JP4974160B2 - Continuous degassing deaerator - Google Patents

Continuous degassing deaerator Download PDF

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JP4974160B2
JP4974160B2 JP2007131494A JP2007131494A JP4974160B2 JP 4974160 B2 JP4974160 B2 JP 4974160B2 JP 2007131494 A JP2007131494 A JP 2007131494A JP 2007131494 A JP2007131494 A JP 2007131494A JP 4974160 B2 JP4974160 B2 JP 4974160B2
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liquid
annular groove
side wall
deaeration
continuous
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JP2008284451A (en
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俊二 別惣
晃治 榎本
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Izumi Food Machinery Co Ltd
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Description

本発明は、液中から気体成分を除去する連続脱気脱泡装置に関し、特に、取り出し管との剪断による細かい気泡の発生を防止するとともに、液取り出し管の先端が液中に埋没するような構造をなくし、洗浄等のメンテナンスを容易にすることができる連続脱気脱泡装置に関するものである。   The present invention relates to a continuous deaeration and deaeration apparatus that removes a gas component from a liquid, and in particular, prevents generation of fine bubbles due to shearing with a take-out pipe, and the tip of the liquid take-out pipe is buried in the liquid. The present invention relates to a continuous deaeration and deaeration device that can eliminate the structure and facilitate maintenance such as cleaning.

例えば、高粘度の中に含まれている小さな気泡を脱泡するには長い時間が必要で、大体において、一晩の放置により脱泡していることが多い。
また、短い時間で脱泡しようとする場合はバッチ式の脱泡装置が用いられるが、連続式の大量処理を目指した効率のよい脱泡装置が求められている。
For example, it takes a long time to degas small bubbles contained in a high viscosity, and in general, the bubbles are often degassed by being left overnight.
Moreover, when defoaming is attempted in a short time, a batch type defoaming apparatus is used, but an efficient defoaming apparatus aimed at continuous mass processing is demanded.

連続処理の場合は、真空缶の中で液を回転させ、遠心力にて脱泡する装置があり、例えば、下記の特許文献1に開示される連続脱気脱泡装置が知られている。
この連続脱気脱泡装置は、真空缶の中ある回転体に連続的に液を注入し、液に遠心力をかけることにより脱泡するとともに、回転している液をその内側から取り出し管を通じて取り出す構造となっている。
In the case of continuous processing, there is a device that rotates a liquid in a vacuum can and defoams by centrifugal force. For example, a continuous deaeration and defoaming device disclosed in Patent Document 1 below is known.
This continuous degassing defoaming device continuously injects liquid into a rotating body in a vacuum can and defoams the liquid by applying centrifugal force. At the same time, the rotating liquid is taken out from the inside through a tube. It has a structure to take out.

しかしながら、この従来の連続脱気脱泡装置においては、液の取り出し口が高速で回転する液と接触する形となり、剪断を与えることから液に細かい気泡を発生させるという問題がある。
また、食品の製造においては、取り出し管はその先端が液の中に埋没していることになり、その管の先端部が洗浄できないという問題があった。
特開2000−246008号公報
However, in this conventional continuous deaeration device, there is a problem in that fine liquid bubbles are generated in the liquid because the liquid outlet is in contact with the liquid rotating at a high speed and shear is applied.
Further, in the production of food, the tip of the take-out tube is buried in the liquid, and there is a problem that the tip of the tube cannot be cleaned.
JP 2000-246008 A

本発明は、上記従来の連続脱気脱泡装置が有する問題点に鑑み、取り出し管との剪断による細かい気泡の発生を防止するとともに、液取り出し管の先端が液中に埋没するような構造をなくし、洗浄等のメンテナンスを容易にすることができる連続脱気脱泡装置を提供することを目的とする。   In view of the problems of the conventional continuous deaeration and deaeration apparatus, the present invention has a structure that prevents the generation of fine bubbles due to shearing with the take-out pipe and that the tip of the liquid take-out pipe is buried in the liquid. An object of the present invention is to provide a continuous deaeration and deaeration device that can easily eliminate maintenance such as cleaning.

上記目的を達成するため、本発明の連続脱気脱泡装置は、回転円筒に連続的に液を注入し、液に遠心力をかけることにより脱泡する連続脱気脱泡装置において、回転円筒の内側に液溜まりとなる少なくとも1本の環状溝を形成するとともに、該回転円筒と共に回転する円盤を周縁部が環状溝に没するように設け、環状溝の最上部に回転中心方向に向けて形成した側壁の長さを最下部に回転中心方向に向けて形成した側壁の長さより大きくすることにより、前記最上部の側壁を前記最下部の側壁より高い壁に形成し、前記最上部側壁によって囲まれた回転中心側に円盤上に液を供給する液供給部を設けたことを特徴とする。 In order to achieve the above object, a continuous degassing defoaming apparatus according to the present invention is a continuous degassing defoaming apparatus in which liquid is continuously injected into a rotating cylinder and defoamed by applying centrifugal force to the liquid. And at least one annular groove serving as a liquid pool is formed inside, and a disk that rotates together with the rotating cylinder is provided so that the peripheral edge is submerged in the annular groove, and directed toward the center of rotation at the top of the annular groove. the length of the formed side wall by greater than the length of the side wall which is formed toward the center of rotation to the bottom, the forming a sidewall of the top in the wall have higher than the side wall of the bottom, the top of the A liquid supply unit for supplying liquid onto the disk is provided on the rotation center side surrounded by the side wall.

この場合において、1本の環状溝に複数の円盤を設けることができる。   In this case, a plurality of disks can be provided in one annular groove.

また、環状溝の最下部の側壁から逆漏斗状の回転ガイドを延設することができる。   Moreover, the reverse funnel-shaped rotation guide can be extended from the lowest side wall of the annular groove.

また、環状溝の最下部の側壁の下に、固定側として逆漏斗状の液受けガイドを設置することができる。   Moreover, a reverse funnel-shaped liquid receiving guide can be installed as a fixed side under the lowermost side wall of the annular groove.

本発明の連続脱気脱泡装置によれば、回転円筒に連続的に液を注入し、液に遠心力をかけることにより脱泡する連続脱気脱泡装置において、回転円筒の内側に液溜まりとなる少なくとも1本の環状溝を形成するとともに、該回転円筒と共に回転する円盤を周縁部が環状溝に没するように設け、環状溝の最上部に回転中心方向に向けて形成した側壁の長さを最下部に回転中心方向に向けて形成した側壁の長さより大きくすることにより、前記最上部の側壁を前記最下部の側壁より高い壁に形成し、前記最上部側壁によって囲まれた回転中心側に円盤上に液を供給する液供給部を設けることから、液供給部から供給した液を遠心力により環状溝に移動させ、この環状溝の円盤より上で遠心力による脱泡を行うとともに、円盤を堰板として脱泡された液だけをくぐらせ、最下部の側壁の内側から剪断を与えることなく自然に流下させることができる。
これにより、従来のような取り出し管の剪断による細かい気泡の発生を防止するとともに、取り出し管の先端が液中に埋没するような構造をなくし、洗浄等のメンテナンスを容易にすることができる。
この場合、回転円筒に環状溝と円盤を複数設けることにより、液の脱泡を段階的に連続して行うことができる。
According to the continuous deaeration and deaeration apparatus of the present invention, in the continuous deaeration and deaeration apparatus that continuously injects liquid into the rotating cylinder and defoams by applying centrifugal force to the liquid, the liquid pool is stored inside the rotating cylinder. And at least one annular groove is formed, and a disk that rotates together with the rotating cylinder is provided so that the peripheral edge is submerged in the annular groove, and the length of the side wall formed at the uppermost part of the annular groove toward the rotation center. by larger than the length of the sidewall formed toward the center of rotation at the bottom of the form a side wall of the top in the wall have higher than the bottom of the side wall, said enclosed by the top of the side wall Since a liquid supply unit that supplies liquid on the disk is provided on the rotation center side, the liquid supplied from the liquid supply unit is moved to the annular groove by centrifugal force, and defoamed by centrifugal force above the circular groove disk. And defoaming the disk as a dam plate The liquid alone was preferably under, can be made to flow naturally without giving shear from the inside of the bottom of the side wall.
As a result, it is possible to prevent generation of fine bubbles due to shearing of the take-out pipe as in the prior art, and to eliminate the structure in which the tip of the take-out pipe is buried in the liquid, thereby facilitating maintenance such as cleaning.
In this case, by providing a plurality of annular grooves and disks on the rotating cylinder, the liquid can be degassed continuously in a stepwise manner.

また、1本の環状溝に複数の円盤を設けることにより、液の脱泡を段階的に細密に行うことができる。   Further, by providing a plurality of disks in one annular groove, the liquid can be degassed minutely and stepwise.

また、環状溝の最下部の側壁から逆漏斗状の回転ガイドを延設することにより、遠心力が付与された状態で流下する脱泡後の液を放射状に案内して円滑に流下させることができる。   In addition, by extending a reverse funnel-shaped rotation guide from the lowest side wall of the annular groove, the defoamed liquid that flows down in a state where centrifugal force is applied can be guided radially and flowed smoothly. it can.

また、環状溝の最下部の側壁の下に、固定側として逆漏斗状の液受けガイドを設置することにより、遠心力が付与された状態で流下する脱泡後の液を放射状に案内して円滑に流下させることができる。   In addition, by installing a reverse funnel-shaped liquid receiving guide as a fixed side under the lowermost side wall of the annular groove, the defoamed liquid that flows down with centrifugal force applied is guided radially. It can flow smoothly.

以下、本発明の連続脱気脱泡装置の実施の形態を、図面に基づいて説明する。   DESCRIPTION OF EMBODIMENTS Hereinafter, embodiments of a continuous deaeration and deaeration apparatus according to the present invention will be described with reference to the drawings.

図1に、本発明の連続脱気脱泡装置の一実施例を示す。
この連続脱気脱泡装置は、回転円筒1に連続的に液を注入し、液Aに遠心力をかけることにより脱泡するもので、回転円筒1の内側に液溜まりとなる少なくとも1本の環状溝2を形成するとともに、該回転円筒1と共に回転する円盤3を周縁部が環状溝2に没するように設け、環状溝2の最上部の側壁21を最下部の側壁22より高く形成し、該最上部側壁21の内側に円盤3上に液Aを供給する液供給部4を設けている。
In FIG. 1, one Example of the continuous deaeration deaerator of this invention is shown.
This continuous degassing deaerator is a device that continuously injects liquid into the rotating cylinder 1 and applies a centrifugal force to the liquid A to defoam. An annular groove 2 is formed, and a disk 3 that rotates together with the rotating cylinder 1 is provided so that a peripheral edge is submerged in the annular groove 2, and an uppermost side wall 21 of the annular groove 2 is formed higher than a lowermost side wall 22. The liquid supply part 4 for supplying the liquid A onto the disk 3 is provided inside the uppermost side wall 21.

回転円筒1は、固定側として設置された真空缶5の内部に配設されており、真空缶5を上から貫通する回転軸6に前記円盤3を介して接続されている。
真空缶5は真空ポンプ(図示省略)に接続されており、内部を真空状態にすることにより、遠心力で液Aから分離された泡Bを破砕し消滅させる。
また、真空缶5の内部には、回転円筒1を取り囲むように中間筒7が固設されており、該中間筒7の下部は内側に折り返されて、回転円筒1の下に下向きに広がる逆漏斗状の液受けガイド71を形成している。
The rotating cylinder 1 is disposed inside a vacuum can 5 installed as a fixed side, and is connected via the disk 3 to a rotating shaft 6 penetrating the vacuum can 5 from above.
The vacuum can 5 is connected to a vacuum pump (not shown), and crushes and extinguishes the bubbles B separated from the liquid A by centrifugal force by making the inside vacuum.
In addition, an intermediate cylinder 7 is fixed inside the vacuum can 5 so as to surround the rotating cylinder 1, and a lower portion of the intermediate cylinder 7 is folded inward and spreads downward below the rotating cylinder 1. A funnel-shaped liquid receiving guide 71 is formed.

また、回転円筒1の内側には、図2にも示すように、回転時に液溜まりとなる1又は2本の環状溝2が形成されており、各環状溝2には、回転円筒1と同軸の円盤3がその周縁部を環状溝2の液溜まりに没するように設けられている。
環状溝2の最下部の側壁22からは、下向きに広がる逆漏斗状の回転ガイド23が延設されており、この回転ガイド23の外側には前記した中間筒7の液受けガイド71が配設
されている。
In addition, as shown in FIG. 2, one or two annular grooves 2 that form a liquid pool during rotation are formed inside the rotating cylinder 1, and each annular groove 2 is coaxial with the rotating cylinder 1. The disc 3 is provided so that its peripheral edge is immersed in the liquid pool of the annular groove 2.
A reverse funnel-shaped rotation guide 23 extending downward is extended from the lowermost side wall 22 of the annular groove 2, and the liquid receiving guide 71 of the intermediate cylinder 7 is disposed outside the rotation guide 23. Has been.

円盤3は回転軸6に直接固定されるとともに、連結部材31を介して回転円筒1を回転軸6に連結しており、円盤3と回転円筒1はモータ(図示省略)により高速で一体に回転する。
また、図3に示すように、円盤3を1本の環状溝2に複数設けることも可能であり、これにより、液Aの脱泡を段階的に細密に行うことができる。
なお、円盤3の回転軸6付近には、円盤3の上でも連通して真空が保たれるように通気口(図示省略)が設けられている。
The disk 3 is directly fixed to the rotating shaft 6 and the rotating cylinder 1 is connected to the rotating shaft 6 via a connecting member 31. The disk 3 and the rotating cylinder 1 are integrally rotated at a high speed by a motor (not shown). To do.
Moreover, as shown in FIG. 3, it is also possible to provide a plurality of disks 3 in one annular groove 2, whereby the liquid A can be degassed minutely and stepwise.
Note that a vent (not shown) is provided near the rotary shaft 6 of the disk 3 so as to communicate with the disk 3 and maintain a vacuum.

次に、本実施例の連続脱気脱泡装置の作用を説明する。
高速で回転する回転円筒1に対し、処理液Aは環状溝2の最上部側壁21の内側から円盤3上に供給される。
供給された液Aは遠心力により円盤3上を薄膜状で外側に移動し、環状溝2内で遠心力により脱泡され、脱泡された液Aは外側に、泡Bは内側に分離する。
環状溝2の液Aは高速で回転しており、図1〜図3に示すように、環状溝2の中央に設けられた円盤3を埋没させた形の液面を形成する。
これにより、液面の内側に浮かび上がる泡Bは、堰板となる円盤3をくぐることなくその位置にとどまり、真空缶5の真空により破砕され消滅する。
一方、脱泡後の液Aは円盤3の外側をくぐって下へと移動し、回転円筒1よりオーバーフローし、固定側の液受けガイド71に到達し、その後重力により落下していく。
Next, the operation of the continuous deaeration and deaeration device of this embodiment will be described.
The processing liquid A is supplied onto the disk 3 from the inside of the uppermost side wall 21 of the annular groove 2 with respect to the rotating cylinder 1 that rotates at high speed.
The supplied liquid A moves outward in the form of a thin film on the disk 3 by centrifugal force, is defoamed by centrifugal force in the annular groove 2, and the defoamed liquid A is separated to the outside and the foam B is separated to the inside. .
The liquid A in the annular groove 2 rotates at a high speed, and forms a liquid surface in which a disk 3 provided in the center of the annular groove 2 is buried, as shown in FIGS.
Thereby, the foam B floating inside the liquid surface stays at the position without passing through the disk 3 serving as the weir plate, and is crushed and disappeared by the vacuum of the vacuum can 5.
On the other hand, the liquid A after defoaming moves downward through the outside of the disk 3, overflows from the rotating cylinder 1, reaches the liquid receiving guide 71 on the fixed side, and then drops due to gravity.

この場合、図2に示すように、回転円筒1に環状溝2と円盤3を複数設けた場合は、このような液の脱泡が段階的に連続して行われる。   In this case, as shown in FIG. 2, when a plurality of annular grooves 2 and disks 3 are provided in the rotating cylinder 1, such defoaming of the liquid is continuously performed in a stepwise manner.

また、図3に示すように、1本の環状溝2に複数の円盤3を設けた場合は、1枚目の円盤3をくぐった液Aは、2枚目の円盤3との間でさらに脱泡される。
そして、脱泡後の液Aは2枚目の円盤3をくぐってさらに下へと移動し、液面の内側に浮かび上がる泡Bは、円盤3をくぐることなく真空缶5の真空により破砕され消滅する。
In addition, as shown in FIG. 3, when a plurality of disks 3 are provided in one annular groove 2, the liquid A that has passed through the first disk 3 further passes between the second disk 3. Defoamed.
Then, the liquid A after defoaming moves further down through the second disk 3, and the bubbles B floating inside the liquid surface are crushed by the vacuum of the vacuum can 5 without going through the disk 3. Disappear.

[実験例1]
食品添加物CMC(カルボキシメチルセルロースナトリウム、ニチリン化学工業株式会社キッコレートF−120)を攪拌機付きのタンクにて水に溶解し、原料液を得た。
この原料液をポンプで本実施例の連続脱気脱泡装置に導入し、連続脱気脱泡装置より排出された脱泡後のサンプルを得た。
原料液のサンプル及び脱泡した液のサンプルを、デシケーターにて真空下に置き、体積膨張を計測して脱気率を得た。
その結果を下記表1に示す。
なお、脱気率は、次のように計算した。
脱気率%=(原料の膨張体積−脱泡後の膨張体積)÷原料の膨張体積×100
[Experimental Example 1]
A food additive CMC (sodium carboxymethylcellulose, Nichirin Chemical Industry Co., Ltd., Kikkolate F-120) was dissolved in water in a tank equipped with a stirrer to obtain a raw material solution.
This raw material liquid was introduced into the continuous degassing deaerator of this example with a pump to obtain a sample after defoaming discharged from the continuous degassing deaerator.
A sample of the raw material liquid and a sample of the defoamed liquid were placed under vacuum with a desiccator, and volume expansion was measured to obtain a deaeration rate.
The results are shown in Table 1 below.
The deaeration rate was calculated as follows.
Degassing rate% = (expanded volume of raw material−expanded volume after defoaming) ÷ expanded volume of raw material × 100

Figure 0004974160
Figure 0004974160

かくして、本実施例の連続脱気脱泡装置は、回転円筒1に連続的に液Aを注入し、液Aに遠心力をかけることにより脱泡する連続脱気脱泡装置において、回転円筒1の内側に液溜まりとなる少なくとも1本の環状溝2を形成するとともに、該回転円筒1と共に回転する円盤3を周縁部が環状溝2に没するように設け、環状溝2の最上部の側壁21を最下部の側壁22より高く形成し、該最上部側壁21の内側に円盤3上に液Aを供給する液供給部4を設けることから、液供給部4から供給した液Aを遠心力により環状溝2に移動させ、この環状溝2の円盤3より上で遠心力による脱泡を行うとともに、円盤3を堰板として脱泡された液Aだけをくぐらせ、最下部の側壁22の内側から剪断を与えることなく自然に流下させることができる。
これにより、従来のような取り出し管の剪断による細かい気泡の発生を防止するとともに、取り出し管の先端が液中に埋没するような構造をなくし、洗浄等のメンテナンスを容易にすることができる。
この場合、図2に示すように、回転円筒1に環状溝2と円盤3を複数設けることにより、液Aの脱泡を段階的に連続して行うことができる。
Thus, the continuous degassing deaerator of this embodiment is the continuous degassing deaerator in which the liquid A is continuously injected into the rotating cylinder 1 and defoamed by applying centrifugal force to the liquid A. At least one annular groove 2 that forms a liquid pool, and a disk 3 that rotates together with the rotating cylinder 1 is provided so that the peripheral edge is submerged in the annular groove 2. 21 is formed higher than the lowermost side wall 22, and the liquid supply part 4 for supplying the liquid A is provided on the disk 3 inside the uppermost side wall 21, so that the liquid A supplied from the liquid supply part 4 is subjected to centrifugal force. Is moved to the annular groove 2 and defoamed by centrifugal force above the disk 3 of the annular groove 2, and only the liquid A that has been defoamed is passed through the disk 3 as a weir plate. It can flow down naturally without giving shear from the inside.
As a result, it is possible to prevent generation of fine bubbles due to shearing of the take-out pipe as in the prior art, and to eliminate the structure in which the tip of the take-out pipe is buried in the liquid, thereby facilitating maintenance such as cleaning.
In this case, as shown in FIG. 2, by providing a plurality of annular grooves 2 and disks 3 in the rotating cylinder 1, the liquid A can be degassed continuously in a stepwise manner.

また、図3に示すように、1本の環状溝2に複数の円盤3を設けることにより、液Aの脱泡を段階的に細密に行うことができる。   Further, as shown in FIG. 3, by providing a plurality of disks 3 in one annular groove 2, the defoaming of the liquid A can be performed minutely and stepwise.

また、環状溝2の最下部の側壁22から逆漏斗状の回転ガイド23を延設することにより、遠心力が付与された状態で流下する脱泡後の液Aを放射状に案内して円滑に流下させることができる。
また、環状溝2の最下部の側壁22の下に、固定側として逆漏斗状の液受けガイド71を設置することにより、遠心力が付与された状態で流下する脱泡後の液Aを放射状に案内して円滑に流下させることができる。
Further, by extending a reverse funnel-shaped rotation guide 23 from the lowermost side wall 22 of the annular groove 2, the defoamed liquid A flowing down in a state where centrifugal force is applied is radially guided to smoothly. Can flow down.
Further, by installing a reverse funnel-shaped liquid receiving guide 71 as a fixed side under the lowermost side wall 22 of the annular groove 2, the defoamed liquid A that flows down in a state where centrifugal force is applied is radial. It is possible to smoothly flow down by guiding to.

以上、本発明の連続脱気脱泡装置について、その実施例に基づいて説明したが、本発明は上記実施例に記載した構成に限定されるものではなく、その趣旨を逸脱しない範囲において適宜その構成を変更することができる。   As mentioned above, although the continuous deaeration deaeration apparatus of this invention was demonstrated based on the Example, this invention is not limited to the structure described in the said Example, In the range which does not deviate from the meaning, the The configuration can be changed.

本発明の連続脱気脱泡装置は、取り出し管との剪断による細かい気泡の発生を防止するとともに、液取り出し管の先端が液中に埋没するような構造をなくし、洗浄等のメンテナンスを容易にするという特性を有していることから、例えば、食品工業や薬品工業、化学
工業における粘度品の脱泡の用途に好適に用いることができる。
The continuous deaeration and deaeration device of the present invention prevents the generation of fine bubbles due to shearing with the take-out pipe, and eliminates the structure in which the tip of the liquid take-out pipe is buried in the liquid, facilitating maintenance such as cleaning. For example, it can be suitably used for the defoaming of viscous products in the food industry, the pharmaceutical industry, and the chemical industry.

本発明の連続脱気脱泡装置の第1実施例を示す断面図である。It is sectional drawing which shows 1st Example of the continuous deaeration deaerator of this invention. 同第2実施例を示す断面図である。It is sectional drawing which shows the 2nd Example. 同第3実施例を示す断面図である。It is sectional drawing which shows the 3rd Example.

1 回転円筒
2 環状溝
21 最上部側壁
22 最下部側壁
23 回転ガイド
3 円盤
31 連結部材
4 液供給部
5 真空缶
6 回転軸
7 中間筒
71 液受けガイド
DESCRIPTION OF SYMBOLS 1 Rotating cylinder 2 Annular groove 21 Uppermost side wall 22 Lowermost side wall 23 Rotating guide 3 Disc 31 Connecting member 4 Liquid supply part 5 Vacuum can 6 Rotating shaft 7 Intermediate cylinder 71 Liquid receiving guide

Claims (4)

回転円筒に連続的に液を注入し、液に遠心力をかけることにより脱泡する連続脱気脱泡装置において、回転円筒の内側に液溜まりとなる少なくとも1本の環状溝を形成するとともに、該回転円筒と共に回転する円盤を周縁部が環状溝に没するように設け、環状溝の最上部に回転中心方向に向けて形成した側壁の長さを最下部に回転中心方向に向けて形成した側壁の長さより大きくすることにより、前記最上部の側壁を前記最下部の側壁より高い壁に形成し、前記最上部側壁によって囲まれた回転中心側に円盤上に液を供給する液供給部を設けたことを特徴とする連続脱気脱泡装置。 In the continuous deaeration and deaeration device that continuously injects liquid into the rotating cylinder and defoams by applying centrifugal force to the liquid, and forming at least one annular groove serving as a liquid pool inside the rotating cylinder, A disk that rotates with the rotating cylinder is provided so that the peripheral edge is immersed in the annular groove, and the length of the side wall formed in the uppermost part of the annular groove toward the rotation center is formed in the lowermost part in the direction of the rotation center. by greater than the length of the side wall, the top of the upper portion of the side wall is formed in the wall have higher than the side wall of the bottom, the center of rotation side surrounded by the top of the side wall, solution supplying liquid onto the disk A continuous deaeration and deaeration apparatus comprising a supply unit. 1本の環状溝に複数の円盤を設けたことを特徴とする請求項1記載の連続脱気脱泡装置。   The continuous deaeration apparatus according to claim 1, wherein a plurality of disks are provided in one annular groove. 環状溝の最下部の側壁から逆漏斗状の回転ガイドを延設したことを特徴とする請求項1又は2記載の連続脱気脱泡装置。   The continuous deaeration and deaeration apparatus according to claim 1 or 2, wherein a reverse funnel-shaped rotation guide is extended from a lowermost side wall of the annular groove. 環状溝の最下部の側壁の下に、固定側として逆漏斗状の液受けガイドを設置したことを特徴とする請求項1、2又は3記載の連続脱気脱泡装置。   4. A continuous deaeration / deaeration apparatus according to claim 1, wherein a reverse funnel-shaped liquid receiving guide is provided as a fixed side under the lowermost side wall of the annular groove.
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WO2015027552A1 (en) 2013-09-02 2015-03-05 海斯摩尔生物科技有限公司 Industrial defoaming method for high-viscosity pure chitosan spinning solution
WO2015027553A1 (en) 2013-09-02 2015-03-05 海斯摩尔生物科技有限公司 Industrial deaeration apparatus for high viscosity pure chitosan spinning solution
JP6302321B2 (en) * 2014-03-28 2018-03-28 プライミクス株式会社 Liquid treatment equipment for battery electrode coating production
CN113750576A (en) * 2021-09-14 2021-12-07 柳州市豪杰特化工机械有限责任公司 Centrifugal vacuum defoaming equipment of online continuous processing

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