JPH0464495B2 - - Google Patents
Info
- Publication number
- JPH0464495B2 JPH0464495B2 JP25561688A JP25561688A JPH0464495B2 JP H0464495 B2 JPH0464495 B2 JP H0464495B2 JP 25561688 A JP25561688 A JP 25561688A JP 25561688 A JP25561688 A JP 25561688A JP H0464495 B2 JPH0464495 B2 JP H0464495B2
- Authority
- JP
- Japan
- Prior art keywords
- screw
- barrier
- type
- zone
- injection
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 230000004888 barrier function Effects 0.000 claims description 25
- 238000002347 injection Methods 0.000 claims description 21
- 239000007924 injection Substances 0.000 claims description 21
- 239000000463 material Substances 0.000 claims description 17
- 238000010107 reaction injection moulding Methods 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 8
- 238000004898 kneading Methods 0.000 description 8
- 230000006835 compression Effects 0.000 description 5
- 238000007906 compression Methods 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000011344 liquid material Substances 0.000 description 4
- 230000010006 flight Effects 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012948 isocyanate Substances 0.000 description 2
- 150000002513 isocyanates Chemical class 0.000 description 2
- 229920005862 polyol Polymers 0.000 description 2
- 150000003077 polyols Chemical class 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 229920006311 Urethane elastomer Polymers 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920013716 polyethylene resin Polymers 0.000 description 1
Landscapes
- Injection Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は多液反応性樹脂の射出成形に用いる
反応射出成形用スクリユに関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a reaction injection molding screw used for injection molding of multi-component reactive resins.
[従来の技術]
高混練を目的とするスクリユのデザインは各方
面で研究され、種々のものが開発されている。こ
のうち一軸スクリユによるものとしては大別し
て、
(1) スクリユの一部に動的ミキシング部を設けた
方式。[Prior Art] The design of screws for the purpose of high kneading has been studied in various fields, and various designs have been developed. Among these, those using a single-shaft screw can be broadly divided into: (1) A method in which a dynamic mixing section is provided in a part of the screw.
(2) スクリユの一部に流動抵抗を増加させてエネ
ルギー変換を大きくする区間を設けた方式。(2) A method in which a section is provided in a part of the screw to increase flow resistance and increase energy conversion.
(3) スクリユ溝深さを液状に起状させて未溶融樹
脂に圧縮伸長を繰り返しさせるウエーブ方式。(3) A wave method in which the depth of the screw groove is raised in a liquid state and the unmolten resin is repeatedly compressed and stretched.
の3方式がある。There are three methods.
上記方式(1)の動的ミキシング部としては、スク
リユ軸の周囲に複数枚の凸条を平行または傾斜形
成したダルメージ型、軸周囲に複数本のピンを突
設したピン型など知られている。 As the dynamic mixing section of the above method (1), known methods include a dalmage type in which a plurality of protrusions are formed around a screw shaft in parallel or at an angle, and a pin type in which a plurality of pins are protruded around the shaft. .
また方式(2)のエネルギー変換手段としてあ、ス
クリユフライト間の軸周囲に、該フライトよりリ
ード角の大きいバリアフライトを設けたバリアフ
ライト変軸周囲に環状のバリアリングを設けたせ
き止めリング型、バリアリングの幅を拡げた状態
のチヨークを設けた円筒間隙型、軸周囲に形成し
た大径部分に多数の凹溝を並設したフルーテツド
バリア型などが知られている。 Further, as an energy conversion means of method (2), a dam ring type in which a barrier flight with a larger lead angle than the flight is provided around the axis between the screw flights and an annular barrier ring is provided around the variable axis; Known types include a cylindrical gap type in which a choke is provided with the width of the barrier ring expanded, and a fluted barrier type in which a large number of grooves are arranged in parallel in a large diameter portion formed around the shaft.
更にまた特公昭58−2056号公報に記載されてい
るように、上記方法を組合わせてメータリングゾ
ーンを構成したものもある。 Furthermore, as described in Japanese Patent Publication No. 58-2056, there is also a metering zone constructed by combining the above methods.
[発明が解決しようとする課題]
しかし上述の手段は、ペレツト状の樹脂材料の
溶融と混練とを目的とするものであるから、それ
をLIM(Liquid Injection Molding)のようにシ
リコーンゴム、エポキシ樹脂、ウレタンゴム、ポ
リエチレン樹脂等と液状硬化剤の混練計量や、
RIM(Reaction Injection Molding)のようにポ
リオール液とイソシアネート液の混練計量に用い
ると、不都合な事態が生じて混練を充分に行なえ
ない問題があつた。[Problems to be Solved by the Invention] However, since the above-mentioned method is aimed at melting and kneading pellet-like resin materials, it is possible to melt and knead resin materials in the form of pellets. , kneading and measuring urethane rubber, polyethylene resin, etc. and liquid curing agent,
When RIM (Reaction Injection Molding) is used for kneading and measuring polyol liquids and isocyanate liquids, an inconvenient situation arises and there is a problem in that sufficient kneading cannot be carried out.
これはLIM、RIMに用いられる液状材料が低
粘土であり、しかもペールポンプや供給プランジ
ヤなどによつて加圧された状態で射出装置内に供
給されることから、動的ミキシング部を備えたも
のであつても、充分な混練が行なわれないままに
通過してしまい、そのままの状態でキヤビテイに
充填される結果、硬化反応にむらが生じるからで
ある。このようなことは、流路抵抗を設けたもの
であつても、また溝深さを液状に変化させたもの
でも大差なく生じ、そこに得られる製品は強度が
劣つたものとなる。 This is because the liquid material used for LIM and RIM is low in clay and is supplied into the injection device under pressure by a pail pump, supply plunger, etc., so it is equipped with a dynamic mixing section. Even if it is, the material passes through without being sufficiently kneaded and is filled into the cavity in that state, resulting in uneven curing reaction. This kind of thing occurs regardless of whether the channel resistance is provided or the groove depth is changed to a liquid state, and the resulting product is inferior in strength.
更にまた特公昭58−2056号では、流路抵抗によ
り流出を抑え、その手前で混練を行なえ得ること
から、上記方式のものより高混練となるが、高圧
化で混練がなされるため、射出筒内にて反応が進
行してしまい、これが成形品質に悪影響を及ぼ
し、場合によつては射出筒内にて硬化してしまう
他、ミキシング部の手前側では層状流れの引き延
ばしのみがなされ、その後に撹拌されるため、混
練も充分ではない問題があつた。 Furthermore, in Japanese Patent Publication No. 58-2056, the outflow can be suppressed by the resistance of the flow path, and the mixing can be performed before the outflow, resulting in higher mixing than the above method, but since the mixing is done at high pressure, the injection tube The reaction progresses inside the injection tube, which adversely affects the molding quality, and in some cases causes hardening inside the injection cylinder.In addition, the laminar flow is only stretched out in front of the mixing section, and then Because of the stirring, there was a problem that the kneading was not sufficient.
この発明は上記問題を解決するために考えられ
たものであつて、その目的は簡単な構成で液状材
料と液状硬化剤との混練を充分に行なうことがで
き反応射出成形を行なう上にきわめて効果的な新
た構成のスクリユを提供することにある。 This invention was devised to solve the above problems, and its purpose is to be able to sufficiently knead a liquid material and a liquid curing agent with a simple structure, and to be extremely effective in performing reaction injection molding. The aim is to provide a new configuration of scrolls.
[課題を解決するための手段]
上記目的による発明は、射出スクリユのメータ
リングゾー開始部分に流路抵抗を増加させるバリ
ア部を備え、スクリユ回転時に材料の撹拌を行な
うミキシング部をフイードゾーンの終端部分に備
えてなり、また上記バリア部はせき止めリング
型、円筒型隙型、バリアフライト型、フルーテツ
ドバリア型等からなり、上記ミキシング部はダル
メージ型、ピン型等の1つまたは複数或はそれら
の組合せからなる。[Means for Solving the Problems] The invention according to the above object includes a barrier section for increasing the flow path resistance at the starting part of the metering zone of the injection screw, and a mixing section for stirring the material when the screw rotates at the end part of the feed zone. The barrier section is of a dam ring type, cylindrical gap type, barrier flight type, fluted barrier type, etc., and the mixing section is of one or more of a dalmage type, a pin type, etc., or a combination thereof. Consists of combinations.
[作 用]
上記記載による反応射出成形用スクリユは、フ
イードゾーンに供給された液化材料と液状硬化剤
とが、フイードゾーンで引き伸ばされたのち、ミ
キシング部により撹拌分配されるとともに拡散さ
れて、コンプレツシヨンゾーンに送られ、更に引
き伸ばされて、バリア部で再度拡散されてからメ
ータリングゾーンに入り、再びメータリングゾー
ンで引き伸ばされて均質化されつつスクリユ前部
への移送される。[Function] In the reaction injection molding screw described above, the liquefied material and liquid curing agent supplied to the feed zone are stretched in the feed zone, and then stirred and distributed by the mixing section and diffused, resulting in compression. The material is sent to the metering zone, further stretched, diffused again in the barrier section, enters the metering zone, stretched again in the metering zone, homogenized, and transferred to the front section of the screw.
[実施例]
図中1は射出スクリユで、射出筒2内に回転か
つ進退自在に設けられている。このスクリユ1の
後部は、スクリユ最前進時にて射出筒2の後部の
供給口4に干渉せぬ位置に設けたUパツキング3
により、樹脂洩れが生じないようにしてある。[Embodiment] In the figure, reference numeral 1 denotes an injection screw, which is provided in the injection cylinder 2 so as to be rotatable and movable forward and backward. The rear part of the screw 1 is provided with a U-packing 3 provided at a position that does not interfere with the supply port 4 at the rear of the injection tube 2 when the screw is fully advanced.
This prevents resin leakage.
また射出スクリユ1のフライト5を有する部分
は、上記供給口4に位置する後部側より谷径の小
さなフイードゾーンA、谷径が徐々に拡径するコ
ンプレツシヨンゾーンB、谷径の大きなメータリ
ングゾーンCの3ゾーンに区画され、フライト5
は各ゾーンごとにスクリユ軸の周囲に螺旋状に設
けてある。 In addition, the portion of the injection screw 1 having the flights 5 has a feed zone A with a smaller valley diameter than the rear side located at the supply port 4, a compression zone B where the valley diameter gradually increases, and a metering zone with a large valley diameter. Divided into 3 zones of C, Flight 5
is provided in a spiral around the screw shaft for each zone.
上記フイードゾーンAの終端部分にはスクリユ
回転時に材料の撹拌を行なうミキシング部6が、
フイードゾーンAより小さな開口面積にて形成さ
れ、また上記メータリングゾーン開始部分は流路
抵抗を増加させるバリア部7に形成してある。 At the end of the feed zone A, there is a mixing section 6 that stirs the material when the screw rotates.
It is formed with a smaller opening area than the feed zone A, and the metering zone starting portion is formed in a barrier section 7 that increases flow resistance.
第1図に示すミキシング部6は、突起61を8
個づつ所要間隔を空けて交互に位置をずらせて2
列に軸周囲に設けた2連のダルメージ型からなる
が、これ以外にスクリユ軸の周囲に複数枚の凸条
62を平行または傾斜形成したダルメージ型(第
7図から第9図参照)、軸周囲に複数本のピン6
3を交互に多重に突設したピン型(第10図及び
第11図参照)などをもつて形成される。 The mixing section 6 shown in FIG.
Alternately shift the positions of each piece at the required intervals 2
It consists of two Dalmage molds arranged around the shaft in a row, but there are also Dalmage molds in which a plurality of protrusions 62 are formed parallel or inclined around the screw shaft (see Figs. 7 to 9), and a shaft. Multiple pins 6 around
It is formed with a pin type (see FIG. 10 and FIG. 11) in which multiple numbers of 3 are protruded from each other alternately.
また第1図のバリア部7も、射出筒内径より僅
かに小径なリングの幅を拡げた状態のチヨーク7
1を軸周囲に突設した円筒間隙型からなるが、他
にフライト5よりもリード角が大きいとフライト
72を軸周囲に設けてなるバリアフライト型(第
4図参照)、リング73によるせき止めリング型
(第5図参照)、軸周囲に形成した大径部分に多数
の凹溝74を並設したフルーテツドバリア型(第
6図参照)などにより形成される。 Furthermore, the barrier part 7 in FIG.
It consists of a cylindrical gap type in which flight 1 is protruded around the shaft, but if the lead angle is larger than flight 5, there is also a barrier flight type in which flight 72 is installed around the shaft (see Fig. 4), and a damming ring with ring 73. It is formed by a mold (see FIG. 5), a fluted barrier type (see FIG. 6), etc. in which a large number of grooves 74 are arranged in parallel in a large diameter portion formed around the shaft.
なお図中8は供給口4に設けた供給ブロツク
で、液状材料路9と液状硬化剤路10とを有す
る。 In the figure, reference numeral 8 denotes a supply block provided at the supply port 4, which has a liquid material path 9 and a liquid curing agent path 10.
上記射出スクリユ1を内装した射出筒2に、供
給路4からポリオール液とイソシアネート液など
の材料を供給するとともに、射出スクリユ1を通
常の手段により回転して背圧を制御しつつ混練計
量を行なうと、ミキシング部6とバリア部7では
開口面積が小さく流路抵抗が大きいことから、材
料が低粘度であつても簡単に通過してしまうこと
はなく、フライト5間に形成されたスクリユ溝に
滞留する。 Materials such as polyol liquid and isocyanate liquid are supplied from the supply path 4 to the injection cylinder 2 in which the injection screw 1 is installed, and the injection screw 1 is rotated by ordinary means to perform kneading and metering while controlling the back pressure. Since the opening area of the mixing part 6 and the barrier part 7 is small and the flow resistance is large, even if the material has a low viscosity, it will not easily pass through, and the material will not easily pass through the screw groove formed between the flights 5. stay.
上記フイードゾーンAに供給された材料は、供
給圧とフライト5による移送力により前方へ送ら
れながら引き伸ばし混練され、ミキシング部6に
て撹拌分配されるとともに拡散されてコンプレツ
シヨンゾーンBに送られる。 The material supplied to the feed zone A is stretched and kneaded while being sent forward by the supply pressure and the transfer force by the flight 5, and is then agitated and distributed in the mixing section 6, and is sent to the compression zone B after being dispersed.
コンプレツシヨンゾーンBでは、材料は前方に
移送されながら再度引き伸ばし混練作用を受け、
また前方にバリア部7があることから、メータリ
ングゾーンCへの移送量が制限される。この制限
によりコンプレツシヨンゾーンB内の材料圧は大
きくなり、充分な混練とバリア部7を越えてメー
タリングゾーンCに移送するのに必要なエネルギ
ーが蓄積される。 In compression zone B, the material is transferred forward and subjected to stretching and kneading action again.
Furthermore, since there is a barrier section 7 in front, the amount transferred to the metering zone C is limited. This restriction increases the material pressure in the compression zone B and stores the energy required for sufficient mixing and transfer across the barrier section 7 to the metering zone C.
メータリングゾーンCでは、まずバリア部7に
て拡散が行なわれ、更に材料は引き伸ばし混練さ
れつつ前方へ移送されて軽量される。この際バリ
ア部7の前部にフライト5が存することにより、
温度の均一化が図られ、また安定した計量が行な
われる。 In the metering zone C, diffusion is first performed in the barrier section 7, and the material is further transferred to the front while being stretched and kneaded to reduce its weight. At this time, since the flight 5 exists in the front part of the barrier part 7,
This ensures uniform temperature and stable measurement.
[発明の効果]
この発明は上述のように、射出スクリユ1のメ
ータリングゾーンCの開始部分に、流路抵抗を増
加させるバリア部7を設け、スクリユ回転時に材
料の撹拌を行なうミキシング部6をフイードゾー
ンAの終端部分に設けてなることから、複数種の
液状材料を不要な圧力の下に混練することがな
く、また材料の滞留も長く、各ゾーンを移動する
間に充分に混練さて計量される結果、射出後の硬
化反応にむらがなく、強度に優れた反応射出成形
品が得られる。[Effects of the Invention] As described above, the present invention includes a barrier section 7 that increases the flow path resistance at the beginning of the metering zone C of the injection screw 1, and a mixing section 6 that stirs the material when the screw rotates. Since it is provided at the end of feed zone A, multiple types of liquid materials are not kneaded under unnecessary pressure, and the material stays for a long time so that it is sufficiently kneaded and weighed while moving through each zone. As a result, the curing reaction after injection is uniform, and a reaction injection molded product with excellent strength can be obtained.
図面はこの発明に係る反応射出用スクリユの実
施例を示すもので、第1図は射出筒に内装した状
態における一部縦断正面図図、第2図は第1図
−線断面図、第3図は−線断面図、第4図
から第6図はバリア部の他の実施例の説明図、第
7図から第11図はミキシング部の他の実施例の
説明図である。
1……射出スクリユ、2……射出筒、4……供
給口、5……フライト、6……ミキシング部、7
……バリア部。
The drawings show an embodiment of the reaction injection screw according to the present invention, in which FIG. 1 is a partially vertical front view of the reaction injection screw installed inside the injection tube, FIG. 2 is a cross-sectional view taken along the line of FIG. The figure is a cross-sectional view taken along the - line, FIGS. 4 to 6 are explanatory diagrams of other embodiments of the barrier section, and FIGS. 7 to 11 are explanatory diagrams of other embodiments of the mixing section. 1... Injection screw, 2... Injection tube, 4... Supply port, 5... Flight, 6... Mixing section, 7
...Barrier section.
Claims (1)
に流路抵抗を増加させるバリア部を備え、スクリ
ユ回転時に材料の撹拌を行なうミキシング部をフ
イードゾーンの終端部分に備えてなることを特徴
とする反応射出成形用スクリユ。 2 第1項記載の反応射出成形用スクリユにおい
て、上記バリア部はせき止めリング型、円筒間隙
型、バリアフライト型、フルーテツドバリア型等
からなり、上記ミキシング部はダルメージ型、ピ
ン型等の1つまたは複数或はそれらの組合せから
なることを特徴とする反応射出成形用スクリユ。[Scope of Claims] 1. A barrier part for increasing flow path resistance is provided at the starting part of the metering zone of the injection screw, and a mixing part for stirring the material when the screw rotates is provided at the end part of the feed zone. A screw for reaction injection molding. 2. In the screw for reaction injection molding according to item 1, the barrier part is of a dam ring type, cylindrical gap type, barrier flight type, fluted barrier type, etc., and the mixing part is one of a damage type, a pin type, etc. 1. A screw for reaction injection molding, characterized in that it consists of a plurality of or a combination thereof.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25561688A JPH02102015A (en) | 1988-10-11 | 1988-10-11 | Screw for reaction injection molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25561688A JPH02102015A (en) | 1988-10-11 | 1988-10-11 | Screw for reaction injection molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02102015A JPH02102015A (en) | 1990-04-13 |
JPH0464495B2 true JPH0464495B2 (en) | 1992-10-15 |
Family
ID=17281221
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25561688A Granted JPH02102015A (en) | 1988-10-11 | 1988-10-11 | Screw for reaction injection molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02102015A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6728462B1 (en) | 2019-10-30 | 2020-07-22 | 株式会社ソディック | Injection device |
-
1988
- 1988-10-11 JP JP25561688A patent/JPH02102015A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPH02102015A (en) | 1990-04-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4897236A (en) | Method and apparatus for the continuous manufacture of rubber or polymer-based mixtures containing additives | |
US4478516A (en) | Apparatus for mixing and blending constituents of a flow of thermoplastics material | |
US3817675A (en) | Apparatus for dispensing colorant in plasticized thermoplastic material | |
EP3815870B1 (en) | Extruding system and method of extruding | |
EP3412423B1 (en) | Mechanism for mixing supercritical fluid and polymer raw material melt | |
US11911945B2 (en) | Injection molding machine and injection molding method | |
JP4928315B2 (en) | Continuous mixing equipment | |
US2785438A (en) | Plastics extruder with mixing head | |
US5413475A (en) | Serial two-stage extruder | |
US6241375B1 (en) | Shear ring screw | |
JPH0839651A (en) | Thermoplastic resin extruder | |
JPH11179766A (en) | Method and apparatus for kneading injection molding of composite resin | |
CN102225317A (en) | Conical double rotor continuous mixing unit | |
US4112516A (en) | Plasticizing device of an injection molding machine for plastics | |
JP2004216725A (en) | Tire molding method and ribbon-shaped rubber extruder | |
JPH0464495B2 (en) | ||
CN101554771A (en) | Device for preparing polymer | |
JPH0564809A (en) | Single-shaft kneading reactive extruding device | |
CN212288645U (en) | Screw structure of plasticizing charging barrel | |
JP7601556B2 (en) | Injection molding apparatus and injection molding method | |
US3245662A (en) | Eccentric ring distributor | |
JP4254626B2 (en) | Injection device for injection molding machine and foam injection molding method | |
US3664639A (en) | Mixing device | |
CN212312417U (en) | Mixing arrangement is used in production of full vulcanization polyolefin elastomer | |
CN216579069U (en) | High-efficient plastify structure of extruding |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20081015 Year of fee payment: 16 |
|
EXPY | Cancellation because of completion of term |