発泡複合体を押出成形する方法であって,上記第
1ダイスからは,複数列かつ複数段に配置したノズルよ
り,上記芯材用発泡性樹脂を押出すと共に発泡させて芯
材を形成しながら,一方上記第2ダイスから上記表皮材
を上記芯材の外側に押出すと共に該表面材を直ちに冷却
サイジングに導き,上記芯材用発泡性樹脂の発泡力によ
って上記表皮材を上記冷却サイジングの内面に押し当て
て,上記芯材用発泡性樹脂によって形成された複数列か
つ複数段の芯材よりなる発泡体の外表面に上記表皮材を
被覆してなる押出し発泡複合体を製造することを特徴と
する押し出し発泡複合体の製造方法である。According to the first aspect of the present invention, a foaming resin for a core made of a thermoplastic resin containing a foaming agent is extruded from a first die of a first extruder. A skin material made of an expandable thermoplastic resin is extruded from a second die of a second extruder, and is made of the foamable resin for a core material outside the first die and the second die provided at the tip of both extruders. A method of extrusion-molding a foamed composite comprising the core material and the outer skin material covered with the skin material, wherein the first die is provided with a plurality of nozzles arranged in a plurality of rows and a plurality of stages to form the foamable resin for a core material. While the core material is formed by extruding and foaming the core material, the surface material is extruded from the second die to the outside of the core material, and the surface material is immediately led to cooling sizing, and the foamable resin for the core material is formed. Of the above skin material by the foaming power of The extruded foam composite is obtained by covering the outer surface of a foam consisting of a plurality of rows and a plurality of stages of a core material formed of the above foamable resin for the core material by pressing against the inner surface of the cooling sizing. A method for producing an extruded foam composite, which is characterized by being produced.
【0009】本発明において最も注目すべき点は,上記
芯材用発泡性樹脂を上記第1ダイスのノズルから複数列
かつ複数段に連続的に押し出すと共に,一方上記表皮材
を第2押出機の上記第2ダイスから連続的に押し出し,
芯材用発泡性樹脂は発泡させて複数列かつ複数段の芯材
からなる発泡体となし,一方表皮材は上記発泡体の外周
に被覆させていくこと,次いで直ちに冷却サイジングに
おいて所望形状に冷却賦形することである。The most notable point in the present invention is that the foamable resin for the core material is continuously extruded from the nozzle of the first die in a plurality of rows and a plurality of stages, while the skin material is extruded by a second extruder. Continuously extruded from the second die,
The foaming resin for the core material is foamed to form a foam consisting of a plurality of rows and a plurality of stages of the core material, while the skin material is coated on the outer periphery of the foam, and then immediately cooled to a desired shape by cooling sizing. It is shaping.
【0010】本発明においては,複数列かつ複数段に押
出した芯材用発泡性樹脂を第1ダイスの出口において発
泡させ,この発泡により得た芯材の周囲に上記表皮材を
被覆していく。そのため,芯材における発泡セルが均一
となり,また発泡セル膜が破れることなく独立気泡性を
有する,高倍率の発泡体が得られる。もしも,ダイス内
において芯材用発泡性樹脂の周囲に表皮材を合流させ
て,芯材用発泡性樹脂を表皮材により被覆したり,ダイ
ス内において芯材用発泡性樹脂を発泡させてダイス内で
表皮材を被覆する場合には,上記のごとき効果を得るこ
とはできない。In the present invention, the foaming resin for the core material extruded in a plurality of rows and a plurality of stages is foamed at the outlet of the first die, and the skin material is coated around the core material obtained by the foaming. . As a result, a foam having a high magnification can be obtained in which the foamed cells in the core material are uniform and the foamed cell membrane has closed cells without breaking. If a skin material is joined around the foamable resin for the core material in the die, the foamable resin for the core material is covered with the skin material, or the foamable resin for the core material is foamed in the die, and the inside of the die is expanded. In the case of covering the skin material with the above, the above effects cannot be obtained.
【0011】また,上記のごとき優れた芯材からなる発
泡体の表面に,芯材の発泡と殆ど同時に表皮材を被覆す
る。そのため,表皮材と発泡体の融着及び芯材同志の融
着が確実にできるという効果を得ることができる。ま
た,各ノズルから押出され発泡した芯材は複数列かつ複
数段に形成されると共に互いに隣接する芯材と融着して
いる。そのため,押出し発泡複合体の剛性も向上する。
また,押出し発泡複合体は,発泡体と表皮材とからなる
ので軽量である。Further, the surface of the foam made of the excellent core material is coated with the skin material almost simultaneously with the foaming of the core material. Therefore, it is possible to obtain an effect that fusion between the skin material and the foam and fusion between the core materials can be reliably performed. The core material extruded and foamed from each nozzle is formed in a plurality of rows and a plurality of stages, and is fused to the core materials adjacent to each other. Therefore, the rigidity of the extruded foam composite is also improved.
Also, the extruded foam composite is lightweight because it is composed of a foam and a skin material.
【0012】したがって,本発明によれば,発泡セルの
均一性,独立気泡性が良好で,高発泡倍率の芯材を有
し,かつ軽量で剛性の高い,押出し発泡複合体の製造方
法を提供することができる。Therefore, according to the present invention, there is provided a method for producing an extruded foamed composite which is excellent in uniformity and closed-cell properties of foam cells, has a core material having a high expansion ratio, is lightweight and has high rigidity. can do.
【0013】上記冷却サイジングとは,所望の形状を得
るための冷却型による成形をいう。また,所望形状に冷
却賦形とは,表皮材を冷却サイジングで冷却しながら,
芯材用発泡性樹脂の発泡圧で,発泡複合体の冷却サイジ
ングへの密着度を高めることにより,冷却しながら賦形
することをいう。The above-mentioned cooling sizing refers to molding by a cooling mold to obtain a desired shape. In addition, cooling shaping to the desired shape means that the skin material is cooled by cooling sizing,
Forming while cooling by increasing the degree of adhesion of the foamed composite to cooling sizing by the foaming pressure of the foamable resin for the core material.
【0014】上記の表皮材としては,非発泡性又は低発
泡性の熱可塑性樹脂を用いる。上記非発泡性熱可塑性樹
脂は発泡剤を用いず,低発泡性熱可塑性樹脂は少量の発
泡剤を用いる。そして,上記熱可塑性樹脂としては,ポ
リスチレン,アクリル・ブタジェン・スチレン(AB
S),樹脂等のスチレン系樹脂,各種ポリエチレン,ポ
リプロピレン樹脂,ポリプロとαオレフィンとの共重合
体等のポリオレフィン系樹脂,ポリ塩化ビニル樹脂,酢
酸ビニル樹脂,各種ナイロン樹脂,各種アクリル樹脂,
ポリカーボネート樹脂,及びこれらの混合樹脂がある。
また,これらの樹脂に充填剤例えばタルク,炭酸カルシ
ュウム,マイカ等を添加したり,各種顔料を添加して用
いることができる。As the skin material, a non-foaming or low-foaming thermoplastic resin is used. The non-foamable thermoplastic resin does not use a foaming agent, and the low-foamable thermoplastic resin uses a small amount of a foaming agent. As the thermoplastic resin, polystyrene, acrylic butadiene styrene (AB)
S), styrene resins such as resins, various polyethylenes, polypropylene resins, polyolefin resins such as copolymers of polypropylene and α-olefin, polyvinyl chloride resins, vinyl acetate resins, various nylon resins, various acrylic resins,
There are polycarbonate resins and their mixed resins.
In addition, fillers such as talc, calcium carbonate, mica, and the like can be added to these resins, or various pigments can be used.
【0015】この発明方法が特に効果を発揮するのは,
スチレン系樹脂,或いはポリプロピレン樹脂に充填剤を
添加した樹脂である。この場合には,剛性が高く,比較
的安価である。また,製品の外観を良好にするために,
前述した表皮材に少量の発泡剤を添加して,低発泡体と
して使用することが好ましい。The present method is particularly effective because
A resin obtained by adding a filler to a styrene resin or a polypropylene resin. In this case, the rigidity is high and the cost is relatively low. Also, in order to improve the appearance of the product,
It is preferable to add a small amount of a foaming agent to the above-mentioned skin material and use it as a low foamed body.
【0016】また,上記の芯材用発泡性樹脂としては,
発泡剤を含有させた熱可塑性樹脂を用いる。該熱可塑性
樹脂としては,上記表皮材について示した熱可塑性樹脂
と同様のものを用いることができる。また,上記発泡剤
としては,プロパン,n−ブタン,i−ブタン,ペンタ
ン,ヘキサン等の脂肪族炭化水素系,或いはシクロブタ
ン,シクロペンタン,シクロヘキサン等の環式脂肪族炭
化水素系などの揮発性発泡剤,アゾジカルボンアミド,
アゾビスイソブチルニトリル,重炭酸ナトリュム等の分
解型発泡剤がある。また,更には無機発泡剤として空
気,二酸化炭素,窒素等を用いることができる。又これ
らの発泡剤を適宜混合して用いることができる。Further, as the foamable resin for the core material,
A thermoplastic resin containing a foaming agent is used. As the thermoplastic resin, those similar to the thermoplastic resins shown for the skin material can be used. Examples of the foaming agent include volatile foams such as aliphatic hydrocarbons such as propane, n-butane, i-butane, pentane and hexane, and cycloaliphatic hydrocarbons such as cyclobutane, cyclopentane and cyclohexane. Agent, azodicarbonamide,
There are decomposable blowing agents such as azobisisobutylnitrile and sodium bicarbonate. Further, air, carbon dioxide, nitrogen, or the like can be used as the inorganic foaming agent. Further, these foaming agents can be appropriately mixed and used.
【0017】また,芯材用発泡性樹脂に対する発泡剤の
添加量は,好ましくは3〜15wt%である。また揮発
性の発泡剤の添加の仕方には,含有された発泡樹脂ビー
ズを用いることもできるし,例えば押出機中で発泡剤を
注入することもできる。なお,発泡体の倍率の調整は,
発泡剤の添加量,ノズルの口径,押出機の回転数,温
度,引き取り速度によって自由に変えることができる。The amount of the foaming agent added to the foaming resin for the core material is preferably 3 to 15% by weight. As a method of adding a volatile foaming agent, foamed resin beads contained therein can be used, and for example, a foaming agent can be injected in an extruder. In addition, the adjustment of the magnification of the foam
It can be freely changed depending on the amount of the foaming agent added, the nozzle diameter, the number of revolutions of the extruder, the temperature, and the take-up speed.
【0018】また,より均一性のある発泡セルを得るた
めに用いる核剤としては,ポリエチレンワックス,エチ
レンビスアミド,ヘキサブロモシクロドデカン,及びメ
タクリル酸低級アルキルエステル単位を5重量%以上含
むメタクリル酸低級アルキルエステル系重合体等の有機
系核剤,タルク,シリカ等の無機系核剤及び水から選ば
れる1種以上を用いる。これらの核剤は,芯材用発泡性
樹脂に対して0.2〜5wt%好ましくは,0.4〜
2.0wt%含有することが好ましい。The nucleating agent used to obtain a more uniform foam cell includes polyethylene wax, ethylene bisamide, hexabromocyclododecane, and lower alkyl methacrylate containing 5% by weight or more of lower alkyl methacrylate units. At least one selected from an organic nucleating agent such as an ester polymer, an inorganic nucleating agent such as talc and silica, and water is used. These nucleating agents are used in an amount of 0.2 to 5 wt%, preferably 0.4 to 5 wt%, based on the foaming resin for the core material.
It is preferable to contain 2.0 wt%.
【0019】また,芯材用発泡性樹脂の出口と表皮材の
出口の間に間隙を設けておく場合には,例えば7〜50
倍という高い発泡倍率の芯材を得ることができる。When a gap is provided between the outlet of the foaming resin for the core material and the outlet of the skin material, for example, 7 to 50
A core material having a high expansion ratio of 2 times can be obtained.
【0020】次に,請求項2の発明のように,上記第1
ダイスは,上記第2押出機との間に,上記第1ダイス内
における上記芯材用発泡性樹脂の温度が上記表皮材の温
度よりも20℃以上低い温度となるように調節するため
の断熱機構を有することが好ましい。この場合には,芯
材用の発泡性樹脂を低温で押出し,第1ダイス内で極め
て高い背圧をかけて押出すことができ,高倍率の発泡セ
ルの均一性,独立性を得ることができる。Next, as in the second aspect of the present invention, the first
A die is provided between the second extruder and the second extruder so as to control the temperature of the foaming resin for the core material in the first die to be at least 20 ° C. lower than the temperature of the skin material. It is preferable to have a mechanism. In this case, the foaming resin for the core material can be extruded at a low temperature and can be extruded by applying an extremely high back pressure in the first die, and the uniformity and independence of the high magnification foam cell can be obtained. it can.
【0021】即ち,芯材用発泡性樹脂に発泡剤を含有さ
せて押出すと,一般的に樹脂の溶融粘度が下がり,押出
機内の背圧がかからず,更に第1ダイスの出口の背圧も
かからず発泡倍率が上がらない。しかし,上記のごと
く,温度調整して,樹脂温度を低くした場合は,樹脂の
溶融粘度が上がるため,上記高い背圧が可能となり,上
記効果が得られる。また,上記断熱機構としては,例え
ば実施形態例に示すごとき,熱媒チャンバー方式,或い
は断熱板方式,空気冷却チャンバー方式などを用いる。That is, when a foaming agent is added to the foaming resin for the core material and extruded, the melt viscosity of the resin generally decreases, no back pressure is applied in the extruder, and the back of the outlet of the first die is further reduced. No pressure is applied and the expansion ratio does not increase. However, as described above, when the temperature is adjusted to lower the resin temperature, the melt viscosity of the resin increases, so that the above-mentioned high back pressure becomes possible, and the above-mentioned effect is obtained. As the heat insulating mechanism, for example, a heat medium chamber method, a heat insulating plate method, an air cooling chamber method, or the like as shown in the embodiment is used.
【0022】次に,請求項3の発明のように,上記芯材
用発泡性樹脂は,上記第1ダイスに設けた,ノズル1個
の開口面積が30mm2以下の複数列かつ複数段のノズ
ルから押し出すと共に,発泡倍率7〜50倍に発泡させ
ることが好ましい。この場合には,芯材用発泡性樹脂の
背圧が上がり発泡倍率を高めることができる。Next, as in the third aspect of the present invention, the foamable resin for the core material is provided in the first die and is provided in a plurality of rows and a plurality of stages of nozzles each having an opening area of 30 mm 2 or less. It is preferable that the foam is extruded from the foam and foamed at a foaming ratio of 7 to 50 times. In this case, the back pressure of the expandable resin for the core material is increased, and the expansion ratio can be increased.
【0023】次に,上記ノズルの開口面積が30mm2
未満の場合には,同じノズルから,同形状の円柱状発泡
体が成形され,1本1本の発泡倍率がより一層均一とな
る。なお,上記ノズルから成形される発泡体は,円形
状,楕円形状,或いは四角形以上の多角形の形状でも良
い。なお,上記ノズルの開口面積の下限については,加
圧困難性,目づまり等の点から0.03mm2とするこ
とが好ましい。また,上記発泡倍率が7倍未満の場合に
は軽量化が不充分となり,コストが高くなるおそれがあ
り,一方50倍を越えると独立気泡性が低下し,強度の
弱い発泡体となるおそれがある。Next, the opening area of the nozzle is 30 mm 2
If it is less than the same nozzle, the same columnar foam is molded from the same nozzle, and the foaming ratio of each foam becomes more uniform. The foam formed from the nozzle may have a circular shape, an elliptical shape, or a polygonal shape having a square shape or more. The lower limit of the opening area of the nozzle is preferably set to 0.03 mm 2 from the viewpoint of difficulty in pressurization and clogging. When the expansion ratio is less than 7 times, the weight reduction becomes insufficient and the cost may increase. On the other hand, when the expansion ratio exceeds 50 times, the closed cell properties may decrease and the foam may have low strength. is there.
【0024】次に,請求項4の発明のように,上記芯材
用発泡性樹脂は,ポリスチレン系樹脂75〜97.8重
量%と発泡剤2〜20重量%と核剤0.2〜5重量%と
よりなり,上記表皮材はスチレン系熱可塑性樹脂である
ことが好ましい。この場合には,ポリスチレン系樹脂は
汎用樹脂で比較的原料価格も安く,発泡剤の保持力も高
い上成形性が良い。また,核剤を用いることで発泡セル
の均一性も良く,発泡倍率も高倍となり,秤量当りの剛
性,コスト面も有利となる。Next, as in the invention of claim 4, the foamable resin for the core material is composed of 75 to 97.8% by weight of a polystyrene resin, 2 to 20% by weight of a foaming agent and 0.2 to 5% of a nucleating agent. %, And the skin material is preferably a styrene-based thermoplastic resin. In this case, the polystyrene resin is a general-purpose resin that is relatively inexpensive in raw materials, has high holding power for the blowing agent, and has good moldability. In addition, the use of the nucleating agent improves the uniformity of the foam cells, increases the expansion ratio, and is advantageous in terms of rigidity per weight and cost.
【0025】上記ポリスチレン系樹脂が75重量%未満
では,高発泡となりすぎ強度が弱くなるという問題があ
り,一方97.8重量%を超えると,発泡倍率が低く軽
量化が充分達成できないという問題がある。If the amount of the polystyrene resin is less than 75% by weight, there is a problem that the foaming becomes too high and the strength is weak, while if it exceeds 97.8% by weight, the problem is that the expansion ratio is low and the weight reduction cannot be sufficiently achieved. is there.
【0026】また,発泡剤が2重量%未満では高発泡倍
率が得られず,一方20重量%を超えると発泡倍率が上
がりすぎ,強度の弱い芯材となる。また,余分の発泡ガ
スのために表皮材と芯材間にガス溜りができ,表皮材と
芯材とが融着し難いという問題がある。また,核剤が
0.2重量%未満では発泡セルの均一化を図ることが困
難となり,一方5重量%を超えても発泡セルの均一化は
向上せず,経済的に不利になる。なお,好ましくは1〜
4重量%である。If the amount of the foaming agent is less than 2% by weight, a high expansion ratio cannot be obtained, while if it exceeds 20% by weight, the expansion ratio becomes too high, resulting in a core material having low strength. In addition, there is a problem that gas is formed between the skin material and the core material due to the excess foaming gas, so that the skin material and the core material are not easily fused. Further, if the nucleating agent is less than 0.2% by weight, it is difficult to achieve uniformity of the foamed cells, while if it exceeds 5% by weight, the uniformity of the foamed cells is not improved, which is economically disadvantageous. In addition, preferably 1 to
4% by weight.
【0027】次に,請求項5の発明のように,上記表皮
材はスチレン系熱可塑性樹脂70〜30重量%とオレフ
ィン系熱可塑性樹脂30〜70重量%とからなる主成分
と,該主成分100重量%に対して熱可塑性エラストマ
ーを1〜7重量%配合してなることが好ましい。Next, as in the invention of claim 5, the skin material comprises a main component consisting of 70 to 30% by weight of a styrene-based thermoplastic resin and 30 to 70% by weight of an olefin-based thermoplastic resin. It is preferable to mix 1 to 7% by weight of a thermoplastic elastomer with respect to 100% by weight.
【0028】この場合には,オレフィン系熱可塑性樹脂
を用いることによりスチレン系熱可塑性樹脂の欠点であ
る耐薬品性が向上する。また,熱可塑性エラストマーを
付与することによって,互いに相溶性が向上し,耐薬品
性,耐熱性,更に外観の優れた製品を得ることができ
る。In this case, the use of the olefin-based thermoplastic resin improves the chemical resistance, which is a disadvantage of the styrene-based thermoplastic resin. In addition, by adding a thermoplastic elastomer, compatibility with each other is improved, and a product having excellent chemical resistance, heat resistance, and appearance can be obtained.
【0029】上記スチレン系熱可塑性樹脂が70重量%
を超えると耐薬品性,耐熱性が悪くなるという問題があ
り,一方30重量%未満では芯材との融着不良の問題が
ある。また,オレフィン系熱可塑性樹脂が30重量%未
満では,耐薬品性,耐熱性が悪くなるという問題があ
り,一方70重量%を超えると芯材との融着性が不良に
なるという問題がある。70% by weight of the above styrene thermoplastic resin
If the amount exceeds 30%, the chemical resistance and heat resistance deteriorate. On the other hand, if the amount is less than 30% by weight, there is a problem of poor fusion with the core material. If the olefin-based thermoplastic resin is less than 30% by weight, there is a problem that chemical resistance and heat resistance are deteriorated, while if it is more than 70% by weight, there is a problem that the fusion property with the core material becomes poor. .
【0030】また,熱可塑性エラストマーが1重量%未
満の場合は,オレフィン系熱可塑性樹脂とスチレン系熱
可塑性樹脂との相溶性が悪くなり外観不良の問題があ
る。一方7重量%を超えると表皮材の剛性が低下し,出
来上がった発泡複合体の剛性が低下するという問題があ
る。When the content of the thermoplastic elastomer is less than 1% by weight, the compatibility between the olefin-based thermoplastic resin and the styrene-based thermoplastic resin becomes poor, and there is a problem of poor appearance. On the other hand, if it exceeds 7% by weight, there is a problem that the rigidity of the skin material is reduced, and the rigidity of the foamed composite is reduced.
【0031】次に,請求項6の発明のように,上記熱可
塑性エラストマーは,スチレン・ブタジエン・スチレン
(SBS)又はスチレン・エチレン・ブタジエン・スチ
レン(SEBS)であることが好ましい。この場合に
は,相溶性が良く,表皮材の外観性に優れた発泡複合体
を得ることができる。Next, as in the invention of claim 6, the thermoplastic elastomer is preferably styrene-butadiene-styrene (SBS) or styrene-ethylene-butadiene-styrene (SEBS). In this case, a foam composite having good compatibility and excellent appearance of the skin material can be obtained.
【0032】次に,請求項7の発明のように,芯材用発
泡性樹脂を発泡させてなる複数列かつ複数段の芯材より
なる発泡体と,該発泡体の周囲を一体的に被覆してなる
非発泡熱可塑性樹脂又は低発泡性熱可塑性樹脂よりなる
表皮材とよりなり,かつ上記複数列かつ複数段の芯材は
その隣接部分が互いに融着していることを特徴とする押
出し発泡複合体がある。Next, a foam comprising a plurality of rows and a plurality of stages of a core material obtained by foaming a foamable resin for a core material, and the periphery of the foam material are integrally covered. Extrusion characterized by a skin material made of a non-foamed thermoplastic resin or a low-foamable thermoplastic resin, and wherein the plurality of rows and the plurality of stages of the core material are fused together at adjacent portions. There are foam composites.
【0033】この場合には,各芯材の発泡性が均一でこ
れらを表皮材が一体的に被覆してなる,発泡セルの均一
性,独立気泡性が良好で高発泡倍率の芯材を有し,かつ
軽量で剛性の高い発泡複合体を提供することができる。
かかる押出し発泡複合体は,上記製造方法により得るこ
とができる。In this case, each core material has a uniform foaming property and a skin material integrally covers the core material. The core material has good uniformity of foam cells, good closed cells and high expansion ratio. In addition, a lightweight, highly rigid foam composite can be provided.
Such an extruded foam composite can be obtained by the above production method.
【0034】次に,請求項8の発明のように,上記表皮
材の肉厚は,複数列かつ複数段の芯材よりなる発泡体の
肉厚の0.1〜25%であることが好ましい。この場合
には,特に軽くて,剛性が高く,コストが低いという効
果を得ることができる。上記肉厚が0.1%未満では発
泡複合体の剛性が低下し,一方25%を超えると剛性は
向上するが,複合体が重くなり,コストも高くなるとい
う問題がある。Next, as in the invention of claim 8, the thickness of the skin material is preferably 0.1 to 25% of the thickness of the foam formed of the core material in a plurality of rows and a plurality of stages. . In this case, the effects of being particularly light, having high rigidity, and low cost can be obtained. When the thickness is less than 0.1%, the rigidity of the foamed composite is reduced. On the other hand, when the thickness is more than 25%, the rigidity is improved, but there is a problem that the composite becomes heavy and the cost increases.
【0035】次に,請求項9の発明のように,上記各芯
材はその表面に上記芯材用発泡性樹脂によるスキン層を
有し,該スキン層は互いに融着していることが好まし
い。この場合には,各芯材が上記スキン層によって覆わ
れ,かつスキン層は互いに融着しているので,特に押出
し発泡複合体の剛性が高くなる。なお,上記スキン層の
厚みは0.1〜20μmとすることが好ましい。0.1
μm未満では,剛性向上の効果が低く,一方20μmを
越えるとスキン層が互いに十分に融着しないおそれがあ
る。Next, as in the ninth aspect of the present invention, it is preferable that each core material has a skin layer made of the foamable resin for the core material on its surface, and the skin layers are fused to each other. . In this case, since each core material is covered by the skin layer and the skin layers are fused to each other, the rigidity of the extruded foam composite is particularly increased. Preferably, the thickness of the skin layer is 0.1 to 20 μm. 0.1
If it is less than μm, the effect of improving rigidity is low, while if it exceeds 20 μm, the skin layers may not be sufficiently fused to each other.
【0036】次に,請求項10の発明のように,上記芯
材はポリスチレン系樹脂であり,表皮材はスチレン系熱
可塑性樹脂であることが好ましい。この場合には,剛性
の高い発泡複合体となると共に,ポリスチレン系樹脂が
汎用樹脂のため比較的安価な発泡複合体を得ることがで
きる。Next, as in the tenth aspect of the present invention, it is preferable that the core material is a polystyrene resin and the skin material is a styrene thermoplastic resin. In this case, a foam composite having high rigidity can be obtained, and a relatively inexpensive foam composite can be obtained because the polystyrene resin is a general-purpose resin.
【0037】次に,請求項11の発明のように,上記表
皮材はスチレン系熱可塑性樹脂70〜30重量%とオレ
フィン系熱可塑性樹脂30〜70重量%とからなる主成
分と,該主成分100重量%に対して熱可塑性エラスト
マーを1〜7重量%配合してなることが好ましい。この
場合には,上記請求項5と同様の効果を得ることができ
る。Next, as in the eleventh aspect of the present invention, the skin material comprises a main component comprising 70 to 30% by weight of a styrene-based thermoplastic resin and 30 to 70% by weight of an olefin-based thermoplastic resin. It is preferable to mix 1 to 7% by weight of a thermoplastic elastomer with respect to 100% by weight. In this case, the same effects as those of the fifth aspect can be obtained.
【0038】次に,請求項12の発明のように,上記熱
可塑性エラストマーは,スチレン・ブタジエン・スチレ
ン(SBS)又はスチレン・エチレン・ブタジエン・ス
チレン(SEBS)であることが好ましい。この場合に
は,上記請求項6と同様の効果を得ることができる。Next, it is preferable that the thermoplastic elastomer is styrene-butadiene-styrene (SBS) or styrene-ethylene-butadiene-styrene (SEBS). In this case, the same effect as the above-described claim 6 can be obtained.
【0039】[0039]
【発明の実施の形態】実施形態例1 本発明の実施形態例にかかる押出し発泡複合体及びその
製造方法につき,図1〜図5を用いて説明する。まず,
本例において得ようとする発泡複合体5は,図5に示す
ごとく,芯材用発泡性樹脂を発泡させてなる複数列かつ
複数段,即ち5列,2段の芯材100と,これらの周囲
を一体的に被覆してなる非発泡熱可塑性樹脂又は低発泡
性熱可塑性樹脂よりなる表皮材30とよりなる。BEST MODE FOR CARRYING OUT THE INVENTION Embodiment 1 An extruded foam composite and a method for producing the same according to an embodiment of the present invention will be described with reference to FIGS. First,
As shown in FIG. 5, the foam composite 5 to be obtained in this example has a plurality of rows and a plurality of rows of foamed resin for the core material, that is, five rows and two steps of the core material 100, and It comprises a skin material 30 made of a non-foamed thermoplastic resin or a low-foamable thermoplastic resin whose periphery is integrally coated.
【0040】また,上記複数列かつ複数段の芯材100
は,その隣接部分のスキン層15が互いに融着してい
る。即ち,各芯材100は,多数の発泡粒子101から
なりその周囲はスキン層15により囲まれている。そし
て,各スキン層15は互いに融着している。これによっ
て,複数列かつ複数段の芯材が一体化された発泡体10
4を形成している。上記のスキン層15は,成形時にノ
ズルから吐出される際に形成される。The core material 100 having a plurality of rows and a plurality of stages is provided.
The skin layer 15 of the adjacent portion is fused to each other. That is, each core material 100 is composed of a large number of expanded particles 101, and the periphery thereof is surrounded by the skin layer 15. The skin layers 15 are fused to each other. As a result, a foam 10 in which a plurality of rows and a plurality of stages of a core material are integrated
4 are formed. The above-mentioned skin layer 15 is formed when it is discharged from a nozzle during molding.
【0041】次に,上記発泡複合体5を製造するに当っ
ては,図1,図4に示すごとく,発泡剤を含有させた熱
可塑性樹脂よりなる芯材用発泡性樹脂10を第1押出機
1の第1ダイス2から押し出し,一方非発泡熱可塑性樹
脂又は低発泡性熱可塑性樹脂よりなる表皮材30を第2
押出機3の第2ダイス33から押し出す。そして,両押
出機の先端に設けた上記第1ダイス2及び第2ダイス3
3の外部において,上記芯材用発泡性樹脂からなる芯材
100の外周に上記表皮材30を被覆してなる発泡複合
体5を押出成形する。Next, as shown in FIGS. 1 and 4, a foaming resin 10 for a core material made of a thermoplastic resin containing a foaming agent is first extruded. While extruding from the first die 2 of the machine 1, the skin material 30 made of non-foamed thermoplastic resin or low-foamable thermoplastic resin
Extrude from the second die 33 of the extruder 3. Then, the first die 2 and the second die 3 provided at the tip of both extruders.
Outside the core 3, a foam composite 5 is formed by covering the outer periphery of the core material 100 made of the foamable resin for the core material with the skin material 30.
【0042】そして,上記第1ダイス2からは,複数列
かつ複数段に配置したノズル25より,上記芯材用発泡
性樹脂10を押出すと共に発泡させて芯材100を形成
しながら,一方上記第2ダイス33から上記表皮材30
を上記複数列かつ複数段の芯材100の外側に押出すと
共に該表面材30を直ちに冷却サイジング4に導く。こ
のとき,上記芯材用発泡性樹脂の発泡力によって,上記
表皮材30を上記冷却サイジング4の内面に押し当て
て,上記芯材用発泡性樹脂によって形成された複数列か
つ複数段のの芯材5よりなる発泡体104の外表面に上
記表皮材30を被覆する。From the first die 2, the core resin 100 is extruded and foamed from the nozzles 25 arranged in a plurality of rows and a plurality of stages to form the core material 100. From the second die 33 to the skin material 30
Is pushed out of the core material 100 in a plurality of rows and a plurality of stages, and the surface material 30 is immediately led to the cooling sizing 4. At this time, the skin material 30 is pressed against the inner surface of the cooling sizing 4 by the foaming force of the foaming resin for the core material, and a plurality of rows and a plurality of stages of cores formed by the foaming resin for the core material are formed. The skin material 30 is coated on the outer surface of the foam 104 made of the material 5.
【0043】以下,これらにつき詳述する。まず,上記
押出発泡成形を実施するための発泡成形装置は,図1〜
図4に示すごとく,第1ダイス2に芯材用発泡性樹脂1
0を送入する第1押出機1,及び第2ダイス33に表皮
材30を送入する第2押出機3とを有する。そして,第
1ダイス2の後流側には冷却サイジング4,冷却水槽4
5,引取機46を順次配設してなる(図4)。Hereinafter, these will be described in detail. First, a foam molding apparatus for performing the above extrusion foam molding is shown in FIGS.
As shown in FIG. 4, the foaming resin 1 for the core material is placed on the first die 2.
And a second extruder 3 for feeding the skin material 30 to the second die 33. On the downstream side of the first die 2, cooling sizing 4, cooling water tank 4
5, a take-up machine 46 is sequentially arranged (FIG. 4).
【0044】第1ダイス2は,図1〜図3に示すごと
く,芯材用発泡性樹脂10を押し出す,10個のノズル
25と,該ノズル25へ芯材用発泡性樹脂10をガイド
するガイド部24とを有する。ガイド部24の間には,
これらを区画するマニホールド23が設けてある。ま
た,図1,図4に示すごとく,上記10個のノズル25
の周囲には,これらを取り囲むように,表皮材出口とし
ての環状長方形の,表皮材形成用のスリット28が設け
てある。As shown in FIGS. 1 to 3, the first die 2 extrudes the core foaming resin 10, ten nozzles 25, and a guide for guiding the core foaming resin 10 to the nozzles 25. And a part 24. Between the guide parts 24,
A manifold 23 for partitioning these is provided. As shown in FIG. 1 and FIG.
Is provided with a slit 28 for forming a skin material, which is an annular rectangular shape as a skin material outlet so as to surround them.
【0045】また,第2押出機3は,表皮材30を上記
スリット28へガイドするための流路32を有する。ま
た,図3に示すごとく,第1ダイス2は,第2押出機3
の第2ダイス33における装着穴35内に挿入配置され
る。これにより,第1ダイス2と第2ダイス33との間
に上記スリット28が形成される。The second extruder 3 has a flow path 32 for guiding the skin material 30 to the slit 28. In addition, as shown in FIG. 3, the first die 2 is
Is inserted into the mounting hole 35 of the second die 33. Thus, the slit 28 is formed between the first die 2 and the second die 33.
【0046】また,上記第1ダイス2は,上記第2押出
機3の第2ダイス33との間に,上記第1ダイス2内に
おける上記芯材用発泡性樹脂10の温度が上記表皮材3
0の温度よりも20℃以上低い温度となるように調節す
るための,断熱機構としてのチャンバー22を有する。
このチャンバー22は,熱媒流路構造を有し,その内部
に熱媒が流通するようになっている。The temperature of the foaming resin 10 for the core material in the first die 2 is set between the first die 2 and the second die 33 of the second extruder 3.
It has a chamber 22 as a heat insulating mechanism for adjusting the temperature to be lower than the temperature of 0 by 20 ° C. or more.
The chamber 22 has a heat medium flow path structure in which the heat medium flows.
【0047】次に図1〜図4を用いて製造方法について
詳しく説明する。第1押出機1から押し出された芯材用
発泡性樹脂10は第1押出機1と第1ダイス2を接続す
るジョイント11を通り第1ダイス2に導かれる。第1
ダイス2の空間部21は,幅方向に溶融樹脂を均一に広
げるためのコートハンガー形状部で,しかも中央部は外
周部に比べ樹脂流路間隙を狭めてある。芯材用発泡性樹
脂10は,後方部のマニホールド23に流れ,より均一
化され,各ノズル25に導かれ,最終的に第1ダイス2
の先端に設けたノズル25からダイス外へ押し出されて
発泡して行く。Next, the manufacturing method will be described in detail with reference to FIGS. The core expandable resin 10 extruded from the first extruder 1 is guided to the first die 2 through a joint 11 connecting the first extruder 1 and the first die 2. First
The space 21 of the die 2 is a coat hanger-shaped portion for uniformly spreading the molten resin in the width direction, and the center portion has a narrower resin passage gap than the outer peripheral portion. The foaming resin 10 for the core material flows into the rear manifold 23, is made more uniform, is guided to the nozzles 25, and finally becomes the first die 2.
Is extruded out of the die from the nozzle 25 provided at the tip of the nozzle and foams.
【0048】一方,表皮材30は第2押出機3の第2ダ
イス33から押し出され,流路32で幅方向に広げられ
上下両側面に均一に肉厚が分流され,第1ダイス2の出
口に導かれる。第1ダイス2の出口は上記スリット28
を有し,第2押出機3のスクリュー回転数によって表皮
材30の肉厚が芯材肉厚の25%以下になるように調整
する。On the other hand, the skin material 30 is extruded from the second die 33 of the second extruder 3, is spread in the width direction in the flow path 32, and is uniformly distributed on both upper and lower sides, and the outlet of the first die 2. It is led to. The exit of the first die 2 is the slit 28
The thickness of the skin material 30 is adjusted to 25% or less of the core material thickness by the screw rotation speed of the second extruder 3.
【0049】そして,上記複数列かつ複数段の各ノズル
25から押し出された芯材用発泡性樹脂10は,そこで
発泡して合計10個の芯材100となる。これら芯材1
00の各スキン層15は互いに融着する。そして,これ
ら10個の芯材100からなる発泡体104の外周を上
記表皮材30が覆った成形品が得られる。The foaming resin 10 for the core material extruded from the nozzles 25 in a plurality of rows and a plurality of stages is foamed there to become a total of ten core materials 100. These core materials 1
The 00 skin layers 15 are fused together. Then, a molded product in which the skin material 30 covers the outer periphery of the foam body 104 including the ten core materials 100 is obtained.
【0050】このとき,上記芯材10の発泡力によっ
て,上記表皮材30は冷却サイジング4の冷却材の内側
面に押し当てられる。そして,表皮材30と発泡体10
4の外周面とが融着される。なお,上記芯材用発泡性樹
脂10の発泡は,上記スリット28により形成された角
筒箱状の上記表皮材30の中で行なわれる。この成形品
は,冷却サイジング4の内部,冷却水槽45を経てキャ
タピラ式の引取機46により引き取られていく。At this time, the skin material 30 is pressed against the inner surface of the cooling material of the cooling sizing 4 by the foaming force of the core material 10. Then, the skin material 30 and the foam 10
4 is fused to the outer peripheral surface. The foaming of the foaming resin 10 for the core material is performed in the skin material 30 in the shape of a rectangular box formed by the slit 28. This molded product is taken off by a caterpillar type take-up machine 46 through a cooling water tank 45 inside the cooling sizing 4.
【0051】以上により,図5に示すごとく,複数列か
つ複数段の10個の芯材100が融着して形成された発
泡体104とその周囲を一体的に被覆した表皮材30と
からなる発泡複合体5が得られる。そして,各芯材10
0は,それぞれその外周にスキン層15を有し,このス
キン層15の隣接部分は互いに融着している。As described above, as shown in FIG. 5, a foam 104 formed by fusing a plurality of rows and a plurality of stages of ten core materials 100 and a skin material 30 integrally covering the periphery thereof. The foam composite 5 is obtained. And each core material 10
No. 0 has a skin layer 15 on the outer periphery thereof, and adjacent portions of the skin layer 15 are fused to each other.
【0052】また,隣接するスキン層15の間,及びス
キン層15と表皮材30との間には,菱形状,半菱形三
角状又は四角状の小さい間隙16が形成されている(図
5)。この間隙16は,押出し発泡複合体を上記のごと
く成形する際に,各芯材100が発泡して,芯材100
間の間隔が小さくなっていくとき,これらの間に残存し
ている空気を後方側,即ち第1ダイス2側へスムーズに
排出していくガス排出路の役目又は前方側へのガス排出
路の役目を果す。これにより,芯材100の発泡が円滑
に行なわれ均一に発泡した芯材が得られる。Small diamond-shaped, semi-diamond-shaped, triangular or square gaps 16 are formed between the adjacent skin layers 15 and between the skin layer 15 and the skin material 30 (FIG. 5). . When the extruded foam composite is formed as described above, each of the cores 100 expands, and the gap 16
When the distance between them becomes smaller, the gas remaining in the gap between them becomes smoother to the rear side, that is, to the first die 2 side, or the gas discharge path to the front side. Play a role. As a result, the core material 100 is smoothly foamed, and a uniformly foamed core material is obtained.
【0053】本例においては,複数列かつ複数段に押し
出した芯材用発泡性樹脂10を,第1ダイス2の出口に
おいて発泡させ,この発泡により得た複数列かつ複数段
の芯材100からなる発泡体100の周囲に上記表皮材
30を被覆していく。そのため,芯材100における発
泡セルが均一となり,また独立気泡性即ち発泡セル膜が
破れることなく,高倍率の発泡体が得られる。In this example, the foaming resin 10 for the core material extruded in a plurality of rows and a plurality of steps is foamed at the outlet of the first die 2, and the foamed resin 10 for the plurality of rows and the plurality of steps is obtained from the foamed core material 100. The skin material 30 is coated around the foam body 100. Therefore, the foam cells in the core material 100 become uniform, and a high-magnification foam can be obtained without closing cells, that is, without breaking the foam cell film.
【0054】もしも,第1ダイス内において芯材用発泡
性樹脂10の周囲に表皮材30を合流させて,芯材用発
泡性樹脂を表皮材により被覆したり,第1ダイスにおい
て芯材用発泡性樹脂を発泡させて第1ダイス内で表皮材
30を被覆する場合には,上記のごとき効果を得ること
はできない。If the skin material 30 is merged around the core foaming resin 10 in the first die, the core foaming resin is covered with the skin material, or the core foaming is performed in the first die. When the skin material 30 is covered in the first die by foaming the conductive resin, the above effects cannot be obtained.
【0055】また,ノズル25を設けた第1ダイス出口
面20と,表皮材の出口であるスリット28との間に,
環状長方形のスキ間361を設定してある(図2)。そ
のため,例えば7〜50倍という高い発泡倍率の芯材を
得ることができる。Further, between the first die exit surface 20 provided with the nozzle 25 and the slit 28 which is the exit of the skin material,
An annular rectangular gap 361 is set (FIG. 2). Therefore, a core material having a high expansion ratio of, for example, 7 to 50 times can be obtained.
【0056】また,上記のごとき優れた芯材100から
なる発泡体104の表面に,芯材の発泡と殆ど同時に表
皮材30を被覆する。そのため,表皮材30と発泡体1
04との融着及び芯材100同志の融着が確実にできる
という効果を得ることができる。また,各ノズルから押
出され発泡した芯材は複数列かつ複数段に形成されると
共に互いに隣接する芯材100と融着している。そのた
め,押出し発泡複合体5の剛性も向上する。また,押出
し発泡複合体5は,発泡体と表皮材とからなるので軽量
である。The surface of the foam 104 made of the excellent core material 100 is covered with the skin material 30 almost simultaneously with the foaming of the core material. Therefore, the skin material 30 and the foam 1
The effect that the fusion with the core material 04 and the fusion of the core materials 100 can be surely performed can be obtained. The core material extruded and foamed from each nozzle is formed in a plurality of rows and a plurality of stages, and is fused with the core material 100 adjacent to each other. Therefore, the rigidity of the extruded foam composite 5 is also improved. Further, the extruded foam composite 5 is lightweight because it is composed of the foam and the skin material.
【0057】実施形態例2 次に,本発明の具体的実施例及び比較例について説明す
る。表皮材として,アクリル・ブタジェン・スチレン
(ABS)樹脂を用い,第1押出機は,65mm口径,
L/D=24,圧縮比=2.4のフルフライトのスクリ
ューを用い,シリンダーの温度は,ホッパー側より,1
80−190−200−200℃とし,第2ダイスは2
00℃とした。スクリュー回転数は30RPMとした。
第2ダイス出口の樹脂の温度は200℃であった。Embodiment 2 Next, specific examples and comparative examples of the present invention will be described. Acrylic butadiene styrene (ABS) resin was used as the skin material.
A full-flight screw with L / D = 24 and compression ratio = 2.4 was used.
80-190-200-200 ° C, the second die is 2
The temperature was set to 00 ° C. The screw rotation speed was 30 RPM.
The temperature of the resin at the exit of the second die was 200 ° C.
【0058】芯材用発泡性樹脂としては,発泡剤として
のブタン7wt%を含侵したポリスチレン樹脂を用い
た。また,ポリスチレン樹脂100wt%に対して核剤
としてタルク1.2wt%を混合した。第2押出機は,
45mm口径,L/D=20,圧縮比=2.4のフルフ
ライトのスクリューを用い,シリンダーの温度は,ホッ
パー側より,110−120−120℃とし,ダイスヘ
ッドは130℃とした。断熱チャンバーの熱媒の温度は
130℃とし,ポンプで循環した。スクリュー回転数
は,35RPMとした。ダイス出口での発泡性樹脂温度
は120℃であった。As the foaming resin for the core material, a polystyrene resin impregnated with 7% by weight of butane as a foaming agent was used. Also, 1.2 wt% of talc was mixed as a nucleating agent with 100 wt% of polystyrene resin. The second extruder
A full-flight screw having a diameter of 45 mm, L / D = 20, and a compression ratio of 2.4 was used. The temperature of the cylinder was 110-120-120 ° C. from the hopper side, and the die head was 130 ° C. The temperature of the heat medium in the adiabatic chamber was set at 130 ° C. and circulated by a pump. The screw rotation speed was 35 RPM. The temperature of the foamable resin at the exit of the die was 120 ° C.
【0059】第2ダイス出口における表皮材の温度は1
95℃,芯材用発泡性樹脂の温度は125℃であつた。
表皮材と芯材用発泡性樹脂の温度差(ΔT)は70℃で
あった。表皮材を押し出すスリットの形状は,内側18
mm×193mm,外側20mm×195mmの長方形
のスリット状にし,スリットの間隙は,1mmとした。
芯材用発泡性樹脂用の第2ダイスの形状は,縦35m
m,横187mmの大きさの縦方向の中央部に,直径
2.5mmのノズルをピッチ21.5mmの間隙で配置
し,両端は,7.5mmとした。The temperature of the skin material at the exit of the second die is 1
The temperature of the foamable resin for the core material was 125 ° C.
The temperature difference (ΔT) between the skin material and the foamable resin for the core material was 70 ° C. The shape of the slit that extrudes the skin material is 18 inside.
A rectangular slit having a size of 193 mm × 20 mm × 195 mm outside was formed, and the gap between the slits was 1 mm.
The shape of the second die for foaming resin for core material is 35m in length.
A nozzle having a diameter of 2.5 mm was arranged at a gap of 21.5 mm at the center in the vertical direction having a size of 187 mm in width, and both ends were set to 7.5 mm.
【0060】冷却サイジングにおける冷却板の形状は縦
50mm,横200mmの箱状とし,中間部から上下に
割れる形状にし,温度30℃とし,発泡複合体を冷却し
た。引き取り速度は1m/分で成形した。The shape of the cooling plate in the cooling sizing was box-shaped with a length of 50 mm and a width of 200 mm, the shape was split vertically from the middle part, the temperature was 30 ° C., and the foam composite was cooled. Molding was performed at a take-up speed of 1 m / min.
【0061】得られた発泡複合体は,外観は極めて良好
で,表皮材30の平均肉厚は1.0mmで,芯材100
の発泡状態は均一で平均発泡倍率は15倍であった。ま
た,表皮材30と発泡体104の外周面とは融着し,1
0個の芯材の被膜15間の融着も十分であった。上記ス
キン層15は1〜20μmの厚みであった。The foamed composite obtained had an extremely good appearance, the average thickness of the skin material 30 was 1.0 mm, and the core material 100
Had a uniform foaming state and an average expansion ratio of 15 times. Further, the skin material 30 and the outer peripheral surface of the foam 104 are fused together,
The fusion between the 0 core material coatings 15 was also sufficient. The skin layer 15 had a thickness of 1 to 20 μm.
【0062】実施形態例3 表皮材として,ポリプロピレン樹脂60wt%に充填剤
としてタルク40wt%を含有した樹脂を用い,シリン
ダーの温度は,ホッパー側より,190−200−21
0−210℃とし,第2ダイスは210℃とした。第1
ダイス出口における表皮材の温度は200℃,芯材用発
泡性樹脂の温度は125℃であつた。樹脂温度差(Δ
T)は75℃であった。芯材の平均発泡倍率は15倍で
発泡状態も均一であった。また,表皮と芯材は異種材料
のため融着は不充分であったが,芯材の層間の融着は十
分で,発泡複合体の剛性は充分に高かった。それ以外
は,実施形態例2と同じであった。Embodiment 3 As the skin material, a resin containing 60 wt% of polypropylene resin and 40 wt% of talc as a filler was used, and the temperature of the cylinder was 190-200-21 from the hopper side.
The temperature was 0 to 210 ° C, and the temperature of the second die was 210 ° C. First
The temperature of the skin material at the exit of the die was 200 ° C, and the temperature of the foamable resin for the core material was 125 ° C. Resin temperature difference (Δ
T) was 75 ° C. The average foaming ratio of the core material was 15 times, and the foamed state was uniform. Although the skin and the core material were dissimilar materials, the fusion was insufficient, but the fusion between the core layers was sufficient, and the rigidity of the foam composite was sufficiently high. Other than that, it was the same as the second embodiment.
【0063】実施形態例4 本例は,図6に示すごとく,芯材100を3列2段毎
に,左右に区分するようにリブ305を設けた例を示
す。上記リブ305は,発泡複合体5の厚み方向に,1
ケ所に設けられ,その材料及び厚みは表皮材30と同じ
である。Fourth Embodiment As shown in FIG. 6, this embodiment shows an example in which the ribs 305 are provided so as to divide the core material 100 into three rows and two rows at right and left sides. The rib 305 is positioned at 1 in the thickness direction of the foam composite 5.
The material and thickness are the same as those of the skin material 30.
【0064】この押出し発泡複合体5の成形に当って
は,ダイスに上記リブ305を形成するための押出口を
設けておく。本例により得られた押出し発泡複合体5
は,上記リブ305を有するので,強度が高い。その他
は実施形態例1と同様であり,実施形態例1と同様の効
果を得ることができる。In forming the extruded foam composite 5, an extrusion port for forming the rib 305 is provided in the die. Extruded foam composite 5 obtained according to this example
Has the ribs 305, and thus has high strength. Other configurations are the same as those of the first embodiment, and the same effects as those of the first embodiment can be obtained.
【0065】実施形態例5 本例は,図7に示すごとく,6列3段の芯材100から
なる発泡体104を表皮材30により被覆した押出し発
泡複合体5である。その他は実施形態例1と同様であ
る。Embodiment 5 As shown in FIG. 7, this embodiment is an extruded foam composite 5 in which a foam 104 composed of a core material 100 having six rows and three stages is covered with a skin material 30. Others are the same as the first embodiment.
【0066】実施形態例6 本例は,図8に示すごとく,左方に凹部58,右方に凸
部59を有する押出し発泡複合体5を示す。該押出し発
泡複合体5は,複数列かつ複数段の芯材100からなる
発泡体104と,その表面に被覆した表皮材30とより
なる。該押出し発泡複合体5は,図8の左右方向におい
て,上記凹部58に上記凸部59を嵌合して,施工して
いく,パネル材として用いられる。その他は,実施形態
例1と同様である。Embodiment 6 In this embodiment, as shown in FIG. 8, an extruded foam composite 5 having a concave portion 58 on the left and a convex portion 59 on the right is shown. The extruded foam composite 5 includes a foam 104 composed of a core material 100 having a plurality of rows and a plurality of stages, and a skin material 30 covering the surface thereof. The extruded foam composite 5 is used as a panel material to be fitted and fitted to the recess 58 in the left-right direction in FIG. Other configurations are the same as those of the first embodiment.
【0067】実施形態例7 本例は,図9に示すごとく,2段の芯材100を有する
押出し発泡複合体5である。そして,上段の6個の芯材
100と,下段の複数の芯材100とはその中心が半個
分づつズレた状態にある。その他は実施形態例1と同様
である。Embodiment 7 This embodiment is an extruded foam composite 5 having a two-stage core material 100 as shown in FIG. The upper six core members 100 and the lower core members 100 are in a state where the centers thereof are shifted by half each. Others are the same as the first embodiment.
【0068】実施形態例8 本例は,図10に示すごとく,上下2段の芯材100を
有する押出し発泡複合体5である。そして,下段の芯材
100は,上段の芯材100の半分の厚みである。ま
た,下段の1つの芯材は,上段の1つの芯材の1.5倍
の幅を有している。その他は実施形態例1と同様であ
る。Eighth Embodiment As shown in FIG. 10, this embodiment is an extruded foam composite 5 having an upper and lower two-stage core material 100. The lower core material 100 is half the thickness of the upper core material 100. Further, the lower one core has a width 1.5 times that of the upper core. Others are the same as the first embodiment.
【0069】実施形態例9 本例は,図11に示すごとく,第1ダイスに設ける各種
のノズル形状を示している。同図の(A)は円形6,
(B)は四隅に円弧部611を有する角形61,(C)
は頂部621が半円状の十字形62,(D)は四隅に突
出円弧部631を有する四角形63,(E)は二隅に突
出円弧部631を有する四角形63,(F)は一隅にに
突出円弧部631を有する四角形63,(G)は細長形
状の長方形64である。Embodiment 9 As shown in FIG. 11, this embodiment shows various nozzle shapes provided in the first die. (A) of FIG.
(B) is a square 61 having arc portions 611 at four corners, (C).
Is a cross shape 62 whose top 621 is semicircular, (D) is a square 63 having protruding arc portions 631 at four corners, (E) is a rectangle 63 having protruding arc portions 631 at two corners, and (F) is a The square 63 (G) having the protruding arc portion 631 is an elongated rectangle 64.
【0070】これらの各種ノズル形状は,所望する芯材
の断面形状に応じて,適宜選択する。例えば,(A),
(B)のノズル形状の場合は,発泡複合体の内部に位置
する芯材の押出し用ノズルに用いることが好ましい。ま
た,発泡倍率が低く,芯材間の間隙16(図5参照)が
大きくなる場合には,(C),(D)のノズルが好まし
い。この場合は,上記頂部621,突出円弧部631か
らの押出発泡部分が間隙16の間の一部分又は全部を埋
める。そのため,間隙16が小さい均一な発泡複合体が
得られる。These various nozzle shapes are appropriately selected according to the desired cross-sectional shape of the core material. For example, (A),
In the case of the nozzle shape of (B), it is preferable to use it for a nozzle for extruding a core material located inside the foamed composite. When the foaming ratio is low and the gap 16 between the core materials (see FIG. 5) is large, the nozzles (C) and (D) are preferable. In this case, the extruded foam part from the top part 621 and the protruding arc part 631 fills a part or all of the space between the gaps 16. Therefore, a uniform foam composite having a small gap 16 can be obtained.
【0071】また,(E),(F)については多数列,
多数段の芯材の中でコーナー部分に位置する芯材を押出
す場合のノズルとして好ましい。この場合には,発泡複
合体のコーナー部と表皮材との間の間隙を上記突出円弧
部631からの押出発泡部分で埋めることができ,コー
ナー部分の剛性を高めることができる。なお,上記
(A)〜(G)は,代表的なものを例示したもので,こ
れに限定されるものではない。Further, for (E) and (F), a multi-column
It is preferable as a nozzle for extruding a core material located at a corner portion among a multi-stage core material. In this case, the gap between the corner portion of the foamed composite and the skin material can be filled with the extruded foamed portion from the protruding arc portion 631, and the rigidity of the corner portion can be increased. The above (A) to (G) are representative examples, and the present invention is not limited thereto.
【0072】[0072]
【発明の効果】本発明によれば,発泡セルの均一性,独
立気泡性が良好で,高発泡倍率の芯材を有し,かつ軽量
で剛性の高い,押出し発泡複合体及びその製造方法を提
供することができる。According to the present invention, there is provided an extruded foam composite having good uniformity of foam cells, good closed cells, a core material having a high expansion ratio, light weight and high rigidity, and a method for producing the same. Can be provided.
【図1】実施形態例1にかかる,発泡複合体の成形装置
の断面説明図。FIG. 1 is a cross-sectional explanatory view of a foaming composite molding apparatus according to a first embodiment.
【図2】実施形態例1にかかる,発泡複合体の成形装置
の第1ダイスの先端部の説明図。FIG. 2 is an explanatory view of a tip portion of a first die of the foam composite molding apparatus according to the first embodiment.
【図3】実施形態例1にかかる,発泡複合体の成形装置
の第2押出機に第1ダイスを組付ける状態の説明図。FIG. 3 is an explanatory view of a state in which a first die is assembled to a second extruder of the foam composite molding apparatus according to the first embodiment.
【図4】実施形態例1にかかる,発泡複合体の成形装置
の全体平面図。FIG. 4 is an overall plan view of an apparatus for molding a foamed composite according to the first embodiment.
【図5】実施形態例1において,得られた発泡複合体の
断面斜視図。FIG. 5 is a cross-sectional perspective view of the foam composite obtained in the first embodiment.
【図6】実施形態例4において,得られた発泡複合体の
断面斜視図。FIG. 6 is a cross-sectional perspective view of a foam composite obtained in a fourth embodiment.
【図7】実施形態例5において,得られた発泡複合体の
断面斜視図。FIG. 7 is a cross-sectional perspective view of a foam composite obtained in a fifth embodiment.
【図8】実施形態例6において,得られた発泡複合体の
断面斜視図。FIG. 8 is a sectional perspective view of a foam composite obtained in a sixth embodiment.
【図9】実施形態例7において,得られた発泡複合体の
断面斜視図。FIG. 9 is a cross-sectional perspective view of a foam composite obtained in a seventh embodiment.
【図10】実施形態例8において,得られた発泡複合体
の断面斜視図。FIG. 10 is a cross-sectional perspective view of a foam composite obtained in an eighth embodiment.
【図11】実施形態例9における,第1ダイスのノズル
の各種断面形状の説明図。FIG. 11 is an explanatory view of various cross-sectional shapes of a nozzle of a first die in a ninth embodiment.
1..第1押出機, 10...芯材用発泡性樹脂, 100...芯材, 104...発泡体, 2...第1ダイス, 25...ノズル, 3...第2押出機, 30...表皮材, 305...リブ, 5...発泡複合体, 1. . First extruder, 10 . . 100. foamable resin for core material; . . Core material, 104. . . Foam, 2. . . First die, 25. . . Nozzle, 3. . . Second extruder, 30. . . Skin material, 305. . . Ribs, 5. . . Foam composite,
───────────────────────────────────────────────────── フロントページの続き (72)発明者 服部 忠 三重県四日市市川尻町1000番地 三菱化学 ビーエーエスエフ株式会社内 Fターム(参考) 4F207 AA03 AA13 AA45 AA46 AB02 AG01 AG03 AG20 AH43 AH46 AR06 KA01 KA11 KB22 KK76 KL58 KL65 ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Tadashi Hattori 1000 Kawajiri-cho, Yokkaichi-shi, Mie F-term in Mitsubishi Chemical BSF Ltd. (reference) 4F207 AA03 AA13 AA45 AA46 AB02 AG01 AG03 AG20 AH43 AH46 AR06 KA01 KA11 KB22 KK76 KL58 KL65
Claims (12)
る芯材用発泡性樹脂を第1押出機の第1ダイスから押し
出し,一方非発泡熱可塑性樹脂又は低発泡性熱可塑性樹
脂よりなる表皮材を第2押出機の第2ダイスから押し出
し,両押出機の先端に設けた上記第1ダイス及び第2ダ
イスの外部において,上記芯材用発泡性樹脂からなる芯
材の外周に上記表皮材を被覆してなる発泡複合体を押出
成形する方法であって,上記第1ダイスからは,複数列
かつ複数段に配置したノズルより,上記芯材用発泡性樹
脂を押出すと共に発泡させて芯材を形成しながら,一方
上記第2ダイスから上記表皮材を上記芯材の外側に押出
すと共に該表面材を直ちに冷却サイジングに導き,上記
芯材用発泡性樹脂の発泡力によって上記表皮材を上記冷
却サイジングの内面に押し当てて,上記芯材用発泡性樹
脂によって形成された複数列かつ複数段の芯材よりなる
発泡体の外表面に上記表皮材を被覆してなる押出し発泡
複合体を製造することを特徴とする押し出し発泡複合体
の製造方法。1. A foaming resin for a core material comprising a thermoplastic resin containing a foaming agent is extruded from a first die of a first extruder, while a skin comprising a non-foaming thermoplastic resin or a low foaming thermoplastic resin. The material is extruded from the second die of the second extruder, and the outer skin material is formed on the outer periphery of the core material made of the foamable resin for the core outside the first die and the second die provided at the tip of both extruders. A foamed composite formed by coating the foamed resin for the core material by extruding and foaming the foamable resin for the core material from the first die through nozzles arranged in a plurality of rows and a plurality of stages. While forming the material, the surface material is extruded from the second die to the outside of the core material, and the surface material is immediately led to cooling sizing, and the surface material is formed by the foaming force of the foamable resin for the core material. Inside of the above cooling sizing To produce an extruded foam composite formed by covering the outer surface of a foam comprising a plurality of rows and a plurality of stages of a core material formed of the foamable resin for a core material with the skin material. A method for producing an extruded foam composite.
上記第2押出機との間に,上記第1ダイス内における上
記芯材用発泡性樹脂の温度が上記表皮材の温度よりも2
0℃以上低い温度となるように調節するための断熱機構
を有することを特徴とする押出し発泡複合体の製造方
法。2. The method according to claim 1, wherein the first die comprises:
The temperature of the foaming resin for the core material in the first die is lower than the temperature of the skin material by two times between the second extruder and the second die.
A method for producing an extruded foam composite, comprising a heat insulating mechanism for adjusting the temperature to a temperature lower than 0 ° C.
泡性樹脂は,上記第1ダイスに設けた,ノズル1個の開
口面積が30mm2以下の複数列かつ複数段のノズルか
ら押し出すと共に,発泡倍率7〜50倍に発泡させるこ
とを特徴とする押出し発泡複合体の製造方法。3. The foaming resin for core material according to claim 1, wherein the foamable resin for the core material is extruded from a plurality of rows and a plurality of rows of nozzles provided in the first die and having an opening area of one nozzle of 30 mm 2 or less. And a foaming ratio of 7 to 50 times.
上記芯材用発泡性樹脂は,ポリスチレン系樹脂75〜9
7.8重量%と発泡剤2〜20重量%と核剤0.2〜5
重量%とよりなり,上記表皮材はスチレン系熱可塑性樹
脂であることを特徴とする押出し発泡複合体の製造方
法。4. The method according to claim 1, wherein:
The foamable resin for the core material is a polystyrene resin 75 to 9
7.8% by weight, foaming agent 2 to 20% by weight, nucleating agent 0.2 to 5
% By weight, wherein the skin material is a styrene-based thermoplastic resin.
上記表皮材はスチレン系熱可塑性樹脂70〜30重量%
とオレフィン系熱可塑性樹脂30〜70重量%とからな
る主成分と,該主成分100重量%に対して熱可塑性エ
ラストマーを1〜7重量%配合してなることを特徴とす
る押出し発泡複合体の製造方法。5. The method according to claim 1, wherein:
The above skin material is 70 to 30% by weight of a styrene thermoplastic resin.
And an olefinic thermoplastic resin in an amount of from 30 to 70% by weight, and a thermoplastic elastomer in an amount of from 1 to 7% by weight based on 100% by weight of the main component. Production method.
トマーは,スチレン・ブタジエン・スチレン(SBS)
又はスチレン・エチレン・ブタジエン・スチレン(SE
BS)であることを特徴とする押出し発泡複合体の製造
方法。6. The thermoplastic elastomer according to claim 5, wherein the thermoplastic elastomer is styrene-butadiene-styrene (SBS).
Or styrene-ethylene-butadiene-styrene (SE
(BS).
列かつ複数段の芯材よりなる発泡体と,該発泡体の周囲
を一体的に被覆してなる非発泡熱可塑性樹脂又は低発泡
性熱可塑性樹脂よりなる表皮材とよりなり,かつ上記複
数列かつ複数段の芯材はその隣接部分が互いに融着して
いることを特徴とする押出し発泡複合体。7. A foam comprising a plurality of rows and a plurality of stages of a core material obtained by foaming a foamable resin for a core material, and a non-foamed thermoplastic resin or a non-foamed thermoplastic resin integrally covering the periphery of the foam material. An extruded foam composite comprising a skin material made of an expandable thermoplastic resin, and wherein the plurality of rows and the plurality of stages of the core material are fused to each other at adjacent portions thereof.
は,複数列かつ複数段の芯材よりなる発泡体の肉厚の
0.1〜25%であることを特徴とする押出し発泡複合
体。8. The extruded foam composite according to claim 7, wherein the thickness of the skin material is 0.1 to 25% of the thickness of the foam comprising a plurality of rows and a plurality of stages of the core material. body.
その表面に上記芯材用発泡性樹脂によるスキン層を有
し,該スキン層は互いに融着していることを特徴とする
押出し発泡複合体。9. The extrusion method according to claim 7, wherein each core material has a skin layer made of the foamable resin for the core material on a surface thereof, and the skin layers are fused to each other. Foam composite.
て,上記芯材はポリスチレン系樹脂であり,表皮材はス
チレン系熱可塑性樹脂であることを特徴とする押出し発
泡複合体。10. The extruded foam composite according to claim 7, wherein the core material is a polystyrene resin, and the skin material is a styrene thermoplastic resin.
て,上記表皮材はスチレン系熱可塑性樹脂70〜30重
量%とオレフィン系熱可塑性樹脂30〜70重量%とか
らなる主成分と,該主成分100重量%に対して熱可塑
性エラストマーを1〜7重量%配合してなることを特徴
とする押出し発泡複合体。11. The skin material according to claim 7, wherein the skin material comprises a main component comprising 70 to 30% by weight of a styrene-based thermoplastic resin and 30 to 70% by weight of an olefin-based thermoplastic resin. An extruded foam composite comprising 1 to 7% by weight of a thermoplastic elastomer with respect to 100% by weight of a main component.
ラストマーは,スチレン・ブタジエン・スチレン(SB
S)又はスチレン・エチレン・ブタジエン・スチレン
(SEBS)であることを特徴とする押出し発泡複合
体。12. The method according to claim 11, wherein the thermoplastic elastomer is styrene-butadiene-styrene (SB).
S) or styrene-ethylene-butadiene-styrene (SEBS).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP07350699A JP3587717B2 (en) | 1999-03-18 | 1999-03-18 | Method for producing extruded foam composite and foam composite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP07350699A JP3587717B2 (en) | 1999-03-18 | 1999-03-18 | Method for producing extruded foam composite and foam composite |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000263624A true JP2000263624A (en) | 2000-09-26 |
| JP3587717B2 JP3587717B2 (en) | 2004-11-10 |
Family
ID=13520216
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP07350699A Expired - Fee Related JP3587717B2 (en) | 1999-03-18 | 1999-03-18 | Method for producing extruded foam composite and foam composite |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3587717B2 (en) |
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| WO2012174106A3 (en) * | 2011-06-13 | 2013-04-18 | Fiber Composites, Llc | Composites utilizing polymeric capstocks and methods of manufacture |
| EP2602086A1 (en) * | 2011-12-08 | 2013-06-12 | Veka AG | Method for producing a plastic hollow profile with at least one hollow chamber with a foamed body and an extrusion tool therefor |
| JP2016135970A (en) * | 2015-01-23 | 2016-07-28 | マックストン株式会社 | Floor panel |
| JPWO2021095727A1 (en) * | 2019-11-11 | 2021-05-20 | ||
| WO2021095727A1 (en) * | 2019-11-11 | 2021-05-20 | マクセルホールディングス株式会社 | Method for producing resin foam board |
| JP7258179B2 (en) | 2019-11-11 | 2023-04-14 | マクセル株式会社 | Method for manufacturing resin foam board |
| US11572646B2 (en) | 2020-11-18 | 2023-02-07 | Material Innovations Llc | Composite building materials and methods of manufacture |
| US12172421B2 (en) | 2020-11-18 | 2024-12-24 | Rise Building Products Llc | Composite building materials and methods of manufacture |
| WO2025126738A1 (en) * | 2023-12-15 | 2025-06-19 | 株式会社カネカ | Heat insulation sash and method for manufacturing same |
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