JPH0442094Y2 - - Google Patents
Info
- Publication number
- JPH0442094Y2 JPH0442094Y2 JP19828387U JP19828387U JPH0442094Y2 JP H0442094 Y2 JPH0442094 Y2 JP H0442094Y2 JP 19828387 U JP19828387 U JP 19828387U JP 19828387 U JP19828387 U JP 19828387U JP H0442094 Y2 JPH0442094 Y2 JP H0442094Y2
- Authority
- JP
- Japan
- Prior art keywords
- mixing
- mixture
- housing
- viscosity
- delivery pump
- 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
- 239000007788 liquid Substances 0.000 claims description 20
- 238000003756 stirring Methods 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 17
- 238000000465 moulding Methods 0.000 claims description 11
- 239000006260 foam Substances 0.000 claims description 10
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 claims description 4
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000013329 compounding Methods 0.000 claims description 4
- 239000005011 phenolic resin Substances 0.000 claims description 4
- 229920001568 phenolic resin Polymers 0.000 claims description 4
- 229920005989 resin Polymers 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 239000012258 stirred mixture Substances 0.000 claims description 2
- 229920001187 thermosetting polymer Polymers 0.000 claims description 2
- 239000004615 ingredient Substances 0.000 description 7
- 238000013019 agitation Methods 0.000 description 5
- 238000005187 foaming Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010097 foam moulding Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- -1 neutralizers Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
Landscapes
- Injection Moulding Of Plastics Or The Like (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
この考案は、発泡成形品の製造において、硬質
ウレタンフオーム又はフエノール樹脂フオーム等
の反応性配合成分を、ハウジング内に設定された
混合かく拌部にて混合された粘度上昇の混合液
を、直接吸引送出する送出ポンプを、吐出口に連
結して、圧力の上昇を抑制すると共に、反応性混
合液を、最短時間にて成形部へ配送成形すること
を目指した熱硬化性樹脂の高粘度かく拌混合液送
出装置に関するものである。[Detailed description of the invention] [Industrial application field] This invention is used in the production of foam molded products to mix and stir reactive ingredients such as hard urethane foam or phenolic resin foam in a mixing and agitation unit set in a housing. A delivery pump that directly suctions and sends out the mixed liquid with increased viscosity mixed in the process is connected to the discharge port to suppress the increase in pressure and deliver the reactive mixed liquid to the molding section in the shortest possible time. This invention relates to a device for delivering a high-viscosity stirred mixture of thermosetting resin.
従来、この系統の反応性配合成分の混合装置と
しては、回転軸に多数の突起翼を設けて、かく拌
混合する系統のもので、すべて混合のみを主体と
するものであり、充分な混合可能と考えられるも
のは、たとえば、特公昭32−6376号、特公昭34−
6732号、特開昭48−63361号等の公報記載のもの、
また、高粘度においては、充分な混合が困難と考
えられるものは、たとえば、実公昭49−15928号、
特公昭50−23875号等の公報記載のものがある。
その外、高粘度配合成分の混合には不適当である
が、動力を使用しない自然落下による螺状混合路
によつて混合する系統、たとえば、特公昭42−
7235号公報記載のものがある。
Conventionally, this system of mixing devices for reactive components has been equipped with a number of protruding blades on the rotating shaft to stir and mix, and all of these systems have been used for mixing only, and have been able to mix sufficiently. For example, Tokuko No. 32-6376, Tokuko No. 34-
6732, JP-A No. 48-63361, etc.,
In addition, high viscosity materials that are considered difficult to mix sufficiently include, for example, Utility Model Publication No. 49-15928,
Some are described in publications such as Japanese Patent Publication No. 50-23875.
In addition, although it is not suitable for mixing high viscosity ingredients, there are systems that mix by a spiral mixing path using natural falling without using power, for example,
There is one described in Publication No. 7235.
上記混合かく拌系統の場合、混合液の粘度が比
較的低い場合は、かく拌装置の内部の圧力変化の
変動が少ないので作業上問題とはならないが、硬
質ウレタンフオーム又はフエノール樹脂フオーム
の場合、出発原料は、通常2000cp(25℃)程度で
あるが、所要の配合成分、中和剤、難燃剤、充填
剤、その他の添加剤等の各種成分の添加によつて
粘度は上昇する。特に高い粘度になつた場合、か
く拌装置内の内部圧力が急激に増加し、高粘度高
圧状態となつて吐出され、混合液の送り出しが困
難となり、吐出口に設けられた成形装置への注入
用ホースの脱落その他不円滑な吐出等の不具合を
生起し、製造の停止、または、かく拌装置の損傷
をもたらす等、作業工程に支障を招来するもので
ある。 In the case of the above-mentioned mixing and stirring system, if the viscosity of the mixed liquid is relatively low, there will be little pressure change inside the stirring device, so there will be no problem in operation, but in the case of hard urethane foam or phenolic resin foam, The starting material is usually about 2000 cp (25°C), but the viscosity increases by adding various ingredients such as necessary compounding ingredients, neutralizers, flame retardants, fillers, and other additives. When the viscosity becomes particularly high, the internal pressure inside the stirring device increases rapidly, resulting in a high viscosity and high pressure state being discharged, making it difficult to send out the mixed liquid and injecting it into the molding device installed at the discharge port. This causes troubles such as falling of the hose and other problems such as unsmooth discharge, which causes problems in the work process, such as stopping production or damaging the agitation device.
〔考案が解決しようとする問題点〕
上記従来の混合かく拌系統の装置において、高
粘度の混合液にて、硬質ウレタンフオーム又はフ
エノール樹脂フオームのボード類やパネル類を作
る場合、粘度が高いと吐出圧力が大きくなり、こ
の吐出される高圧混合液を成形部へ配給するた
め、吐出口に長いホースおよび注入パイプを連結
するとさらに圧力は上昇する。この吐出圧力が高
い時の問題点としては、
回転子の回転数が落ち、混合液のかく拌不
良、
回転軸から混合樹脂が逆流し、かく拌ヘツド
の固化、
ホースの破断又は脱落、
ホースの内部壁に高粘度混合物の付着により
所要量の流量の減少、
多成分配合系の場合、供給圧力変動の招来に
よる流量比の変動をもたらす。[Problems to be solved by the invention] In the above-mentioned conventional mixing and stirring system equipment, when making boards or panels of hard urethane foam or phenolic resin foam using a high viscosity liquid mixture, if the viscosity is high, The discharge pressure increases, and if a long hose and injection pipe are connected to the discharge port in order to distribute the discharged high-pressure mixed liquid to the molding section, the pressure will further increase. Problems when this discharge pressure is high include a drop in rotor rotation speed, poor stirring of the mixed liquid, mixed resin flowing back from the rotating shaft, solidification of the stirring head, rupture or falling off of the hose, and failure of the hose. The adhesion of a highly viscous mixture to the internal wall reduces the required flow rate, and in the case of a multi-component blend system, fluctuations in the flow rate ratio occur due to fluctuations in supply pressure.
因つて、上記の問題点の吐出圧力を低下し、短
時間に充分な混合と一定の移送速度にて吐出する
必要と共に、吐出口から出る吐出混合液を、成形
部へ配給するための配給管の設定によつて、さら
に圧力の上昇を招来することのないように、さら
に積極的に吸引排出して成形部へ配給する必要が
ある。特に、配合成分が比較的粘度の高い場合、
反応性が比較的早い場合は、導入される配合成分
を急速に混合かく拌し、吐出混合物を急速に成形
部へ配給成形する必要がある。特に発泡体の場合
は、混合物の粘度の上昇、反応の進行を極力避け
て成形部へ供給発泡硬化することである。 Therefore, it is necessary to reduce the discharge pressure of the above-mentioned problem, to achieve sufficient mixing in a short time and to discharge at a constant transfer speed, and a distribution pipe for distributing the discharged mixed liquid discharged from the discharge port to the molding section. In order to prevent further increase in pressure due to the settings of , it is necessary to more actively suck and discharge the fluid and distribute it to the molding section. In particular, when the ingredients are relatively viscous,
If the reactivity is relatively fast, it is necessary to rapidly mix and stir the introduced ingredients and rapidly distribute the discharged mixture to the molding section. Particularly in the case of foam, the mixture should be supplied to the molding section and cured by foaming while avoiding an increase in the viscosity of the mixture and progression of the reaction as much as possible.
上記の問題点を解消するため、可及的短時間に
混合配給して成形を行うため、混合かく拌部にて
急速混合かく拌を行ない、混合かく拌部の吐出口
に、ルーツ(Roots)ポンプ又はギヤーポンプ等
の送出ポンプを連結して積極的に吸引し、その先
端にホースおよびパイプを連結して、成形部の所
定の位置へ、吐出混合液を搬送するように構成す
るものである。詳細は、実施例において図面に基
づいて具体的に説明する。
In order to solve the above problems, in order to mix and distribute and form in the shortest possible time, rapid mixing and agitation is performed in the mixing and agitation section, and roots are placed at the outlet of the mixing and agitation section. A delivery pump such as a pump or a gear pump is connected to actively suck the liquid, and a hose and a pipe are connected to the tip of the pump to convey the discharged mixed liquid to a predetermined position in the molding section. Details will be specifically explained in Examples based on the drawings.
この考案のかく拌混合液送出装置は、混合かく
拌部にて急速混合を行ない、送出ポンプにて積極
的に吸引送出するため、混合液の粘度上昇が抑制
され、低粘度、低反応状態の発泡性混合液が得ら
れる。
The mixing and mixing device of this invention performs rapid mixing in the mixing and stirring section and actively sucks and delivers the mixture using the delivery pump, thereby preventing the viscosity of the mixture from increasing and producing a foaming mixture with low viscosity and low reaction.
第1図は、この考案の高粘度かく拌混合液送出
装置のハウジング内の機構並びに送出ポンプ内部
機構の概要正面図で、ハウジング内の混合かく拌
部は、回転軸に棒状の突起翼を配列固定したもの
で、送出ンポンプは、混合かく拌部の吐出口に送
出ポンプを連結するものであり、本例は、送出ポ
ンプの一例としてルーツポンプを使用したもので
ある。
Fig. 1 is a schematic front view of the mechanism inside the housing of the high viscosity stirred mixed liquid delivery device of this invention and the internal mechanism of the delivery pump. The delivery pump is a fixed one, and the delivery pump is connected to the discharge port of the mixing and stirring section, and in this example, a Roots pump is used as an example of the delivery pump.
第2図は、第1図の他の実施例を示したもの
で、混合かく拌部の形態が第1図と異なるだけで
ある。すなわち、ハウジング内の混合かく拌部
は、回転軸に角形の突起翼を千鳥状に配列固定し
たもので、送出ポンプの連結は、第1図と同様で
ある。 FIG. 2 shows another embodiment of FIG. 1, and the only difference from FIG. 1 is the form of the mixing and stirring section. That is, the mixing/stirring section in the housing has rectangular protruding blades arranged and fixed in a staggered manner around the rotating shaft, and the connection of the delivery pump is the same as that shown in FIG. 1.
なお、第2図においては、角形の突起翼の上部
の回転部に溝を形成し、混合液が回転によつて逆
方向に上昇するのを抑制するように対処されてい
るものである。 In addition, in FIG. 2, a groove is formed in the rotating part of the upper part of the rectangular protruding wing to suppress the mixed liquid from rising in the opposite direction due to rotation.
図において、1はハウジング、2は回転軸、3
は突起翼で、第1図は、棒状の各突起翼3を回転
軸2の同一円周上に複数個、上下に複数列を固定
配置して混合かく拌部を形成するものである。第
2図の3aは角形の突起翼で、回転軸に千鳥状に
配列固定されている。4は混合液の吐出口、5,
6は配合成分の導入口で、必要に応じて増加され
る。7は吐出口と送出ポンプとを連結する連結
管、8は送出ポンプ、9は混合液を成形部へ送出
する送出口である。本例は、送出ポンプにルーツ
ポンプの一例を示したものであるが、ギヤーポン
プ等が適宜に使用される。なお、10は混合かく
拌部の上部の回転部の周囲に設けられた溝であ
る。 In the figure, 1 is the housing, 2 is the rotating shaft, and 3
In FIG. 1, a plurality of bar-shaped protrusion blades 3 are fixedly arranged on the same circumference of the rotary shaft 2 in multiple rows above and below to form a mixing and stirring section. 3a in FIG. 2 is a rectangular protruding wing, which is arranged and fixed in a staggered manner on the rotating shaft. 4 is a discharge port for mixed liquid; 5;
Reference numeral 6 is an inlet for introducing ingredients, which is increased as necessary. Reference numeral 7 designates a connecting pipe that connects the discharge port and the delivery pump, 8 designates the delivery pump, and 9 designates the delivery port that delivers the mixed liquid to the molding section. Although this example shows an example of a Roots pump as the delivery pump, a gear pump or the like may be used as appropriate. Note that 10 is a groove provided around the rotating part at the upper part of the mixing and stirring part.
第3図は、従来の混合かく拌装置のハウジング
内の機構の概要正面図で、1はハウジング、2は
回転軸、3は棒状の突起翼で回転軸2の同一円周
上に複数個、上下に複数列を固定配置して混合か
く拌部を構成するもので、4は混合液の吐出口で
ある。 FIG. 3 is a schematic front view of the mechanism inside the housing of a conventional mixing/stirring device, in which 1 is the housing, 2 is a rotating shaft, 3 is a plurality of rod-shaped protruding blades on the same circumference of the rotating shaft 2, A plurality of rows are fixedly arranged above and below to constitute a mixing/stirring section, and 4 is a discharge port for the mixed liquid.
この考案の装置は、前記作用の項に記述のとお
り、混合液の粘度上昇が抑制され、バラツキの少
ない均等な低粘度、低反応状態の発泡性混合液が
成形部に供給され、発泡成形化され、高歩留り
で、均一な所要の発泡製品が得られる。
As described in the operation section, the device of this invention suppresses the increase in the viscosity of the liquid mixture, and supplies a foaming liquid mixture with a uniform low viscosity and low reaction state with little variation to the molding section, resulting in foam molding. The desired foamed product is obtained with high yield and uniformity.
第1図は、この考案の高粘度かく拌混合液送出
装置のハウジング内の機構並びに送出ポンプ内機
構の概要正面図、第2図は、この考案の他の実施
例のハウジング内の機構並びに送出ポンプ内機構
の概要正面図、第3図は、従来の混合かく拌装置
のハウジング内の機構の概要正面図である。
1……ハウジング、2……回転軸、3,3a…
…突起翼、4……吐出口、5,6……反応性配合
成分液の導入口、8……送出ポンプ。
Figure 1 is a schematic front view of the mechanism inside the housing and the mechanism inside the delivery pump of the high viscosity stirred mixed liquid delivery device of this invention, and Figure 2 is a schematic front view of the mechanism inside the housing and the delivery pump of another embodiment of this invention. FIG. 3 is a schematic front view of the mechanism inside the housing of a conventional mixing and stirring device. 1...Housing, 2...Rotating shaft, 3, 3a...
... protruding wing, 4 ... discharge port, 5, 6 ... inlet for reactive compounding component liquid, 8 ... delivery pump.
Claims (1)
ーム等の反応性配合成分をかく拌混合するハウジ
ング内に、導入される複数の反応性配合成分液を
混合しうる、回転軸に多数の突起翼を固定した混
合かく拌部を形成し、混合液を低圧に保持するよ
うに、ハウジングの下部の吐出口に、成形部へ吸
引送出する送出ポンプを連結した構成を特徴とす
る熱硬化性樹脂の高粘度かく拌混合液送出装置。 A mixing/stirring device with a large number of protruding blades fixed to a rotating shaft that can mix a plurality of reactive compounding component liquids introduced into a housing that stirs and mixes reactive compounding components such as hard urethane foam or phenolic resin foam. A high-viscosity stirred mixture of thermosetting resin characterized by a configuration in which a delivery pump is connected to the discharge port at the bottom of the housing to suck and deliver the mixture to the molding part so as to maintain the mixture at a low pressure. Sending device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19828387U JPH0442094Y2 (en) | 1987-12-25 | 1987-12-25 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19828387U JPH0442094Y2 (en) | 1987-12-25 | 1987-12-25 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01101819U JPH01101819U (en) | 1989-07-10 |
JPH0442094Y2 true JPH0442094Y2 (en) | 1992-10-05 |
Family
ID=31488802
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19828387U Expired JPH0442094Y2 (en) | 1987-12-25 | 1987-12-25 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0442094Y2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4708094B2 (en) * | 2005-06-03 | 2011-06-22 | 株式会社ソディックプラステック | Injection device for liquid resin molding machine |
JP4628229B2 (en) * | 2005-09-16 | 2011-02-09 | 株式会社ソディックプラステック | Mixing device for liquid resin molding and injection equipment |
-
1987
- 1987-12-25 JP JP19828387U patent/JPH0442094Y2/ja not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPH01101819U (en) | 1989-07-10 |
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