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JP7079488B2 - Foam resin molding mold and foam resin molding method - Google Patents
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JP7079488B2 - Foam resin molding mold and foam resin molding method - Google Patents

Foam resin molding mold and foam resin molding method Download PDF

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JP7079488B2
JP7079488B2 JP2018154008A JP2018154008A JP7079488B2 JP 7079488 B2 JP7079488 B2 JP 7079488B2 JP 2018154008 A JP2018154008 A JP 2018154008A JP 2018154008 A JP2018154008 A JP 2018154008A JP 7079488 B2 JP7079488 B2 JP 7079488B2
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裕一 中村
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SANPOU KANAGATA SEISAKUSHO LTD.
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Description

本願発明は、予備発泡後の発泡ビーズを充填して一定形状に成型する発泡樹脂成型金型、及び発泡樹脂成型方法に関する。 The present invention relates to a foamed resin molding die that is filled with foamed beads after pre-foaming and molded into a constant shape, and a foamed resin molding method.

従来から、発泡樹脂の重合工程、予備発泡工程、及び、成型工程を経て発泡樹脂製品を製造することが行われている。発泡樹脂材料としては、ポリスチレン、ポリオレフィン、ポリプロピレン、ポリエチレン等が挙げられる。以下、発泡樹脂材料として、ポリスチレンを使用する場合について説明する。重合工程においては、ポリスチレンモノマー(石油から精製されたポリスチレンの原材料)を重合し、発泡剤を加えて直径約0.3~1.0mmの原料ビーズを形成する。予備発泡工程においては、原料ビーズに約100°Cの蒸気を当てて原料ビーズを予備発泡させて膨張させ、直径約2.0~5.0mmの発泡ビーズを形成する。以下、「発泡ビーズ」と言うときは、予備発泡後のビーズを言う。 Conventionally, a foamed resin product has been manufactured through a foaming resin polymerization step, a preliminary foaming step, and a molding step. Examples of the foamed resin material include polystyrene, polyolefin, polypropylene, polyethylene and the like. Hereinafter, a case where polystyrene is used as the foamed resin material will be described. In the polymerization step, a polystyrene monomer (a raw material of polystyrene purified from petroleum) is polymerized, and a foaming agent is added to form raw material beads having a diameter of about 0.3 to 1.0 mm. In the pre-foaming step, the raw material beads are pre-foamed and expanded by applying steam at about 100 ° C. to form foamed beads having a diameter of about 2.0 to 5.0 mm. Hereinafter, the term "foamed beads" refers to beads after pre-foaming.

成型工程による成型体の形成は、凹面を有する第1構成型と、第1構成型の凹面を覆う第2構成型と、第1構成型と第2構成型との間に生じる空間よって形成される成型室とを備える発泡樹脂成型金型により行われる。発泡樹脂成型金型による成型工程は、発泡ビーズを成型室に充填する充填工程、第1構成型又は第2構成型に加熱蒸気(過熱蒸気)を当てる片面加熱工程、第1構成型及び第2構成型に加熱蒸気を当てる両面加熱工程、第1構成型等を冷却水によって冷却する水冷工程、成型室等を真空吸引して冷却する真空吸引工程、及び、成型体を成型室から取り出す離型工程から成る。 The formation of the molded body by the molding process is formed by the space formed between the first configuration type having a concave surface, the second configuration type covering the concave surface of the first configuration type, and the first configuration type and the second configuration type. It is performed by a foamed resin molding die provided with a molding chamber. The molding process using the foamed resin molding mold includes a filling step of filling the molding chamber with foamed beads, a single-sided heating step of applying heated steam (superheated steam) to the first configuration type or the second configuration type, and the first configuration type and the second configuration type. A double-sided heating process in which heated steam is applied to the configuration mold, a water cooling process in which the first configuration mold is cooled by cooling water, a vacuum suction process in which the molding chamber is vacuum-sucked and cooled, and a mold removal process in which the molded body is taken out from the molding chamber. It consists of processes.

成型工程において発泡樹脂製品を製造する従来の発泡樹脂成型金型の一例として、発泡樹脂成型金型100を、図13に示す。発泡樹脂成型金型100は、凹面102を有する凹型(第1構成型)104と、凹型104の凹面102を覆う凸型(第2構成型)106と、凹型104と凸型106との間に生じる空間によって形成される成型室108と、凹型104に対して成型室108と反対側に設けられた第1流体室110と、凸型106に対して成型室108と反対側に設けられた第2流体室112と、発泡ビーズを成型室108へ導入する発泡ビーズ経路114と、を備えている。凹型104及び凸型106は、成型室108に加熱蒸気を送るため等の理由から、複数のスリット122が設けられている。発泡樹脂成型金型10は、成型工程の中の片面加熱工程及び両面加熱工程において、開閉弁129を開いた蒸気流入経路128から第1流体室110又は第2流体室112に加熱蒸気を送り、加熱蒸気をスリット122を介して成型室108に送る。両面加熱工程により、成型室108内の発泡ビーズ群は膨張し融着し成型体120(図14に示す)に変化する。片面加熱工程及び両面加熱工程における加熱蒸気の温度は、約150~160°Cである。 FIG. 13 shows a foamed resin molding mold 100 as an example of a conventional foamed resin molding mold for manufacturing a foamed resin product in a molding process. The foamed resin molding mold 100 is formed between the concave mold (first configuration type) 104 having the concave surface 102, the convex mold (second configuration type) 106 covering the concave surface 102 of the concave mold 104, and the concave mold 104 and the convex mold 106. The molding chamber 108 formed by the generated space, the first fluid chamber 110 provided on the opposite side of the molding chamber 108 with respect to the concave mold 104, and the first fluid chamber 110 provided on the opposite side of the molding chamber 108 with respect to the convex mold 106. It includes a two-fluid chamber 112 and a foamed bead path 114 that introduces the foamed beads into the molding chamber 108. The concave 104 and the convex 106 are provided with a plurality of slits 122 for reasons such as sending heated steam to the molding chamber 108. The foam resin molding die 10 sends heated steam from the steam inflow path 128 in which the on-off valve 129 is opened to the first fluid chamber 110 or the second fluid chamber 112 in the single-sided heating step and the double-sided heating step in the molding step. The heated steam is sent to the molding chamber 108 through the slit 122. By the double-sided heating step, the foamed beads group in the molding chamber 108 expands and fuses to change into the molded body 120 (shown in FIG. 14). The temperature of the heated steam in the single-sided heating step and the double-sided heating step is about 150 to 160 ° C.

両面加熱工程の次の水冷工程において、図14(a)に示すように、約60°Cの冷却水を、開閉弁117を開いた冷却水流入経路116から第1流体室110及び第2流体室112に流入させて凹型104及び凸型106に当て、開閉弁119を開いた冷却水流出弁118から流出させることにより、片面加熱工程及び両面加熱工程で加熱された凹型104、凸型106及び成型体120を冷却する。図14において、各弁の中心に記載する「-」は、弁を閉じた状態を示す。成型工程の中の真空吸引工程においては、図14(b)に示すように、開閉弁125を開いた真空吸引経路124から第1流体室110及び第2流体室112の空気を吸引し、第1流体室110内及び第2流体室112内等を略真空状態にすることにより、凹型104、凸型106及び成型体120を冷却する。水冷工程及び真空吸引工程により、凹型104の温度は、約120°Cから約65°Cに冷却される。 In the water cooling step following the double-sided heating step, as shown in FIG. 14A, the cooling water at about 60 ° C. is supplied to the first fluid chamber 110 and the second fluid from the cooling water inflow path 116 in which the on-off valve 117 is opened. The concave 104, convex 106 and The molded body 120 is cooled. In FIG. 14, “−” described in the center of each valve indicates a state in which the valve is closed. In the vacuum suction step in the molding step, as shown in FIG. 14B, the air in the first fluid chamber 110 and the second fluid chamber 112 is sucked from the vacuum suction path 124 in which the on-off valve 125 is opened, and the first is The concave mold 104, the convex mold 106, and the molded body 120 are cooled by putting the inside of the first fluid chamber 110 and the inside of the second fluid chamber 112 into a substantially vacuum state. The temperature of the concave 104 is cooled from about 120 ° C to about 65 ° C by the water cooling step and the vacuum suction step.

しかし、水冷工程において、図14(a)に示すように、成型体120は冷却されることにより収縮し、成型体120と、凹型104及び凸型106と、の間に隙間が生じ、隙間には、両面加熱工程及び水冷工程において成型体120から生じている蒸気が入り込み、隙間に入り込んだ蒸気は、冷却された凹型104及び凸型106によって温度降下し、ドレン水(凝縮水、蒸気が温度降下により液化した水)のドレン境膜126が生じる。ドレン境膜126の温度は約90°Cであり、凹型104、凸型106及び成型体120を約65°Cに冷却していく過程において、ドレン境膜126の潜熱の分だけ、長時間冷却する必要があった。このため、凹型104、凸型106及び成型体120の冷却の迅速化を図ることができなかった。 However, in the water cooling step, as shown in FIG. 14A, the molded body 120 shrinks due to cooling, and a gap is formed between the molded body 120 and the concave 104 and the convex 106, and the gap is formed. In the double-sided heating step and the water cooling step, steam generated from the molded body 120 enters, and the steam that has entered the gap is lowered in temperature by the cooled concave 104 and convex 106, and drain water (condensed water, steam is the temperature). A drain boundary film 126 (water liquefied by the descent) is formed. The temperature of the drain boundary film 126 is about 90 ° C, and in the process of cooling the concave 104, the convex 106 and the molded body 120 to about 65 ° C, it is cooled for a long time by the latent heat of the drain boundary film 126. I had to do it. Therefore, it was not possible to speed up the cooling of the concave mold 104, the convex mold 106, and the molded body 120.

特開平10-643号公報Japanese Unexamined Patent Publication No. 10-643

本願発明は、凹型、凸型及び成型体の冷却の迅速化を図ることのできる発泡樹脂成型金型及び発泡樹脂成型方法を提供することを目的とする。 An object of the present invention is to provide a foamed resin molding die and a foamed resin molding method capable of speeding up cooling of a concave mold, a convex mold and a molded body.

本願発明の発泡樹脂成型金型は、
凹面を有する第1構成型と、
前記第1構成型の前記凹面を覆う第2構成型と、
前記第1構成型と前記第2構成型との間に生じる空間よって形成される成型室と、を備え、
前記第1構成型は、前記成型室とは反対側の面と、前記成型室と、の間で流体が通過可能であり、該第1構成型の板厚方向に対する垂直方向を長手方向とする複数の第1スリットを有し、
前記第2構成型は、前記成型室とは反対側の面と、前記成型室と、の間で流体が通過可能であり、該第2構成型の板厚方向に対する垂直方向を長手方向とする複数の第2スリットを有し、
前記第1構成型の前記成型室側は、前記第1スリットに連続し、水が溜まる複数の第1水溜部が設けられ、
前記第2構成型の前記成型室側は、前記第2スリットに連続し、水が溜まる複数の第2水溜部が設けられたことを特徴とする。
The foamed resin molding mold of the present invention is
The first configuration type with a concave surface and
The second configuration type that covers the concave surface of the first configuration type and
A molding chamber formed by a space generated between the first configuration type and the second configuration type is provided.
The first configuration mold allows fluid to pass between the surface opposite to the molding chamber and the molding chamber, and the direction perpendicular to the plate thickness direction of the first configuration mold is the longitudinal direction. Has multiple first slits,
The second configuration mold allows fluid to pass between the surface opposite to the molding chamber and the molding chamber, and the direction perpendicular to the plate thickness direction of the second configuration mold is the longitudinal direction. Has multiple second slits,
The molding chamber side of the first configuration type is provided with a plurality of first water reservoirs that are continuous with the first slit and collect water.
The molding chamber side of the second configuration type is characterized in that a plurality of second water reservoirs are provided continuously with the second slit to collect water.

本願発明の発泡樹脂成型金型は、前記発泡樹脂成型金型において、
前記第1水溜部は、前記第1構成型に当てられる水の一部が前記第1スリットを通過して溜まるように構成され、
前記第2水溜部は、前記第2構成型に当てられる水の一部が前記第1スリットを通過して溜まるように構成されたことを特徴とする。
The foamed resin molding die of the present invention is the foamed resin molding die.
The first water reservoir is configured so that a part of the water applied to the first configuration type passes through the first slit and collects.
The second water reservoir is characterized in that a part of the water applied to the second configuration type is configured to pass through the first slit and collect.

本願発明の発泡樹脂成型金型は、前記発泡樹脂成型金型において、
前記第1構成型に当てられる水が、前記第1構成型の板厚方向に放水され、前記第2構成型に当てられる水が、前記第2構成型の板厚方向に放水されるように構成されたことを特徴とする。
The foamed resin molding die of the present invention is the foamed resin molding die.
The water applied to the first configuration type is discharged in the plate thickness direction of the first configuration type, and the water applied to the second configuration type is discharged in the plate thickness direction of the second configuration type. It is characterized by being configured.

本願発明の発泡樹脂成型金型は、前記発泡樹脂成型金型において、
前記第1水溜部及び前記第2水溜部が、前記成型室側を開口部とする凹部形状であることを特徴とする。
The foamed resin molding die of the present invention is the foamed resin molding die.
The first water reservoir and the second water reservoir are characterized by having a concave shape with the molding chamber side as an opening.

本願発明の発泡樹脂成型金型は、前記発泡樹脂成型金型において、
前記第1構成型は、前記成型室とは反対側の面に、前記第1スリットに連続する第1貫通孔を有する第1突出部を備え、
前記第2構成型は、前記成型室とは反対側の面に、前記第2スリットに連続する第2貫通孔を有する第2突出部を備えたことを特徴とする。
The foamed resin molding die of the present invention is the foamed resin molding die.
The first configuration type is provided with a first protrusion having a first through hole continuous with the first slit on a surface opposite to the molding chamber.
The second configuration type is characterized in that a second protrusion having a second through hole continuous with the second slit is provided on a surface opposite to the molding chamber.

本願発明の発泡樹脂成型金型は、前記発泡樹脂成型金型において、
前記第1構成型に対して前記成型室とは反対側に設けられた第1流体室と、
前記第2構成型に対して前記成型室とは反対側に設けられた第2流体室と、
発泡ビーズを前記成型室へ導入する発泡ビーズ経路と、
を備え、
前記第1流体室及び前記第2流体室は、
前記成型室内へ蒸気を送るための蒸気流入経路と、
前記成型室へ送った前記蒸気を流出させる蒸気流出経路と、
水が流入する水流入経路と、
流入した前記水を流出させる水流出経路と、
空気が吸引される真空吸引経路と、
を備えたことを特徴とする。
The foamed resin molding die of the present invention is the foamed resin molding die.
A first fluid chamber provided on the side opposite to the molding chamber with respect to the first configuration type,
A second fluid chamber provided on the side opposite to the molding chamber with respect to the second configuration type,
The foamed bead path for introducing the foamed beads into the molding chamber, and
Equipped with
The first fluid chamber and the second fluid chamber are
The steam inflow path for sending steam into the molding chamber and
A steam outflow path for outflowing the steam sent to the molding chamber,
The water inflow route and the water inflow route
The water outflow route that causes the inflowing water to flow out,
The vacuum suction path where air is sucked and
It is characterized by being equipped with.

本願発明の発泡樹脂成型方法は、
前記請求項1~6のいずれかに記載する発泡樹脂成型金型を使用した発泡樹脂成型方法であり、
前記成型室に発泡ビーズを充填するステップと、
前記第1構成型及び前記第2構成型に蒸気を当てるステップと、
前記発泡樹脂成型金型の前記第1構成型及び前記第2構成型に水を当てるステップと、を含むことを特徴とする。
The foamed resin molding method of the present invention is
The foamed resin molding method using the foamed resin molding die according to any one of claims 1 to 6.
The step of filling the molding chamber with foamed beads,
The step of applying steam to the first configuration type and the second configuration type,
It is characterized by including a step of applying water to the first structural mold and the second structural mold of the foamed resin molding die.

本願発明の発泡樹脂成型方法は、前記発泡樹脂成型方法において、
前記第1水溜部は、前記第1構成型に当てられる水の一部が前記第1スリットを通過して溜まり、
前記第2水溜部は、前記第2構成型に当てられる水の一部が前記第1スリットを通過して溜まることを特徴とする。
The foamed resin molding method of the present invention is the same as the foamed resin molding method.
In the first water reservoir, a part of the water applied to the first configuration type passes through the first slit and collects.
The second water reservoir is characterized in that a part of the water applied to the second configuration type passes through the first slit and is collected.

本願発明の発泡樹脂成型金型によれば、第1構成型及び第2構成型に水が当てられる水冷工程において成型室内の成型体のまわりに生じるドレン境膜の熱が、真空吸引して成型室を冷却する真空吸引工程において、第1水溜部又は第2水溜部に溜まっている水へ移動する。このため、ドレン境膜に接する成型体の冷却を促進することができる。また、真空吸引工程において、第1水溜部及び第2水溜部に溜まっている水が蒸気化することにより、第1構成型及び第2構成型等の熱は気化熱に使用され、第1構成型及び第2構成型等の冷却を促進することができる。本願発明の発泡樹脂成型金型によれば、ドレン境膜から第1水溜部等に溜まっている水への熱移動と、第1構成型等の熱が気化熱に使用されることとの相乗効果により、第1構成型等の冷却をより促進することができる。 According to the foamed resin molding die of the present invention, the heat of the drain boundary film generated around the molded body in the molding chamber is vacuum-sucked and molded in the water cooling process in which water is applied to the first structural mold and the second structural mold. In the vacuum suction step of cooling the chamber, the water is moved to the water stored in the first water reservoir or the second water reservoir. Therefore, it is possible to promote cooling of the molded body in contact with the drain boundary film. Further, in the vacuum suction step, the water accumulated in the first water reservoir and the second water reservoir is vaporized, so that the heat of the first configuration type and the second configuration type is used for the heat of vaporization, and the first configuration It is possible to promote cooling of the mold and the second configuration mold and the like. According to the foamed resin molding die of the present invention, there is a synergistic effect between the heat transfer from the drain boundary film to the water accumulated in the first water reservoir and the like and the heat of the first configuration type and the like being used for the heat of vaporization. Due to the effect, cooling of the first configuration type and the like can be further promoted.

本願発明の発泡樹脂成型金型を示す図であり、同図(a)は正面断面図であり、同図(b)は一部拡大正面断面図であり、同図(c)はA-A線切断部断面図である。It is a figure which shows the foam resin molding die of this invention, FIG. 3A is a front sectional view, FIG. 2B is a partially enlarged front sectional view, and FIG. It is sectional drawing of the line cut part. 図1に示す発泡樹脂成型金型の充填工程における使用状態を示す正面断面図である。It is a front sectional view which shows the use state in the filling process of the foaming resin molding die shown in FIG. 図1に示す発泡樹脂成型金型の片面加熱工程における使用状態を示す正面断面図である。FIG. 3 is a front sectional view showing a state of use in the single-sided heating step of the foamed resin molding die shown in FIG. 1. 図1に示す発泡樹脂成型金型の両面加熱工程における使用状態を示す断正面断面図である。FIG. 3 is a sectional front sectional view showing a state of use in the double-sided heating step of the foamed resin molding die shown in FIG. 1. 図1に示す発泡樹脂成型金型の水冷工程における使用状態を示す図であり、同図(a)は正面断面図であり、同図(b)は一部拡大正面断面図である。It is a figure which shows the use state in the water cooling process of the foamed resin molding die shown in FIG. 1, FIG. 1A is a front sectional view, and FIG. 1B is a partially enlarged front sectional view. 図1に示す発泡樹脂成型金型の真空吸引工程における使用状態を示す断正面断面図である。FIG. 3 is a sectional front sectional view showing a state of use in the vacuum suction step of the foamed resin molding die shown in FIG. 1. 本願発明の発泡樹脂成型金型の他の実施形態を示す一部拡大正面断面図である。It is a partially enlarged front sectional view which shows the other embodiment of the foaming resin molding die of this invention. 同図(a)及び(b)は、本願発明の発泡樹脂成型金型の更に他の実施形態を示す一部拡大正面断面図である。FIGS. (A) and (b) are partially enlarged front sectional views showing still another embodiment of the foamed resin molding die of the present invention. 同図(a)及び(b)は、本願発明の発泡樹脂成型金型の更に他の実施形態を示す一部拡大正面断面図である。FIGS. (A) and (b) are partially enlarged front sectional views showing still another embodiment of the foamed resin molding die of the present invention. 本願発明の発泡樹脂成型金型の更に他の実施形態を示す図であり、同図(a)は一部拡大正面断面図であり、同図(b)はA-A線切断部断面図である。It is a figure which shows still another embodiment of the foam resin molding die of this invention, FIG. (A) is a partially enlarged front sectional view, and FIG. be. 本願発明の発泡樹脂成型金型の更に他の実施形態を示す図であり、同図(a)は正面図であり、同図(b)は一部拡大正面断面図である。It is a figure which shows the other embodiment of the foamed resin molding die of this invention, FIG. 3A is a front view, and FIG. 2B is a partially enlarged front sectional view. 図11の発泡樹脂成型金型の第1構成型を示す斜視図である。It is a perspective view which shows the 1st structural mold of the foam resin molding die of FIG. 従来の発泡樹脂成型金型を示す図であり、同図(a)は正面断面図であり、同図(b)は一部拡大正面断面図である。It is a figure which shows the conventional foam resin molding die, FIG. 6A is a front sectional view, and FIG. 2B is a partially enlarged front sectional view. 図13に示す発泡樹脂成型金型の使用状態を示す図であり、同図(a)は水冷工程における使用状態を示す断正面断面図であり、同図(b)は真空吸引工程における使用状態を示す断正面断面図である。13 is a diagram showing a usage state of the foamed resin molded mold shown in FIG. 13, FIG. 13A is a cut-off front sectional view showing a usage state in the water cooling process, and FIG. 13B is a usage state in the vacuum suction process. It is a cut-off front sectional view which shows.

次に、本願発明の実施形態について、図面に基づいて詳細に説明する。図1において、符号10は、本願発明の発泡樹脂成型金型を示す。 Next, embodiments of the present invention will be described in detail with reference to the drawings. In FIG. 1, reference numeral 10 indicates a foamed resin molding die of the present invention.

(発泡樹脂成型金型10の構成)
発泡樹脂成型金型10は、図1(a)に示すように、凹面12を有する凹型(第1構成型)14と、凸面13を有し、凸面13が凹型14の凹面12内に配置された状態で凹面12を覆う凸型(第2構成型)16と、凹面12と凸面13との間に生じる空間によって形成される成型室18と、凹型14に対して成型室18と反対側に設けられた第1流体室201と、凸型16に対して成型室18と反対側に設けられた第2流体室202と、発泡ビーズを成型室18へ導入する発泡ビーズ経路24と、を備えている。発泡樹脂成型金型10は、図1(a)に示す状態に対してX軸まわりに90°回転させた状態でも使用され得る。
(Structure of foamed resin molding mold 10)
As shown in FIG. 1A, the foamed resin molding die 10 has a concave mold (first configuration type) 14 having a concave surface 12 and a convex surface 13, and the convex surface 13 is arranged in the concave surface 12 of the concave mold 14. A convex mold (second configuration type) 16 that covers the concave surface 12 in a vertical state, a molding chamber 18 formed by a space created between the concave surface 12 and the convex surface 13, and a molding chamber 18 on the opposite side of the concave mold 14 to the molding chamber 18. It is provided with a first fluid chamber 201 provided, a second fluid chamber 202 provided on the opposite side of the convex mold 16 from the molding chamber 18, and a foamed bead path 24 for introducing foamed beads into the molding chamber 18. ing. The foamed resin molded mold 10 can also be used in a state of being rotated by 90 ° around the X axis with respect to the state shown in FIG. 1 (a).

発泡樹脂成型金型10の成型室18によって形成する製品は、略コの字断面を有する発泡樹脂容器である。このため、図1(a)に示すように、成型室18は、略コの字断面を有する。また、形成する発泡樹脂容器の板厚は略一定である。このため、成型室18の厚みW1が略一定となるように、凹型14の凹面12と凸型16の凸面13とは略平行になるように構成されている。 The product formed by the molding chamber 18 of the foamed resin molding die 10 is a foamed resin container having a substantially U-shaped cross section. Therefore, as shown in FIG. 1A, the molding chamber 18 has a substantially U-shaped cross section. Further, the plate thickness of the foamed resin container to be formed is substantially constant. Therefore, the concave surface 12 of the concave mold 14 and the convex surface 13 of the convex mold 16 are configured to be substantially parallel so that the thickness W1 of the molding chamber 18 is substantially constant.

凹型14は、第1流体室201と成型室18との間で流体(蒸気又は水)が通過可能であり、凹型14の板厚W2(図1(b)に示す)方向に対する垂直方向を長手方向とする複数の第1スリット261を有している。凹型14の成型室18側は、第1流体室201と成型室18との間で流体が通過可能であり、第1スリット261に連続する複数の第1水溜部281が設けられている。第1水溜部281は、図1(c)に示すように、長方形断面を有する。第1水溜部281は、成型室18側を開口部とする凹部形状である。第1水溜部281の幅W3は、直径約2.0~5.0mmの発泡ビーズが入り込まないように、直径約2.0mm未満である。第1水溜部281の幅W3は、第1スリット261の幅W4よりも大きく構成されている。第1スリット261の幅W4は、0.2~1.5mmであり、蒸気又は水が通過できればよいため狭くてもよい一方で、第1水溜部281の幅W3は、約2.0mm未満の範囲で極力大きくし、より多量の水が付着し溜まりやすくなるように構成されている。 The concave mold 14 allows fluid (steam or water) to pass between the first fluid chamber 201 and the molding chamber 18, and is longitudinal in the direction perpendicular to the plate thickness W2 (shown in FIG. 1B) of the concave mold 14. It has a plurality of first slits 261 in the direction. On the molding chamber 18 side of the concave mold 14, fluid can pass between the first fluid chamber 201 and the molding chamber 18, and a plurality of first water reservoirs 281 continuous with the first slit 261 are provided. The first reservoir 281 has a rectangular cross section as shown in FIG. 1 (c). The first water reservoir 281 has a concave shape with the molding chamber 18 side as an opening. The width W3 of the first water reservoir 281 is less than about 2.0 mm in diameter so that foamed beads having a diameter of about 2.0 to 5.0 mm do not enter. The width W3 of the first water reservoir 281 is larger than the width W4 of the first slit 261. The width W4 of the first slit 261 is 0.2 to 1.5 mm and may be narrow as long as steam or water can pass therethrough, while the width W3 of the first water reservoir 281 is less than about 2.0 mm. It is configured to be as large as possible in the range so that a larger amount of water can easily adhere and accumulate.

凸型16は、第2流体室202と成型室18との間で流体(蒸気又は水)が通過可能であり、凸型16の凸面13と平行な方向(凸型16の板厚W5(図1(b)に示す)方向に対する垂直方向)を長手方向とする複数の第2スリット262を有している。凸型16の成型室18側は、第2流体室202と成型室18との間で流体が通過可能であり、第2スリット262に連続する複数の第2水溜部282が設けられている。第2スリット262の形状及び寸法は、第1スリット261と同一である。第2水溜部282の形状及び寸法は、第1水溜部281と同一である。 The convex mold 16 allows fluid (steam or water) to pass between the second fluid chamber 202 and the molding chamber 18, and is in a direction parallel to the convex surface 13 of the convex mold 16 (plate thickness W5 of the convex mold 16 (FIG. FIG. It has a plurality of second slits 262 whose longitudinal direction is (the direction perpendicular to the direction (shown in 1 (b))). On the molding chamber 18 side of the convex mold 16, fluid can pass between the second fluid chamber 202 and the molding chamber 18, and a plurality of second water reservoirs 282 continuous with the second slit 262 are provided. The shape and dimensions of the second slit 262 are the same as those of the first slit 261. The shape and dimensions of the second reservoir 282 are the same as those of the first reservoir 281.

第1流体室201及び第2流体室202は、図1(a)に示すように、発泡ビーズ経路24から成型室18内へ発泡ビーズを送る時に成型室18等の空気を抜くための空気流出経路46と、成型室18内の発泡ビーズ群へ加熱蒸気(蒸気)をボイラ(図示しない)から送る蒸気流入経路26と、成型室18内の発泡ビーズへ送った加熱蒸気を流出させる蒸気流出経路28と、第1流体室201及び第2流体室202に60°Cの冷却水(水)を給水器(図示しない)から送る冷却水流入経路(水流入経路)30と、第1流体室201等に送った冷却水を流出させる冷却水流出経路(水流出経路)32と、第1流体室201及び第2流体室202から真空ポンプ(図示しない)へ空気を吸引する真空吸引経路34と、を備えている。空気流出経路46は、開閉弁48を、蒸気流入経路26は、開閉弁36を、蒸気流出経路28は、開閉弁38を、冷却水流入経路30は、開閉弁40を、冷却水流出経路32は、開閉弁42を、真空吸引経路34は、開閉弁44を、各々備えている。第1流体室201及び第2流体室202内には、冷却水流入経路30に接続され、凹型14又は凸型16に向かって凹型14又は凸型16の板厚W2又はW5方向に放水するスプレーノズル(図示しない)が備えられている。 As shown in FIG. 1A, the first fluid chamber 201 and the second fluid chamber 202 have an air outflow for removing air from the molding chamber 18 and the like when the foamed beads are sent from the foamed bead path 24 into the molding chamber 18. A path 46, a steam inflow path 26 for sending heated steam (steam) from a boiler (not shown) to a group of foamed beads in the molding chamber 18, and a steam outflow path for discharging the heated steam sent to the foamed beads in the molding chamber 18. 28, a cooling water inflow path (water inflow path) 30 for sending cooling water (water) at 60 ° C to the first fluid chamber 201 and the second fluid chamber 202 from a water dispenser (not shown), and a first fluid chamber 201. A cooling water outflow path (water outflow path) 32 for flowing out the cooling water sent to the above, a vacuum suction path 34 for sucking air from the first fluid chamber 201 and the second fluid chamber 202 to a vacuum pump (not shown), and the like. Is equipped with. The air outflow path 46 has an on-off valve 48, the steam inflow path 26 has an on-off valve 36, the steam outflow path 28 has an on-off valve 38, and the cooling water inflow path 30 has an on-off valve 40, and the cooling water outflow path 32. Is provided with an on-off valve 42, and the vacuum suction path 34 is provided with an on-off valve 44. In the first fluid chamber 201 and the second fluid chamber 202, a spray connected to the cooling water inflow path 30 and discharging water toward the concave 14 or the convex 16 in the plate thickness W2 or W5 of the concave 14 or the convex 16. A nozzle (not shown) is provided.

(作用及び効果)
本願発明の発泡樹脂成型金型10は、原料ビーズを形成する重合工程、発泡ビーズを形成する予備発泡工程、及び、発泡樹脂製品を成型する成型工程の中の、成型工程において使用される。成型工程は、発泡ビーズを成型室18に充填する充填工程、成型室18内の発泡ビーズ群の片面に加熱蒸気(過熱蒸気、蒸気)を当てる片面加熱工程、成型室18内の発泡ビーズ群の両面に加熱蒸気を当てる両面加熱工程、冷却水によって凹型14又は凸型16等を冷却する水冷工程、第1流体室201及び第2流体室202から空気を吸引して凹型14等を冷却する真空吸引工程、及び、成型体を成型室から取り出す離型工程から成る。
(Action and effect)
The foamed resin molding die 10 of the present invention is used in a molding step in a polymerization step of forming raw material beads, a preliminary foaming step of forming foamed beads, and a molding step of molding a foamed resin product. The molding step includes a filling step of filling the foamed beads into the molding chamber 18, a one-sided heating step of applying heating steam (superheated steam, steam) to one side of the foamed bead group in the molding chamber 18, and a foaming bead group in the molding chamber 18. A double-sided heating step in which heated steam is applied to both sides, a water cooling step in which the concave 14 or the convex 16 or the like is cooled by cooling water, and a vacuum for sucking air from the first fluid chamber 201 and the second fluid chamber 202 to cool the concave 14 or the like. It consists of a suction step and a mold removal step of removing the molded body from the molding chamber.

(充填工程)
発泡ビーズ経路24から成型室18内へ、ポリスチレンの複数個の発泡ビーズ(以下、「発泡ビーズ」と言うときは、特に断らない限り複数個の発泡ビーズを言う)が送られる。フィーダー23から発泡ビーズ経路24に送られた発泡ビーズに、空気供給機25から圧縮空気が供給されることにより、図2に示すように、成型室18内に発泡ビーズが充填される。この時、開閉弁48が開かれ、成型室18内の空気が、第1スリット261、第2スリット262、第1流体室201及び第2流体室202等を介して、空気流出経路46から抜かれる。各図において、各開閉弁の中心に記載する「-」は、弁を閉じた状態を示す。
(Filling process)
A plurality of polystyrene foam beads (hereinafter, when referred to as "foam beads", refer to a plurality of foam beads unless otherwise specified) are sent from the foam bead path 24 into the molding chamber 18. Compressed air is supplied from the air supply machine 25 to the foamed beads sent from the feeder 23 to the foamed bead path 24, so that the foamed beads are filled in the molding chamber 18 as shown in FIG. At this time, the on-off valve 48 is opened, and the air in the molding chamber 18 is discharged from the air outflow path 46 via the first slit 261 and the second slit 262, the first fluid chamber 201, the second fluid chamber 202, and the like. Slit. In each figure, "-" described in the center of each on-off valve indicates a state in which the valve is closed.

(片面加熱工程)
約150~160°Cの加熱蒸気(過熱蒸気)により、成型室18内の発泡ビーズ群50が加熱される。ボイラ(図示しない)から送られた加熱蒸気が、図3に示すように、第1流体室201側の蒸気流入経路26から第1流体室201に送られる。第1流体室201に送られた加熱蒸気は、凹型14の第1スリット261及び第1水溜部281を通って、成型室18内へ送られ、成型室18内の発泡ビーズ群50の一方面に当たり、発泡ビーズ群50同士の隙間を通って、凸型16の第2水溜部282及び第2スリット262を通って、第2流体室202に送られ、第2流体室202側の蒸気流出経路28から流出し、成型室18内の発泡ビーズ群50が加熱される。この時、第1流体室201側の開閉弁36及び第2流体室202側の開閉弁38が開かれる。
(One-sided heating process)
The foamed bead group 50 in the molding chamber 18 is heated by the heated steam (superheated steam) at about 150 to 160 ° C. As shown in FIG. 3, the heated steam sent from the boiler (not shown) is sent to the first fluid chamber 201 from the steam inflow path 26 on the first fluid chamber 201 side. The heated steam sent to the first fluid chamber 201 is sent into the molding chamber 18 through the first slit 261 and the first water reservoir 281 of the concave mold 14, and is sent to the molding chamber 18 on one side of the foamed bead group 50 in the molding chamber 18. It is sent to the second fluid chamber 202 through the gap between the foamed bead groups 50, through the second water reservoir 282 and the second slit 262 of the convex type 16, and is sent to the second fluid chamber 202, and the steam outflow path on the second fluid chamber 202 side. Outflow from 28, the foamed bead group 50 in the molding chamber 18 is heated. At this time, the on-off valve 36 on the first fluid chamber 201 side and the on-off valve 38 on the second fluid chamber 202 side are opened.

次に、図示しないが、成型室18内の発泡ビーズ群50の他方面からの加熱が行われる。すなわち、加熱蒸気が、第2流体室202側の蒸気流入経路26から第2流体室202に送られ、凸型16の第2スリット262及び第2水溜部282を通って、成型室18内へ送られ、成型室18内の発泡ビーズ同士の隙間を通り、凹型14の第1水溜部281及び第1スリット261を通って、第1流体室202に送られ、第1流体室201側の蒸気流出経路28から流出する。この時、第2流体室202側の開閉弁36及び第1流体室201側の開閉弁38が開かれる。これらの片面加熱工程により、成型室18内の発泡ビーズは湿った状態となる。これらの片面加熱工程においては、加熱蒸気の一部は、凹型14の裏面58(成型室18と反対側の面)又は凸型16の裏面60(成型室18と反対側の面)に当たり、温度降下し、約90°Cのドレン水(凝縮水、蒸気が温度降下により液化した水)となり、凹型14の裏面58等に沿って流れ落ちる。また、加熱蒸気の一部は、凹型14の第1スリット261及び第1水溜部281又は凹型14の第1スリット261及び第1水溜部281を通って発泡ビーズ群50に当たり、温度降下し、ドレン水となって発泡ビーズ群50同士の隙間に滞留する。 Next, although not shown, heating is performed from the other surface of the foamed bead group 50 in the molding chamber 18. That is, the heated steam is sent from the steam inflow path 26 on the second fluid chamber 202 side to the second fluid chamber 202, passes through the second slit 262 of the convex 16 and the second water reservoir 282, and enters the molding chamber 18. The steam is sent to the first fluid chamber 202 through the gap between the foam beads in the molding chamber 18, through the first water reservoir 281 and the first slit 261 of the concave mold 14, and is the steam on the first fluid chamber 201 side. It flows out from the outflow route 28. At this time, the on-off valve 36 on the second fluid chamber 202 side and the on-off valve 38 on the first fluid chamber 201 side are opened. By these single-sided heating steps, the foamed beads in the molding chamber 18 become moist. In these one-sided heating steps, a part of the heated steam hits the back surface 58 of the concave mold 14 (the surface opposite to the molding chamber 18) or the back surface 60 of the convex mold 16 (the surface opposite to the molding chamber 18), and the temperature is increased. It descends to become drain water (condensed water, water liquefied by steam due to temperature drop) at about 90 ° C, and flows down along the back surface 58 and the like of the concave shape 14. Further, a part of the heated steam hits the foamed bead group 50 through the first slit 261 and the first water reservoir 281 of the concave shape 14 or the first slit 261 and the first water reservoir portion 281 of the concave mold 14, and the temperature drops and drains. It becomes water and stays in the gap between the foamed bead groups 50.

(両面加熱工程)
図4に示すように、2箇所の開閉弁36が開かれ、2箇所の蒸気流入経路26から、150°C~160°Cの加熱蒸気が、第1流体室201及び第2流体室202に送られる。これにより、凹型14及び凸型16はビーズ融着温度(ポリスチレンの場合、約120°C)まで昇温する。加熱蒸気は、凹型14の第1スリット261及び第1水溜部281、又は凸型16の第2スリット262及び第2水溜部282を通って、成型室18内に入る。成型室18内においては、発泡ビーズ群50同士の隙間に滞留するドレン水が沸騰し蒸発しながら発泡ビーズが膨らみ融着する。ドレン水が蒸発して生じた蒸気は、第1水溜部281及び第1スリット261等を通過して第1流体室201等へ排気される。成型室18内の発泡ビーズが膨らみ融着し固化することにより、図4に示すように、成型体52が形成される。なお、成型体52の形成後も、成型体52から蒸気が生じている。両面加熱工程における成型室18内の圧力は、約1.6~2kg/cmである。
(Double-sided heating process)
As shown in FIG. 4, two on-off valves 36 are opened, and heated steam at 150 ° C to 160 ° C flows from the two steam inflow paths 26 into the first fluid chamber 201 and the second fluid chamber 202. Sent. As a result, the concave 14 and the convex 16 are heated to the bead fusion temperature (about 120 ° C in the case of polystyrene). The heated steam enters the molding chamber 18 through the first slit 261 and the first water reservoir 281 of the concave mold 14 or the second slit 262 and the second water reservoir portion 282 of the convex mold 16. In the molding chamber 18, the drain water staying in the gaps between the foamed bead groups 50 boils and evaporates while the foamed beads swell and fuse. The steam generated by the evaporation of the drain water passes through the first water reservoir 281 and the first slit 261 and is exhausted to the first fluid chamber 201 and the like. As shown in FIG. 4, the molded body 52 is formed by the foamed beads in the molding chamber 18 swelling, fusing and solidifying. Even after the molded body 52 is formed, steam is generated from the molded body 52. The pressure in the molding chamber 18 in the double-sided heating step is about 1.6 to 2 kg / cm 2 .

(水冷工程)
図5(a)に示すように、2箇所の開閉弁40及び2箇所の開閉弁42が開かれ、給水器から約60°Cの冷却水が、2箇所の冷却水流入経路30から第1流体室201及び第2流体室202へ送られ、2箇所の冷却水流出経路32から流出される。第1流体室201及び第2流体室202内においては、冷却水流入経路30に接続されているスプレーノズル(図示しない)から凹型14等に向かって凹型14等の板厚方向(図5(a)において第1流体室201及び第2流体室202内に実線矢印で示す方向、X軸又はZ軸方向)に放水される。第1流体室201で放水された水の一部は、第1スリット261を通って第1水溜部281に入り込み、表面張力又は毛細管現象により第1水溜部281に付着し溜まる。第2流体室202で放水された水の一部は、第2スリット262を通って第2水溜部282に入り込み、表面張力により第2水溜部282に付着し溜まる。
(Water cooling process)
As shown in FIG. 5A, two on-off valves 40 and two on-off valves 42 are opened, and cooling water at about 60 ° C from the water supply is first from the two cooling water inflow paths 30. It is sent to the fluid chamber 201 and the second fluid chamber 202, and is discharged from the two cooling water outflow paths 32. In the first fluid chamber 201 and the second fluid chamber 202, the plate thickness direction of the concave mold 14 or the like is directed from the spray nozzle (not shown) connected to the cooling water inflow path 30 toward the concave mold 14 or the like (FIG. 5 (a). ), Water is discharged into the first fluid chamber 201 and the second fluid chamber 202 in the direction indicated by the solid arrow, the X-axis or the Z-axis direction). A part of the water discharged in the first fluid chamber 201 enters the first water reservoir 281 through the first slit 261 and adheres to and accumulates in the first water reservoir 281 due to surface tension or a capillary phenomenon. A part of the water discharged in the second fluid chamber 202 enters the second water reservoir 282 through the second slit 262, and adheres to and accumulates in the second water reservoir 282 due to surface tension.

凹型14及び凸型16は温度降下し、成型室18内の成型体52が温度降下し、成型体52は、図5に示すように、収縮する。成型体52が収縮することにより、成型体52と凹型14及び凸型16との間に隙間54が生じる。隙間54には、成型体52から生じている蒸気が入り込み、隙間54に入り込んだ蒸気は、冷却された凹型14及び凸型16に当たって温度降下し、約90°Cのドレン水のドレン境膜56となる。ドレン境膜56の熱は、低温側である第1水溜部281の水及び第2水溜部282の水へ移動する。このため、ドレン境膜56に接する成型体52の冷却を促進することができる。 The temperature of the concave mold 14 and the convex mold 16 drops, the temperature of the molded body 52 in the molding chamber 18 drops, and the molded body 52 shrinks as shown in FIG. As the molded body 52 contracts, a gap 54 is created between the molded body 52 and the concave mold 14 and the convex mold 16. Steam generated from the molded body 52 enters the gap 54, and the steam entering the gap 54 hits the cooled concave mold 14 and the convex mold 16 to lower the temperature, and the drain boundary film 56 of drain water at about 90 ° C. It becomes. The heat of the drain boundary film 56 is transferred to the water of the first reservoir 281 and the water of the second reservoir 282 on the low temperature side. Therefore, it is possible to promote cooling of the molded body 52 in contact with the drain boundary film 56.

(真空吸引工程)
図6に示すように、2箇所の開閉弁44が開かれ、第1流体室201及び第2流体室202の空気が、真空吸引経路34から真空ポンプ(図示しない)へ吸引される。第1流体室201及び第2流体室202の空気が吸引されることにより、成型室18、第1スリット261及び第1水溜部281等の空気が吸引される。成型室18等の空気が吸引されることにより、成型室18等の圧力は降下し、成型室18等に残存している水は蒸気化し(水の相変化を示す図示しないp-T線図に基づく)、蒸気が真空吸引経路34から吸引排出される。また、成型室18、第1スリット261及び第1水溜部281等の空気が吸引されることにより、成型室18等の中の蒸気は断熱膨張し、成型室18等の圧力が降下し、成型室18等は温度降下する。
(Vacuum suction process)
As shown in FIG. 6, two on-off valves 44 are opened, and the air in the first fluid chamber 201 and the second fluid chamber 202 is sucked from the vacuum suction path 34 to the vacuum pump (not shown). By sucking the air in the first fluid chamber 201 and the second fluid chamber 202, the air in the molding chamber 18, the first slit 261 and the first water reservoir 281 is sucked. When the air in the molding chamber 18 or the like is sucked, the pressure in the molding chamber 18 or the like drops, and the water remaining in the molding chamber 18 or the like is vaporized (p-T diagram showing the phase change of water). The steam is sucked and discharged from the vacuum suction path 34. Further, when the air in the molding chamber 18, the first slit 261 and the first water reservoir 281 is sucked, the steam in the molding chamber 18 and the like adiabatically expands, the pressure in the molding chamber 18 and the like drops, and molding is performed. The temperature of the chamber 18 and the like drops.

真空吸引工程において、第1水溜部281及び第2水溜部282に溜まっている水へ、ドレン境膜56の熱が移動する。このため、ドレン境膜56に接する凹型14、凸型16、及び成型体52等の冷却を促進することができる。また、第1水溜部281及び第2水溜部282に水が溜まっていることにより、第1水溜部281及び第2水溜部282に溜まっている水が蒸気化する。一方、ドレン水であるドレン境膜56が蒸気化する。凹型14、凸型16及び成型室18等の熱は、第1水溜部281等の水及びドレン境膜56の気化熱に使用される。発泡樹脂成型金型10は、第1水溜部281及び第2水溜部282を備えるため、第1水溜部281及び第2水溜部282に溜まった水の分だけ、従来の発泡樹脂成型金型に比して、気化熱に使用される熱量が多くなる。これにより、凹型14等の冷却を促進することができる。発泡樹脂成型金型10によれば、ドレン境膜56から第1水溜部281等に溜まっている水への熱移動と、凹型14等の熱が気化熱に使用されることとの相乗効果により、凹型14等の冷却をより促進することができる。 In the vacuum suction step, the heat of the drain boundary film 56 is transferred to the water accumulated in the first water reservoir 281 and the second water reservoir 282. Therefore, it is possible to promote cooling of the concave shape 14, the convex shape 16, the molded body 52, etc., which are in contact with the drain boundary film 56. Further, since the water is accumulated in the first reservoir 281 and the second reservoir 282, the water accumulated in the first reservoir 281 and the second reservoir 282 is vaporized. On the other hand, the drain boundary film 56, which is drain water, vaporizes. The heat of the concave mold 14, the convex mold 16, the molding chamber 18, etc. is used for the heat of vaporization of the water in the first water reservoir 281 and the like and the drain boundary film 56. Since the foamed resin molding die 10 includes the first water reservoir 281 and the second water reservoir 282, the amount of water accumulated in the first water reservoir 281 and the second water reservoir 282 is increased to the conventional foamed resin molding die. In comparison, the amount of heat used for the heat of vaporization increases. This makes it possible to promote cooling of the concave shape 14 and the like. According to the foamed resin molding mold 10, the heat transfer from the drain boundary film 56 to the water accumulated in the first water reservoir 281 and the like and the heat of the concave mold 14 and the like are used for the heat of vaporization due to the synergistic effect. , The cooling of the concave mold 14 and the like can be further promoted.

(離型工程)
凸型16が凹型14に対して、シリンダ機構等(図示しない)によって離隔され、成形室18から成型体52が取り出される。成型体52が取り出された時、凹型14及び凸型16の温度は、約65°Cである。
(Release process)
The convex mold 16 is separated from the concave mold 14 by a cylinder mechanism or the like (not shown), and the molded body 52 is taken out from the molding chamber 18. When the molded body 52 is taken out, the temperatures of the concave mold 14 and the convex mold 16 are about 65 ° C.

以上、本願発明の一実施形態について説明したが、本願発明は上述の実施形態に限定されない。例えば、上述の発泡樹脂成型金型10において、図7に示すように、凹型(第1構成型)14の裏面58に、第1スリット261に連続する第1貫通孔61を有する第1突出部71を備え、凸型(第2構成型)16の裏面60に、第2スリット262に連続する第2貫通孔62を有する第2突出部72を備えてもよい。片面加熱工程においては、図1に示す発泡樹脂成型金型10に関する片面加熱工程の説明で上述したように、加熱蒸気の一部は、凹型14の裏面58又は凸型16の裏面60に当たり、温度降下し、約90°Cのドレン水となり、凹型14の裏面58等に沿って流れ落ちる。第1突出部71及び第2突出部72を備えることにより、流れ落ちるドレン水は、第1突出部71等に当たり、第1スリット261等を回避し、ドレン水が第1スリット261等に侵入して付着するのを防止できる。このため、蒸気が第1スリット261等を通過して成型室18に送られることが確保される。 Although one embodiment of the present invention has been described above, the present invention is not limited to the above-described embodiment. For example, in the above-mentioned foamed resin molding die 10, as shown in FIG. 7, a first protruding portion having a first through hole 61 continuous with the first slit 261 on the back surface 58 of the concave mold (first configuration type) 14. 71 may be provided, and a second protrusion 72 having a second through hole 62 continuous with the second slit 262 may be provided on the back surface 60 of the convex type (second configuration type) 16. In the single-sided heating step, as described above in the description of the single-sided heating step regarding the foamed resin molding die 10 shown in FIG. 1, a part of the heated steam hits the back surface 58 of the concave mold 14 or the back surface 60 of the convex mold 16 and the temperature. It descends to become drain water at about 90 ° C, and flows down along the back surface 58 and the like of the concave mold 14. By providing the first protrusion 71 and the second protrusion 72, the drain water that flows down hits the first protrusion 71 and the like, avoids the first slit 261 and the like, and the drain water invades the first slit 261 and the like. It can be prevented from adhering. Therefore, it is ensured that the steam passes through the first slit 261 and the like and is sent to the molding chamber 18.

なお、水冷工程において、スプレーノズル(図示しない)から凹型14等に向かって、凹型14又は凸型16の板厚方向に、放水されるため、冷却水は、第1貫通孔61を介して第1スリット261から第1水溜部281に十分に送られ、第2貫通孔62を介して第2スリット262から第2水溜部282に十分に送られる。このため、第1水溜部281及び第2水溜部282の上述の効果は維持される。 In the water cooling step, water is discharged from the spray nozzle (not shown) toward the concave 14 and the like in the plate thickness direction of the concave 14 or the convex 16, so that the cooling water is discharged through the first through hole 61. It is sufficiently sent from the 1 slit 261 to the first water reservoir 281 and sufficiently sent from the second slit 262 to the second water reservoir 282 through the second through hole 62. Therefore, the above-mentioned effects of the first reservoir 281 and the second reservoir 282 are maintained.

また、本願発明の発泡樹脂成型金型10が備える第1水溜部281及び第2水溜部282の形状及び寸法は特に限定されない。例えば、図8(a)又は図8(b)に示す第1水溜部281及び第2水溜部282を備えた発泡樹脂成型金型10であってもよい。図8(a)又は(b)に示す第1水溜部281及び第2水溜部282は、第1スリット261及び第2スリット262よりも下方にのみ設けられている。表面張力により水が第1スリット261及び第2スリット262に付着して溜まるのに十分と考えられるからである。第1水溜部281の幅W3及び第2水溜部282の幅W6は、直径約2.0~5.0mmの発泡ビーズが入り込まないように、直径約2.0mm未満である。 Further, the shape and dimensions of the first water reservoir 281 and the second water reservoir 282 included in the foamed resin molding die 10 of the present invention are not particularly limited. For example, the foamed resin molded mold 10 provided with the first water reservoir 281 and the second water reservoir 282 shown in FIG. 8A or FIG. 8B may be used. The first water reservoir 281 and the second water reservoir 282 shown in FIGS. 8A or 8B are provided only below the first slit 261 and the second slit 262. This is because it is considered sufficient for water to adhere to and accumulate in the first slit 261 and the second slit 262 due to surface tension. The width W3 of the first reservoir 281 and the width W6 of the second reservoir 282 are less than about 2.0 mm in diameter so that foamed beads having a diameter of about 2.0 to 5.0 mm do not enter.

また、図9(a)又は(b)に示す第1水溜部281及び第2水溜部282を備えた発泡樹脂成型金型10であってもよい。図9(a)又は(b)に示す第1水溜部281及び第2水溜部282は、凹面12又は凸面13側が広がっている。ドレン境膜56に接触する部分を広くして、ドレン境膜56から第1水溜部281又は第2水溜部282への熱移動の迅速化を図り、ドレン境膜56に接する成型体52等の冷却を促進することができる。第1水溜部281の最大幅W3及び第2水溜部282の最大幅W6は、直径約2.0~5.0mmの発泡ビーズが入り込まないように、直径約2.0mm未満である。 Further, the foamed resin molded mold 10 provided with the first water reservoir 281 and the second water reservoir 282 shown in FIGS. 9A or 9B may be used. The concave surface 12 or the convex surface 13 side of the first water reservoir 281 and the second water reservoir 282 shown in FIGS. 9A or 9B is widened. The portion in contact with the drain boundary film 56 is widened to speed up the heat transfer from the drain boundary film 56 to the first water reservoir 281 or the second water reservoir 282, and the molded body 52 or the like in contact with the drain boundary film 56 is used. Cooling can be promoted. The maximum width W3 of the first reservoir 281 and the maximum width W6 of the second reservoir 282 are less than about 2.0 mm in diameter so that foamed beads having a diameter of about 2.0 to 5.0 mm do not enter.

また、図10(a)及び(b)に示す第1水溜部281及び第2水溜部282を備えた発泡樹脂成型金型10であってもよい。図10(a)及び(b)に示す第1水溜部281及び第2水溜部282は、1個の第1水溜部281が2個の第1スリット261に連続し、1個の第2水溜部282が2個の第2スリット262に連続している。第1水溜部281及び第2水溜部282の体積を大きくして、第1水溜部281等に溜める水の量を多くすることができる。この場合、図10(b)に示すように、第2水溜部282は、第2スリット262の長手方向に対して垂直方向(Z軸方向)が長手方向であり、第2水溜部282の幅W6は、直径約2.0~5.0mmの発泡ビーズが入り込まないように、直径約2.0mm未満である。第1水溜部281は第2水溜部282と形状及び寸法は同一である。また、1個の第1水溜部281が3個以上の第1スリット261に連続し、1個の第2水溜部282が3個以上の第2スリット262に連続するように構成してもよい。 Further, the foamed resin molded mold 10 provided with the first water reservoir 281 and the second water reservoir 282 shown in FIGS. 10A and 10B may be used. In the first water reservoir 281 and the second water reservoir 282 shown in FIGS. 10A and 10B, one first water reservoir 281 is continuous with two first slits 261 and one second water reservoir. The portion 282 is continuous with the two second slits 262. The volume of the first water reservoir 281 and the second water reservoir 282 can be increased to increase the amount of water stored in the first water reservoir 281 or the like. In this case, as shown in FIG. 10B, the second water reservoir 282 has a longitudinal direction (Z-axis direction) perpendicular to the longitudinal direction of the second slit 262, and the width of the second water reservoir 282. W6 has a diameter of less than about 2.0 mm so that foamed beads having a diameter of about 2.0 to 5.0 mm do not enter. The first water reservoir 281 has the same shape and dimensions as the second water reservoir 282. Further, one first reservoir 281 may be configured to be continuous with three or more first slits 261 and one second reservoir 282 may be continuous with three or more second slits 262. ..

また、発泡樹脂成型金型10において、第1構成型は図1に示す凹型14に限定されず、第2構成型は図1に示す凸型16に限定されない。例えば、図11(a)に示すように、半円形断面を有する第1構成型314及び第2構成型316であってもよい。第1構成型314は、図12に示すように、表面(成型室18と反対側の面)358に複数の凹部271が設けられ、各凹部271の底面に複数のスリット261が設けられている。第1構成型314の成型室18側には、図11(b)に示すように、スリット261に連続する水溜部281が設けられている。第1構成型314と第2構成型316とは、発泡ビーズ経路24が第1構成型314に設けられ第2構成型316に設けられないこと以外、形状及び寸法が同一である。成型室18は、第1構成型314と第2構成型316との間に生じる空間よって形成される。半円形断面を有する第1構成型314と半円形断面を有する第2構成型316とを備える発泡樹脂成型金型10によって、円柱形状のフロート(浮き体)を形成することができる。 Further, in the foamed resin molded mold 10, the first structural mold is not limited to the concave mold 14 shown in FIG. 1, and the second structural mold is not limited to the convex mold 16 shown in FIG. For example, as shown in FIG. 11A, the first configuration type 314 and the second configuration type 316 having a semicircular cross section may be used. As shown in FIG. 12, the first configuration type 314 is provided with a plurality of recesses 271 on the surface (the surface opposite to the molding chamber 18) 358, and a plurality of slits 261 on the bottom surface of each recess 271. .. As shown in FIG. 11B, a water reservoir 281 continuous with the slit 261 is provided on the molding chamber 18 side of the first configuration type 314. The first configuration type 314 and the second configuration type 316 have the same shape and dimensions except that the foamed bead path 24 is provided in the first configuration type 314 and not in the second configuration type 316. The molding chamber 18 is formed by a space created between the first configuration type 314 and the second configuration type 316. A cylindrical float can be formed by the foamed resin molding die 10 including the first structural mold 314 having a semi-circular cross section and the second structural mold 316 having a semi-circular cross section.

以上、本願発明の発泡樹脂成型金型について、図面に基づいて説明したが、図示したものに限定されない。例えば、第1水溜部及び第2水溜部の形状及び寸法を互いに異ならせてもよい。また、第1構成型が、凹面を有し、第2構成型が、第1構成型の凹面を覆う平板状であってもよい。 The foamed resin molding die of the present invention has been described above with reference to the drawings, but the present invention is not limited to the illustrated one. For example, the shapes and dimensions of the first reservoir and the second reservoir may be different from each other. Further, the first configuration type may have a concave surface, and the second configuration type may have a flat plate shape covering the concave surface of the first configuration type.

10:発泡樹脂成型金型
12:凹面
13:凸面
14:凹型(第1構成型)
16:凸型(第2構成型)
18:成型室
24:発泡ビーズ経路
26:蒸気流入経路
28:蒸気流出経路
30:冷却水流入経路(水流入経路)
32:冷却水流出経路(水流出経路)
32:冷却水流出経路
34:真空吸引経路
46:空気流出経路
50:発泡ビーズ群
52:成型体
54:隙間
56:ドレン境膜
261:第1スリット
262:第2スリット
281:第1水溜部
282:第2水溜部
10: Foam resin molding mold 12: Concave surface 13: Convex surface 14: Concave mold (first configuration type)
16: Convex type (second configuration type)
18: Molding chamber 24: Foamed bead path 26: Steam inflow path 28: Steam outflow path 30: Cooling water inflow path (water inflow path)
32: Cooling water outflow route (water outflow route)
32: Cooling water outflow path 34: Vacuum suction path 46: Air outflow path 50: Foamed beads group 52: Molded body 54: Gap 56: Drain boundary film 261: First slit 262: Second slit 281: First water reservoir 282 : 2nd water reservoir

Claims (8)

凹面を有する第1構成型と、
前記第1構成型の前記凹面を覆う第2構成型と、
前記第1構成型と前記第2構成型との間に生じる空間よって形成される成型室と、を備え、
前記第1構成型は、前記成型室とは反対側の面と、該成型室と、の間で流体が通過可能であり、該第1構成型の板厚方向に対する垂直方向を長手方向とする複数の第1スリットを有し、
前記第2構成型は、前記成型室とは反対側の面と、前記成型室と、の間で流体が通過可能であり、該第2構成型の板厚方向に対する垂直方向を長手方向とする複数の第2スリットを有し、
前記第1構成型の前記成型室側は、前記第1スリットに連続し、水が溜まる複数の第1水溜部が設けられ、
前記第2構成型の前記成型室側は、前記第2スリットに連続し、水が溜まる複数の第2水溜部が設けられた発泡樹脂成型金型。
The first configuration type with a concave surface and
The second configuration type that covers the concave surface of the first configuration type and
A molding chamber formed by a space generated between the first configuration type and the second configuration type is provided.
The first configuration mold allows fluid to pass between the surface opposite to the molding chamber and the molding chamber, and the direction perpendicular to the plate thickness direction of the first configuration mold is the longitudinal direction. Has multiple first slits,
The second configuration mold allows fluid to pass between the surface opposite to the molding chamber and the molding chamber, and the direction perpendicular to the plate thickness direction of the second configuration mold is the longitudinal direction. Has multiple second slits,
The molding chamber side of the first configuration type is provided with a plurality of first water reservoirs that are continuous with the first slit and collect water.
The molding chamber side of the second configuration mold is a foamed resin molding die in which a plurality of second water reservoirs are provided which are continuous with the second slit and where water is collected.
前記第1水溜部は、前記第1構成型に当てられる水の一部が前記第1スリットを通過して溜まるように構成され、
前記第2水溜部は、前記第2構成型に当てられる水の一部が前記第1スリットを通過して溜まるように構成された
請求項1に記載する発泡樹脂成型金型。
The first water reservoir is configured so that a part of the water applied to the first configuration type passes through the first slit and collects.
The foamed resin molding die according to claim 1, wherein the second water reservoir is configured so that a part of water applied to the second configuration mold passes through the first slit and collects.
前記第1構成型に当てられる水が、前記第1構成型の板厚方向に放水され、前記第2構成型に当てられる水が、前記第2構成型の板厚方向に放水されるように構成された請求項1又は2に記載する発泡樹脂成型金型。 The water applied to the first configuration type is discharged in the plate thickness direction of the first configuration type, and the water applied to the second configuration type is discharged in the plate thickness direction of the second configuration type. The foamed resin molding die according to claim 1 or 2, which is configured. 前記第1水溜部及び前記第2水溜部が、前記成型室側を開口部とする凹部形状である請求項1~3のいずれかに記載する発泡樹脂成型金型。 The foamed resin molding die according to any one of claims 1 to 3, wherein the first water reservoir and the second water reservoir have a concave shape with the molding chamber side as an opening. 前記第1構成型は、前記成型室とは反対側の面に、前記第1スリットに連続する第1貫通孔を有する第1突出部を備え、
前記第2構成型は、前記成型室とは反対側の面に、前記第2スリットに連続する第2貫通孔を有する第2突出部を備えた請求項1~4のいずれかに記載する発泡樹脂成型金型。
The first configuration type is provided with a first protrusion having a first through hole continuous with the first slit on a surface opposite to the molding chamber.
The foam according to any one of claims 1 to 4, wherein the second configuration type is provided with a second protrusion having a second through hole continuous with the second slit on a surface opposite to the molding chamber. Resin molding mold.
前記第1構成型に対して前記成型室とは反対側に設けられた第1流体室と、
前記第2構成型に対して前記成型室とは反対側に設けられた第2流体室と、
発泡ビーズを前記成型室へ導入する発泡ビーズ経路と、
を備え、
前記第1流体室及び前記第2流体室は、
前記成型室へ蒸気を送るための蒸気流入経路と、
前記成型室へ送った前記蒸気を流出させる蒸気流出経路と、
水が流入する水流入経路と、
流入した前記水を流出させる水流出経路と、
空気が吸引される真空吸引経路と、
を備えた請求項1~5のいずれかに記載する発泡樹脂成型金型。
A first fluid chamber provided on the side opposite to the molding chamber with respect to the first configuration type,
A second fluid chamber provided on the side opposite to the molding chamber with respect to the second configuration type,
The foamed bead path for introducing the foamed beads into the molding chamber, and
Equipped with
The first fluid chamber and the second fluid chamber are
The steam inflow path for sending steam to the molding chamber and
A steam outflow path for outflowing the steam sent to the molding chamber,
The water inflow route and the water inflow route
The water outflow route that causes the inflowing water to flow out,
The vacuum suction path where air is sucked and
The foamed resin molding die according to any one of claims 1 to 5.
前記請求項1~6のいずれかに記載する発泡樹脂成型金型を使用した発泡樹脂成型方法であり、
前記成型室に発泡ビーズを充填するステップと、
前記第1構成型及び前記第2構成型に蒸気を当てるステップと、
前記発泡樹脂成型金型の前記第1構成型及び前記第2構成型に水を当てるステップと、を含む発泡樹脂成型方法。
The foamed resin molding method using the foamed resin molding die according to any one of claims 1 to 6.
The step of filling the molding chamber with foamed beads,
The step of applying steam to the first configuration type and the second configuration type,
A foamed resin molding method comprising a step of applying water to the first constitutional mold and the second constitutional mold of the foamed resin molding die.
前記第1水溜部は、前記第1構成型に当てられる水の一部が前記第1スリットを通過して溜まり、
前記第2水溜部は、前記第2構成型に当てられる水の一部が前記第2スリットを通過して溜まる請求項7に記載する発泡樹脂成型方法。
In the first water reservoir, a part of the water applied to the first configuration type passes through the first slit and collects.
The foamed resin molding method according to claim 7, wherein the second water reservoir portion is a part of water applied to the second configuration type and collects through the second slit.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012051182A (en) 2010-08-31 2012-03-15 Sekisui Plastics Co Ltd Foaming mold, and foam molded article formed using the same
JP2013223996A (en) 2012-04-23 2013-10-31 Sekisui Kaseihin Yamaguchi:Kk Forming apparatus
JP2019051595A (en) 2017-09-12 2019-04-04 株式会社山正製作所 Mold for foam molding

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5848112Y2 (en) * 1979-11-14 1983-11-02 積水化成品工業株式会社 Steam vents in foam molding equipment

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012051182A (en) 2010-08-31 2012-03-15 Sekisui Plastics Co Ltd Foaming mold, and foam molded article formed using the same
JP2013223996A (en) 2012-04-23 2013-10-31 Sekisui Kaseihin Yamaguchi:Kk Forming apparatus
JP2019051595A (en) 2017-09-12 2019-04-04 株式会社山正製作所 Mold for foam molding

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