JP2007106021A - Resin foamed molding and its manufacturing process - Google Patents
Resin foamed molding and its manufacturing process Download PDFInfo
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- JP2007106021A JP2007106021A JP2005300272A JP2005300272A JP2007106021A JP 2007106021 A JP2007106021 A JP 2007106021A JP 2005300272 A JP2005300272 A JP 2005300272A JP 2005300272 A JP2005300272 A JP 2005300272A JP 2007106021 A JP2007106021 A JP 2007106021A
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- Moulds For Moulding Plastics Or The Like (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Molding Of Porous Articles (AREA)
Abstract
Description
本発明は、自動車の内装材等に用いられる樹脂発泡成形体およびその製造方法に関する。 The present invention relates to a resin foam molded body used for automobile interior materials and the like, and a method for producing the same.
従来より、以下のようにして、一対の成形型を離間(コアバック)させて発泡樹脂成形材料を射出成形することが行われている。
まず、雌雄対の成形型を型締めして形成されるキャビティに発泡剤を含む樹脂成形材料を加熱溶融させて充填し、所定秒数の経過後、前記雌雄対の成形型を相互に所定距離だけ離間させてキャビティの容積を拡張する。すると、キャビティ内に充填された樹脂成形材料は、内圧が開放され、内部に含まれる発泡剤が発泡してキャビティに追随して膨張する。その後、樹脂成形材料は、多数の気泡を有する状態で固化し、樹脂発泡成形体とされる。
上記樹脂発泡成形体は、金型に接して成形の早い段階で冷却形成された表面のスキン層と、該スキン層の内側に発泡剤の発泡にともなって形成された発泡層とを有する構造とされている。得られる樹脂発泡成形体は、軽量で触感が柔らかく、自動車の内装用のパネル等での用途がある。また、成形工程が一工程で済む合理的な利点がある。
Conventionally, a foamed resin molding material is injection molded by separating a pair of molds (core back) as follows.
First, a resin molding material containing a foaming agent is heated and melted and filled in a cavity formed by clamping a male and female mold, and after a predetermined number of seconds, the male and female molds are placed at a predetermined distance from each other. The cavity volume is expanded by being spaced apart by a distance. Then, the resin molding material filled in the cavity is released from the internal pressure, and the foaming agent contained therein expands to follow the cavity and expand. Thereafter, the resin molding material is solidified in a state having a large number of bubbles to form a resin foam molding.
The resin foam molded body has a structure having a skin layer on the surface formed by cooling in contact with a mold at an early stage of molding, and a foam layer formed along with foaming of the foaming agent inside the skin layer. Has been. The obtained resin foam molded article is lightweight and soft to the touch, and has applications in automobile interior panels and the like. In addition, there is a reasonable advantage that the molding process is completed in one step.
特許文献1には、スキン層、低発泡層、高発泡層の少なくとも3種類の層をこの順に含有し、低発泡層の近傍の高発泡層に存在する気泡の厚み方向の径(Da1)と該厚み方向と垂直な方向の径(Da2)との比(Da1/Da2)が1〜4であり、高発泡層の厚み方向中心近傍の気泡の厚み方向の径(Db1)と該厚み方向と垂直な方向の径(Db2)との比(Db1/Db2)が4を超え10以下である、熱可塑性樹脂発泡成形体が記載されている。同文献の段落0015では、高発泡層部分の拡大写真について、低発泡層に接する部分の0.5mm角に相当する領域を取り、この領域に含まれる気泡とその大部分が0.5mm角の領域に含まれる気泡についてそれぞれの厚み方向の径(Da1)と該厚み方向と垂直な方向の径(Da2)を測定し、個数平均値を算出することにより求めることが記載されている。 Patent Document 1 contains at least three types of layers, a skin layer, a low foam layer, and a high foam layer, in this order, and the diameter (Da1) in the thickness direction of the bubbles present in the high foam layer near the low foam layer. The ratio (Da1 / Da2) to the diameter (Da2) in the direction perpendicular to the thickness direction is 1 to 4, the diameter (Db1) in the thickness direction of the bubble near the center of the thickness direction of the high foam layer and the thickness direction A thermoplastic resin foam molded article having a ratio (Db1 / Db2) to a diameter (Db2) in a vertical direction of more than 4 and 10 or less is described. In paragraph 0015 of the same document, for the enlarged photograph of the high foam layer part, an area corresponding to 0.5 mm square of the part in contact with the low foam layer is taken, and the bubbles contained in this area and most of them are 0.5 mm square. It is described that the bubbles contained in the region are obtained by measuring the diameter (Da1) in the thickness direction and the diameter (Da2) in the direction perpendicular to the thickness direction and calculating the number average value.
特許文献2には、内在するセルが厚み方向に紡錘状に延びたポリオレフィン発泡体からなるクッション層と表面層とを含む床材であって、クッション層の厚さが2〜15mmで、発泡倍率が4〜20倍で、内在するセルのアスペクト比Dz/Dxyの平均値が1.1〜4である衝撃吸収床材が記載されている。
特許文献1記載の熱可塑性樹脂発泡成形体は、0.5mm角の領域に含まれる気泡から径Da1,Da2を求めており、気泡の最大長径が0.5mm程度と小さい気泡を多数有するものである。このため、発泡成形体内部の通気性が無く、自動車の内装材としての触感が良好であるとは言えず、吸音性が高いとは言えなかった。
特許文献2記載の衝撃吸収床材も、アスペクト比の平均値が1.1〜4と、特許文献1記載の熱可塑性樹脂発泡成形体よりも小さいため、最大長径が1mmに達するような非常に細長いセルは存在しない。また、同公報図1(b)に示すように、セルどうしが連通していないため、床材内部の通気性が無く、内装材としての触感が良好であるとは言えず、吸音性も高いとは言えなかった。
The thermoplastic resin foam molded article described in Patent Document 1 has a diameter Da1, Da2 obtained from bubbles contained in a 0.5 mm square region, and has a large number of small bubbles with a maximum long diameter of about 0.5 mm. is there. For this reason, there is no air permeability inside the foam molded article, and it cannot be said that the tactile sensation as an automobile interior material is good, and the sound absorption is not high.
Since the shock absorbing floor material described in Patent Document 2 also has an average aspect ratio of 1.1 to 4, which is smaller than the thermoplastic resin foam molded body described in Patent Document 1, the maximum major axis is very large, reaching 1 mm. There are no elongated cells. Further, as shown in FIG. 1B, since the cells are not communicated with each other, there is no air permeability inside the flooring, and it cannot be said that the tactile sensation as an interior material is good, and the sound absorption is high. I couldn't say that.
本発明は、上記課題に鑑みてなされたもので、軽量ながら厚み方向への圧縮力に対して座屈しにくく自動車の内装材として良好な弾性かつ良好な触感を得ることができるとともに、高い吸音性を得ることが可能な樹脂発泡成形体の提供を目的とする。 The present invention has been made in view of the above-mentioned problems, and is lightweight and hardly buckled against a compressive force in the thickness direction, and can provide good elasticity and good tactile sensation as an automobile interior material, and has high sound absorption. It is an object of the present invention to provide a resin foam molded product capable of obtaining the above.
上記目的を達成するため、本発明は、互いに近接および離反可能な一対の成形型を所定の近接位置に近接させたときに形成されるキャビティに発泡剤を含む樹脂成形材料を充填した後、前記一対の成形型を所定の離間位置まで離間させて前記キャビティを拡張させることにより該キャビティ内の樹脂成形材料に発泡セルを形成させて成形した樹脂発泡成形体であって、前記近接位置にあるときの前記一対の成形型の間の距離を1.0〜10.0mmとし、前記近接位置から前記離間位置までの離間距離を1.0〜50.0mmとして、表面に非発泡のスキン層を形成しながら前記一対の成形型の離間方向へ前記離間距離以下で1.0mm以上となるように気泡を連続させて霜柱状に発泡セルを伸長させて成形したことを特徴とする。 In order to achieve the above-mentioned object, the present invention fills a cavity formed when a pair of molds capable of approaching and separating from each other are brought close to a predetermined proximity position with a resin molding material containing a foaming agent, and then A resin foam molded body formed by forming a foam cell in a resin molding material in the cavity by separating a pair of molds to a predetermined separation position and expanding the cavity, and when the resin is in the proximity position The distance between the pair of molds is set to 1.0 to 10.0 mm, and the separation distance from the proximity position to the separation position is set to 1.0 to 50.0 mm to form a non-foamed skin layer on the surface. However, the foamed cells were formed by extending the foamed cells in the form of frost columns so that the distance between the pair of molds is 1.0 mm or more in the separation direction.
本樹脂発泡成形体は、表面に非発泡のスキン層が形成され、内部に離間方向へ1mm以上と非常に細長い連続気泡の霜柱状発泡セルが形成されている。各発泡セルの容積が大きくなり、成形体の組織が低密度になっても、離間方向とは垂直な方向における発泡セルの壁どうしの距離が小さいため、軽量ながら厚み方向への圧縮力に対して座屈しにくく自動車の内装材として良好な弾性かつ良好な触感を得ることができる。また、発泡セルが非常に細長い連続気泡の霜柱状に形成されるので、樹脂発泡成形体内部に通気性があり、高い吸音性を得ることが可能になる。 The resin foamed molded article has a non-foamed skin layer formed on the surface thereof, and a very elongated open-cell frosted columnar foam cell of 1 mm or more in the separation direction is formed inside. Even if the volume of each foam cell is large and the structure of the molded product is low in density, the distance between the foam cell walls in the direction perpendicular to the separation direction is small, so it is lightweight but can withstand the compressive force in the thickness direction. It is hard to buckle and can provide good elasticity and good tactile sensation as an automobile interior material. In addition, since the foam cell is formed in the shape of a very elongated open-cell frost column, the inside of the resin foam molded body has air permeability, and high sound absorption can be obtained.
また、本発明の樹脂発泡成形体は、前記キャビティに充填された樹脂成形材料内で前記離間方向とは垂直な方向へ該離間方向の温度分布を異ならせて前記一対の成形型を離間させることにより表面に非発泡のスキン層を形成しながら前記温度分布の異なりに応じた空洞を内部に形成して成形したことを特徴とする。
本樹脂発泡成形体は、キャビティに充填された樹脂成形材料内で離間方向とは垂直な方向へ異ならせた該離間方向の温度分布の異なりに応じた空洞が内部に形成されている。これにより、樹脂発泡成形体内部の通気性が高くされるので、軽量で、高い吸音性を得ることが可能になる。
Further, the resin foam molded body of the present invention separates the pair of molds by varying the temperature distribution in the separation direction in a direction perpendicular to the separation direction in the resin molding material filled in the cavity. Thus, a non-foamed skin layer is formed on the surface, and a cavity corresponding to the difference in temperature distribution is formed inside and molded.
In the resin foam molded body, cavities are formed in the resin molding material filled in the cavities according to the difference in temperature distribution in the separation direction which is different in the direction perpendicular to the separation direction. Thereby, since the air permeability inside the resin foam molding is increased, it is possible to obtain light weight and high sound absorption.
上述した樹脂発泡成形体の製造方法にも発明が存在し、同様の作用、効果が得られる。 The invention also exists in the method for producing the resin foam molded body described above, and the same action and effect can be obtained.
請求項1、請求項10にかかる発明によれば、軽量ながら厚み方向への圧縮力に対して座屈しにくく自動車の内装材として良好な弾性かつ良好な触感を得ることができるとともに、高い吸音性を得ることが可能な樹脂発泡成形体を提供することができる。
請求項2にかかる発明では、造核剤が適度な核形成材となって、気泡が適度に緻密かつ均一に形成され、高い吸音性を維持しながら内装材としての触感を向上させることができる。
請求項3にかかる発明では、吸音性を向上させることができるとともに、内装材としての弾性および触感をさらに良好にさせることができる。
According to the first and tenth aspects of the invention, while being lightweight, it is difficult to buckle against compressive force in the thickness direction, and can provide good elasticity and good tactile sensation as an automobile interior material, and also has high sound absorption It is possible to provide a resin foam molded article capable of obtaining the above.
In the invention according to claim 2, the nucleating agent becomes an appropriate nucleating material, the bubbles are formed in a moderately dense and uniform manner, and the tactile sensation as the interior material can be improved while maintaining high sound absorption. .
In the invention according to the third aspect, the sound absorption can be improved, and the elasticity and tactile sensation as the interior material can be further improved.
請求項4にかかる発明では、発泡セルを安定して霜柱状に形成することができるので、高い吸音性を維持しながら内装材としての弾性および触感をさらに良好にさせることができる。
請求項5、請求項6にかかる発明では、吸音性をさらに向上させた樹脂発泡成形体を得ることができる。
請求項7にかかる発明では、良好な吸音性の樹脂発泡成形体を容易に得ることができる。
請求項8にかかる発明では、発泡セルを安定して霜柱状に形成することができるので、高い吸音性を維持しながら内装材としての弾性および触感をさらに良好にさせることができる。
In the invention according to claim 4, since the foamed cell can be stably formed in a frost column shape, the elasticity and tactile sensation as the interior material can be further improved while maintaining high sound absorption.
In the invention concerning Claim 5 and Claim 6, the resin foam molded object which further improved the sound-absorbing property can be obtained.
In the invention concerning Claim 7, a favorable sound-absorbing resin foam molded article can be easily obtained.
In the invention according to claim 8, since the foam cell can be stably formed in a frost column shape, the elasticity and tactile sensation as the interior material can be further improved while maintaining high sound absorption.
請求項9、請求項11にかかる発明では、軽量で、高い吸音性を得ることが可能な樹脂発泡成形体を提供することができる。
請求項12にかかる発明では、タルク量を調整することにより吸音性を調節して樹脂発泡成形体を製造することができる。
According to the ninth and eleventh aspects of the present invention, it is possible to provide a resin foam molded body that is lightweight and capable of obtaining high sound absorption.
In the invention according to claim 12, the resin foam molded article can be produced by adjusting the sound absorption by adjusting the amount of talc.
以下、下記の順序に従って本発明の実施の形態について説明する。
(1)樹脂発泡成形体の製造方法:
(2)変形例:
(3)実施例:
Hereinafter, embodiments of the present invention will be described in the following order.
(1) Manufacturing method of resin foam molding:
(2) Modification:
(3) Example:
(1)樹脂発泡成形体の製造方法:
図1は本発明の一実施形態にかかる樹脂発泡成形体M10の製造方法を模式的に示す図、図2は本製造方法に用いられる発泡射出成形機10を模式的に示す図、図3は樹脂発泡成形体M10の構造を垂直断面にて示す図、図4は別の樹脂発泡成形体の構造を垂直断面にて示す図、図5は成形型11の移動量を示すタイミングチャート、図6は変形例において成形型11の移動量を示すタイミングチャートである。
本樹脂発泡成形体M10は、自動車の内装材等に用いられる。
(1) Manufacturing method of resin foam molding:
FIG. 1 is a diagram schematically showing a method of manufacturing a resin foam molded body M10 according to an embodiment of the present invention, FIG. 2 is a diagram schematically showing a foam injection molding machine 10 used in the present manufacturing method, and FIG. FIG. 4 is a diagram showing the structure of the resin foam molded body M10 in a vertical section, FIG. 4 is a diagram showing the structure of another resin foam molded body in a vertical section, FIG. 5 is a timing chart showing the amount of movement of the molding die 11, and FIG. These are timing charts showing the amount of movement of the mold 11 in the modified example.
The resin foam molded body M10 is used for automobile interior materials and the like.
本製造方法では、互いに近接および離反可能な一対の成形型11,12を所定の近接位置L1に近接させたときに形成されるキャビティC1に発泡剤を含む樹脂成形材料M1を充填した後、前記一対の成形型11,12を所定の離間位置L2まで離間(コアバック)させて前記キャビティC1を拡張させることにより該拡張したキャビティC1内の樹脂成形材料に霜柱状の発泡セルM13を形成させて樹脂発泡成形体M10を成形する。成形体M10は、平板状、曲板状、シート状、等、薄く広がった形状に形成され、該成形体の表面は、平面形状、曲面形状、凹凸形状、等、様々な形状とすることができる。
ここで、近接位置L1にあるときの一対の成形型11,12の間の距離d1は、1.0〜10.0mmとされている。距離d1を下限以上にすると厚み方向(離間方向D1)の途中で発泡セルが切断されず霜柱状発泡セルが厚み方向へ十分に長くなって内部の通気性が大きくなることにより良好な吸音性が得られ内装材として良好な弾性かつ良好な触感が得られる点で好ましく、距離d1を上限以下にすると樹脂発泡成形体が固くなりすぎないとともに霜柱状発泡セルが厚み方向へ十分に長くなって内部の通気性が大きくなることにより良好な吸音性が得られ良好な弾性かつ良好な触感が得られる点で好ましいためである。また、近接位置L1から離間位置L2までの離間距離(コアバック距離)d2は、1.0〜50.0mmとされ、より好ましくは4.0〜7.0mmとされる。距離d2を下限以上にすると離間方向D1において発泡セルが1.0mm以上と十分に長くなって内部の通気度が大きくなることにより良好な吸音性が得られる点で好ましく、距離d2を上限以下にすると厚み方向の途中で発泡セルが切断されないことにより内装材として良好な弾性かつ良好な触感が得られる点で好ましいためである。なお、樹脂発泡成形体M10の厚みd3は、d1+d2となる。
そして、本製造方法は、表面に非発泡のスキン層M16を形成しながら、一対の成形型11,12の離間方向D1へ前記離間距離d2以下の範囲内で1.0mm以上となるように気泡を連続させて霜柱状に発泡セルM13を伸長させて、樹脂発泡成形体M10を成形する。
In this manufacturing method, the resin molding material M1 containing a foaming agent is filled into the cavity C1 formed when a pair of molds 11 and 12 that can approach and separate from each other are brought close to a predetermined proximity position L1, and then the above-mentioned The pair of molds 11 and 12 are separated (core back) to a predetermined separation position L2 to expand the cavity C1, thereby forming a frost column-shaped foam cell M13 in the resin molding material in the expanded cavity C1. Resin foam molding M10 is molded. The molded body M10 is formed in a thin and wide shape such as a flat plate shape, a curved plate shape, a sheet shape, and the surface of the molded body may have various shapes such as a planar shape, a curved surface shape, and an uneven shape. it can.
Here, the distance d1 between the pair of molds 11 and 12 when in the proximity position L1 is set to 1.0 to 10.0 mm. When the distance d1 is greater than or equal to the lower limit, the foamed cells are not cut in the middle of the thickness direction (separating direction D1), and the frost columnar foamed cells are sufficiently long in the thickness direction to increase the internal air permeability, thereby providing good sound absorption. The obtained interior material is preferable in terms of obtaining good elasticity and good tactile sensation, and if the distance d1 is set to the upper limit or less, the resin foam molded body does not become too hard and the frost columnar foam cell becomes sufficiently long in the thickness direction and the inside. This is because it is preferable in that good air-absorbing property can be obtained and good elasticity and good tactile sensation can be obtained. Further, the separation distance (core back distance) d2 from the proximity position L1 to the separation position L2 is 1.0 to 50.0 mm, more preferably 4.0 to 7.0 mm. It is preferable that the distance d2 is not less than the lower limit in that the foamed cell is sufficiently long as 1.0 mm or more in the separation direction D1 and the internal air permeability is increased so that good sound absorption can be obtained. Then, it is because it is preferable at the point from which a favorable elasticity and a favorable tactile sensation are obtained as an interior material by a foam cell not being cut | disconnected in the middle of the thickness direction. The thickness d3 of the resin foam molded body M10 is d1 + d2.
Then, in this manufacturing method, while forming the non-foamed skin layer M16 on the surface, the air bubbles are adjusted to 1.0 mm or more in the range of the separation distance d2 or less in the separation direction D1 of the pair of molds 11 and 12. The foamed cell M13 is elongated in a frost column shape to form a resin foam molded body M10.
本樹脂発泡成形体M10は、一対の成形型11,12の成形面に接触した両側の表面に非発泡のスキン層M16,M16が形成され、両スキン層M16,M16に挟まれた内部が発泡層M12とされている。
スキン層M16は、液状の樹脂成形材料よりも温度の低い成形型11,12の成形面に接した部分の樹脂成形材料が早く温度低下して発泡せずに固化することにより、非発泡の状態で形成される。その結果、スキン層の空隙率は、1%未満とされる。
スキン層の厚みd4は、樹脂成形材料の温度、成形型11,12の成形面の温度、成形型11,12の離間のタイミングで制御される。樹脂成形材料の温度や成形型の成形面の温度を低くするか成形型の離間のタイミングを遅くするとスキン層が厚くなり、樹脂成形材料の温度や成形型の成形面の温度を高くするか成形型の離間のタイミングを早くするとスキン層が薄くなる。スキン層の厚みd4は、成形型11,12の間の距離d1の半分未満の範囲内で0.1〜1.0mmが好ましい。厚みd4が前記下限以上になると内装材として良好な弾性かつ良好な触感が得られ、厚みd4が前記上限以下になると樹脂発泡成形体が固くなりすぎず良好な弾性かつ良好な触感が得られる点で好ましいためである。
In the resin foam molded body M10, non-foamed skin layers M16 and M16 are formed on both surfaces in contact with the molding surfaces of the pair of molds 11 and 12, and the inside sandwiched between the skin layers M16 and M16 is foamed. The layer is M12.
The skin layer M16 is in a non-foamed state because the temperature of the resin molding material in contact with the molding surfaces of the molding dies 11, 12 having a temperature lower than that of the liquid resin molding material is rapidly lowered and solidified without foaming. Formed with. As a result, the porosity of the skin layer is less than 1%.
The thickness d4 of the skin layer is controlled by the temperature of the resin molding material, the temperature of the molding surfaces of the molding dies 11 and 12, and the timing of the separation of the molding dies 11 and 12. If the temperature of the resin molding material or the molding surface of the molding die is lowered or the timing of separating the molding die is delayed, the skin layer becomes thick, and the temperature of the resin molding material or the molding surface of the molding die is increased or molded. If the mold separation timing is advanced, the skin layer becomes thinner. The thickness d4 of the skin layer is preferably 0.1 to 1.0 mm within a range less than half of the distance d1 between the molds 11 and 12. When the thickness d4 is not less than the above lower limit, good elasticity and good tactile sensation can be obtained as an interior material, and when the thickness d4 is not more than the above upper limit, the resin foam molded article is not too hard and good elasticity and good tactile sensation can be obtained. This is because it is preferable.
発泡層M12は、離間方向D1へ離間距離d2以下で1.0mm以上気泡を連続させて霜柱状に伸長した発泡セルM13が形成されている。
図3を参照して説明すると、コアバックの初期に生じた樹脂成形材料中の多数のミクロな気泡は、成形型の離間および発泡剤の発泡作用により離間方向D1へ伸長し、略離間方向に隣接する他の気泡との間に連結口M13aが生じ、離間方向へ柱状につながっていく。図の例では、気泡a1,a2,a3,a4が離間方向へ連通して柱状の連続セルが形成されていることが示されている。一方、離間方向とは垂直な方向D2へは、隣接する他の気泡の存在により成長が抑えられるが、セルの壁が薄くなることにより隣接する他の気泡との間に連結口M13bが生じる。その結果、離間方向D1へ伸長した霜柱状の発泡セルM13が形成される。図の例では、気泡a2と気泡b2とが連通し、気泡a1と気泡c1とが連通して、発泡セルが霜柱状に組織化されていることが示されている。
発泡セルM13は、離間方向の長さd5が上記垂直方向D2における柱状の各セルの径に対して極めて大きく、楕円体ないし紡錘体という概念とは異なる形状になっている。ここで、発泡セルの離間方向の長さd5は、連通した気泡の中で離間方向D1へ最も長い部分の長さ、すなわち図3において連通した気泡の中で最も上側となる上下方向の位置と最も下側となる上下方向の位置との上下方向の差の長さをいうものとする。また、上記垂直方向D2の断面で見ると、気泡a1,a2,a3,a4のように気泡が千鳥状につながっていく結果、セルの断面はジグザグとなり、円形ないし楕円形という概念とは異なる形状になる傾向がある。なお、発泡セルは、発泡層の両側にある両スキン層に繋がる長さとなることもある。
The foamed layer M12 is formed with foamed cells M13 that are expanded in a frost column shape by continuing bubbles of 1.0 mm or more in the separation direction D1 with a separation distance d2 or less.
Referring to FIG. 3, a large number of micro bubbles in the resin molding material generated at the initial stage of the core back expand in the separation direction D1 due to the separation of the mold and the foaming action of the foaming agent, and in the substantially separation direction. A connection port M13a is formed between other adjacent bubbles, and is connected in a columnar shape in the separation direction. In the example of the figure, it is shown that bubbles a1, a2, a3, and a4 communicate with each other in the separating direction to form a columnar continuous cell. On the other hand, in the direction D2 perpendicular to the separation direction, the growth is suppressed by the presence of other adjacent bubbles, but the connection port M13b is formed between the other adjacent bubbles due to the thin wall of the cell. As a result, a frost column-like foam cell M13 extending in the separation direction D1 is formed. In the example of the figure, it is shown that the bubbles a2 and the bubbles b2 communicate with each other, the bubbles a1 and the bubbles c1 communicate with each other, and the foamed cells are organized in a frost column shape.
The foam cell M13 has a length d5 in the separation direction that is very large with respect to the diameter of each columnar cell in the vertical direction D2, and has a shape different from the concept of an ellipsoid or spindle. Here, the length d5 of the foam cell in the separation direction is the length of the longest portion of the connected bubbles in the separation direction D1, that is, the vertical position that is the uppermost of the bubbles communicated in FIG. The length of the difference in the vertical direction from the lowest vertical position is assumed. Further, when viewed in the cross section in the vertical direction D2, as a result of the bubbles being connected in a staggered manner like the bubbles a1, a2, a3, and a4, the cross section of the cell becomes zigzag, which is different from the concept of a circle or ellipse. Tend to be. In addition, a foam cell may become the length connected with the both skin layers in the both sides of a foam layer.
発泡層M12は、霜柱状の発泡セルM13が形成される結果、離間方向とは垂直な方向D1へ通気性を有するように形成される。ここで、前記垂直方向D2へ厚み5.0mmとなるように切断したときのJIS L1096のフラジール形法による通気度が0.4cc/cm2/sec以上となるように発泡層を形成すると、高い吸音性の樹脂発泡成形体が得られる。ここで、発泡層の前記垂直方向D2の通気度を大きくするには、例えば、発泡セルM13を離間方向D1へ長くすればよく、成形型の離間距離d2を長くすればよい。また、成形型の離間距離d2を調整することにより、発泡層の前記垂直方向D2の通気度を調節することができる。
さらに、発泡層の密度が0.03〜0.5g/cm3となるように樹脂発泡成形体を成形すると、厚み方向への圧縮力に対して座屈しにくく内装材として良好な弾性かつ良好な触感を得るとともに高い吸音性を得ることが可能になる。ここで、発泡層の密度を小さくするには、例えば、発泡セルM13を離間方向D1へ長くすればよく、成形型の離間距離d2を長くすればよい。また、成形型の離間距離d2を調整することにより、発泡層の密度を調節することができる。なお、発泡倍率は、近接位置にあるときの一対の成形型の間の距離をd1、離間距離をd2として、(d1+d2)/d1とする。求められる発泡倍率と樹脂成形材料の密度とスキン層の厚みd4とから発泡層の密度のおおよそを求めることができるので、発泡倍率と樹脂成形材料の密度とスキン層の厚みd4をみて発泡層の密度を調節することができる。
The foam layer M12 is formed so as to have air permeability in the direction D1 perpendicular to the separation direction as a result of the formation of the frost column-like foam cell M13. Here, when the foamed layer is formed so that the air permeability according to the fragile method of JIS L1096 when cut to a thickness of 5.0 mm in the vertical direction D2 is 0.4 cc / cm 2 / sec or more, it is high. A sound-absorbing resin foam molding is obtained. Here, in order to increase the air permeability of the foam layer in the vertical direction D2, for example, the foam cell M13 may be elongated in the separation direction D1, and the separation distance d2 of the mold may be increased. Further, the air permeability in the vertical direction D2 of the foam layer can be adjusted by adjusting the separation distance d2 of the mold.
Furthermore, when the resin foam molded body is molded so that the density of the foamed layer is 0.03 to 0.5 g / cm 3, it is less likely to buckle against the compressive force in the thickness direction and has good elasticity and good as an interior material. It becomes possible to obtain tactile sensation and high sound absorption. Here, in order to reduce the density of the foam layer, for example, the foam cell M13 may be lengthened in the separation direction D1, and the separation distance d2 of the mold may be lengthened. Further, the density of the foam layer can be adjusted by adjusting the separation distance d2 of the mold. The expansion ratio is (d1 + d2) / d1, where d1 is the distance between the pair of molds when they are close to each other, and d2 is the separation distance. Since the approximate density of the foamed layer can be obtained from the required foaming ratio, the density of the resin molding material, and the thickness d4 of the skin layer, the density of the foamed layer can be determined by examining the foaming ratio, the density of the resin molding material, and the thickness d4 of the skin layer. The density can be adjusted.
なお、図4に示すように、発泡層M12においてスキン層M16,M16に接触する表面側の部分に、離間方向D2へ短い発泡セルM15を有する中間層M14が形成されてもよい。発泡セルM15は、隣接する気泡が連結も連通もしていない独立セルでもよい。 As shown in FIG. 4, an intermediate layer M <b> 14 having a foam cell M <b> 15 that is short in the separation direction D <b> 2 may be formed on the surface side of the foam layer M <b> 12 that contacts the skin layers M <b> 16 and M <b> 16. The foam cell M15 may be an independent cell in which adjacent bubbles are not connected or communicated.
樹脂成形材料M1を構成する樹脂としては、加熱して溶融させることができる観点から熱可塑性樹脂(合成樹脂の一種)が好ましいが、フェノール樹脂やユリア樹脂等の各種熱硬化性樹脂(合成樹脂の一種)、合成樹脂にゴム成分等の軟質成分を配合してエラストマー的な性質を高めた改質樹脂、等を用いることができる。
熱可塑性樹脂としては、オレフィン系樹脂やオレフィン系熱可塑性エラストマー等を用いることができ、単独重合体でも、2種以上のモノマーを共重合させた共重合体でも、オレフィンと不飽和カルボン酸とを共重合させた共重合体でも、これらの組み合わせでもよく、具体的には、ポリプロピレン、ポリエチレン、アクリロニトリルブタジエンスチレン樹脂(ABS樹脂)、ポリエチレンテレフタレート(PET)、ポリアミド、ポリスチレン、これらの組み合わせ、これらの樹脂にゴム成分を配合した改質樹脂、等を用いることができる。
The resin constituting the resin molding material M1 is preferably a thermoplastic resin (a kind of synthetic resin) from the viewpoint of being able to be heated and melted, but various thermosetting resins (such as a phenolic resin and a urea resin) 1 type), a modified resin in which a soft component such as a rubber component is blended with a synthetic resin to improve elastomeric properties, and the like can be used.
As the thermoplastic resin, an olefin resin, an olefin thermoplastic elastomer, or the like can be used. Either a homopolymer or a copolymer obtained by copolymerizing two or more types of monomers, an olefin and an unsaturated carboxylic acid can be used. Copolymerized copolymers or combinations thereof may be used. Specifically, polypropylene, polyethylene, acrylonitrile butadiene styrene resin (ABS resin), polyethylene terephthalate (PET), polyamide, polystyrene, combinations thereof, these resins For example, a modified resin in which a rubber component is blended can be used.
樹脂成形材料M1に含ませる発泡剤としては、常温1気圧で気体の不活性ガスや揮発性有機化合物等の物理発泡剤、加熱により分解または反応してガスを発生する化学発泡剤、これらの組み合わせ、を用いることができる。発泡剤に不活性ガスを用いると、樹脂と反応せず、樹脂を劣化させることがないので好ましい。不活性ガスとしては、二酸化炭素、窒素、アルゴン、ヘリウム、ネオン、これらの組み合わせ、等を用いることができる。揮発性有機化合物としては、ブタンやペンタン等の炭化水素を発生させる揮発性発泡剤等を用いることができる。化学発泡剤としては、炭酸アンモニウムや炭酸水素ナトリウム等の炭酸ガス等を発生させる無機系発泡剤、ポリカルボン酸やアゾ化合物等の有機化合物のガスを発生させる有機系発泡剤、等を用いることができる。 The foaming agent contained in the resin molding material M1 includes a physical foaming agent such as a gas inert gas or a volatile organic compound at a normal temperature of 1 atm, a chemical foaming agent that decomposes or reacts by heating to generate gas, and a combination thereof. Can be used. It is preferable to use an inert gas for the foaming agent because it does not react with the resin and does not deteriorate the resin. As the inert gas, carbon dioxide, nitrogen, argon, helium, neon, a combination thereof, or the like can be used. As the volatile organic compound, a volatile foaming agent that generates hydrocarbons such as butane and pentane can be used. As the chemical foaming agent, an inorganic foaming agent that generates a carbon dioxide gas such as ammonium carbonate or sodium hydrogen carbonate, an organic foaming agent that generates a gas of an organic compound such as polycarboxylic acid or azo compound, or the like may be used. it can.
ここで、不活性ガスに造核剤を併用すると、造核剤が適度な核形成材となって、気泡が適度に緻密かつ均一に形成され、より高い吸音性を維持しながら内装材としての触感の良好な樹脂発泡成形体を形成することができる。造核剤を含まない樹脂成形材料に対する造核剤の添加割合は、物理発泡剤を発泡させる核として機能する配合割合であればよく、例えば、造核剤を含まない樹脂成形材料100重量部に対して1重量部以上50重量部未満(より好ましくは1〜20重量部)の範囲内とすることができる。また、造核剤として化学発泡剤を用いる場合、化学発泡剤は不活性ガスの発泡を補助する機能を有する。なお、造核剤の配合割合を調整することにより、発泡セルの緻密度を調節し、吸音性を調節することができる。また、樹脂成形材料に注入する不活性ガスの圧力は、0.5〜20MPaが好ましく。1.5〜7.0MPaがさらに好ましい。不活性ガスの圧力を前記下限以上にすると、樹脂成形材料に対する不活性ガスの溶解量が十分となり、高発泡倍率の樹脂発泡成形体が得られる点で好ましい。一方、不活性ガスの圧力を前記上限以下にすると、不活性ガスの無駄が無くなり、ガス注入装置や金型に汎用品を用いることができる結果安価になるので好ましい。 Here, when a nucleating agent is used in combination with an inert gas, the nucleating agent becomes an appropriate nucleating material, and bubbles are formed moderately densely and uniformly, and as an interior material while maintaining higher sound absorption A resin foam molded article having good tactile sensation can be formed. The addition ratio of the nucleating agent with respect to the resin molding material not containing the nucleating agent may be a blending ratio that functions as a nucleus for foaming the physical foaming agent. For example, 100 parts by weight of the resin molding material not containing the nucleating agent On the other hand, it can be in the range of 1 to 50 parts by weight (more preferably 1 to 20 parts by weight). Moreover, when using a chemical foaming agent as a nucleating agent, a chemical foaming agent has the function to assist foaming of an inert gas. In addition, by adjusting the blending ratio of the nucleating agent, the density of the foamed cells can be adjusted and the sound absorption can be adjusted. Further, the pressure of the inert gas injected into the resin molding material is preferably 0.5 to 20 MPa. 1.5 to 7.0 MPa is more preferable. When the pressure of the inert gas is set to the above lower limit or more, the amount of the inert gas dissolved in the resin molding material is sufficient, which is preferable in that a resin foam molded body having a high expansion ratio can be obtained. On the other hand, it is preferable to set the pressure of the inert gas below the upper limit because the inert gas is not wasted and a general-purpose product can be used for the gas injection device and the mold, resulting in a low cost.
樹脂成形材料M1を樹脂と発泡剤のみで構成してもよいが、樹脂成形材料M1に添加剤を含ませてもよい。添加剤としては、タルク等の充てん材、核剤、顔料、滑剤、酸化防止剤、熱安定剤、紫外線吸収剤、帯電防止剤、これらの組み合わせ、等を用いることができる。樹脂成形材料中の各材料の配合割合は、樹脂の性質を十分に残す観点からは、樹脂を50重量%以上(好ましくは65重量%以上)、添加剤を50重量%未満(好ましくは35重量%未満)とすることができる。
樹脂成形材料にタルクを含ませると発泡セルを小さくさせることができ、タルクの配合量を多くするほど発泡セルを小さくすることができる。そこで、樹脂成形材料に含まれるタルクの重量比を調整することにより、発泡セルの大きさを調節して樹脂発泡成形体を成形することができる。従って、タルク量を調整することにより、樹脂発泡成形体の吸音性を調節することができる。
The resin molding material M1 may be composed of only a resin and a foaming agent, but an additive may be included in the resin molding material M1. As additives, fillers such as talc, nucleating agents, pigments, lubricants, antioxidants, heat stabilizers, ultraviolet absorbers, antistatic agents, combinations thereof, and the like can be used. The blending ratio of each material in the resin molding material is 50% by weight (preferably 65% by weight or more) of resin and less than 50% by weight of additive (preferably 35% by weight) from the viewpoint of sufficiently retaining the properties of the resin. %)).
When talc is included in the resin molding material, the foam cell can be made smaller, and the foam cell can be made smaller as the blending amount of talc is increased. Therefore, by adjusting the weight ratio of talc contained in the resin molding material, the size of the foam cell can be adjusted to mold the resin foam molded body. Therefore, by adjusting the amount of talc, the sound absorption property of the resin foam molded article can be adjusted.
本樹脂発泡成形体を成形するのに適する射出成形機としては、公知のインラインスクリュー式の射出成形機を用いることが可能であり、形態(堅型、横型)や駆動方式(油圧式、電動式等)は問わない。
図2は、本樹脂発泡成形体を成形するための発泡射出成形機の一例を示している。発泡射出成形機10は、雄型11、雌型12、成形材料投入ホッパ13、ガス貯留タンク14、樹脂成形材料の押出方向を軸とした円筒形状の外筒部材15、該外筒部材に挿入されたスクリュー16、外筒部材15の途中に付設されたガス注入装置17、スクリュー16を回転駆動する図示しないモータ、等を備え、部材11〜16が金属製とされている。スクリュー16のL/D比は、例えば、20程度とすることができる。外筒部材15の先に取り付けられる成形型11,12は、雌雄対の金型とされ、型締め状態で密閉された所要のキャビティC1を形成する。ガス注入装置17は、例えば、不活性ガスの注入圧力を一定圧力に制御する。
発泡射出成形機10は、射出口15aから液状(溶融状態を含む)の樹脂成形材料をキャビティC1に射出し、雌型12から雄型11を所定の離間位置まで離間させてキャビティC1内の樹脂成形材料を発泡させ、該樹脂成形材料を固化または硬化させて成形することにより、樹脂発泡射出成形体M10を形成する。そして、金型11,12を開けて成形体M10を取り出すことにより、樹脂発泡射出成形体の製造の1サイクルが終了する。
なお、成形型11として、スライドコアを用いた金型を用いてもよい。
As an injection molding machine suitable for molding the resin foam molded body, a known in-line screw type injection molding machine can be used, and its form (solid type, horizontal type) and drive system (hydraulic type, electric type) Etc.) does not matter.
FIG. 2 shows an example of a foam injection molding machine for molding the resin foam molding. The foam injection molding machine 10 includes a male mold 11, a female mold 12, a molding material charging hopper 13, a gas storage tank 14, a cylindrical outer cylinder member 15 centering on the extrusion direction of the resin molding material, and inserted into the outer cylinder member. The members 11 to 16 are made of metal, including a screw 16, a gas injection device 17 attached in the middle of the outer cylinder member 15, a motor (not shown) that rotationally drives the screw 16, and the like. The L / D ratio of the screw 16 can be set to about 20, for example. The molds 11 and 12 attached to the tip of the outer cylinder member 15 are male and female molds, and form a required cavity C1 sealed in a clamped state. For example, the gas injection device 17 controls the injection pressure of the inert gas to a constant pressure.
The foam injection molding machine 10 injects a liquid (including a molten state) resin molding material from the injection port 15a into the cavity C1, and separates the male mold 11 from the female mold 12 to a predetermined separation position, thereby resin in the cavity C1. By foaming the molding material and solidifying or curing the resin molding material, the resin foam injection molded body M10 is formed. Then, by opening the molds 11 and 12 and taking out the molded body M10, one cycle of manufacturing the resin foam injection molded body is completed.
A mold using a slide core may be used as the mold 11.
次に、図1と図5を参照して、本樹脂発泡成形体の製造方法の各ステップを、キャビティ内の樹脂成形材料の状態の変化と併せて説明する。なお、樹脂成形材料を構成する樹脂として、熱可塑性樹脂を用いるものとする。
樹脂発泡成形体M10を成形する際、特に重要なのは、成形型の離間のタイミングと、コアバック時のコアバック速度と、コアバック時の成形樹脂の粘度である。発泡射出成形では、成形型のコアバックのタイミングや速度が重要であり、これによって、形成されるスキン層の厚さや、発泡層のセルの倍率、形状が種々に変化することが知られている。
Next, with reference to FIG. 1 and FIG. 5, each step of the manufacturing method of this resin foam molding is demonstrated with the change of the state of the resin molding material in a cavity. Note that a thermoplastic resin is used as the resin constituting the resin molding material.
When molding the resin foam molded body M10, particularly important are the timing of mold separation, the core back speed during core back, and the viscosity of the molding resin during core back. In foam injection molding, the timing and speed of the core back of the mold are important, and it is known that the thickness of the skin layer to be formed, the magnification and shape of the cells of the foam layer change variously. .
まず、図1の上段に示すように、型開き状態にある雌雄対の成形型11,12を閉じ、キャビティC1を形成する(図5のタイミングt1〜t2)。このとき、成形型11は所定の近接位置L1にあり、成形型11,12間の距離はd1とされている。また、発泡剤を含む樹脂成形材料M1は高温の液状とされ、成形型11,12は30〜80℃にされている。なお、樹脂成形材料を融点以上に加熱して溶融状態にすれば、高温の液状にすることができる。例えば、熱可塑性樹脂に融点160℃のポリプロピレンを用いる場合、樹脂成形材料を170〜230℃程度に加熱してポリプロピレンを溶融させる。次に、図1の中段に示すように、溶融状態の樹脂成形材料M1を、射出圧100〜200MPa、充填時間0.5〜5秒でキャビティC1内に射出して、金型11,12内に充填する(図5のタイミングt2〜t3)。射出圧、充填時間は、主に射出する樹脂成形材料の量、すなわち、樹脂発泡成形体の大きさによって増減する。ここで、型11,12の温度が低いため、型11,12の成形面に接した部分の樹脂成形材料は、先に冷却されて固化し、型11,12の間の距離d1の半分未満の範囲内で0.1〜1.0mmの非発泡のスキン層として形成される。一方、スキン層よりも内側にある樹脂成形材料は、溶融状態を維持している。 First, as shown in the upper part of FIG. 1, the male and female molds 11 and 12 in the mold open state are closed to form the cavity C1 (timing t1 to t2 in FIG. 5). At this time, the mold 11 is at a predetermined proximity position L1, and the distance between the molds 11 and 12 is d1. Moreover, the resin molding material M1 containing a foaming agent is a high-temperature liquid, and the molds 11 and 12 are set to 30 to 80 ° C. In addition, if a resin molding material is heated more than melting | fusing point and it is made into a molten state, it can be made a high temperature liquid state. For example, when polypropylene having a melting point of 160 ° C. is used as the thermoplastic resin, the resin molding material is heated to about 170 to 230 ° C. to melt the polypropylene. Next, as shown in the middle part of FIG. 1, the molten resin molding material M1 is injected into the cavity C1 with an injection pressure of 100 to 200 MPa and a filling time of 0.5 to 5 seconds. (Timing t2 to t3 in FIG. 5). The injection pressure and the filling time vary mainly depending on the amount of the resin molding material to be injected, that is, the size of the resin foam molded body. Here, since the temperature of the molds 11 and 12 is low, the resin molding material in the portion in contact with the molding surface of the molds 11 and 12 is cooled and solidified first, and is less than half of the distance d1 between the molds 11 and 12. In the range of 0.1 to 1.0 mm as a non-foamed skin layer. On the other hand, the resin molding material inside the skin layer maintains a molten state.
樹脂成形材料を射出すると、ミクロな気泡が複数生じ始める。樹脂成形材料に造核剤を含ませた場合、造核剤が核形成材となり、溶融状態の樹脂成形材料の中で造核剤を中心として不活性ガスが集結し、等方性の球形に近い形で径が0.1mm未満のミクロな気泡が多数生じ始める。この段階が、初期発泡段階である。
成形型11,12を近接位置L1で保持する時間T1(図5のタイミングt3〜t4)は、1〜10秒が好ましく、3〜7秒がさらに好ましい。保持時間T1を3秒以上にすると樹脂成形材料の粘度が適度に高くなって離間方向D1の途中で発泡セルが切断されにくくなり、保持時間T1を前記上限以下にすると固化による発泡不足が生じなくなる。なお、樹脂成形材料の温度や成形型の温度が低い場合や成形型11を離間させる速度(離間速度)を遅くする場合には、樹脂の粘度が上がり過ぎないように保持時間T1を短くすればよい。成形型が近接位置に保持されると、その間に、スキン層が形成され、スキン層より内側の樹脂成形材料の温度が低下して剪断粘度が上昇する。
When the resin molding material is injected, a plurality of micro bubbles start to be generated. When a nucleating agent is included in the resin molding material, the nucleating agent becomes a nucleating material, and in the molten resin molding material, inert gas gathers around the nucleating agent to form an isotropic spherical shape. A large number of micro bubbles having a diameter of less than 0.1 mm begin to form. This stage is the initial foaming stage.
The time T1 (timing t3 to t4 in FIG. 5) for holding the molds 11 and 12 at the proximity position L1 is preferably 1 to 10 seconds, and more preferably 3 to 7 seconds. When the holding time T1 is set to 3 seconds or more, the viscosity of the resin molding material is moderately high, and the foamed cells are not easily cut in the separation direction D1, and when the holding time T1 is set to the upper limit or less, insufficient foaming due to solidification does not occur. . When the temperature of the resin molding material or the temperature of the mold is low, or when the speed at which the mold 11 is separated (separation speed) is slowed, the holding time T1 can be shortened so that the resin viscosity does not increase too much. Good. When the mold is held in the proximity position, a skin layer is formed between them, the temperature of the resin molding material inside the skin layer is lowered, and the shear viscosity is increased.
タイミングt4の後、図1の下段に示すように、雌雄の成形型11,12を所定の離間位置L2まで相互に離間させ、キャビティC1の容積を拡張させる(図5のタイミングt4〜t5)。すると、初期発泡段階で樹脂成形材料内に形成された複数のミクロのセルは、成形型の離間に伴って離間方向D1にのみ伸長されて、略離間方向に隣接する他の気泡と連通するとともに離間方向とは垂直な方向D2へも隣接する他の気泡と一部連通する。その結果、離間方向D1へ伸長した霜柱状の発泡セルM13を有する発泡層が表面のスキン層どうしの間に形成され、該発泡層が離間方向とは垂直な方向D2へ通気性を有するように形成される。
上記離間段階の際、成形型11の離間速度V1は、1〜80mm/秒が好ましく、10〜60mm/秒がさらに好ましい。離間速度V1を前記下限以上にすると発泡が起こらないような現象が生じないためであり、離間速度V1を前記上限以下にすると霜柱状発泡セルの組織が崩れる現象が生じないためであるとともに汎用的な射出成形機を用いることができる結果安価な射出成形機で済むためである。なお、近接位置L1から離間位置L2まで離間する時間は、0.02〜3秒程度とされる。
上記離間段階(成形型11,12を離間させているとき)で、キャビティ内でスキン層よりも内側にある樹脂成形材料の温度(例えばキャビティの中心の温度)を試験温度とした該樹脂成形材料の溶融張力は、0.1〜30gfであるのが好ましく、0.2〜1.0gfであるのがさらに好ましい。ただし、成形樹脂材料の溶融張力は、JIS K7199に準拠した(株)東洋精機製作所製のキャピラリーレオメータ「キャピログラフ1C型」を用い、シリンダの下端に直径1.0mmのキャピラリーを装着して、前記試験温度にした樹脂成形材料をシリンダ内に充填し、キャピラリーレオメータのピストンを降下速度10mm/minで降下させてシリンダ内の樹脂成形材料をキャピラリーから糸状に押し出し、同時に、押し出された樹脂成形材料を5.0m/minの引き取り速度で引き取る際に測定される溶融張力とする。樹脂成形材料が熱可塑性の材料である場合、樹脂成形材料を加熱して溶融させ、成形型11,12が近接位置L1にあるときのキャビティに溶融状態の樹脂成形材料を射出して、成形型11,12を離間させるときにキャビティ内にある樹脂成形材料の中で最も高い温度を試験温度として、当該試験温度の溶融状態の樹脂成形材料をシリンダ内に充填し、ピストンを降下させて樹脂成形材料を糸状に押し出して引き取る際に溶融張力を測定すればよい。成形樹脂材料の溶融張力が0.1gf未満と小さいと成形型を離間させたときに発泡セルの壁が切れてしまい発泡セルが霜柱状に形成されないため0.1gf以上にするのが好ましく、成形樹脂材料の溶融張力が大きすぎる(30gfよりも大)と成形型を離間させても発泡セルが霜柱状に形成されずに通気度もほとんどなく吸音性も低いため30gf以下にするのが好ましい。
After the timing t4, as shown in the lower part of FIG. 1, the male and female molds 11 and 12 are separated from each other to a predetermined separation position L2, and the volume of the cavity C1 is expanded (timing t4 to t5 in FIG. 5). Then, the plurality of micro cells formed in the resin molding material in the initial foaming stage are expanded only in the separation direction D1 with the separation of the molding die, and communicate with other bubbles that are substantially adjacent in the separation direction. A part of the air bubbles communicates with other adjacent bubbles in the direction D2 perpendicular to the separation direction. As a result, a foam layer having frost column-like foam cells M13 extending in the separation direction D1 is formed between the skin layers on the surface so that the foam layer has air permeability in a direction D2 perpendicular to the separation direction. It is formed.
In the separation step, the separation speed V1 of the mold 11 is preferably 1 to 80 mm / second, and more preferably 10 to 60 mm / second. This is because when the separation speed V1 is equal to or higher than the lower limit, a phenomenon in which foaming does not occur does not occur, and when the separation speed V1 is equal to or lower than the upper limit, a phenomenon that the structure of the frosted columnar foam cell does not collapse occurs. This is because an inexpensive injection molding machine can be used. The time for separating from the proximity position L1 to the separation position L2 is about 0.02 to 3 seconds.
In the separation step (when the molds 11 and 12 are spaced apart), the resin molding material in which the temperature of the resin molding material inside the skin layer in the cavity (for example, the temperature at the center of the cavity) is used as the test temperature The melt tension of is preferably from 0.1 to 30 gf, more preferably from 0.2 to 1.0 gf. However, the melt tension of the molding resin material was determined by using a capillary rheometer “Capillograph 1C type” manufactured by Toyo Seiki Seisakusho Co., Ltd. in accordance with JIS K7199 and attaching a capillary with a diameter of 1.0 mm to the lower end of the cylinder. The cylinder is filled with the resin molding material at a temperature, the piston of the capillary rheometer is lowered at a descending speed of 10 mm / min, and the resin molding material in the cylinder is extruded from the capillary into a thread shape. At the same time, the extruded resin molding material is 5 The melt tension measured when the sheet is drawn at a take-up speed of 0.0 m / min. When the resin molding material is a thermoplastic material, the resin molding material is heated and melted, and the molten resin molding material is injected into the cavity when the molding dies 11 and 12 are in the proximity position L1. The highest temperature among the resin molding materials in the cavity when separating 11 and 12 is set as the test temperature, the resin molding material in a molten state at the test temperature is filled into the cylinder, and the piston is lowered to form the resin molding. What is necessary is just to measure melt tension, when material is extruded and taken out in the shape of a thread. If the melt tension of the molding resin material is as small as less than 0.1 gf, the foamed cell wall is cut when the mold is separated and the foamed cell is not formed in the form of frost columns. If the melt tension of the resin material is too large (greater than 30 gf), even if the mold is separated, the foamed cells are not formed in the form of frost columns, and the air permeability is hardly present and the sound absorption is low.
また、成形型の離間距離d2は、得ようとする樹脂発泡成形体の発泡倍率によって定まるものであり、近接位置L1にあるときの成形型11,12の間の距離d1の1〜9倍(樹脂発泡成形体の発泡倍率が2〜10倍)が好ましく、距離d1の2〜5倍(樹脂発泡成形体の発泡倍率が3〜6倍)がさらに好ましい。言い換えると、成形型11,12を近接位置L1から離間位置L2まで離間させるときのキャビティC1の容積比は、2〜10が好ましく、3〜6がさらに好ましい。キャビティの容積比(離間距離d2)を前記下限以上にすると離間方向D1において発泡セルが霜柱状で十分に長くなって通気度が大きくなることにより吸音性が良好になり、上限以下にすると厚み方向(離間距離D1)の途中で発泡セルが切断されないことにより内装材として良好な弾性かつ良好な触感が得られるためである。
本製造方法では、近接位置にあるときの両成形型の間の距離d1を1.0〜10.0mmとし、離間距離d2を1.0〜50.0mmとしているので、発泡セルM13は離間方向D1へ離間距離d2以下で1.0mm以上気泡が連続して伸長した霜柱状に形成される。
Further, the mold separation distance d2 is determined by the expansion ratio of the resin foam molding to be obtained, and is 1 to 9 times the distance d1 between the molds 11 and 12 when in the proximity position L1 ( The foaming ratio of the resin foam molding is preferably 2 to 10 times, and more preferably 2 to 5 times the distance d1 (the foaming ratio of the resin foam molding is 3 to 6 times). In other words, the volume ratio of the cavity C1 when the molds 11 and 12 are separated from the proximity position L1 to the separation position L2 is preferably 2 to 10, and more preferably 3 to 6. When the volume ratio of the cavities (separation distance d2) is greater than or equal to the lower limit, the foamed cells are frost columns in the separation direction D1 and become sufficiently long and the air permeability is increased. This is because the foamed cells are not cut in the middle of (separation distance D1), so that good elasticity and good tactile sensation can be obtained as an interior material.
In this manufacturing method, the distance d1 between the two molds at the close position is set to 1.0 to 10.0 mm, and the separation distance d2 is set to 1.0 to 50.0 mm. D1 is formed in a frost column shape in which bubbles are continuously extended by 1.0 mm or more at a separation distance d2 or less.
なお、一対の成形型11,12を離間させる速度V1について近接位置L1から離間し始めた位置での速度よりも離間位置L2へ到達する位置での速度の方を大きくして樹脂発泡成形体を成形すると、発泡セルを安定して霜柱状に形成することができるので、高い吸音性を維持しながら内装材としての弾性および触感をさらに良好にさせることができる。例えば、図6の上段に示すように、タイミングt4〜t5において成形型11の離間速度V1を徐々に上げることにより、近接位置L1から離間し始めた位置での速度よりも離間位置L2へ到達する位置での速度の方を大きくする。また、図6の下段に示すように、タイミングt4〜t5において成形型11の離間速度V1を段階的に上げることにより、近接位置L1から離間し始めた位置での速度よりも離間位置L2へ到達する位置での速度の方を大きくする。 In addition, the speed at the position reaching the separation position L2 is made larger than the speed at the position where the pair of molds 11 and 12 are separated from the proximity position L1 at the speed V1, and the resin foam molded body is obtained. When molded, the foam cell can be stably formed in a frost column shape, so that the elasticity and tactile sensation as the interior material can be further improved while maintaining high sound absorption. For example, as shown in the upper part of FIG. 6, by gradually increasing the separation speed V1 of the mold 11 at timings t4 to t5, the speed reaches the separation position L2 rather than the speed at the position where the separation mold 11 starts to separate from the proximity position L1. Increase the speed at the position. Further, as shown in the lower part of FIG. 6, by increasing the separation speed V1 of the mold 11 stepwise at timings t4 to t5, the separation position L2 is reached rather than the speed at the position where the separation position L1 starts to separate. Increase the speed at the position where you want to go.
上記離間段階を終了すると、成形型11を離間位置L2で所定時間保持する(図5のタイミングt5〜t6)。成形型を離間位置で保持する時間T2は、内部の発泡層が冷却されて固化する時間があればよく、例えば、約30秒とすればよい。
最後に、離間位置L2で型締め状態にある成形型11,12を開き、キャビティを開放し(図5のタイミングt6〜t7)、樹脂発泡成形体M10を取り出すことにより、一連の製造サイクルが終了する。
When the separation step is completed, the mold 11 is held at the separation position L2 for a predetermined time (timing t5 to t6 in FIG. 5). The time T2 for holding the mold in the spaced position is sufficient if the internal foamed layer is cooled and solidified, for example, about 30 seconds.
Finally, the molds 11 and 12 in the clamped state are opened at the separation position L2, the cavity is opened (timing t6 to t7 in FIG. 5), and the resin foam molded body M10 is taken out to complete a series of manufacturing cycles. To do.
形成される樹脂発泡成形体M10は、薄く広がった形状とされ、表面に非発泡のスキン層M16が形成されるとともに、内部に離間方向へ1mm以上連続気泡で伸長した霜柱状発泡セル13を有する通気性の発泡層M12が形成される。各発泡セルの容積が大きく樹脂発泡成形体の組織が低密度でも、離間方向とは垂直な方向における発泡セルの壁どうしの距離が小さいため、軽量ながら厚み方向への圧縮力に対して座屈しにくく自動車の内装材として良好な弾性かつ良好な触感が得られる。また、発泡セルが非常に細長い連続気泡の霜柱状に形成されるので、内部に通気性を有する樹脂発泡成形体が形成され、高い吸音性が得られる。 The formed resin foam molded body M10 has a thin and widened shape, and has a non-foamed skin layer M16 formed on the surface thereof, and has frost columnar foam cells 13 that are elongated by 1 mm or more of open cells in the separating direction. A breathable foam layer M12 is formed. Even if the volume of each foam cell is large and the structure of the resin foam molding is low density, the distance between the foam cell walls in the direction perpendicular to the separation direction is small, so it is lightweight and buckles against compressive force in the thickness direction. It is difficult to obtain good elasticity and good tactile sensation as an automobile interior material. In addition, since the foam cell is formed in the shape of a very elongated open-cell frost column, a resin foam molded body having air permeability is formed inside, and high sound absorption is obtained.
本樹脂発泡成形体を吸音材として利用する場合、内部の発泡層を表面に出す加工をすればよく、例えば、樹脂発泡成形体を厚み方向の途中で表面に並行させて切断して発泡層を露出させて吸音材を形成してもよいし、樹脂発泡成形体を厚み方向へ切断して発泡層を露出させて吸音材を形成してもよい。 When using this resin foam molded article as a sound absorbing material, it suffices to process the internal foam layer on the surface. For example, the resin foam molded article is cut in parallel with the surface in the middle of the thickness direction to remove the foam layer. The sound absorbing material may be formed by being exposed, or the sound absorbing material may be formed by cutting the resin foam molded body in the thickness direction to expose the foam layer.
(2)変形例:
図7〜図9に示すように、キャビティに充填された樹脂成形材料内で離間方向D1とは垂直な方向D2へ該離間方向の温度分布を異ならせて一対の成形型を離間させることにより、表面に非発泡のスキン層(M26a,b)を形成しながら前記温度分布の異なりに応じた空洞(M25)を内部に形成して、樹脂発泡成形体を成形してもよい。
(2) Modification:
As shown in FIGS. 7 to 9, by separating the pair of molds by making the temperature distribution in the separation direction different in the direction D2 perpendicular to the separation direction D1 in the resin molding material filled in the cavity, While forming a non-foamed skin layer (M26a, b) on the surface, a cavity (M25) corresponding to the difference in the temperature distribution may be formed inside to mold the resin foam molded article.
図7と図8に示す例では、表面に凸部(ディンプル)M27および凹部M28を形成するようにしてキャビティに充填された樹脂成形材料M1内で離間方向D1とは垂直な方向D2へ該離間方向の温度分布を異ならせることにより、該温度分布の異なりに応じた空洞M25を内部に形成して樹脂発泡成形体M20を成形している。
本樹脂発泡成形体M20は、厚み方向(離間方向D1)の片面に多数の凸部M27を凹部M28から膨出させた形状とされ、図7のA1−A1の位置から見た垂直断面図(図7の下段に記載)のように、凸部M27および凹部M28の形状に沿ったスキン層M26aと凹凸の無い表面側のスキン層M26bと両スキン層M26a,bに挟まれた発泡層M22とを有する構造とされている。発泡層M22では、凹部M28の位置に対応して離間方向D1へ離間距離d2以下で1.0mm以上となるように気泡を連続させて霜柱状に伸長させた発泡セルM23が形成され、凸部M27の位置に対応して発泡セルが途中で切断されて空洞M25が形成されている。
In the example shown in FIGS. 7 and 8, the separation D1 is perpendicular to the separation direction D1 in the resin molding material M1 filled in the cavity so as to form the projections (dimples) M27 and the depressions M28 on the surface. By varying the temperature distribution in the direction, the cavity M25 corresponding to the difference in the temperature distribution is formed inside, and the resin foam molded body M20 is molded.
This resin foam molded body M20 has a shape in which a large number of convex portions M27 are bulged from the concave portion M28 on one surface in the thickness direction (separating direction D1), and is a vertical cross-sectional view as viewed from the position A1-A1 in FIG. As shown in the lower part of FIG. 7, the skin layer M26a along the shape of the convex portion M27 and the concave portion M28, the skin layer M26b on the surface side having no irregularities, and the foam layer M22 sandwiched between both skin layers M26a, b It is set as the structure which has. In the foam layer M22, foam cells M23 are formed in which bubbles are continuously extended in a frost column shape so as to be 1.0 mm or more with a separation distance d2 or less in the separation direction D1 corresponding to the position of the recess M28. Corresponding to the position of M27, the foam cell is cut halfway to form a cavity M25.
図8は、一対の成形型21,22の構造および該成形型21,22の間に形成されるキャビティC2に充填された樹脂成形材料M1の温度分布を示す断面図である。
表面に凹凸を形成する側の成形型21の成形面には、樹脂発泡成形体の凸部M27に合わせた形状の凹部21aが形成されるとともに、樹脂発泡成形体の凹部M28に合わせた形状の凸部21bが形成されている。その他の成形型21,22の構成は、上述した成形型11,12の構成と同様にしている。なお、近接位置にあるときの成形型21,22の間の距離d1は、成形型21の凸部21bと成形型22の成形面との間の距離であるとする。
凹部M28からの凸部M27の高さ(凸部21bからの凹部21aの深さ)は、空洞M25を確実に形成する観点から、例えば、0.2〜2.0mmとすることができる。表面に沿った断面が円形となるように各凸部M27を形成する場合、凸部M27の径(凹部21aの径)は、空洞M25を確実に形成する観点から、例えば、2.0〜10.0mmとすることができる。
なお、凸部M27は、断面多角形など様々な形状とすることができる。また、樹脂発泡成形体の表面を、凸部に多数の凹部が形成された凸凹模様としてもよい。樹脂発泡成形体の凹凸は、片面のみならず、両面に形成されてもよい。
樹脂発泡成形体の表面に凹凸を形成することにより、凹凸を形成しない場合と比べて成形型の離間距離d2を短くしても空洞が形成されて高い通気性が得られ、良好な吸音性が得られる。従って、表面に凹凸を形成していない樹脂発泡成形体と比べて、軽量化させたり、吸音性を向上させたり、樹脂発泡成形体を薄くさせたりすることができる。
FIG. 8 is a cross-sectional view showing the structure of the pair of molds 21 and 22 and the temperature distribution of the resin molding material M1 filled in the cavity C2 formed between the molds 21 and 22.
On the molding surface of the mold 21 on the side where the irregularities are formed, a concave portion 21a having a shape corresponding to the convex portion M27 of the resin foam molded body is formed, and a shape corresponding to the concave portion M28 of the resin foam molded body is formed. Convex part 21b is formed. The other molds 21 and 22 have the same configuration as the molds 11 and 12 described above. It is assumed that the distance d1 between the molds 21 and 22 at the close position is a distance between the convex portion 21b of the mold 21 and the molding surface of the mold 22.
The height of the convex portion M27 from the concave portion M28 (depth of the concave portion 21a from the convex portion 21b) can be set to, for example, 0.2 to 2.0 mm from the viewpoint of reliably forming the cavity M25. When forming each convex part M27 so that the cross section along the surface is circular, the diameter of the convex part M27 (diameter of the concave part 21a) is, for example, 2.0 to 10 from the viewpoint of reliably forming the cavity M25. .0 mm.
In addition, the convex part M27 can be made into various shapes, such as a cross-sectional polygon. Further, the surface of the resin foam molded body may have a concavo-convex pattern in which a large number of concave portions are formed on the convex portions. The unevenness of the resin foam molded body may be formed not only on one side but also on both sides.
By forming irregularities on the surface of the resin foam molded article, a cavity is formed even when the mold separation distance d2 is shortened compared to the case where irregularities are not formed, and high air permeability is obtained, and good sound absorption is obtained. can get. Therefore, it is possible to reduce the weight, improve the sound absorption, or make the resin foam molded body thinner than a resin foam molded body having no irregularities on the surface.
キャビティC2に充填された樹脂成形材料M1について、便宜上、所定の温度(例えば、樹脂成形材料が固化する温度)以下の低温領域R1,R2と、該所定の温度より高温の高温領域R3(図8中、点を付した領域)とに領域分けすることにする。樹脂成形材料の温度分布は、離間方向とは垂直な方向D2のいずれの位置(実際には薄く広がった樹脂発泡成形体の縁部を除く)でも表面側の低温領域R1,R2に高温領域R3が挟まれた分布となる。ここで、低温領域R1,R2は略一定の厚みになり、凸部M27に対応する位置では凹部M28に対応する位置よりも高温領域R3が離間方向D1へ拡がった状態になる。この状態で成形型21,22を所定の離間位置まで離間させると、凹部M28に対応する位置では霜柱状の発泡セルM23が形成される一方、凸部M27に対応する位置では高温領域R3が広い結果発泡セルが途中で切断されて空洞M25が形成される。 For the resin molding material M1 filled in the cavity C2, for convenience, the low temperature regions R1, R2 below a predetermined temperature (for example, the temperature at which the resin molding material solidifies) and the high temperature region R3 (FIG. 8) higher than the predetermined temperature. The area is divided into areas with dots. The temperature distribution of the resin molding material is such that in any position in the direction D2 perpendicular to the separation direction (excluding the edge of the resin foam molding that has spread thinly), the high temperature region R3 is in the low temperature region R1, R2 on the surface side. The distribution is sandwiched between. Here, the low temperature regions R1 and R2 have a substantially constant thickness, and the high temperature region R3 is expanded in the separation direction D1 at the position corresponding to the convex portion M27 than at the position corresponding to the concave portion M28. When the molds 21 and 22 are separated to a predetermined separation position in this state, a frost column-shaped foam cell M23 is formed at a position corresponding to the recess M28, while a high temperature region R3 is wide at a position corresponding to the protrusion M27. As a result, the foam cell is cut in the middle to form a cavity M25.
以上により、樹脂発泡成形体内部の通気性が高くされるので、軽量で、高い吸音性を得ることが可能になる。また、本樹脂発泡成形体を衝撃吸収材として用いる場合、内部に空洞が形成されるので、軽量化される結果薄くさせることができる。また、本樹脂発泡成形体を吸音材として用いる場合、吸音性を向上させることができる。 As described above, since the air permeability inside the resin foam molded article is increased, it is possible to obtain light weight and high sound absorption. Moreover, when using this resin foam molding as an impact-absorbing material, since a cavity is formed inside, it can be made thin as a result of weight reduction. Moreover, when using this resin foam molded object as a sound-absorbing material, sound-absorbing property can be improved.
なお、キャビティ内の樹脂成形材料内で離間方向とは垂直な方向D2へ該離間方向の温度分布を異ならせることができれば、同様にして発泡層に空洞を形成することができる。
図9は、一対の成形型31,32の構造および該成形型31,32の間に形成されるキャビティC3に充填された樹脂成形材料M1の温度分布を示す断面図である。
本変形例では、樹脂発泡成形体の表面に凹凸を形成していない。その代わり、温度差を生じさせるための成形型31の成形面には、樹脂発泡成形体に形成する空洞の位置に合わせて絶縁材31aを埋め込んでいる。該絶縁材は、多孔質無機素材などの断熱材などとされ、樹脂成形材料から樹脂成形材料よりも低温の成形型に吸収される熱量を少なくさせる素材とされている。その他の成形型31,32の構成は、上述した成形型11,12の構成と同様にしている。
If the temperature distribution in the separation direction can be varied in the direction D2 perpendicular to the separation direction in the resin molding material in the cavity, the void can be formed in the foamed layer in the same manner.
FIG. 9 is a cross-sectional view showing the structure of the pair of molds 31 and 32 and the temperature distribution of the resin molding material M1 filled in the cavity C3 formed between the molds 31 and 32. As shown in FIG.
In this modification, no irregularities are formed on the surface of the resin foam molded article. Instead, the insulating material 31a is embedded in the molding surface of the molding die 31 for generating a temperature difference in accordance with the position of the cavity formed in the resin foam molded body. The insulating material is a heat insulating material such as a porous inorganic material, and is a material that reduces the amount of heat absorbed from the resin molding material to a molding die at a lower temperature than the resin molding material. The other molds 31 and 32 have the same configuration as the molds 11 and 12 described above.
樹脂成形材料M1の温度分布は、離間方向とは垂直な方向D2のいずれの位置(実際には薄く広がった樹脂発泡成形体の縁部を除く)でも表面側の低温領域R11,R12に高温領域R13が挟まれた分布となる。ここで、絶縁材31aの部分を除く成形型31に接する低温領域R11aと成形型32に接する低温領域R12とは略一定の厚みになり、絶縁材31aに接する低温領域R11bは低温領域R11aよりも薄くなる。その結果、キャビティC3に充填された樹脂成形材料M1では、絶縁材31aに対応する位置ではその他の位置よりも高温領域R3が離間方向D1へ拡がった状態になる。この状態で成形型31,32を所定の離間位置まで離間させると、絶縁材31aを除く部分に対応する位置では霜柱状の発泡セルが形成される一方、絶縁材31aに対応する位置では高温領域R13が広い結果発泡セルが途中で切断されて空洞が形成される。
以上により、軽量で、高い吸音性を得ることが可能な樹脂発泡成形体が形成される。
The temperature distribution of the resin molding material M1 is a high temperature region in the low temperature regions R11 and R12 on the surface side at any position in the direction D2 perpendicular to the separation direction (in practice, excluding the edge of the resin foam molding that has spread thinly). R13 is sandwiched. Here, the low temperature region R11a in contact with the molding die 31 except for the insulating material 31a and the low temperature region R12 in contact with the molding die 32 have a substantially constant thickness, and the low temperature region R11b in contact with the insulating material 31a is smaller than the low temperature region R11a. getting thin. As a result, in the resin molding material M1 filled in the cavity C3, the high temperature region R3 is expanded in the separation direction D1 at the position corresponding to the insulating material 31a than at the other positions. When the molds 31 and 32 are separated to a predetermined separation position in this state, a frost column-shaped foam cell is formed at a position corresponding to a portion excluding the insulating material 31a, while a high temperature region is formed at a position corresponding to the insulating material 31a. As a result of the wide R13, the foamed cell is cut in the middle to form a cavity.
As described above, a resin foam molded body that is lightweight and capable of obtaining high sound absorption is formed.
なお、図9に示した例では、樹脂発泡成形体の表面に凹凸を形成する場合と比べて、表面が滑らかとなるので、良好な外観を得るために表面を滑らかにする必要がある場合に有用な樹脂発泡成形体が得られる。一方、表面に凹凸を形成する場合には、成形型に絶縁材を埋める場合と比べて成形型の構造が簡易で済み、成形型を安価にすることが求められている場合等に有用である。 In addition, in the example shown in FIG. 9, since the surface becomes smooth compared with the case where unevenness is formed on the surface of the resin foam molded article, the surface needs to be smoothed to obtain a good appearance. Useful resin foam moldings are obtained. On the other hand, when forming irregularities on the surface, the structure of the mold is simple compared to the case where an insulating material is buried in the mold, and it is useful when it is required to reduce the cost of the mold. .
(3)実施例:
以下、実施例を示して具体的に本発明を説明するが、本発明は実施例により限定されるものではない。
以下の実施例、比較例全てにおいて、射出成形機として宇部興産機械株式会社製射出成形機MD350SIV(型締力最大3430kN、L/D=20)を用い、樹脂成形材料の射出圧を100MPaとした。近接位置にある金型間に形成されるキャビティの形状を200×400×2mmの平板形とし、キャビティの容積を160cm3とした。従って、近接位置にある成形型間の距離d1は、2mmとなる。また、型締めの際の金型の移動速度を10mm/秒とした。キャビティには、溶融状態の樹脂成形材料をフルショットで充填した。溶融状態の樹脂成形材料の充填時間を、1秒とした。金型を近接位置から離間位置へ離間させる移動速度を53mm/秒とした。
また、不活性ガスとして、CO2ガスを用いた。
さらに、溶融張力を測定するためのキャピラリーレオメータとして、JIS K7199に準拠した(株)東洋精機製作所製のキャピラリーレオメータ「キャピログラフ1C型」を用い、シリンダの下端に直径1.0mmのキャピラリーを装着した。近接位置にある金型間のキャビティに溶融状態の樹脂成形材料を射出して金型を離間させるときにキャビティの中心部の温度(キャビティ内にある樹脂成形材料の中で最も高い温度)を試験温度として、当該試験温度に加熱して溶融させた樹脂成形材料をシリンダ内に充填し、キャピラリーレオメータのピストンを降下速度10mm/minで降下させてシリンダ内の樹脂成形材料をキャピラリーから糸状に押し出し、同時に、押し出された樹脂成形材料を5.0m/minの引き取り速度で引き取る際の溶融張力を測定した。なお、金型が近接位置にあるときに210℃の樹脂成形材料をキャビティに射出して金型を近接位置で4〜7秒間保持した後、金型を離間位置へ離間させるときにキャビティ内でスキン層よりも内側(発泡層となる部分)の温度は、約190℃であるため、実施例1〜4と比較例2では試験温度を190℃にした。一方、金型が近接位置にあるときに210℃の樹脂成形材料をキャビティに射出して金型を近接位置で保持する時間を1秒未満とし、金型を離間位置へ離間させるときにキャビティ内でスキン層よりも内側の温度は、約210℃であるため、比較例1では試験温度を210℃にした。
(3) Example:
EXAMPLES Hereinafter, although an Example is shown and this invention is demonstrated concretely, this invention is not limited by an Example.
In all of the following examples and comparative examples, an injection molding machine MD350SIV manufactured by Ube Industries Co., Ltd. (maximum clamping force 3430 kN, L / D = 20) was used as the injection molding machine, and the injection pressure of the resin molding material was set to 100 MPa. . The shape of the cavity formed between the molds at close positions was a flat plate of 200 × 400 × 2 mm, and the cavity volume was 160 cm 3 . Therefore, the distance d1 between the molds in the close position is 2 mm. In addition, the moving speed of the mold during mold clamping was set to 10 mm / second. The cavity was filled with a molten resin molding material in a full shot. The filling time of the molten resin molding material was 1 second. The moving speed for separating the mold from the proximity position to the separation position was 53 mm / second.
Further, as the inert gas, using CO 2 gas.
Furthermore, as a capillary rheometer for measuring melt tension, a capillary rheometer “Capillograph 1C type” manufactured by Toyo Seiki Seisakusho Co., Ltd. compliant with JIS K7199 was used, and a capillary having a diameter of 1.0 mm was attached to the lower end of the cylinder. Test the temperature at the center of the cavity (the highest temperature among the resin molding materials in the cavity) when injecting molten resin molding material into the cavities between the molds in close proximity to separate the molds As the temperature, the resin molding material heated and melted to the test temperature is filled in the cylinder, the piston of the capillary rheometer is lowered at a descending speed of 10 mm / min, and the resin molding material in the cylinder is extruded from the capillary into a thread shape, At the same time, the melt tension when the extruded resin molding material was drawn at a take-up speed of 5.0 m / min was measured. When the mold is in the proximity position, the resin molding material at 210 ° C. is injected into the cavity, and the mold is held in the proximity position for 4 to 7 seconds. Then, the mold is moved to the separation position in the cavity. Since the temperature inside the skin layer (the portion that becomes the foam layer) is about 190 ° C., the test temperature was set to 190 ° C. in Examples 1 to 4 and Comparative Example 2. On the other hand, when the mold is in the proximity position, the resin molding material at 210 ° C. is injected into the cavity and the time for holding the mold in the proximity position is set to less than 1 second, and the mold is moved to the separation position. Since the temperature inside the skin layer is about 210 ° C., the test temperature was 210 ° C. in Comparative Example 1.
[実施例1]
樹脂成形材料を構成する熱可塑性樹脂として、プロピレン−エチレン共重合物(サンアロマー株式会社製サンアロマー(商標)ポリプロピレン樹脂、グレードPM970W、密度0.90g/cm3、MI=30、ブロックコポリマー)を用いた。
造核剤として、永和化成工業株式会社製ポリスレンEE207(化学発泡剤)を用いた。
試験区毎に、各素材の配合割合を以下のようにし、不活性ガスの注入圧力を以下のようにするとともに、離間距離d2、成形体の発泡倍率、型締め圧力、金型を近接位置で保持する時間T1、金型を近接位置から離間位置へ離間させる移動速度V1、を以下のようにした。なお、造核剤の添加量は、造核剤を除く樹脂成形材料100重量部当たりの重量で示している。以下も、同様である。そして、造核剤を含む樹脂成形材料を210℃に加熱し、不活性ガスを注入してキャビティ内に射出し、成形後に脱型して、樹脂発泡成形体のサンプルを試作した。このとき、金型の温度は、30〜60℃であった。また、熱可塑性樹脂について、試験温度を190℃として試験温度以外を上述した条件として溶融張力を測定したところ、0.2gfであった。
試験区1 試験区2
熱可塑性樹脂 100重量% 100重量%
造核剤 10重量部 0重量部
ガス注入圧力(MPa) 4.0 4.0
離間距離d2(mm) 7.0 5.0
成形体の発泡倍率 4.5 3.5
型締め圧力(kN) 2000 2000
近接位置の保持時間T1 6秒 6秒
[Example 1]
A propylene-ethylene copolymer (Sun Allomer (trademark) polypropylene resin, grade PM970W, density 0.90 g / cm 3 , MI = 30, block copolymer) manufactured by Sun Allomer Co., Ltd. was used as the thermoplastic resin constituting the resin molding material. .
Polyslene EE207 (chemical foaming agent) manufactured by Eiwa Chemical Industry Co., Ltd. was used as a nucleating agent.
For each test section, the mixing ratio of each material is set as follows, the injection pressure of the inert gas is set as follows, the separation distance d2, the foaming magnification of the molded body, the clamping pressure, and the mold at the close positions. The holding time T1 and the moving speed V1 for separating the mold from the proximity position to the separation position were as follows. The addition amount of the nucleating agent is shown by the weight per 100 parts by weight of the resin molding material excluding the nucleating agent. The same applies to the following. Then, the resin molding material containing the nucleating agent was heated to 210 ° C., injected with an inert gas, injected into the cavity, demolded after molding, and a sample of a resin foam molding was produced as a prototype. At this time, the temperature of the mold was 30 to 60 ° C. Moreover, when the melt tension was measured for the thermoplastic resin under the conditions described above except that the test temperature was 190 ° C., it was 0.2 gf.
Test Zone 1 Test Zone 2
Thermoplastic resin 100% by weight 100% by weight
Nucleating agent 10 parts by weight 0 parts by weight Gas injection pressure (MPa) 4.0 4.0
Separation distance d2 (mm) 7.0 5.0
Foaming ratio of molded body 4.5 3.5
Clamping pressure (kN) 2000 2000
Proximity position holding time T1 6 seconds 6 seconds
[実施例2]
樹脂成形材料を構成する熱可塑性樹脂として、プロピレン−エチレン共重合物(サンアロマー株式会社製サンアロマー(商標)ポリプロピレン樹脂、グレードPMA80X、密度0.90g/cm3、MI=43。P-E共重合物と記載)と、エチレン・プロピレンゴム(ethylene propylene rubber。E-Pゴムと記載)とを用いた。
また、充てん材として、タルク(日本タルク株式会社製MICRO ACE)を用いた。
造核剤として、実施例1と同じ永和化成工業株式会社製ポリスレンEE207を用いた。
各素材の配合割合を以下のようにし、不活性ガスの注入圧力を以下のようにするとともに、離間距離d2、成形体の発泡倍率、型締め圧力、金型を近接位置で保持する時間T1、金型を近接位置から離間位置へ離間させる移動速度V1、を以下のようにした。そして、造核剤を含む樹脂成形材料を210℃に加熱し、不活性ガスを注入してキャビティ内に射出し、成形後に脱型して、樹脂発泡成形体のサンプルを試作した。このとき、金型の温度は、30〜60℃であった。また、P-E共重合物とE-Pゴムとタルクとからなる成形樹脂材料について、試験温度を190℃として試験温度以外を上述した条件として溶融張力を測定したところ、0.5gfであった。
P-E共重合物 60重量%
E-Pゴム 30重量%
タルク 10重量%
造核剤 10重量部
ガス注入圧力(MPa) 4.0
離間距離d2(mm) 7.0
成形体の発泡倍率 4.5
型締め圧力(kN) 2000
近接位置の保持時間T1 5秒
[Example 2]
As a thermoplastic resin constituting the resin molding material, a propylene-ethylene copolymer (Sun Allomer (trademark) polypropylene resin, grade PMA80X, density 0.90 g / cm 3 , MI = 43, manufactured by Sun Allomer Co., Ltd., described as PE copolymer). ) And ethylene propylene rubber (described as EP rubber).
Further, talc (MICRO ACE manufactured by Nippon Talc Co., Ltd.) was used as a filler.
As the nucleating agent, Polyslene EE207 manufactured by Eiwa Kasei Kogyo Co., Ltd. as in Example 1 was used.
The blending ratio of each material is as follows, the inert gas injection pressure is as follows, the separation distance d2, the foaming magnification of the molded body, the clamping pressure, the time T1 for holding the mold in the proximity position, The moving speed V1 for separating the mold from the proximity position to the separation position was as follows. Then, the resin molding material containing the nucleating agent was heated to 210 ° C., injected with an inert gas, injected into the cavity, demolded after molding, and a sample of a resin foam molding was produced as a prototype. At this time, the temperature of the mold was 30 to 60 ° C. The melt tension of the molding resin material composed of PE copolymer, EP rubber, and talc was measured at 190 ° C. and the conditions other than the test temperature described above were 0.5 gf.
PE copolymer 60% by weight
EP rubber 30% by weight
Talc 10% by weight
Nucleating agent 10 parts by weight Gas injection pressure (MPa) 4.0
Separation distance d2 (mm) 7.0
Foaming ratio of molded body 4.5
Clamping pressure (kN) 2000
Proximity position holding time T1 5 seconds
[実施例3]
樹脂成形材料を構成する熱可塑性樹脂として、実施例2と同じプロピレン−エチレン共重合物およびE-Pゴムを用いた。
造核剤として、永和化成工業株式会社製ポリスレンEE275Fを用いた。
試験区毎に、各素材の配合割合を以下のようにし、不活性ガスの注入圧力を以下のようにするとともに、離間距離d2、成形体の発泡倍率、型締め圧力、金型を近接位置で保持する時間T1、金型を近接位置から離間位置へ離間させる移動速度V1、を以下のようにした。試験区3では、樹脂発泡成形体サンプルの厚み方向の片面に、直径3.5mm、高さ0.5mmの円柱状の凸部を多数形成した。ここで、凸部のピッチを8mmとし、凸部の面積比(成形体サンプルの厚み方向へ該方向とは垂直な水平面上に投影したときの成形体サンプルの投影面積に対する凸部の投影面積の総面積の比)を15%とした。そして、造核剤を含む樹脂成形材料を210℃に加熱し、不活性ガスを注入してキャビティ内に射出し、成形後に脱型して、樹脂発泡成形体のサンプルを試作した。このとき、金型の温度は、30〜60℃であった。また、P-E共重合物とE-Pゴムとからなる成形樹脂材料について、試験温度を190℃として試験温度以外を上述した条件として溶融張力を測定したところ、0.2gfであった。
試験区1 試験区2 試験区3
P-E共重合物 70重量% 70重量% 70重量%
E-Pゴム 30重量% 30重量% 30重量%
造核剤 10重量部 10重量部 10重量部
ガス注入圧力(MPa) 3.0 3.0 3.0
離間距離d2(mm) 6.5 4.0 4.0
成形体の発泡倍率 4.3 3.0 3.0
型締め圧力(kN) 1000 1000 1000
近接位置の保持時間T1 7秒 7秒 7秒
[Example 3]
As the thermoplastic resin constituting the resin molding material, the same propylene-ethylene copolymer and EP rubber as in Example 2 were used.
Polyslene EE275F manufactured by Eiwa Chemical Industry Co., Ltd. was used as a nucleating agent.
For each test section, the mixing ratio of each material is set as follows, the injection pressure of the inert gas is set as follows, the separation distance d2, the foaming magnification of the molded body, the clamping pressure, and the mold at the close positions. The holding time T1 and the moving speed V1 for separating the mold from the proximity position to the separation position were as follows. In test group 3, a large number of cylindrical convex portions having a diameter of 3.5 mm and a height of 0.5 mm were formed on one surface in the thickness direction of the resin foam molded body sample. Here, the pitch of the protrusions is 8 mm, and the area ratio of the protrusions (the projected area of the protrusions relative to the projection area of the formed body sample when projected onto the horizontal plane perpendicular to the direction of the thickness of the formed body sample) The ratio of the total area) was 15%. Then, the resin molding material containing the nucleating agent was heated to 210 ° C., injected with an inert gas, injected into the cavity, demolded after molding, and a sample of a resin foam molding was produced as a prototype. At this time, the temperature of the mold was 30 to 60 ° C. Further, regarding the molding resin material composed of PE copolymer and EP rubber, the melt tension was 0.2 gf when the test temperature was 190 ° C. and the melt tension was measured under the conditions other than the test temperature described above.
Test Zone 1 Test Zone 2 Test Zone 3
PE copolymer 70% by weight 70% by weight 70% by weight
EP rubber 30% by weight 30% by weight 30% by weight
Nucleating agent 10 parts by weight 10 parts by weight 10 parts by weight Gas injection pressure (MPa) 3.0 3.0 3.0
Separation distance d2 (mm) 6.5 4.0 4.0
Foaming ratio of molded product 4.3 3.0 3.0
Clamping pressure (kN) 1000 1000 1000
Proximity position holding time T1 7 seconds 7 seconds 7 seconds
[実施例4]
樹脂成形材料を構成する熱可塑性樹脂として、実施例2で用いた樹脂(P-E共重合物とE-Pゴム)の他、オレフィン系熱可塑性エラストマー樹脂(JSR株式会社製結晶擬似架橋型TPO EXCELINK3400。エラストマー樹脂と記載)を用いた。
造核剤として、実施例1と同じ永和化成工業株式会社製ポリスレンEE207を用いた。
各素材の配合割合を以下のようにし、不活性ガスの注入圧力を以下のようにするとともに、離間距離d2、成形体の発泡倍率、型締め圧力、金型を近接位置で保持する時間T1、金型を近接位置から離間位置へ離間させる移動速度V1、を以下のようにした。そして、造核剤を含む樹脂成形材料を210℃に加熱し、不活性ガスを注入してキャビティ内に射出し、成形後に脱型して、樹脂発泡成形体のサンプルを試作した。このとき、金型の温度は、30〜60℃であった。また、P-E共重合物とE-Pゴムとエラストマー樹脂とからなる成形樹脂材料について、試験温度を190℃として試験温度以外を上述した条件として溶融張力を測定したところ、0.6gfであった。
P-E共重合物 35重量%
E-Pゴム 15重量%
エラストマー樹脂 50重量%
造核剤 10重量部
ガス注入圧力(MPa) 4.0
離間距離d2(mm) 6.5
成形体の発泡倍率 4.3
型締め圧力(kN) 2000
近接位置の保持時間T1 7秒
[Example 4]
As the thermoplastic resin constituting the resin molding material, in addition to the resin (PE copolymer and EP rubber) used in Example 2, an olefin-based thermoplastic elastomer resin (crystal pseudo-crosslinked TPO EXCELLINK 3400 manufactured by JSR Corporation. Elastomer resin). Was used).
As the nucleating agent, Polyslene EE207 manufactured by Eiwa Kasei Kogyo Co., Ltd. as in Example 1 was used.
The blending ratio of each material is as follows, the inert gas injection pressure is as follows, the separation distance d2, the foaming magnification of the molded body, the clamping pressure, the time T1 for holding the mold in the proximity position, The moving speed V1 for separating the mold from the proximity position to the separation position was as follows. Then, the resin molding material containing the nucleating agent was heated to 210 ° C., injected with an inert gas, injected into the cavity, demolded after molding, and a sample of a resin foam molding was produced as a prototype. At this time, the temperature of the mold was 30 to 60 ° C. Further, when the melt tension of the molding resin material composed of the PE copolymer, EP rubber and elastomer resin was measured at 190 ° C. and the conditions other than the test temperature described above, it was 0.6 gf.
PE copolymer 35% by weight
EP rubber 15% by weight
50% by weight of elastomer resin
Nucleating agent 10 parts by weight Gas injection pressure (MPa) 4.0
Separation distance d2 (mm) 6.5
Foaming ratio of molded product 4.3
Clamping pressure (kN) 2000
Proximity position holding time T1 7 seconds
[比較例1]
樹脂成形材料を構成する熱可塑性樹脂、タルク、造核剤として、実施例2と同じものを用いた。
各素材の配合割合、不活性ガスの注入圧力、離間距離d2、成形体の発泡倍率、型締め圧力、金型を近接位置から離間位置へ離間させる移動速度V1も実施例2と同じにした。ただし、金型を近接位置で保持する時間T1を1秒未満と短くした。そして、造核剤を含む樹脂成形材料を210℃に加熱し、不活性ガスを注入してキャビティ内に射出し、成形後に脱型して、樹脂発泡成形体のサンプルを試作した。金型を離間位置へ離間させたときにキャビティ内にある樹脂成形材料の中で最も高い温度は、約210℃であった。金型の温度は、30〜60℃であった。また、P-E共重合物とE-Pゴムとタルクとからなる成形樹脂材料について、試験温度を210℃として試験温度以外を上述した条件として溶融張力を測定したところ、0.1gf未満であり、引き取る成形樹脂材料がしばしば切れて、成形樹脂材料の継続的な引き取りができず、溶融張力測定が容易ではなかった。
[比較例2]
樹脂成形材料を構成する熱可塑性樹脂として、オレフィン系熱可塑性エラストマー樹脂(JSR株式会社製結晶擬似架橋型TPO EXCELINK3700N。エラストマー樹脂と記載)を用いた。
造核剤として、実施例1と同じ永和化成工業株式会社製ポリスレンEE207を用いた。
各素材の配合割合を以下のようにし、不活性ガスの注入圧力を以下のようにするとともに、離間距離d2、成形体の発泡倍率、型締め圧力、金型を近接位置で保持する時間T1、金型を近接位置から離間位置へ離間させる移動速度V1、を以下のようにした。そして、造核剤を含む樹脂成形材料を210℃に加熱し、不活性ガスを注入してキャビティ内に射出し、成形後に脱型して、樹脂発泡成形体のサンプルを試作した。このとき、金型の温度は、30〜60℃であった。また、エラストマー樹脂について、試験温度を190℃として試験温度以外を上述した条件として溶融張力を測定しようとしたところ、糸状に押し出された樹脂を引き取る際に樹脂が切れて溶融張力を測定することができなかった。参考として、試験温度を210℃に上げ、樹脂の引き取り速度を1.0m/minまで落として溶融張力を測定したところ、18.8gfであった。従って、キャピラリーの直径を大きくして試験温度190℃、引き取り速度5.0m/minで溶融張力を測定したとすると、30gfよりも大きな溶融張力になると推測される。
エラストマー樹脂 100重量%
造核剤 10重量部
ガス注入圧力(MPa) 4.0
離間距離d2(mm) 5.0
成形体の発泡倍率 3.0
型締め圧力(kN) 1000
近接位置の保持時間T1 4秒
[Comparative Example 1]
The same thing as Example 2 was used as a thermoplastic resin, a talc, and a nucleating agent which comprise a resin molding material.
The blending ratio of each material, the inert gas injection pressure, the separation distance d2, the foaming magnification of the molded body, the mold clamping pressure, and the moving speed V1 for separating the mold from the proximity position to the separation position were also the same as in Example 2. However, the time T1 for holding the mold in the proximity position was shortened to less than 1 second. Then, the resin molding material containing the nucleating agent was heated to 210 ° C., injected with an inert gas, injected into the cavity, demolded after molding, and a sample of a resin foam molding was produced as a prototype. The highest temperature among the resin molding materials in the cavity when the mold was separated to the separation position was about 210 ° C. The temperature of the mold was 30 to 60 ° C. Further, for a molding resin material composed of PE copolymer, EP rubber, and talc, when the test temperature was 210 ° C. and the melt tension was measured under the above-mentioned conditions other than the test temperature, the molding resin was less than 0.1 gf and taken up. The material was often cut out, and the molded resin material could not be continuously taken up, making it difficult to measure the melt tension.
[Comparative Example 2]
As the thermoplastic resin constituting the resin molding material, an olefin-based thermoplastic elastomer resin (crystal pseudo-crosslinked TPO EXCELLINK 3700N manufactured by JSR Corporation, described as an elastomer resin) was used.
As the nucleating agent, Polyslene EE207 manufactured by Eiwa Kasei Kogyo Co., Ltd. as in Example 1 was used.
The blending ratio of each material is as follows, the inert gas injection pressure is as follows, the separation distance d2, the foaming magnification of the molded body, the clamping pressure, the time T1 for holding the mold in the proximity position, The moving speed V1 for separating the mold from the proximity position to the separation position was as follows. Then, the resin molding material containing the nucleating agent was heated to 210 ° C., injected with an inert gas, injected into the cavity, demolded after molding, and a sample of a resin foam molding was produced as a prototype. At this time, the temperature of the mold was 30 to 60 ° C. In addition, for the elastomer resin, when the test temperature was set to 190 ° C. and the melt tension was measured under the conditions described above except for the test temperature, the resin was cut when the resin extruded into a string was taken out, and the melt tension could be measured. could not. As a reference, when the test temperature was raised to 210 ° C. and the take-up speed of the resin was lowered to 1.0 m / min and the melt tension was measured, it was 18.8 gf. Therefore, if the capillary tension is increased and the melt tension is measured at a test temperature of 190 ° C. and a take-off speed of 5.0 m / min, it is estimated that the melt tension is greater than 30 gf.
100% by weight of elastomer resin
Nucleating agent 10 parts by weight Gas injection pressure (MPa) 4.0
Separation distance d2 (mm) 5.0
Foaming ratio of molded product 3.0
Clamping pressure (kN) 1000
Proximity position holding time T1 4 seconds
[試験方法]
実施例および比較例の各樹脂発泡成形体サンプルを厚み方向(離間方向D1)と平行に裁断して、断面の組織、発泡セルの形状、発泡状態を観察し、厚み方向への霜柱状発泡セルの長さを測定した。なお、サンプル断面において厚み方向とは垂直な方向へ30mmの範囲内にある発泡セルの長さの平均を求めて発泡セルの長さとした。
また、図3に示すように、離間方向D1とは垂直な方向D2へ厚みd11が5.0mmとなるよう厚み方向と平行に裁断して試験片を作製し、JIS L1096に規定されたフラジール形法による通気度測定法に従って、前記垂直方向D2への通気度(単位:cc/cm2/sec)を測定した。なお、試験片が単独では規定の試験面積に満たない場合には、複数の試験片を並べて試験面積に合わせた。そして、試験片前後の気圧差を測定し、換算表から通気度に換算した。
さらに、各樹脂発泡成形体サンプルに対して、図10に示すように、厚み方向の片面からスキン層M16を貫通して発泡層M12に至る複数の通気孔M16aを所要径の針の突き刺しにより形成し、ISO 10534-2に規定された垂直入射法に従って、通気孔を形成したスキン層側から音を入射して1000〜6300Hzの範囲で1/3オクターブバンド毎に垂直入射吸音率(単位:%)を測定した。ここで、各通気孔M16aは、成形体サンプルの厚み方向に対する垂直断面が円形で、直径2.0mm、深さ2.0mmとなるように形成した。また、各通気孔は、千鳥状となるように配置し、通気孔どうしの間隔を3.0〜5.0mm、通気孔の開孔率(成形体サンプルの厚み方向へ該方向とは垂直な水平面上に投影したときの成形体サンプルの投影面積に対する通気孔の投影面積の総面積の比)を18%とした。なお、実施例3の試験区3では、凹凸パターンの無い側のスキン層に通気孔を形成した。
[Test method]
Each resin foam molded body sample of Examples and Comparative Examples is cut in parallel with the thickness direction (separation direction D1), and the cross-sectional structure, the shape of the foam cell, and the foam state are observed, and the frost columnar foam cell in the thickness direction. The length of was measured. In addition, the average of the length of the foam cell in the range of 30 mm in the direction perpendicular to the thickness direction in the sample cross section was obtained and used as the length of the foam cell.
In addition, as shown in FIG. 3, a test piece was prepared by cutting in parallel with the thickness direction so that the thickness d11 was 5.0 mm in the direction D2 perpendicular to the separation direction D1, and the fragile shape defined in JIS L1096. The air permeability in the vertical direction D2 (unit: cc / cm 2 / sec) was measured according to the air permeability measurement method by the method. In addition, when the test piece alone did not satisfy the prescribed test area, a plurality of test pieces were arranged to match the test area. And the atmospheric | air pressure difference before and behind a test piece was measured, and it converted into air permeability from the conversion table.
Further, as shown in FIG. 10, a plurality of vent holes M16a penetrating the skin layer M16 from one side in the thickness direction to the foamed layer M12 are formed by piercing a needle having a required diameter for each resin foam molded body sample. In accordance with the normal incidence method specified in ISO 10534-2, sound is incident from the skin layer side where the air vent is formed, and the normal incident sound absorption coefficient (unit:%) for each 1/3 octave band in the range of 1000 to 6300 Hz. ) Was measured. Here, each ventilation hole M16a was formed so that the vertical cross section with respect to the thickness direction of the molded body sample was circular, and had a diameter of 2.0 mm and a depth of 2.0 mm. In addition, the air holes are arranged in a staggered manner, the space between the air holes is 3.0 to 5.0 mm, the air hole opening rate (perpendicular to the direction of the thickness of the molded product sample). The ratio of the total area of the projected area of the vent holes to the projected area of the molded body sample when projected onto the horizontal plane was 18%. In the test group 3 of Example 3, air holes were formed in the skin layer on the side having no uneven pattern.
[試験結果]
結果を、表1に示す。なお、吸音率の欄には、測定周波数域(1000〜6300Hz)で最大の垂直入射吸音率(単位:%)を示した。
The results are shown in Table 1. In the column of the sound absorption coefficient, the maximum normal incident sound absorption coefficient (unit:%) is shown in the measurement frequency range (1000 to 6300 Hz).
図13に示すように、成形樹脂材料の溶融張力が0.1gf未満であった比較例1の樹脂発泡成形体サンプルでは、厚み方向の途中で大きな亀裂が生じ、霜柱状の発泡セルが形成されず、厚み方向への圧縮力に対して座屈しやすい樹脂発泡成形体となった。なお、比較例1のサンプルでは断面を切り出すと連続した亀裂により二つに割れてしまうため、サンプルの端部をテープで仮止めした。従って、図13では、該テープも撮像されている。
図14に示すように、成形樹脂材料の溶融張力が大きかった(推定30gfより大)比較例2の樹脂発泡成形体サンプルでは、霜柱状の発泡セルが形成されず、厚み方向への発泡セルの長さが1mm未満であり、通気度が0.33cc/cm2/sec以下となって低通気性であるとともに、垂直入射吸音率が28%となって良好な吸音性が得られなかった。
一方、例えば図11と図12に示すように、成形樹脂材料の溶融張力が0.2〜0.6gfであった実施例の樹脂発泡成形体サンプルでは、厚み方向へ1mm以上の霜柱状発泡セルが形成され、通気度が0.4cc/cm2/sec以上となってサンプル内部に通気性が得られるとともに、垂直入射吸音率が45〜97%となって比較例よりも良好な吸音性が得られた。また、実施例の樹脂発泡成形体サンプルを厚み方向へ押してみたところ、比較例よりも弾性が良好であるとともに触感が良好であった。
以上より、成形型の離間方向へ離間距離以下で1.0mm以上となるように気泡を連続させて霜柱状に発泡セルを伸長させて樹脂発泡成形体を成形すると、通気度0.4cc/cm2/sec以上の通気性が内部に得られ、軽量ながら厚み方向への圧縮力に対して座屈しにくく自動車の内装材として良好な弾性かつ良好な触感が得られるとともに、高い吸音性が得られることが確認された。
また、成形樹脂材料の溶融張力が0.1gf未満と小さいと金型を離間させたときに発泡セルの壁が切れてしまい発泡セルが霜柱状の組織とならず、成形樹脂材料の溶融張力が大きい(推定30gfより大)と金型を離間させても発泡セルが霜柱状の組織とならずに通気度もほとんどないことが分かった。溶融張力が0.1gf未満と小さいと成形樹脂材料の粘度が小さいため発泡セルが厚み方向の途中で切断されると推測され、溶融張力が大きすぎると発泡セルが厚み方向へ連通しないため霜柱状にならないと推測される。
As shown in FIG. 13, in the resin foam molded article sample of Comparative Example 1 in which the melt tension of the molded resin material was less than 0.1 gf, a large crack occurred in the middle of the thickness direction, and a frost column-shaped foam cell was formed. Therefore, it became a resin foam molded body that was easily buckled against the compressive force in the thickness direction. Note that, in the sample of Comparative Example 1, when the cross section is cut out, it is split into two due to continuous cracks, so the end of the sample is temporarily fixed with a tape. Therefore, in FIG. 13, the tape is also imaged.
As shown in FIG. 14, in the resin foam molded body sample of Comparative Example 2 in which the melt tension of the molded resin material was large (greater than estimated 30 gf), frost column-shaped foam cells were not formed, and the foam cells in the thickness direction The length was less than 1 mm, the air permeability was not more than 0.33 cc / cm 2 / sec, and the air permeability was low, and the normal incident sound absorption coefficient was 28%, and good sound absorption was not obtained.
On the other hand, for example, as shown in FIGS. 11 and 12, in the resin foam molded body sample of the example in which the melt tension of the molded resin material was 0.2 to 0.6 gf, the frost column-shaped foam cell having a thickness of 1 mm or more in the thickness direction. The air permeability is 0.4 cc / cm 2 / sec or more and air permeability is obtained inside the sample, and the normal incident sound absorption coefficient is 45 to 97%, which is better than the comparative example. Obtained. Moreover, when the resin foam molded object sample of the Example was pushed in the thickness direction, the elasticity was better and the tactile sensation was better than the comparative example.
From the above, when the resin foam molded body is formed by extending the foamed cells in the form of frost columns so as to be 1.0 mm or more in the separation direction of the mold, the air permeability is 0.4 cc / cm. Air permeability of 2 / sec or more is obtained in the interior, it is lightweight and is not easily buckled against compressive force in the thickness direction, and it has good elasticity and good tactile sensation as an automobile interior material, and high sound absorption is obtained. It was confirmed.
Also, if the molding resin material has a low melt tension of less than 0.1 gf, the foam cell walls are cut when the mold is separated, and the foam cell does not form a frost columnar structure. It was found that even when the mold was separated from the large (greater than estimated 30 gf), the foamed cells did not have a frost columnar structure and there was almost no air permeability. If the melt tension is less than 0.1 gf, the foamed cell is presumed to be cut in the middle of the thickness direction because the viscosity of the molding resin material is small. If the melt tension is too large, the foam cell does not communicate in the thickness direction. It is speculated that it will not be.
実施例1の試験区1と試験区2とを比較すると、造核剤を使用しなかった試験区2では霜柱状発泡セルが粗い組織になったのに対し、造核剤を使用した試験区1では霜柱状発泡セルがより緻密かつ均一に形成され、樹脂発泡成形体サンプルを厚み方向へ押してみたところ、試験区2よりも触感が良好であった。従って、造核剤を使用すると、造核剤が適度な核形成材となって、気泡が適度に緻密かつ均一に形成され、高い吸音性を維持しながら内装材としての触感が向上することが確認された。 Comparing test group 1 and test group 2 of Example 1, in test group 2 in which no nucleating agent was used, frost columnar foam cells had a rough structure, whereas in test group 2 in which nucleating agent was used, In No. 1, the frost columnar foam cells were formed more densely and uniformly, and when the resin foam molded body sample was pushed in the thickness direction, the tactile sensation was better than in the test section 2. Therefore, when a nucleating agent is used, the nucleating agent becomes an appropriate nucleating material, bubbles are formed in an appropriately dense and uniform manner, and the tactile sensation as an interior material is improved while maintaining high sound absorption. confirmed.
実施例3の試験区2と試験区3とを比較すると、表面を凹凸にしなかった試験区2では通気度が0.4cc/cm2/secで垂直入射吸音率が45%であったのに対し、表面を凹凸にした試験区3では通気度が18.0cc/cm2/secとなって通気性が向上するとともに、垂直入射吸音率が80%となって吸音性が向上した。
以上より、表面に凹凸を形成するようにして空洞を内部に形成して樹脂発泡成形体を成形すると、高い吸音性が得られることが確認された。
A comparison between test group 2 and test group 3 in Example 3 shows that although air permeability was 0.4 cc / cm 2 / sec and normal incidence sound absorption coefficient was 45% in test group 2 where the surface was not uneven. On the other hand, in the test section 3 having a rough surface, the air permeability was 18.0 cc / cm 2 / sec and the air permeability was improved, and the normal incident sound absorption rate was 80% and the sound absorption was improved.
From the above, it was confirmed that a high sound-absorbing property can be obtained by forming a cavity in the interior so as to form irregularities on the surface and molding a resin foam molded article.
以上説明したように、本発明によると、種々の態様により、軽量ながら厚み方向への圧縮力に対して座屈しにくく自動車の内装材として良好な弾性かつ良好な触感を得ることができるとともに、高い吸音性を得ることが可能な樹脂発泡成形体およびその製造方法を提供することができる。 As described above, according to the present invention, various aspects make it possible to obtain a good elasticity and good tactile sensation as an automobile interior material that is lightweight but hardly buckled against a compressive force in the thickness direction. It is possible to provide a resin foam molded article capable of obtaining sound absorption and a method for producing the same.
10…発泡射出成形機、
11,12…一対の成形型、
C1〜C3…キャビティ、
D1…離間方向、D2…離間方向とは垂直な方向、
L1…所定の近接位置、L2…所定の離間位置、
M1…樹脂成形材料、
M10,M20…樹脂発泡成形体、
M12,M22…発泡層、M13,M23…発泡セル、
M14…中間層、
M16,M26a,M26b…スキン層、
M25…空洞、M27…凸部、M28…凹部、
10: Foam injection molding machine,
11, 12 ... a pair of molds,
C1-C3 ... cavity,
D1 ... separation direction, D2 ... direction perpendicular to the separation direction,
L1: a predetermined proximity position, L2: a predetermined separation position,
M1 ... resin molding material,
M10, M20 ... resin foam molding,
M12, M22 ... foam layer, M13, M23 ... foam cell,
M14: middle layer,
M16, M26a, M26b ... skin layer,
M25 ... hollow, M27 ... convex, M28 ... concave,
Claims (12)
前記近接位置にあるときの前記一対の成形型の間の距離を1.0〜10.0mmとし、前記近接位置から前記離間位置までの離間距離を1.0〜50.0mmとして、表面に非発泡のスキン層を形成しながら前記一対の成形型の離間方向へ前記離間距離以下で1.0mm以上となるように気泡を連続させて霜柱状に発泡セルを伸長させて成形した、樹脂発泡成形体。 A cavity formed when a pair of molds that can approach and separate from each other is brought close to a predetermined proximity position, and a resin molding material containing a foaming agent is filled in the cavity, and then the pair of molds are separated to a predetermined separation position. A resin foam molded body formed by forming foam cells in the resin molding material in the cavity by expanding the cavity,
The distance between the pair of molds when in the proximity position is 1.0 to 10.0 mm, and the separation distance from the proximity position to the separation position is 1.0 to 50.0 mm. Resin foam molding, in which foam cells are stretched in the form of frost columns to form a foamed skin layer, and the foam is continuously formed so that the distance between the pair of molds is 1.0 mm or more in the separation direction of the pair of molds. body.
ただし、前記溶融張力は、JIS K7199に準拠したキャピラリーレオメータを用い、シリンダの下端に直径1.0mmのキャピラリーを装着して、前記試験温度にした前記樹脂成形材料を前記シリンダ内に充填し、キャピラリーレオメータのピストンを降下速度10mm/minで降下させて前記シリンダ内の樹脂成形材料を前記キャピラリーから糸状に押し出して5.0m/minの引き取り速度で引き取る際に測定される溶融張力とする。 The melt tension of the resin molding material is 0.1 to 30 gf with the temperature of the resin molding material inside the skin layer in the cavity when the pair of molding dies are spaced apart as the test temperature. The resin foam molded article according to any one of claims 1 to 7, which is molded as described above.
However, for the melt tension, a capillary rheometer compliant with JIS K7199 was used, a capillary having a diameter of 1.0 mm was attached to the lower end of the cylinder, and the resin molding material at the test temperature was filled into the cylinder. The rheometer piston is lowered at a descending speed of 10 mm / min to obtain a melt tension measured when the resin molding material in the cylinder is pushed out from the capillary into a thread shape and taken out at a take-up speed of 5.0 m / min.
前記キャビティに充填された樹脂成形材料内で前記離間方向とは垂直な方向へ該離間方向の温度分布を異ならせて前記一対の成形型を離間させることにより表面に非発泡のスキン層を形成しながら前記温度分布の異なりに応じた空洞を内部に形成して成形した、樹脂発泡成形体。 A cavity formed when a pair of molds that can approach and separate from each other is brought close to a predetermined proximity position, and a resin molding material containing a foaming agent is filled in the cavity, and then the pair of molds are separated to a predetermined separation position. A resin foam molded body formed by forming foam cells in the resin molding material in the cavity by expanding the cavity,
A non-foamed skin layer is formed on the surface by separating the pair of molds by differentiating the temperature distribution in the separation direction in a direction perpendicular to the separation direction in the resin molding material filled in the cavity. However, a resin foam molded article formed by forming a cavity corresponding to the difference in temperature distribution inside.
前記近接位置にあるときの前記一対の成形型の間の距離を1.0〜10.0mmとし、前記近接位置から前記離間位置までの離間距離を1.0〜50.0mmとして、表面に非発泡のスキン層を形成しながら前記一対の成形型の離間方向へ前記離間距離以下で1.0mm以上となるように気泡を連続させて霜柱状に発泡セルを伸長させて前記樹脂発泡成形体を成形することを特徴とする樹脂発泡成形体の製造方法。 A cavity formed when a pair of molds that can approach and separate from each other is brought close to a predetermined proximity position, and a resin molding material containing a foaming agent is filled in the cavity, and then the pair of molds are separated to a predetermined separation position. And expanding the cavity to form a foamed cell in the resin molding material in the cavity to mold a resin foam molded article,
The distance between the pair of molds when in the proximity position is 1.0 to 10.0 mm, and the separation distance from the proximity position to the separation position is 1.0 to 50.0 mm. While forming the foam skin layer, the foamed cells are elongated in the form of frost columns by continuing the bubbles in the separation direction of the pair of molds so that the distance is equal to or less than 1.0 mm. A method for producing a resin foam molded article, comprising molding.
前記キャビティに充填された樹脂成形材料内で前記離間方向とは垂直な方向へ該離間方向の温度分布を異ならせて前記一対の成形型を離間させることにより表面に非発泡のスキン層を形成しながら前記温度分布の異なりに応じた空洞を内部に形成して前記樹脂発泡成形体を成形することを特徴とする樹脂発泡成形体の製造方法。 A cavity formed when a pair of molds that can approach and separate from each other is brought close to a predetermined proximity position, and a resin molding material containing a foaming agent is filled in the cavity, and then the pair of molds are separated to a predetermined separation position. And expanding the cavity to form a foamed cell in the resin molding material in the cavity to mold a resin foam molded article,
A non-foamed skin layer is formed on the surface by separating the pair of molds by differentiating the temperature distribution in the separation direction in a direction perpendicular to the separation direction in the resin molding material filled in the cavity. However, a method for producing a resin foam molded article, wherein the resin foam molded article is formed by forming a cavity corresponding to the difference in temperature distribution inside.
The resin foam is made by using a material containing talc as the resin molding material to make the foam cell small, and by adjusting the weight ratio of the talc contained in the resin molding material to adjust the size of the foam cell. The method for producing a resin foam molded article according to claim 9 or 10, wherein the molded article is molded.
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JP2007230168A (en) * | 2006-03-03 | 2007-09-13 | Hayashi Engineering Inc | Manufacturing method of foamed resin molded product and foamed resin molded product |
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JP2007230168A (en) * | 2006-03-03 | 2007-09-13 | Hayashi Engineering Inc | Manufacturing method of foamed resin molded product and foamed resin molded product |
WO2009001473A1 (en) * | 2007-06-25 | 2008-12-31 | Sanwa Kako Co., Ltd. | Metallocene-ethylene-propylene-diene copolymer rubber-type open-cell foam, and process for producing the same |
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JP2010163508A (en) * | 2009-01-14 | 2010-07-29 | Toagosei Co Ltd | Coating type sound absorbing material |
JP2011110880A (en) * | 2009-11-30 | 2011-06-09 | Sanko Gosei Ltd | Resin molded cover, and resin-molded undercover for automobile using the cover |
JP2011194853A (en) * | 2010-03-24 | 2011-10-06 | Stanley Electric Co Ltd | Method of manufacturing lighting body component for car |
JP2012020544A (en) * | 2010-07-16 | 2012-02-02 | Sekisui Chem Co Ltd | Injection foam molded article |
JP2015033849A (en) * | 2013-07-08 | 2015-02-19 | 積水テクノ成型株式会社 | Thermoplastic resin foam molded body, and method of manufacturing the same |
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WO2024090280A1 (en) * | 2022-10-25 | 2024-05-02 | Dic株式会社 | Multilayer sheet material and method for producing same |
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