JP4127196B2 - Reaction injection mold - Google Patents

Reaction injection mold Download PDF

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JP4127196B2
JP4127196B2 JP2003393750A JP2003393750A JP4127196B2 JP 4127196 B2 JP4127196 B2 JP 4127196B2 JP 2003393750 A JP2003393750 A JP 2003393750A JP 2003393750 A JP2003393750 A JP 2003393750A JP 4127196 B2 JP4127196 B2 JP 4127196B2
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mold
gate
reaction injection
norbornene
thickness
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JP2005153266A (en
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則夫 本田
勝人 広瀬
勝宏 高橋
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株式会社日立ハウステック
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本発明は、反応射出成形用型に関する。更に詳しくは、ボイド、未充填などの欠陥を抑制しながら成形品を製造できる反応射出成形用型に関する。   The present invention relates to a reaction injection mold. More specifically, the present invention relates to a reaction injection mold that can manufacture a molded product while suppressing defects such as voids and unfilled.

ノルボルネン系モノマーとメタセシス重合触媒からなる原料液を混合し、凸型及び凹型で構成される型へ射出し成形品を得る反応射出(RIM)成形法は、従来から良く知られている。例えば、ノルボルネン系モノマーとしてジシクロペンタジエンを用いたRIM成形法で家庭合併処理浄化槽の外槽が成形されている。このような反応射出成形に用いられる型は通常スプール部、ランナー部及びゲート部と呼ばれる反応導入部が形成される。そして、ミキシングヘッドで混合された混合液が、順次スプール部、ランナー部及びゲート部を経て、キャビティ内に圧入される。スプール部、ランナー部及びゲート部の構造については混合液の未充填箇所が生じないように、従来、種々検討されている。例えば、特許文献では、直管形状のゲート部に代えてフィルム形状のゲートを備える反応射出成形用型が提案されている。また、特許文献2ではフィルムゲートを扁平フィルム状とし、かつ、中央部で狭く、端部で広くなる反応射出成形用型が提案されている。しかし、従来の方法では型温度や型締め圧の変動によりゲート開口部の厚みが変化しても、それ応じてゲート開口部を調整するのは困難であり、またゲート開口部を調節するためにはゲート部を削り落とし又は肉盛りするなどで対応したが、その調整の方法ではその部位を削り込むという作業を繰り返さなければならず、決して容易な作業ではなかった。
特開平10−29228号公報 特開2002−46150号公報
A reaction injection (RIM) molding method, in which a raw material liquid composed of a norbornene monomer and a metathesis polymerization catalyst is mixed and injected into a mold composed of a convex mold and a concave mold to obtain a molded product, has been well known. For example, an outer tub of a household combined treatment septic tank is molded by a RIM molding method using dicyclopentadiene as a norbornene-based monomer. A mold used for such reaction injection molding usually has a reaction introduction part called a spool part, a runner part and a gate part. And the liquid mixture mixed with the mixing head is press-fitted into the cavity sequentially through the spool part, the runner part and the gate part. Conventionally, various studies have been made on the structure of the spool portion, the runner portion, and the gate portion so as not to cause an unfilled portion of the mixed liquid. For example, Patent Literature proposes a reaction injection mold having a film-shaped gate instead of a straight pipe-shaped gate portion. Patent Document 2 proposes a reaction injection molding die in which a film gate is formed into a flat film shape and is narrow at the center and wide at the end. However, in the conventional method, even if the gate opening thickness changes due to fluctuations in mold temperature and clamping pressure, it is difficult to adjust the gate opening accordingly. However, in the adjustment method, it was necessary to repeat the work of cutting the part, which was not an easy work.
JP-A-10-29228 JP 2002-46150 A

本発明の課題は、ゲート開口部を容易に調整することができ、型内への注入圧及び混合液の流れを制御し、ボイド、未充填などの不具合を防ぐことができる反応射出成形用型を提供することを目的とする。   An object of the present invention is to provide a reaction injection mold in which the gate opening can be easily adjusted, the injection pressure into the mold and the flow of the mixed liquid are controlled, and defects such as voids and unfilling can be prevented. The purpose is to provide.

上記課題を達成する為、混合液導入部の構造を種々検討した結果、ゲート部を入れ子構造することが効果的であることを見出した。
すなわち、本発明は次のものに関する。
(1) ノルボルネン系モノマーとメタセシス重合触媒からなる原料液を混合し、得られた混合液を凸型と凹型のキャビティ内に注入して反応硬化させる反応射出成形用型であって、前記注入部は、型の下方部にゲート部、その下方部にランナー部及びスプール部が略T字状に形成される構造であり、前記ゲート部は、前記キャビティと同等の長さの入れ子構造であり、長さ方向に分割された複数の入れ子を前記ゲート長さに合わせて組合せることにより、前記ゲート開口部の厚みを、長さ方向において連続的又は段階的に調整することができるようにしてなる反応射出成形用型。
(2) 入れ子構造と型ゲート部の間にスペーサーを挟み、ゲート開口部の厚みを調整できるようにしてなる項(1)に記載の反応射出成形用型。
(3) スペーサーが弾性体である項(2)記載の反応射出成形用型。
(4) 弾性体がスプリングである項(3)記載の反応射出成形用型。

As a result of various studies on the structure of the mixed liquid introduction part in order to achieve the above-mentioned problem, it has been found that it is effective to nest the gate part.
That is, the present invention relates to the following.
(1) A reaction injection mold for mixing a raw material liquid comprising a norbornene-based monomer and a metathesis polymerization catalyst, and pouring the obtained mixed liquid into a convex mold cavity and a concave mold cavity for reaction curing, wherein the injection section Is a structure in which a gate part is formed in the lower part of the mold, and a runner part and a spool part are formed in a substantially T shape in the lower part, and the gate part is a nested structure having a length equivalent to the cavity, By combining a plurality of inserts divided in the length direction according to the gate length, the thickness of the gate opening can be adjusted continuously or stepwise in the length direction. Reaction injection mold.
(2) The reaction injection molding die according to item (1), wherein a spacer is sandwiched between the nested structure and the die gate portion so that the thickness of the gate opening can be adjusted .
(3) The reaction injection mold according to item (2), wherein the spacer is an elastic body .
(4) The reaction injection mold according to item (3), wherein the elastic body is a spring .

本発明の反応射出用型を用いることで、ゲート開口部を容易に調整することができ、ジシクロペンタジエン等のノルボルネン系モノマーから成形欠陥の無い成形品を容易に製造することができる。   By using the reaction injection mold of the present invention, the gate opening can be easily adjusted, and a molded product free from molding defects can be easily produced from a norbornene monomer such as dicyclopentadiene.

以下、図面を参照しながら本発明を具体的に説明する。
図1は本発明に係る一対の反応射出成形用型の外観斜視図である。この反応射出成形用型が型締めされ、複数の原料液が加圧下でミキシングヘッドにより混合され、その混合液が凸型1と凹型2のキャビティ内に射出され反応硬化することで成形品が得られる。使用する型の材質は、通常、金属型を使用するが、合成樹脂、木材など使用することができる。型温は混合液の活性により適宜決定されるが、好ましくは20〜100℃、さらに好ましくは35〜85℃である。
Hereinafter, the present invention will be specifically described with reference to the drawings.
FIG. 1 is an external perspective view of a pair of reaction injection molds according to the present invention. The reaction injection mold is clamped, a plurality of raw material liquids are mixed by a mixing head under pressure, and the mixed liquid is injected into the cavities of the convex mold 1 and the concave mold 2 to be reacted and cured to obtain a molded product. It is done. As the material of the mold to be used, a metal mold is usually used, but synthetic resin, wood and the like can be used. The mold temperature is appropriately determined depending on the activity of the mixed solution, but is preferably 20 to 100 ° C, more preferably 35 to 85 ° C.

図2は本発明に係る一対の反応射出成形用型の凹型から凸型を見た正面図である。注入部は型の下方部にゲート部3が形成され更には、その下方部にランナー部4及びスプール部5が略T字状に形成される構造である。ここで、ゲート部3を型の下方部に配置するのは、エアやガスをキャビティ内上方に逃がし、ボイド等を発生させない為である。   FIG. 2 is a front view of the convex mold viewed from the concave mold of the pair of reaction injection molds according to the present invention. The injection part has a structure in which the gate part 3 is formed in the lower part of the mold, and the runner part 4 and the spool part 5 are formed in a substantially T shape in the lower part. Here, the reason why the gate portion 3 is disposed in the lower portion of the mold is that air or gas escapes upward in the cavity and does not generate voids or the like.

混合液の注入時間は、成形材料の特性上10〜50秒、好ましくは30〜40秒である。注入時間が長すぎると材料が注入中に硬化し未充填箇所が発生し、また短すぎるとエアを巻き込み易いからである。   The injection time of the mixed solution is 10 to 50 seconds, preferably 30 to 40 seconds, due to the characteristics of the molding material. This is because if the injection time is too long, the material hardens during the injection and an unfilled portion is generated, and if it is too short, air is easily involved.

スプール部5の断面積は、混合液を圧入させるポンプの能力及び型の強度から決定しており、注入時間に合せ材料の吐出量を選定する。この時、スプール部断面積が小さすぎると型に掛かる圧力が高くなり、その圧力に耐えられるようにするため型強度を上げなければならない。また、スプール部断面積が大きいと材料が無駄になりやすい。従って、射出圧力は1MPa以下、射出速度は5〜15m/s、スプール部の断面積は約100〜300mmである。 The cross-sectional area of the spool portion 5 is determined from the ability of the pump for press-fitting the mixed liquid and the strength of the mold, and the discharge amount of the material is selected in accordance with the injection time. At this time, if the cross-sectional area of the spool portion is too small, the pressure applied to the mold increases, and the mold strength must be increased in order to withstand the pressure. Further, if the spool section has a large cross-sectional area, the material is likely to be wasted. Therefore, the injection pressure is 1 MPa or less, the injection speed is 5 to 15 m / s, and the cross-sectional area of the spool portion is about 100 to 300 mm 2 .

ランナー部4の長さは、成形物の大きさに依存するが、スプール部の幅の10〜100倍程度ある。ランナー部における混合液流に直角な断面積は、スプール部断面積のおよそ半分程度に設計する。これは、スプール部を出た混合液がランナー部に垂直に衝突し、T字状に2方向に別れる際、圧力が減衰して流れが乱れるのを抑制するためである。   Although the length of the runner part 4 depends on the size of the molded product, it is about 10 to 100 times the width of the spool part. The cross-sectional area perpendicular to the mixed liquid flow in the runner part is designed to be about half of the cross-sectional area of the spool part. This is to prevent the mixed liquid that has exited the spool portion from colliding with the runner portion perpendicularly and separating into two directions in a T-shape, whereby the pressure is attenuated and the flow is disturbed.

本発明に用いる入れ子の材質は、アルミニウム、ステンレス、鉄、銅、ニッケル等の金属、ポリテトラフルオロエチレン等のフッ素樹脂、シリコーン、ウレタンなどのプラスチックなど制限はないが、入れ子挿入側の型材質と同じ物にするのが好ましい。材質を変えると熱膨張係数が違う為入れ子と挿入溝との間に隙間が空いてしまい混合液が入り込む恐れがあるからである。入れ子の形状及び大きさは該ゲート開口部の形状/又は厚みを調整できるものであれば制限はなく、型ゲート部に合わせて適宜決定されるが、一般的には、断面形状が正方形、長方形、台形等であり、幅5〜50mm、厚さ1〜30mm、長さ100〜3000mm、好ましくは幅10〜20mm、厚さ3〜10mm、長さ200〜1500mmである。入れ子の長さは製品となる部分のキャビティの長さと同等にすることが好ましく、入れ子の厚さは連続的/又は段階的に可変させてもかまわない。上記入れ子は、ゲート部長さに合わせて複数の入れ子を組合せることができる。部分的に入れ子を交換できることで、より微調整が可能だからである。入れ子の本数は通常1〜10本であるのが好ましく、夫々の形状/又は厚みは適宜決定することができる。さらに、入れ子と型の間にスペーサーを挿入し、そのスペーサーの厚みを変えることでゲート開口部の厚さを変えることができる。また、スペーサーとして弾性体やスプリングを用いることもできる。ボルトなどで入れ子を締め込む、或いは緩めるだけでその弾性力によりゲートの厚みを調整することができるからである。   The material of the nesting used in the present invention is not limited, such as metal such as aluminum, stainless steel, iron, copper, nickel, fluorine resin such as polytetrafluoroethylene, plastic such as silicone, urethane, etc. The same thing is preferable. This is because, if the material is changed, the coefficient of thermal expansion is different, so that a gap is formed between the insert and the insertion groove, and the mixed solution may enter. The shape and size of the nesting are not limited as long as the shape / or thickness of the gate opening can be adjusted, and are appropriately determined according to the mold gate, but generally the cross-sectional shape is square or rectangular. A trapezoid, etc., having a width of 5 to 50 mm, a thickness of 1 to 30 mm, and a length of 100 to 3000 mm, preferably a width of 10 to 20 mm, a thickness of 3 to 10 mm, and a length of 200 to 1500 mm. The length of the nesting is preferably equal to the length of the cavity of the product part, and the thickness of the nesting may be varied continuously / stepwise. The nesting can be combined with a plurality of nestings in accordance with the gate length. This is because it is possible to make fine adjustments by exchanging the nesting partly. It is preferable that the number of nestings is usually 1 to 10, and the shape / thickness of each can be determined as appropriate. Furthermore, the thickness of the gate opening can be changed by inserting a spacer between the insert and the mold and changing the thickness of the spacer. Further, an elastic body or a spring can be used as the spacer. This is because the thickness of the gate can be adjusted by the elastic force simply by tightening or loosening the insert with a bolt or the like.

本発明において使用されるノルボルネン系モノマーは、メタセシス重合性触媒の存在下に重合反応を行うことにより、成形品を得るものである。そのノルボルネン類としては、 ノルボルネン、ノルボルナジエン、メチルノルボルネン、ジメチルノルボルネン、エチルノルボルネン、エチリデンノルボルネン、ブチルノルボルネン、5−アセチル−2−ノルボルネン、ジメチル−5−ノルボルネン−2,3−ジカルボキシレート、N−ヒドロキシ−5−ノルボルネン−2,3−ジカルボキシイミド、5−ノルボルネン−2−カルボニトリル、5−ノルボルネン−2−カルボキシアルデヒド、5−ノルボルネン−2,3−ジカルボン酸モノメチルエステル、5−ノルボルネン−2,3−ジカルボン酸ジメチルエステル、5−ノルボルネン−2,3−ジカルボン酸ジエチルエステル、5−ノルボルネン−2,3−ジカルボン酸ジ−n−ブチルエステル、5−ノルボルネン−2,3−ジカルボン酸ジシクロヘキシルエステル、5−ノルボルネン−2,3−ジカルボン酸ジベンジルエステル、5−ノルボルネン−2,3−ジカルボン酸無水物、3,6ーエポキシー1,2,3,6ーテトラヒドロフタル酸無水物、5−ノルボルネン−2,3−ジカルボン酸、5−ノルボルネン−2−メタノール、6−トリエトキシシリル−2−ノルボルネン、5−ノルボルネン−2−オールなどの二環ノルボルネン、ジシクロペンタジエン(シクロペンタジエンの二量体)、ジヒドロジシクロペンタジエン、メチルジシクロペンタジエン、ジメチルジシクロペンタジエン、などの三環ノルボルネン、テトラシクロドデセン、メチルテトラシクロドデセン、ジメチルシクロテトラドデセンなどの四環ノルボルネン、トリシクロペンタジエン(シクロペンタジエンの三量体)、テトラシクロペンタジエン(シクロペンタジエンの四量体)などの五環以上のノルボルネンが挙げられる。以上の化合物は、単独で、または複数の併用でもかまわない。
ノルボルネン系モノマーは、特にコストの面より、ジシクロペンタジエンを用いることが好ましい。
The norbornene-based monomer used in the present invention is a product obtained by performing a polymerization reaction in the presence of a metathesis polymerizable catalyst. The norbornenes include norbornene, norbornadiene, methylnorbornene, dimethylnorbornene, ethylnorbornene, ethylidenenorbornene, butylnorbornene, 5-acetyl-2-norbornene, dimethyl-5-norbornene-2,3-dicarboxylate, N-hydroxy -5-norbornene-2,3-dicarboximide, 5-norbornene-2-carbonitrile, 5-norbornene-2-carboxaldehyde, 5-norbornene-2,3-dicarboxylic acid monomethyl ester, 5-norbornene-2, 3-dicarboxylic acid dimethyl ester, 5-norbornene-2,3-dicarboxylic acid diethyl ester, 5-norbornene-2,3-dicarboxylic acid di-n-butyl ester, 5-norbornene-2,3-dicarboxylic acid Acid dicyclohexyl ester, 5-norbornene-2,3-dicarboxylic acid dibenzyl ester, 5-norbornene-2,3-dicarboxylic acid anhydride, 3,6-epoxy-1,2,3,6-tetrahydrophthalic acid anhydride, 5 -Bicyclic norbornene such as norbornene-2,3-dicarboxylic acid, 5-norbornene-2-methanol, 6-triethoxysilyl-2-norbornene, 5-norbornene-2-ol, dicyclopentadiene (dimer of cyclopentadiene) ), Dihydrodicyclopentadiene, methyldicyclopentadiene, dimethyldicyclopentadiene, etc., tricyclic norbornene, tetracyclododecene, methyltetracyclododecene, tetracyclic norbornene, such as dimethylcyclotetradodecene, tricyclopentadiene ( Cyclopentadi Emissions of trimer), tetramer tetra cyclopentadiene (cyclopentadiene) and the pentacyclic or more norbornene like. These compounds may be used alone or in combination.
As the norbornene-based monomer, dicyclopentadiene is preferably used from the viewpoint of cost.

本発明において使用されるメタセシス重合性触媒は、ノルボルネン系モノマーの重合が可能なメタセシス重合性触媒であり、シクロオレフィン系化合物の開環重合用触媒として知られているものを使用することができる。具体例として、タングステン、モリブデン、タンタルなどのハロゲン化物、オキシハロゲン化物、酸化物、有機アンモニウム塩などが挙げられるが、適当な例としては、六塩化タングステン、オキシ四塩化タングステン、酸化タングステン、トリドデシルアンモニウムタングステート、トリ(トリデシル)アンモニウムタングステート、トリオクチルアンモニウムタングステート、などのタングステン化合物;五塩化モリブデン、オキシ三塩化モリブデン、トリドデシルアンモニウムモリブデート、メチルトリカプリルアンモニウムモリブデート、トリ(トリデシル)アンモニウムモリブデートなどのモリブデン化合物;五塩化タンタルなどのタンタル化合物、

Figure 0004127196
等のルテニウム化合物などがある。なお、上記において、C11はシクロヘキシル基、Cはフェニル基、C14はシメンを示す。 The metathesis polymerizable catalyst used in the present invention is a metathesis polymerizable catalyst capable of polymerizing norbornene monomers, and those known as catalysts for ring-opening polymerization of cycloolefin compounds can be used. Specific examples include halides such as tungsten, molybdenum and tantalum, oxyhalides, oxides, and organic ammonium salts. Suitable examples include tungsten hexachloride, tungsten oxytetrachloride, tungsten oxide, and tridodecyl. Tungsten compounds such as ammonium tungstate, tri (tridecyl) ammonium tungstate, trioctyl ammonium tungstate, etc .; molybdenum pentachloride, molybdenum oxytrichloride, tridodecyl ammonium molybdate, methyl tricaprylammonium molybdate, tri (tridecyl) ammonium Molybdate and other molybdenum compounds; tantalum compounds such as tantalum pentachloride,
Figure 0004127196
And ruthenium compounds. In the above, C 6 H 11 represents a cyclohexyl group, C 6 H 5 represents a phenyl group, and C 9 H 14 represents cymene.

本発明において使用される共触媒(活性剤)としては、アルキルアルミニウム、アルキルアルミニウムハライド、アルコキシアルキルアルミニウムハライド、アリールオキシアルキルアルミニウムハライド、有機スズ化合物などが挙げられるが、適当な例としては、トリエチルアルミニウム、トリイソブチルアルミニウム、トリオクチルアルミニウム、メチルアルミニウムセスキクロライド、エチルアルミニウムジクロライド、ジエチルアルミニウムクロライド、エチルアルミニウムセスキクロライド、プロピルアルミニウムジクロライド、イソブチルアルミニウムジクロライド、メチルアルミニウムセスキブロマイド、エチルアルミニウムジブロマイド、エチルアルミニウムジアイオダイド、ジエチルアルミニウムアイオダイド、プロピルアルミニウムジアイオダイド、テトラブチルスズなどがある。   Examples of the cocatalyst (activator) used in the present invention include alkylaluminum, alkylaluminum halide, alkoxyalkylaluminum halide, aryloxyalkylaluminum halide, organotin compound, etc. Suitable examples include triethylaluminum. , Triisobutylaluminum, trioctylaluminum, methylaluminum sesquichloride, ethylaluminum dichloride, diethylaluminum chloride, ethylaluminum sesquichloride, propylaluminum dichloride, isobutylaluminum dichloride, methylaluminum sesquibromide, ethylaluminum dibromide, ethylaluminum diiodide , Diethylaluminum iodide, propyla Mini Umm diiodide, there is such as tetra-butyl tin.

上記のメタセシス重合性触媒は、ノルボルネン系モノマーの1モルに対し、通常、約0.01〜50ミリモル、好ましくは0.1〜20ミリモルの範囲で用いられる。また、共触媒(活性剤)は、メタセシス重合性触媒成分の1モルに対して、通常、0.1〜200モル、好ましくは1〜10モルの範囲で用いられる。   The above-mentioned metathesis polymerizable catalyst is usually used in an amount of about 0.01 to 50 mmol, preferably 0.1 to 20 mmol, per 1 mol of the norbornene monomer. The cocatalyst (activator) is generally used in an amount of 0.1 to 200 mol, preferably 1 to 10 mol, per 1 mol of the metathesis polymerizable catalyst component.

ジシクロペンタジエン含有液を原料液として、重量100kg程度の浄化槽の筐体を製造する場合を例に以下に実施例及び比較例を挙げて、本発明についてさらに具体的に説明する。   The present invention will be described more specifically with reference to the following examples and comparative examples, taking as an example the case of producing a case of a septic tank weighing about 100 kg using a dicyclopentadiene-containing liquid as a raw material liquid.

(実施例1)
アルミ鋳造製の凸型1とニッケル電鋳の凹型2が型締めした後、2液タイプの原料液が加圧下でミキシングヘッドにより混合され、その混合液を凸型1と凹型2のキャビティ内に射出し反応硬化することで筐体を成形できる。混合液の注入時間は、成形材料の特性上35秒程度で注入する。型温度は凸型が40℃、凹型が80℃である。型の下方部にゲート部3が形成され更には、その下方部にランナー部4及びスプール部5が略T字状に形成される構造である。図3は凸型及び凹型が型締めした後の縦断面図である。図4は、図3A部の拡大図である。凸型に設けられた入れ子装着用の溝3に図5で示す3分割された入れ子7を装着する。入れ子はボルトにより型に固定する。入れ子の長さは夫々500mmとし、3本合わせてゲート部長さと同じ1500mmである。入れ子の幅は夫々10mmである。入れ子の厚さは、中央部の入れ子の厚み(t2)が5mm、両端の入れ子の厚み(t1、t3)が4.5mmである。入れ子の材質はアルミニウムである。図6に入れ子7を型に装着した後の図3A部の拡大図を示す。このように凸型及び凹型で形成されたキャビティーは図7のようになり、そのB−B断面図は図8のようになる。このようにできたゲート開口部8の厚みは中央部厚み(t2’)が約0.5mmであり、両端部厚み(t1’、t3’)が約1.0mmである。
また、スプール部5の断面積S1は約180mm、ランナー部4の長さは1500mm、断面積S2は100mmである。上記の型で成形した浄化槽成形品の結果を表1の実施例1に示す。
(Example 1)
After the convex mold 1 made of aluminum casting and the concave mold 2 made of nickel electroforming are clamped, a two-component type raw material liquid is mixed by a mixing head under pressure, and the mixed liquid is put into the cavities of the convex mold 1 and the concave mold 2. The case can be formed by injection and reaction hardening. The mixture liquid is injected in about 35 seconds due to the characteristics of the molding material. The mold temperature is 40 ° C. for the convex mold and 80 ° C. for the concave mold. The gate portion 3 is formed in the lower portion of the mold, and the runner portion 4 and the spool portion 5 are formed in a substantially T-shape in the lower portion. FIG. 3 is a longitudinal sectional view after the convex mold and the concave mold are clamped. FIG. 4 is an enlarged view of the portion shown in FIG. 3A. The nest 7 divided into three shown in FIG. 5 is mounted in the groove 3 for nest mounting provided in the convex shape. The nest is fixed to the mold with bolts. The length of the nesting is 500 mm, and the total length of the nests is 1500 mm, which is the same as the gate length. The width of the nesting is 10 mm each. As for the thickness of the nesting, the nesting thickness (t2) at the center is 5 mm, and the nesting thicknesses (t1, t3) at both ends are 4.5 mm. The material of the nesting is aluminum. FIG. 6 shows an enlarged view of the part of FIG. 3A after the insert 7 is mounted on the mold. Thus, the cavity formed by the convex shape and the concave shape is as shown in FIG. 7, and its BB sectional view is as shown in FIG. The thickness of the gate opening 8 thus formed is about 0.5 mm at the center (t2 ′) and about 1.0 mm at both ends (t1 ′, t3 ′).
Further, the cross-sectional area S1 of the spool portion 5 is about 180 mm 2 , the length of the runner portion 4 is 1500 mm, and the cross-sectional area S2 is 100 mm 2 . The results of the septic tank molded product molded with the above mold are shown in Example 1 of Table 1.

(比較例1)
中央部の入れ子の厚みが4.7mm、両端の入れ子の厚みが4.2mmである入れ子を用いる以外は、実施例1と同様の方法で成形品を得た。その結果を表1の比較例1に示す。
(Comparative Example 1)
A molded product was obtained in the same manner as in Example 1 except that a insert with a thickness of 4.7 mm at the center and a thickness of 4.2 mm at both ends was used. The results are shown in Comparative Example 1 in Table 1.

(比較例2)
中央部の入れ子の厚みが4.7mm、両端の入れ子の厚みが4.5mmである入れ子を用いる以外は、実施例1と同様の方法で成形品を得た。その結果を表1の比較例2に示す。
(Comparative Example 2)
A molded product was obtained in the same manner as in Example 1 except that a insert with a thickness of 4.7 mm at the center and a thickness of 4.5 mm at both ends was used. The results are shown in Comparative Example 2 in Table 1.

Figure 0004127196
表1に示すように型ゲート部の入れ子を入れ替えることで、ゲート開口部を容易に調整することができ、型内への注入圧及び混合液の流れを制御し、ボイド、未充填などの不具合を防ぐことができる。
Figure 0004127196
By changing the nest of the mold gate as shown in Table 1, the gate opening can be easily adjusted, the injection pressure into the mold and the flow of the liquid mixture are controlled, and voids, unfilled defects, etc. Can be prevented.

本発明の一実施例における一対の反応射出成形用型の外観斜視図。The external appearance perspective view of a pair of reaction injection molding type | mold in one Example of this invention. 図1における凸型の正面図。The front view of the convex type in FIG. 凸型及び凹型が型締めした後の縦断面図。The longitudinal cross-sectional view after a convex mold and a concave mold clamp. 図3A部の拡大図。The enlarged view of the FIG. 3A section. 3分割された入れ子。Nesting divided into three. 入れ子を型に装着した後の図3A部の拡大図。FIG. 3B is an enlarged view of the portion shown in FIG. 凸型及び凹型で形成されたキャビティー。Cavity formed by convex and concave molds. 図7のB−B断面図。BB sectional drawing of FIG.

符号の説明Explanation of symbols

1:凸型
2:凹型
3:ゲート部
4:ランナー部
5:スプール部
6:凸型1と凹型2のキャビティー
7:入れ子
8:ゲート開口部
9:ランナー開口部
10:スプール開口部

1: Convex type 2: Concave type 3: Gate part 4: Runner part 5: Spool part 6: Cavity of convex type 1 and concave type 2 7: Nest 8: Gate opening 9: Runner opening 10: Spool opening

Claims (4)

ノルボルネン系モノマーとメタセシス重合触媒からなる原料液を混合し、得られた混合液を凸型と凹型のキャビティ内に注入して反応硬化させる反応射出成形用型であって、前記注入部は、型の下方部にゲート部、その下方部にランナー部及びスプール部が略T字状に形成される構造であり、前記ゲート部は、前記キャビティと同等の長さの入れ子構造であり、長さ方向に分割された複数の入れ子を前記ゲート長さに合わせて組合せることにより、前記ゲート開口部の厚みを、長さ方向において連続的又は段階的に調整することができるようにしてなる反応射出成形用型。   A reaction injection mold for mixing a raw material liquid comprising a norbornene-based monomer and a metathesis polymerization catalyst, and injecting the obtained mixed liquid into a convex mold and a concave mold cavity and curing the reaction, wherein the injection section is a mold The gate portion is formed in the lower portion of the skirt, and the runner portion and the spool portion are formed in a substantially T-shape in the lower portion thereof. The gate portion is a nested structure having the same length as the cavity, and the length direction Reaction injection molding in which the thickness of the gate opening can be adjusted continuously or stepwise in the length direction by combining a plurality of nestings divided into two according to the gate length. Type. 入れ子構造と型ゲート部の間にスペーサーを挟み、ゲート開口部の厚みを調整できるようにしてなる請求項1に記載の反応射出成形用型。 The reaction injection molding die according to claim 1, wherein a spacer is interposed between the nested structure and the die gate portion so that the thickness of the gate opening can be adjusted . スペーサーが弾性体である請求項2記載の反応射出成形用型。 The reaction injection mold according to claim 2, wherein the spacer is an elastic body . 弾性体がスプリングである請求項3記載の反応射出成形用型。 4. The reaction injection mold according to claim 3, wherein the elastic body is a spring .
JP2003393750A 2003-11-25 2003-11-25 Reaction injection mold Expired - Fee Related JP4127196B2 (en)

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