JPH01262112A - Continuous mixing method of two-part cured resin - Google Patents
Continuous mixing method of two-part cured resinInfo
- Publication number
- JPH01262112A JPH01262112A JP9119988A JP9119988A JPH01262112A JP H01262112 A JPH01262112 A JP H01262112A JP 9119988 A JP9119988 A JP 9119988A JP 9119988 A JP9119988 A JP 9119988A JP H01262112 A JPH01262112 A JP H01262112A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- injected
- solvent
- resin
- curing
- 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.)
- Granted
Links
- 229920005989 resin Polymers 0.000 title claims abstract description 43
- 239000011347 resin Substances 0.000 title claims abstract description 43
- 238000000034 method Methods 0.000 title claims description 11
- 239000007788 liquid Substances 0.000 claims abstract description 41
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 31
- 239000002904 solvent Substances 0.000 claims abstract description 26
- 239000000203 mixture Substances 0.000 claims description 3
- 239000000945 filler Substances 0.000 abstract 2
- 230000014759 maintenance of location Effects 0.000 abstract 1
- 238000003756 stirring Methods 0.000 description 13
- 238000002347 injection Methods 0.000 description 11
- 239000007924 injection Substances 0.000 description 11
- 230000003068 static effect Effects 0.000 description 5
- 239000012530 fluid Substances 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
Landscapes
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、二液硬化型樹脂を連続的に混合させる方法
に関し、特に混合装置の始動時における二液の混合方法
に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for continuously mixing two-component curing resins, and particularly to a method for mixing two components at the time of starting up a mixing device.
樹脂フィルムや樹脂シートなどの成形品を成形するにあ
たり、二液硬化型樹脂が広く使われており、この二液硬
化型樹脂の例として、ポリイミド。Two-component curing resins are widely used to mold molded products such as resin films and sheets, and polyimide is an example of this two-component curing resin.
エポキシ、ウレタン、フェノール、不飽和ポリエステル
などが挙げられる。Examples include epoxy, urethane, phenol, and unsaturated polyester.
これらの二液硬化型樹脂は二液、例えば樹脂に硬化剤を
混合させると、徐々に反応して粘性が上昇して(硬化が
始まり)、ついには成形ができなくなる。この二液の混
合後、成形できなくなるまでの時間をポットライフ(可
使時間)といい、ポットライフは温度や二液の混合濃度
などにより長くなったり短くなったりする。このポット
ライフ内で樹脂成形品を成形するため、成形機の直近に
連続混合装置が配置され、この連続混合装置にて二液を
連続的に混合して成形機に供給するようにされている。These two-component curable resins are two-component, for example, when a curing agent is mixed with the resin, the resin gradually reacts and the viscosity increases (hardening begins), eventually making it impossible to mold the resin. The time from when these two liquids are mixed until they can no longer be molded is called the pot life (pot life), and the pot life may be longer or shorter depending on the temperature, the mixed concentration of the two liquids, etc. In order to mold a resin molded product within this pot life, a continuous mixing device is placed in close proximity to the molding machine, and this continuous mixing device continuously mixes the two liquids and supplies the mixture to the molding machine. .
連続混合装置には、気泡を発生させることなく二液を均
一にかつ迅速に混合させるため、二液硬化型樹脂のうち
一液、例えば樹脂を混合容器内に連続的に供給して撹拌
するとともに、他の一液、例えば硬化剤を付勢手段にて
付勢された逆止弁の弁体を硬化剤の注入圧力にて押し開
けて混合容器内に注入して、樹脂と硬化剤とを連続的に
混合させるようにした装置が提供されている。In order to mix the two components uniformly and quickly without generating air bubbles, the continuous mixing device continuously supplies one component of the two-component curing resin, such as resin, into a mixing container and stirs it. , another liquid, for example, a curing agent, is injected into the mixing container by pushing open the valve body of the check valve, which is energized by the urging means, with the injection pressure of the curing agent, thereby mixing the resin and the curing agent. Apparatus is provided for continuous mixing.
このような連続混合装置は、定常運転時においては硬化
剤の注入圧力と逆止弁の弁体が付勢手段にて付勢されて
いる力とは釣り合っているため、硬化剤が一定の流量で
混合容器内に注入される。In such a continuous mixing device, during steady operation, the injection pressure of the curing agent is in balance with the force applied to the valve body of the check valve by the urging means, so that the curing agent is supplied at a constant flow rate. is injected into the mixing vessel.
しかし、始動時においては、第5図に示すように、硬化
剤の注入圧力が弁体を付勢する付勢力に抗して高まり、
ある一定のピーク値に達して弁体が押し開かれた後、定
常運転時の圧力にまで上下動を繰り返しつつ低下してほ
ぼ一定値に安定する挙動を示す。However, at the time of startup, as shown in Figure 5, the injection pressure of the curing agent increases against the biasing force that biases the valve body.
After a certain peak value is reached and the valve body is pushed open, the pressure decreases while repeating up and down movements up to the pressure during steady operation, and then stabilizes at a nearly constant value.
この弁体が押し開かれる運転始動時には、必要量以上の
硬化剤が混合容器内に一気に注入されることとなるため
、硬化剤の混合濃度が高くなってしまう。混合濃度の高
い混合二液は混合容器内から排出されるまでにポットラ
イフが経過してしまい、この硬化の進んだ樹脂が混合容
器内に残って、付着することがあった。硬化の進んだ樹
脂は撹拌翼により細かく切断されて徐々に排出されてく
るため、それが異物として成形品の品質に影響を及ぼす
ような場合には、成形品全てが不良となることがあった
。At the start of operation when the valve body is pushed open, more hardening agent than the required amount is injected into the mixing container at once, resulting in a high mixed concentration of hardening agent. The pot life of the two highly concentrated mixed liquids has elapsed by the time they are discharged from the mixing container, and this hardened resin may remain in the mixing container and adhere thereto. The hardened resin is cut into small pieces by the stirring blades and gradually discharged, so if these foreign substances affect the quality of the molded product, the entire molded product may be defective. .
本発明はこのような課題を解決するために為されたもの
であり、その要旨とするところは、他の一液を注入する
にあたり、非硬化性液体にて弁体を押し開けた後、続い
て硬化性液体を混合容器内に注入するようにしたことに
ある。The present invention has been made to solve these problems, and its gist is that when injecting another liquid, after pushing the valve body open with a non-hardening liquid, The curable liquid is then injected into the mixing container.
かかる本発明方法によれば、二液硬化型樹脂のうち一液
を混合容器内に流しつつ、他の一液を混合容器内に注入
するにあたり、先ず前記一液とは非硬化性の液体によっ
て逆上弁の弁体が押し開かれる。したがって、弁体が付
勢される付勢力に抗して一気に多量の非硬化性液体が混
合容器内に注入されることとなるが、この非硬化性液体
によって混合容器内に流される一液が硬化させられるこ
とはないため、一液と非硬化性液体とは混合又は分離し
た状態で、混合容器内から排出されることとなる。非硬
化性液体により逆止弁の弁体が押し開かれて安定した状
態で、非硬化性液体に続いて硬化性液体が混合容器内に
注入されるため、硬化性液体が必要量以上に注入される
ことはない。According to the method of the present invention, when one part of the two-component curable resin is poured into the mixing container while the other part is injected into the mixing container, the first part is first separated from the other by a non-curing liquid. The valve body of the reversal valve is pushed open. Therefore, a large amount of non-hardening liquid is injected into the mixing container at once against the urging force applied to the valve body, but this non-hardening liquid causes one liquid to flow into the mixing container. Since the liquid is not cured, the liquid and the non-curable liquid are discharged from the mixing container in a mixed or separated state. The non-curing liquid pushes open the valve body of the check valve and in a stable state, the curable liquid is injected into the mixing container after the non-curing liquid, so more curable liquid is injected than the required amount. It will not be done.
混合容器内から排出された混合二液のうち、非硬化性液
体が注入された部分は一定量にわたって廃棄されること
となるが、成形品の不良の原因となる硬化の進んだ樹脂
が細かく切断されて、徐々に排出されてくるという事態
は発生することはない。Of the two liquids discharged from the mixing container, a certain amount of the part into which the non-hardening liquid was injected will be discarded, but the hardened resin will be cut into small pieces, which can cause defects in molded products. A situation where the liquid is gradually discharged will not occur.
次に、本発明の実施例を連続混合装置の一例を示す図面
を参照して、詳しく説明する。Next, embodiments of the present invention will be described in detail with reference to drawings showing an example of a continuous mixing device.
第1図及び第2図において、符号10は二液を連続的に
撹拌して混合させる連続混合装置の混合容器であり、そ
の混合容器10の一端には供給路12から圧送されてき
た樹脂が供給される流入口14が配設されるとともに、
その他端にはノズル状の流出口16が配設されている。In FIGS. 1 and 2, reference numeral 10 is a mixing container of a continuous mixing device that continuously stirs and mixes two liquids, and one end of the mixing container 10 is filled with a resin fed under pressure from a supply path 12. An inlet 14 for supplying the air is provided, and
A nozzle-shaped outlet 16 is provided at the other end.
混合容器10の内面にはほぼ半径方向内側に突出した円
柱状の静撹拌翼18が複数、同一円周上にほぼ等間隔に
配設されるとともに、この同一円周上に配設された複数
の静撹拌翼18からなる静翼列20が複数列(複数段)
にわたって配設されている。On the inner surface of the mixing container 10, a plurality of cylindrical static stirring blades 18 protruding approximately radially inward are disposed on the same circumference at approximately equal intervals, and a plurality of cylindrical static stirring blades 18 are disposed on the same circumference at approximately equal intervals. A plurality of rows (multiple stages) of static blade rows 20 consisting of static stirring blades 18 of
It is located throughout.
混合容器10の内部には、その混合容器10の軸心と同
一の軸心上を回転させられるローター22が収納され、
ローター22は図示しない駆動装置により回転駆動させ
られる。ローター22の外面にはほぼ半径方向外側に突
出した動撹拌翼24が複数、同一円周上にほぼ等間隔に
配設されるとともに、この同一円周上に配設された複数
の動撹拌翼24からなる動翼列26が混合容器10の内
面に配設された静翼列20と交互になるように複数列(
複数段)にわたって配設されている。動撹拌翼24は例
えば円板を切削して形成した後、ローター22の外周に
圧入や焼ばめ等により固着したり、或いは小型のもので
は動撹拌翼24とローター22とを一体的に形成するこ
とも可能である。A rotor 22 is housed inside the mixing container 10 and is rotated on the same axis as that of the mixing container 10.
The rotor 22 is rotationally driven by a drive device (not shown). On the outer surface of the rotor 22, a plurality of dynamic stirring blades 24 protruding approximately radially outward are arranged on the same circumference at approximately equal intervals, and a plurality of dynamic stirring blades 24 are arranged on the same circumference. 24 rotor blade rows 26 are arranged in multiple rows (
(multiple stages). The dynamic stirring blades 24 are formed by cutting a disc, for example, and then fixed to the outer periphery of the rotor 22 by press fitting, shrink fitting, etc., or in the case of a small size, the dynamic stirring blades 24 and the rotor 22 are integrally formed. It is also possible to do so.
したがって、動翼列26は静翼列20と静翼列20との
間をローター22とともに回転駆動させられる。Therefore, the rotor blade rows 26 are rotationally driven together with the rotor 22 between the stator blade rows 20 .
混合容器10の流入口14側に配設された静撹拌翼18
のひとつには、はぼ半径方向内側に開口する注入口28
が形成されていて、混合容器10の中心部すなわちロー
ター22側に向かって硬化剤が注入されるようにされて
いる。Static stirring blades 18 arranged on the inlet 14 side of the mixing container 10
One of the holes has an inlet 28 that opens radially inward.
is formed so that the curing agent is injected toward the center of the mixing container 10, that is, toward the rotor 22 side.
注入口28の他端は第3図に拡大して示すように、逆止
弁30を一体的に備えた構成とされていて、混合容器1
0内の樹脂が注入口28から逆流しないようにされてい
る。逆止弁30は円錐状の弁体32がロッド33を介し
てばね34の付勢力により弁座36に付勢されていて、
流動体が圧送されてくると、その圧力によってばね34
の付勢力に抗して弁体32が弁座36から押し開かれる
ようにされている。逆止弁30は電磁バルブ38を介し
て硬化剤を圧送させるポンプ40と、溶剤を圧送させる
ポンプ42とに接続されていて、電磁バルブ38により
逆止弁30及び注入口28に圧送させる流動体の[1類
が瞬時に切り換えられるようにされている。The other end of the inlet 28 is integrally equipped with a check valve 30, as shown in an enlarged view in FIG.
0 is prevented from flowing back from the injection port 28. The check valve 30 has a conical valve body 32 urged against a valve seat 36 by the urging force of a spring 34 via a rod 33.
When the fluid is pumped, the pressure causes the spring 34 to
The valve body 32 is pushed open from the valve seat 36 against the urging force of the valve body 32 . The check valve 30 is connected to a pump 40 that pumps a curing agent through an electromagnetic valve 38 and a pump 42 that pumps a solvent. [Category 1] can be switched instantly.
なお、混合容器10の外部には外筒44が取り付けられ
ていて、外筒44と混合容器10との間には冷媒などの
流体が流され、混合容器10内が常に一定温度に保たれ
るようにされている。また、符号46はメカニカルシー
ルであり、供給路12から圧送されてきた樹脂が混合容
器10とローター22のシャフト48との間から漏出し
ないようにされている。Note that an outer cylinder 44 is attached to the outside of the mixing container 10, and a fluid such as a refrigerant is flowed between the outer cylinder 44 and the mixing container 10, so that the inside of the mixing container 10 is always kept at a constant temperature. It's like that. Further, reference numeral 46 is a mechanical seal, which prevents the resin fed under pressure from the supply path 12 from leaking from between the mixing container 10 and the shaft 48 of the rotor 22.
このような構成に係る連続混合装置において、供給路1
2から圧送されてきた樹脂は流入口14から混合容器1
0内へ供給され、順次圧送されてくる樹脂の圧力により
流出口16へと流される。In the continuous mixing device having such a configuration, the supply path 1
The resin pressure-fed from 2 flows into the mixing container 1 from the inlet 14.
The pressure of the resin that is supplied into the resin 0 and successively pumped causes it to flow to the outlet 16.
一方、注入口28からは、先ずポンプ42により電磁バ
ルブ38を介して圧送されてきた溶剤が、逆止弁30の
ばね34の付勢力に抗して弁体32を押し開けて注入さ
れる。溶剤が注入口28から混合容器10内に注入され
た後、電磁バルブ38が瞬時に切り換えられて、溶剤に
替わってポンプ40にて圧送された硬化剤が混合容器1
0内に注入される。硬化剤が注入される時、逆止弁30
の弁体32は溶剤により既に押し開かれているため、必
要量以上の硬化剤が一気に注入されることはなく、安定
した状態で硬化剤が注入される。On the other hand, from the injection port 28, the solvent is first forced by the pump 42 through the electromagnetic valve 38, and is injected by pushing the valve body 32 open against the biasing force of the spring 34 of the check valve 30. After the solvent is injected into the mixing container 10 from the injection port 28, the electromagnetic valve 38 is instantly switched, and the curing agent pumped by the pump 40 instead of the solvent is added to the mixing container 1.
Injected into 0. When the curing agent is injected, the check valve 30
Since the valve body 32 has already been pushed open by the solvent, more hardening agent than the required amount is not injected all at once, and the hardening agent is injected in a stable state.
したがって、先ず注入口28から注入された溶剤は混合
容器10内で樹脂と混合させられ、樹脂の粘性を低下さ
せた状態で流出口16から排出される。次いで溶剤に替
わって注入口28から一定量ずつ注入された硬化剤は樹
脂と撹拌翼18,24により撹拌され、硬化剤が均一に
混合させられた樹脂は徐々に硬化しつつ流出口16から
排出される。Therefore, first, the solvent injected from the injection port 28 is mixed with the resin in the mixing container 10, and is discharged from the outflow port 16 with the viscosity of the resin reduced. Next, instead of the solvent, a fixed amount of hardening agent is injected from the injection port 28 and is stirred with the resin by the stirring blades 18 and 24, and the resin with the hardening agent mixed uniformly is gradually hardened and discharged from the outlet 16. be done.
このように、本発明方法によれば、連続混合装置の始動
時に多量の硬化剤が混合容器内に注入されることはない
ため、混合容器内で硬化の進んだ樹脂が滞留して不具合
を発生させる事態は生じない。As described above, according to the method of the present invention, a large amount of curing agent is not injected into the mixing container when the continuous mixing device is started, so that the hardened resin remains in the mixing container and causes problems. There will be no situation where this happens.
以上本発明の一実施例を詳細に説明したが、本発明は上
述の実施例に限定されるものではなく、その他の態様で
も実施することが可能である。Although one embodiment of the present invention has been described in detail above, the present invention is not limited to the above-described embodiment, and can be implemented in other embodiments.
例えば第4図に示すように、逆止弁50を、硬化剤が導
通される導通路52と、溶剤が導通される導通路54と
、これらの導通路52.54を流れる硬化剤、溶剤の流
れを一方向に規制するチエツキ弁56.58及び弁体3
2によって形成される空室60とを備えるように構成し
ても良い。For example, as shown in FIG. 4, the check valve 50 is connected to a conduit passage 52 through which the curing agent is conducted, a conduit passage 54 through which the solvent is conducted, and the curing agent and solvent flowing through these conduit passages 52 and 54. Check valve 56, 58 and valve body 3 that regulate the flow in one direction
It may also be configured to include a cavity 60 formed by 2.
本例においては、先ずチエツキ弁56を閉じた状態で導
通路54から空室60内に溶剤が充填され、次いでチエ
ツキ弁58を閉じた状態で導通路52から硬化剤が圧送
される。硬化剤の圧力により空室60内の溶剤の圧力は
高められ、弁体32はばね34の付勢力に抗して弁座3
6から押し開けられる。その際、注入口28から混合容
器10内に、先ず空室60内に充填された溶剤が注入さ
れ、続いて硬化剤が導通路52から空室60内を充填し
つつ連続的に注入される。ここで、溶剤の量は逆止弁5
0の弁体32が開弁作動させられる際の圧力変動による
2、激な注入量の増加を許容するものであれば足り、溶
剤が充填される空室60の容積により種々設定すること
が可能である。また、チエツキ弁56.58の構造も種
々設定し得るものである。In this example, a solvent is first filled into the cavity 60 from the conduit 54 with the check valve 56 closed, and then a curing agent is pumped through the conduit 52 with the check valve 58 closed. The pressure of the solvent in the cavity 60 is increased by the pressure of the curing agent, and the valve body 32 resists the biasing force of the spring 34 and presses against the valve seat 3.
It can be pushed open from 6. At this time, the solvent filled in the cavity 60 is first injected into the mixing container 10 from the injection port 28, and then the curing agent is continuously injected from the conduction path 52 while filling the cavity 60. . Here, the amount of solvent is the check valve 5
It is sufficient to allow a drastic increase in the amount of injection due to pressure fluctuations when the valve body 32 is opened, and various settings can be made depending on the volume of the empty space 60 filled with solvent. It is. Furthermore, the structure of the check valves 56 and 58 can be set in various ways.
本例によれば、溶剤の注入量が少なくて済み、溶剤との
混合により廃棄させられる樹脂の量が少なくなる利点が
ある。According to this example, the amount of solvent injected is small, and there is an advantage that the amount of resin that is discarded due to mixing with the solvent is reduced.
以上の実施例において、弁体32の開弁作動を溶剤によ
って行わせる場合を例示したが、溶剤のみならず硬化剤
に溶剤を混合させて硬化剤としての機能を低下させた溶
液や、樹脂と全く反応性又は相容性がない流体であって
も良い、要は、注入量の増加によって樹脂の硬化が促進
されない液体であれば足り、非硬化性液体とはこのよう
に解釈されるべきである。In the above embodiments, the case where the valve opening operation of the valve body 32 is performed using a solvent has been illustrated, but not only a solvent but also a solution in which a curing agent is mixed with a solvent to reduce its function as a curing agent, or a resin may be used. It may be a fluid that is not reactive or compatible at all; in short, it is sufficient that the curing of the resin is not promoted by increasing the amount of injection, and a non-curing liquid should be interpreted in this way. be.
また、上述の連続混合装置は一例であり、スパイラル翼
にて連続的に撹拌しつつ混合させる装置であっても良く
、或いはプロペラや回転盤を利用する装置など、二液を
連続的に混合させる装置に本発明は適用される。Further, the above-mentioned continuous mixing device is just an example, and a device that continuously stirs and mixes the two liquids using a spiral blade may be used, or a device that uses a propeller or a rotary disk to continuously mix two liquids. The present invention is applied to a device.
更に、逆止弁の構造は上述の実施例に限定されるもので
はなく、例えばロンドを用いない形式や、付勢手段とし
てばねの代わりにその他の弾性部材や磁力、圧縮空気な
どを利用した形式などでも良い。Furthermore, the structure of the check valve is not limited to the above-mentioned embodiments; for example, there may be a type that does not use a ronde, or a type that uses other elastic members, magnetic force, compressed air, etc. instead of a spring as a biasing means. etc. is also fine.
その他、逆止弁の弁体あるいはロンドにセンサーを設け
、そのセンサーにより弁体が弁座に着座させられるのを
検出して、逆止弁及び注入口に流される流体が硬化剤か
ら溶剤などに切り換えられるように構成することも可能
である等、本発明はその趣旨を逸脱しない範囲内で、当
業者の知識に基づき種々なる変形、改良、修正を加えた
態様で実施することができる。In addition, a sensor is installed on the valve body or rond of the check valve, and the sensor detects when the valve body is seated on the valve seat, and the fluid flowing into the check valve and inlet is changed from the curing agent to the solvent. The present invention can be implemented with various modifications, improvements, and modifications based on the knowledge of those skilled in the art without departing from the spirit thereof, such as being able to be configured to be switched.
かかる本発明は、二液硬化型樹脂を連続的に混合させる
にあたり、非硬化性の液体にて逆止弁の弁体を押し開け
た後、続いて硬化性の液体を圧送して混合容器内に注入
するようにしたため、弁体の開弁作動時に一気に混合容
器内に流入する液体によって二液硬化型樹脂の硬化が促
進させられることはない、したがって、硬化の進んだ樹
脂が混合容器内に滞留・付着し、その樹脂が細かく切断
されて徐々に混合容器から排出されてくるような事態が
生ずることはない、もって、本発明方法にて連続的に混
合させられた二液硬化型樹脂を用いてフィルム等の樹脂
成形品を成形すれば、表面状態、特性に優れ、更にその
低内部欠陥のない品質の優れた製品を提供することが可
能となる。In the present invention, when continuously mixing two-component curable resins, the valve body of the check valve is pushed open with a non-curing liquid, and then the curable liquid is pumped into the mixing container. Since the liquid is injected into the mixing container at once when the valve body is opened, the curing of the two-component curing resin is not accelerated. There is no possibility that the two-component curing resin that has been mixed continuously by the method of the present invention will be stagnated and adhered, and the resin will not be cut into small pieces and gradually discharged from the mixing container. If a resin molded product such as a film is formed using the resin molded product, it becomes possible to provide a product with excellent surface condition and properties, and furthermore, has a low internal defect and is free from internal defects.
第1図は本発明方法が適用される連続混合装置の一例を
示す要部正面断面図、第2図は第1図の平面断面図、第
3図は第1図の要部拡大断面図である。第4図は本発明
の他の実施例を示す要部拡大断面図である。第5図は従
来の連続混合方法によって生ずる不具合を説明するため
の圧力−時間線図である。
10;混合容器
28;注入口
30.50;逆止弁
32;弁体
34;ばね(付勢手段)
40.42;ポンプ
60;空室
特許出願人 鐘淵化学工業株式会社
第1図
第2図
第3図
第4図
第5図Fig. 1 is a front sectional view of the main part showing an example of a continuous mixing device to which the method of the present invention is applied, Fig. 2 is a plan sectional view of Fig. 1, and Fig. 3 is an enlarged sectional view of the main part of Fig. 1. be. FIG. 4 is an enlarged sectional view of a main part showing another embodiment of the present invention. FIG. 5 is a pressure-time diagram for explaining problems caused by the conventional continuous mixing method. 10; Mixing container 28; Inlet 30.50; Check valve 32; Valve body 34; Spring (biasing means) 40.42; Pump 60; Vacant patent applicant Kanekabuchi Chemical Co., Ltd. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5
Claims (2)
に供給して撹拌するとともに、他の一液を付勢手段にて
付勢された逆止弁の弁体を該他の一液の圧力にて押し開
けて前記混合容器内に注入して、前記一液と他の一液と
を連続的に混合させる方法において、 前記他の一液を注入するにあたり、非硬化性液体にて前
記弁体を押し開けた後、続いて硬化性液体を混合容器内
に注入するようにしたことを特徴とする二液硬化型樹脂
の連続混合方法。(1) One part of the two-component curing resin is continuously supplied and stirred into the mixing container, and the other part is energized by the energizing means and the valve body of the check valve is moved to the other part. In the method of continuously mixing the one liquid and the other liquid by pushing it open under pressure and injecting it into the mixing container, when injecting the other liquid, a non-hardening liquid is added. A continuous mixing method for a two-component curable resin, characterized in that after the valve body is pushed open with a liquid, a curable liquid is subsequently injected into a mixing container.
化剤との混合液又は前記一液と反応しない液体であるこ
とを特徴とする請求項1に記載の二液硬化型樹脂の連続
混合方法。(2) The two-component curable resin according to claim 1, wherein the non-curing liquid is the one-component solvent, a mixture of the solvent and a curing agent, or a liquid that does not react with the one-component. continuous mixing method.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9119988A JP2618257B2 (en) | 1988-04-12 | 1988-04-12 | Continuous mixing method for two-part curable resin |
JP63205304A JPH0253830A (en) | 1988-04-12 | 1988-08-17 | Method for forming polyimide |
EP89106402A EP0337386B1 (en) | 1988-04-12 | 1989-04-11 | Process for continuous mixing of a two-liquid curing type resin |
CA000596311A CA1329874C (en) | 1988-04-12 | 1989-04-11 | Process for continuous mixing of a two-liquid curing type resin |
DE8989106402T DE68900819D1 (en) | 1988-04-12 | 1989-04-11 | METHOD FOR CONTINUOUSLY MIXING A HARDENING RESIN FROM TWO LIQUIDS. |
US07/336,389 US5026820A (en) | 1988-04-12 | 1989-04-11 | Process for continuous mixing of a two-liquid curing type resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9119988A JP2618257B2 (en) | 1988-04-12 | 1988-04-12 | Continuous mixing method for two-part curable resin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01262112A true JPH01262112A (en) | 1989-10-19 |
JP2618257B2 JP2618257B2 (en) | 1997-06-11 |
Family
ID=14019768
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9119988A Expired - Fee Related JP2618257B2 (en) | 1988-04-12 | 1988-04-12 | Continuous mixing method for two-part curable resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2618257B2 (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994020286A2 (en) * | 1993-03-10 | 1994-09-15 | Thomas Christopher Arnott | Improvements relating to syntactic materials |
JP2004238449A (en) * | 2003-02-05 | 2004-08-26 | Konishi Co Ltd | Method for forming epoxy resin-based coating film |
KR100480381B1 (en) * | 2001-11-07 | 2005-03-30 | 이태성 | Colored mid-sole manufacture device |
JP2007125518A (en) * | 2005-11-07 | 2007-05-24 | Chuo Kakoki Kk | Apparatus and method for processing liquid material |
JP2008238005A (en) * | 2007-03-26 | 2008-10-09 | Nagoya Institute Of Technology | Dispersing apparatus for liquid raw material |
US8353651B2 (en) | 2008-09-30 | 2013-01-15 | Henkel Corporation | Dry-to-the-touch-moisture-curable compositions and products made therefrom |
JP2013176732A (en) * | 2012-02-28 | 2013-09-09 | Hosokawa Micron Corp | Powder treatment apparatus |
CN117984481A (en) * | 2024-04-07 | 2024-05-07 | 上海阿波罗机械股份有限公司 | Pouring device and method for spent fuel transportation container |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100855560B1 (en) | 2006-07-14 | 2008-09-01 | 김종선 | Two liquid mixing and discharge apparatus |
-
1988
- 1988-04-12 JP JP9119988A patent/JP2618257B2/en not_active Expired - Fee Related
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994020286A2 (en) * | 1993-03-10 | 1994-09-15 | Thomas Christopher Arnott | Improvements relating to syntactic materials |
WO1994020286A3 (en) * | 1993-03-10 | 1994-10-27 | Thomas Christopher Arnott | Improvements relating to syntactic materials |
KR100480381B1 (en) * | 2001-11-07 | 2005-03-30 | 이태성 | Colored mid-sole manufacture device |
JP2004238449A (en) * | 2003-02-05 | 2004-08-26 | Konishi Co Ltd | Method for forming epoxy resin-based coating film |
JP2007125518A (en) * | 2005-11-07 | 2007-05-24 | Chuo Kakoki Kk | Apparatus and method for processing liquid material |
JP2008238005A (en) * | 2007-03-26 | 2008-10-09 | Nagoya Institute Of Technology | Dispersing apparatus for liquid raw material |
US8353651B2 (en) | 2008-09-30 | 2013-01-15 | Henkel Corporation | Dry-to-the-touch-moisture-curable compositions and products made therefrom |
JP2013176732A (en) * | 2012-02-28 | 2013-09-09 | Hosokawa Micron Corp | Powder treatment apparatus |
CN117984481A (en) * | 2024-04-07 | 2024-05-07 | 上海阿波罗机械股份有限公司 | Pouring device and method for spent fuel transportation container |
CN117984481B (en) * | 2024-04-07 | 2024-06-07 | 上海阿波罗机械股份有限公司 | Pouring device and method for spent fuel transportation container |
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---|---|
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