JPH0947647A - Flow plate rotating type mixing and defoaming device - Google Patents

Flow plate rotating type mixing and defoaming device

Info

Publication number
JPH0947647A
JPH0947647A JP7204896A JP20489695A JPH0947647A JP H0947647 A JPH0947647 A JP H0947647A JP 7204896 A JP7204896 A JP 7204896A JP 20489695 A JP20489695 A JP 20489695A JP H0947647 A JPH0947647 A JP H0947647A
Authority
JP
Japan
Prior art keywords
flow plate
liquid
screw pump
pumping pipe
pumping
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.)
Pending
Application number
JP7204896A
Other languages
Japanese (ja)
Inventor
Toshiaki Ifuku
敏秋 井福
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nikku Industry Co Ltd
Original Assignee
Nikku Industry Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nikku Industry Co Ltd filed Critical Nikku Industry Co Ltd
Priority to JP7204896A priority Critical patent/JPH0947647A/en
Publication of JPH0947647A publication Critical patent/JPH0947647A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/84Venting or degassing ; Removing liquids, e.g. by evaporating components
    • B29B7/845Venting, degassing or removing evaporated components in devices with rotary stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0042Degasification of liquids modifying the liquid flow
    • B01D19/0052Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/02Foam dispersion or prevention
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/45Mixing liquids with liquids; Emulsifying using flow mixing
    • B01F23/451Mixing liquids with liquids; Emulsifying using flow mixing by injecting one liquid into another
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/49Mixing systems, i.e. flow charts or diagrams
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/12Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with single shaft
    • B29B7/16Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with single shaft with paddles or arms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/22Component parts, details or accessories; Auxiliary operations
    • B29B7/24Component parts, details or accessories; Auxiliary operations for feeding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/86Component parts, details or accessories; Auxiliary operations for working at sub- or superatmospheric pressure

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Dispersion Chemistry (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

PROBLEM TO BE SOLVED: To improve the film effect and increase the deaeration chance for vacuum defoaming and also improve the agitation effect for a lower liquid reservoir and also improve the pumping-up capability by a screw pump in a pumping-up tube. SOLUTION: A screw pump 7 is installed in a pumping-up tube 6 set vertically on the center of a vacuum tank 15, and an umbrella-shaped flow plate 3 is fixed on the periphery of an upper end section of the pumping-up tube 6, and the pumping-up tube 6 is rotated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、合成樹脂、セラミ
ックなどの液状の高粘度物質の混合ならびに脱泡を行う
流液板回転式混合脱泡装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a flow plate rotating type mixing and defoaming device for mixing and defoaming liquid high viscosity substances such as synthetic resin and ceramics.

【0002】[0002]

【従来の技術】高粘度物質、例えば合成樹脂、セラミッ
クなどを加工する際には、その工程で合成樹脂の注型を
考えると、強力な混合並びにガス抜きが行われなければ
ならないことが多く、特に合成樹脂の例では、混合作用
はしばしば充填材を均一に合成樹脂のなかで分配するた
めに役立つ。また、調整される混合物の粘度は、比較的
広い範囲のものまで対応できるよう詳細設計できるた
め、利用範囲は広い。
2. Description of the Related Art When processing a high-viscosity substance such as a synthetic resin or a ceramic, considering the casting of the synthetic resin in the process, it is often necessary to perform strong mixing and degassing. Especially in the case of synthetic resins, the mixing action often serves to evenly distribute the filler in the synthetic resin. Further, the viscosity of the mixture to be adjusted can be designed in detail so as to correspond to a relatively wide range, so that the application range is wide.

【0003】そこで、従来における真空式脱泡装置で
は、真空槽の中心に立設した揚液管の上端部に、周囲の
真空槽側壁に向って傘状に広がる流液板が一段だけ設け
られているのが通常であり、薄膜状脱泡に必要な薄膜流
液形成時間が充分にとれないため、繰り返し揚液を行わ
ざるを得ないのが実状であった。従って、結果的に脱泡
に長時間かかり、能率が悪く、これの改善が必要となっ
ており、また、揚液管の下端部からスクリューポンプで
吸引し、揚液管へ送り込む力が弱く、液の粘度が低いと
必要高さまで揚液できないという問題もあった。
Therefore, in the conventional vacuum defoaming apparatus, only one step of the liquid flow plate is provided at the upper end of the pumping pipe which is erected at the center of the vacuum chamber and which spreads like an umbrella toward the side wall of the surrounding vacuum chamber. In general, the thin film flow forming time required for thin film defoaming cannot be taken sufficiently, so that it is the actual situation that pumping must be repeated. Therefore, as a result, it takes a long time for defoaming, the efficiency is poor, and improvement of this is required, and the force of sucking with a screw pump from the lower end of the pump and pumping it into the pump is weak. There is also a problem that if the viscosity of the liquid is low, the liquid cannot be pumped up to the required height.

【0004】[0004]

【発明が解決しようとする課題】本発明は、前記従来の
問題点を解決するためになされたものであり、薄膜効果
を上げ、真空脱泡のための脱気チャンスを増やすと同時
に、下部液溜の攪拌効果の改善と、揚液管内でのスクリ
ューポンプによる揚液能力の向上をはかりうる流液板回
転式混合脱泡装置を提供することを目的としている。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems of the prior art, and enhances the thin film effect and increases the degassing chance for vacuum degassing, and at the same time, lower liquid. It is an object of the present invention to provide a flow plate rotating type mixing and defoaming device capable of improving the stirring effect of a reservoir and improving the pumping capacity by a screw pump in a pump.

【0005】[0005]

【課題を解決するための手段】本発明は、真空槽の中心
に垂直に設けた円筒状の揚液管内にスクリューポンプを
設け、かつ揚液管上端部の周囲に傘状の流液板を固定す
ると共に、流液板を固定した揚液管を回転させる回転駆
動機構等を設けた流液板回転式混合脱泡装置からなり、
液が揚液管の上端部へ到達後は周囲の真空槽側壁に向っ
て傘状に広がる流液板を拡散しながらオーバーフローに
より流下し、傘状の流液板が回転していることによっ
て、液の薄膜化が促進され、脱泡効率を高めることがで
きる。
SUMMARY OF THE INVENTION According to the present invention, a screw pump is provided in a cylindrical pumping pipe provided vertically to the center of a vacuum chamber, and an umbrella-shaped flow plate is provided around the upper end of the pumping pipe. It consists of a flow plate rotating type mixing and defoaming device that is provided with a rotation drive mechanism that rotates the pumping pipe that fixes the flow plate.
After the liquid reaches the upper end of the pumping pipe, it flows down by overflow while diffusing the flowing liquid plate spreading like an umbrella toward the surrounding vacuum chamber side wall, and by the rotating umbrella-like flowing liquid plate, The thinning of the liquid is promoted and the defoaming efficiency can be enhanced.

【0006】また、上記の装置において、スクリューポ
ンプの回転方向が揚液管の回転方向と反対方向になって
いることが、その揚液能力を上昇させる上で好ましく、
さらに、揚液管の下端部に補助攪拌羽根を取り付けた
り、さらにはスクリューポンプの下部に攪拌ブレードを
取り付けることが、それぞれ反対方向に回転する補助攪
拌羽根と攪拌ブレードとの相互作用により、液溜での攪
拌効果と、強制的に揚液管へ液を導入させることができ
るので望ましい。
Further, in the above apparatus, it is preferable that the rotation direction of the screw pump is opposite to the rotation direction of the pumping pipe in order to increase the pumping capacity,
In addition, an auxiliary stirring blade may be attached to the lower end of the pumping pipe, or a stirring blade may be attached to the lower part of the screw pump. It is desirable because the stirring effect in (1) and the liquid can be forcibly introduced into the pumping pipe.

【0007】[0007]

【発明の実施の形態】以下図面を参照して本発明の実施
例を説明するが、図1は本発明の流液板回転式混合脱泡
装置の一実施例に係る側断面図で、図2は図1の装置の
傘状の流液板上での液の挙動と流液板の回転方向とを示
す要部平面図であり、そして図3は図1の装置の流液板
上をオーバーフローにて液が流下する構造を示す要部側
断面図である。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a side sectional view showing an embodiment of a flow plate rotating type mixing and defoaming apparatus of the present invention. 2 is a plan view of the essential parts showing the behavior of the liquid on the umbrella-shaped flow plate of the apparatus of FIG. 1 and the rotating direction of the flow plate, and FIG. 3 is a plan view of the flow plate of the apparatus of FIG. It is a principal part side sectional view which shows the structure which the liquid flows down by overflow.

【0008】まず、図1におけるこの装置は、原料投入
口13を上部に有する合成樹脂の混合脱泡を行う真空槽
15の中心に垂直に設けた円筒状の揚液管6内にスクリ
ューポンプ7を設け、さらにこの揚液管6の上端部の周
囲に傘状の流液板3を固定している。また、上記流液板
3を固定した揚液管6を、モータ1で回転させる回転駆
動機構2及び8を設けている。
First, in the apparatus shown in FIG. 1, a screw pump 7 is provided in a cylindrical pumping pipe 6 provided vertically to the center of a vacuum tank 15 for mixing and defoaming a synthetic resin having a raw material inlet 13 in the upper portion. And an umbrella-shaped flow plate 3 is fixed around the upper end of the pumping pipe 6. Further, rotary drive mechanisms 2 and 8 for rotating the pumping pipe 6 to which the flow plate 3 is fixed by the motor 1 are provided.

【0009】さらに、この回転駆動機構2及び8を介し
てスクリューポンプ7の図3に示す回転方向Sを、揚液
管6の回転方向Rと反対方向になるようにしている。ま
た、揚液管6の下端部には補助攪拌羽根9が取り付けら
れており、これは揚液管6と共に回転方向Rに回転し、
一方、スクリューポンプ7の下部には攪拌ブレード10
が取り付けられており、これはスクリューポンプ7と共
に回転方向Sに回転することになる。
Further, the rotational direction S of the screw pump 7 shown in FIG. 3 is set to be opposite to the rotational direction R of the pumping pipe 6 via the rotary drive mechanisms 2 and 8. Further, an auxiliary stirring blade 9 is attached to the lower end portion of the pumping pipe 6, which rotates in the rotation direction R together with the pumping pipe 6,
On the other hand, a stirring blade 10 is provided below the screw pump 7.
Is attached, which rotates in the rotation direction S together with the screw pump 7.

【0010】次に、この実施例の装置の真空槽15の原
料投入口13から原料の液を投入後、真空槽15を真空
にし、スクリューポンプ7をモータ1により速度コント
ロール可能な回転駆動機構2を介して回転させること
で、液を揚液管6内を上昇させ、傘状の流液体3上を真
空槽15の側壁に向かってオーバーフローにより流下さ
せる。その際、スクリューポンプ7と傘状の流液板3と
はそれぞれ逆回転させているので、揚液効率を高め、流
液板3上での薄膜形成を容易かつ確実に可能にし、脱泡
効率を高めることになる。
Next, after the raw material liquid is introduced from the raw material inlet 13 of the vacuum tank 15 of the apparatus of this embodiment, the vacuum tank 15 is evacuated and the screw pump 7 is rotated by the motor 1 to rotate the rotary drive mechanism 2. The liquid is raised in the pumping pipe 6 by rotating the liquid through the flow path, and is made to flow down on the umbrella-shaped flowing liquid 3 toward the side wall of the vacuum tank 15 by overflow. At that time, since the screw pump 7 and the umbrella-shaped flow plate 3 are rotated in reverse, respectively, the pumping efficiency is increased, and a thin film can be easily and surely formed on the flow plate 3, and the defoaming efficiency is improved. Will be increased.

【0011】上記スクリューポンプ7と揚液管6とを逆
方向に回転させるためには、図1及び図3に示すよう
に、モータ1による回転を回転駆動機構2及び8を介し
て伝達することにより行なっている。また、真空槽15
内の下部に溜まった液は、スクリューポンプ7に取り付
けられた攪拌ブレード10がスクリューポンプ7と同時
に回転し、一方、揚液管6の下端部に取り付けられた補
助攪拌羽根9がその逆方向に回転するので、液が効果的
に攪拌混合され、脱泡作用を助けることになると共に、
スクリューポンプ7への液の導入を容易にしている。
In order to rotate the screw pump 7 and the pumping pipe 6 in opposite directions, as shown in FIGS. 1 and 3, the rotation by the motor 1 is transmitted through the rotation drive mechanisms 2 and 8. It is done by. Also, the vacuum tank 15
For the liquid collected in the lower part of the inside, the stirring blade 10 attached to the screw pump 7 rotates simultaneously with the screw pump 7, while the auxiliary stirring blade 9 attached to the lower end of the pumping pipe 6 moves in the opposite direction. As it rotates, the liquid is effectively stirred and mixed, which helps the defoaming action and
The liquid is easily introduced into the screw pump 7.

【0012】さらに、図2において、回転する傘状の流
液板3上の液の挙動を見てみると、流液板3の矢印Rで
示す回転によって、流液板3上の液は矢印Fのように速
度を上げて旋回しながら流下していくことが理解でき
る。これは真空下での液の薄膜化を助けることになり、
実質的に流液板3の面積を大きくしたことと同じ効果が
得られることになり、非常に効率の良い脱泡が可能とな
る。なお、混合及び脱泡後の液は、真空槽15の下部に
設けられた排出口14から排出弁16を介して外部に排
出される。
Further, referring to the behavior of the liquid on the rotating umbrella-shaped flow plate 3 in FIG. 2, the liquid on the flow plate 3 is indicated by the arrow as a result of the rotation of the flow plate 3 indicated by the arrow R. It can be understood that the speed is increased like F to make a turn while flowing down. This will help thin the liquid under vacuum,
Substantially the same effect as that of increasing the area of the flow plate 3 can be obtained, and very efficient defoaming is possible. The liquid after mixing and defoaming is discharged to the outside from the discharge port 14 provided in the lower portion of the vacuum chamber 15 via the discharge valve 16.

【0013】[0013]

【発明の効果】以上に説明したごとく、本発明の流液板
回転式混合脱泡装置によれば下記の効果が得られる。 1.従来の傘状の流液板一枚だけの装置においては不充
分であった薄膜形成が、傘状の流液板を回転させること
により、薄膜形成を容易にし、流液板上の液の流下速度
を上げさせることができ、効率の良い脱泡効果が得られ
る。 2.揚液管の下部に取り付けられた補助攪拌羽根により
液の攪拌効果を向上すると共に、スクリューポンプへの
液の吸引効果を向上し、かつ揚液高さも大きくできる。 3.さらにスクリューポンプに取り付けられた攪拌ブレ
ードが上記補助攪拌羽根と逆方向に回転することにより
液の混合及び脱泡効果を著しく向上することができる。
As described above, the following effects can be obtained by the flow plate rotating type mixing and defoaming apparatus of the present invention. 1. The thin film formation, which was insufficient in the conventional device with only one umbrella-shaped flow plate, facilitates thin film formation by rotating the umbrella-shaped flow plate, and allows the liquid to flow down on the flow plate. The speed can be increased and an efficient defoaming effect can be obtained. 2. The auxiliary stirring blade attached to the lower part of the pump can improve the effect of stirring the liquid, improve the effect of sucking the liquid into the screw pump, and increase the height of the pump. 3. Further, the stirring blade attached to the screw pump rotates in the direction opposite to that of the auxiliary stirring blade, whereby the liquid mixing and defoaming effects can be remarkably improved.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の流液回転式混合脱泡装置の一実施例に
係る側断面図である。
FIG. 1 is a side cross-sectional view according to an embodiment of a flowing liquid rotary type mixing and defoaming apparatus of the present invention.

【図2】図1の装置の流液板上での液の挙動と流液板の
回転方向とを示す要部平面図である。
FIG. 2 is a plan view of relevant parts showing the behavior of the liquid on the flow plate and the rotation direction of the flow plate of the apparatus of FIG.

【図3】図1の装置の流液板上をオーバーフローにて液
が流下する構造を示す要部側断面図である。
FIG. 3 is a side sectional view of an essential part showing a structure in which a liquid flows down on a liquid flow plate of the apparatus of FIG. 1 by overflow.

【符号の説明】[Explanation of symbols]

3 流液板 6 揚液管 7 スクリューポンプ 9 補助攪拌羽根 10 攪拌ブレード 15 真空槽 R 回転方向 S 回転方向 3 Flow Plate 6 Pumping Pipe 7 Screw Pump 9 Auxiliary Stirring Blade 10 Stirring Blade 15 Vacuum Tank R Rotating Direction S Rotating Direction

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 真空槽の中心に垂直に設けた円筒状の揚
液管内にスクリューポンプを設け、かつ揚液管上端部の
周囲に傘状の流液板を固定すると共に、揚液管を回転さ
せる流液板回転式混合脱泡装置。
1. A screw pump is provided in a cylindrical pumping pipe provided vertically to the center of a vacuum chamber, and an umbrella-shaped flow plate is fixed around the upper end of the pumping pipe, and the pumping pipe is provided. Rotating flow plate rotating type mixing and defoaming device.
【請求項2】 スクリューポンプの回転方向が揚液管の
回転方向と反対方向になっている請求項1記載の流液板
回転式混合脱泡装置。
2. The flow plate rotating type mixing and defoaming device according to claim 1, wherein the rotation direction of the screw pump is opposite to the rotation direction of the pumping pipe.
【請求項3】 揚液管の下端部に補助攪拌羽根を取り付
けた請求項1または2記載の流液板回転式混合脱泡装
置。
3. The flow plate rotating type mixing and defoaming device according to claim 1, wherein an auxiliary stirring blade is attached to the lower end of the pumping pipe.
【請求項4】 スクリューポンプの下部に攪拌ブレード
を取り付けた請求項1、2または3記載の流液板回転式
混合脱泡装置。
4. The flow plate rotating type mixing and defoaming device according to claim 1, 2 or 3, wherein a stirring blade is attached to the lower part of the screw pump.
JP7204896A 1995-08-10 1995-08-10 Flow plate rotating type mixing and defoaming device Pending JPH0947647A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7204896A JPH0947647A (en) 1995-08-10 1995-08-10 Flow plate rotating type mixing and defoaming device

Applications Claiming Priority (1)

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Cited By (17)

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JP2002028466A (en) * 2000-05-10 2002-01-29 Mitsubishi Chemicals Corp Granular particles treatment device and producing method for coated fertilizer
US6345908B1 (en) 1999-04-29 2002-02-12 Micafil Ag Device for mixing and degassing a flowable mass
KR100798002B1 (en) * 2001-10-12 2008-01-28 주식회사 포스코 An apparatus of removing bubbles generated in the storage tank for alkalic solution
KR100951239B1 (en) * 2002-09-10 2010-04-05 주식회사 포스코 A plating solution mixing tank
JP2011131130A (en) * 2009-12-22 2011-07-07 Ihi Corp Stirrer
JP2014036925A (en) * 2012-08-15 2014-02-27 Denki Kagaku Kogyo Kk Agitator and manufacturing method of small size plate member
CN104174324A (en) * 2014-09-17 2014-12-03 蓝星有机硅(上海)有限公司 Combined type stirring device
CN104828963A (en) * 2015-04-29 2015-08-12 四川和鼎环保工程有限责任公司 Elevating defoaming aeration tank
JP2016536481A (en) * 2013-09-02 2016-11-24 海斯摩爾生物科技有限公司 High-viscosity pure chitosan spinning solution combined air bubble removal method
JP2016536482A (en) * 2013-09-02 2016-11-24 海斯摩爾生物科技有限公司 High viscosity pure chitosan spinning solution bubble removal device
CN111633829A (en) * 2020-06-05 2020-09-08 芜湖瑞洲新材料有限公司 Material mediation belt cleaning device is mixed to formula of giving tank car each other
CN111701282A (en) * 2020-06-27 2020-09-25 台州弘霖工业设计有限公司 Spiral defoamer
CN112656013A (en) * 2021-01-15 2021-04-16 福建天马科技集团股份有限公司 Agitated vessel is used in aquatic products feed production
CN113415009A (en) * 2021-07-13 2021-09-21 湖北襄亿新新材料科技有限公司 Preparation method of degradable environment-friendly tableware
WO2022223349A1 (en) * 2021-04-22 2022-10-27 ventUP GmbH Processing unit for viscous material
IT202100012026A1 (en) * 2021-05-11 2022-11-11 Vb Soluzioni E Tecnologie S R L CENTRIFUGATION STATION FOR EXTRUSION PLANTS
CN117225017A (en) * 2023-11-14 2023-12-15 内蒙古图微新材料科技有限公司 Preparation device and preparation method of polysulfonate flat ultrafiltration membrane

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6345908B1 (en) 1999-04-29 2002-02-12 Micafil Ag Device for mixing and degassing a flowable mass
JP2002028466A (en) * 2000-05-10 2002-01-29 Mitsubishi Chemicals Corp Granular particles treatment device and producing method for coated fertilizer
KR100798002B1 (en) * 2001-10-12 2008-01-28 주식회사 포스코 An apparatus of removing bubbles generated in the storage tank for alkalic solution
KR100951239B1 (en) * 2002-09-10 2010-04-05 주식회사 포스코 A plating solution mixing tank
JP2011131130A (en) * 2009-12-22 2011-07-07 Ihi Corp Stirrer
JP2014036925A (en) * 2012-08-15 2014-02-27 Denki Kagaku Kogyo Kk Agitator and manufacturing method of small size plate member
JP2016536481A (en) * 2013-09-02 2016-11-24 海斯摩爾生物科技有限公司 High-viscosity pure chitosan spinning solution combined air bubble removal method
JP2016536482A (en) * 2013-09-02 2016-11-24 海斯摩爾生物科技有限公司 High viscosity pure chitosan spinning solution bubble removal device
CN104174324A (en) * 2014-09-17 2014-12-03 蓝星有机硅(上海)有限公司 Combined type stirring device
CN104828963A (en) * 2015-04-29 2015-08-12 四川和鼎环保工程有限责任公司 Elevating defoaming aeration tank
CN111633829A (en) * 2020-06-05 2020-09-08 芜湖瑞洲新材料有限公司 Material mediation belt cleaning device is mixed to formula of giving tank car each other
CN111701282A (en) * 2020-06-27 2020-09-25 台州弘霖工业设计有限公司 Spiral defoamer
CN111701282B (en) * 2020-06-27 2022-08-30 台州弘霖工业设计有限公司 Spiral defoamer
CN112656013A (en) * 2021-01-15 2021-04-16 福建天马科技集团股份有限公司 Agitated vessel is used in aquatic products feed production
CN112656013B (en) * 2021-01-15 2022-07-26 福建天马科技集团股份有限公司 Agitated vessel for aquatic products feed production
WO2022223349A1 (en) * 2021-04-22 2022-10-27 ventUP GmbH Processing unit for viscous material
IT202100012026A1 (en) * 2021-05-11 2022-11-11 Vb Soluzioni E Tecnologie S R L CENTRIFUGATION STATION FOR EXTRUSION PLANTS
WO2022238740A1 (en) * 2021-05-11 2022-11-17 Vb Soluzioni E Tecnologie S.R.L. Centrifugation station for extrusion plants
CN113415009A (en) * 2021-07-13 2021-09-21 湖北襄亿新新材料科技有限公司 Preparation method of degradable environment-friendly tableware
CN113415009B (en) * 2021-07-13 2022-06-17 湖北襄亿新新材料科技有限公司 Preparation method of degradable environment-friendly tableware
CN117225017A (en) * 2023-11-14 2023-12-15 内蒙古图微新材料科技有限公司 Preparation device and preparation method of polysulfonate flat ultrafiltration membrane
CN117225017B (en) * 2023-11-14 2024-01-30 内蒙古图微新材料科技有限公司 Preparation device and preparation method of polysulfonate flat ultrafiltration membrane

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