JPH0213042Y2 - - Google Patents

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Publication number
JPH0213042Y2
JPH0213042Y2 JP1984057262U JP5726284U JPH0213042Y2 JP H0213042 Y2 JPH0213042 Y2 JP H0213042Y2 JP 1984057262 U JP1984057262 U JP 1984057262U JP 5726284 U JP5726284 U JP 5726284U JP H0213042 Y2 JPH0213042 Y2 JP H0213042Y2
Authority
JP
Japan
Prior art keywords
container
filling
vacuum
viscous
viscous material
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
Application number
JP1984057262U
Other languages
Japanese (ja)
Other versions
JPS60171514U (en
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 filed Critical
Priority to JP5726284U priority Critical patent/JPS60171514U/en
Publication of JPS60171514U publication Critical patent/JPS60171514U/en
Application granted granted Critical
Publication of JPH0213042Y2 publication Critical patent/JPH0213042Y2/ja
Granted legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は粘体の脱泡容器に関し、特に高粘性の
粘体を小容器中に気泡を含まないように精度よく
充填するに適する粘体用充填器に用いる脱泡容器
を提供するものである。
[Detailed description of the invention] The present invention relates to a defoaming container for viscous material, and in particular, provides a defoaming container for use in a viscous filling device, which is suitable for filling highly viscous viscous materials into small containers with high precision without containing air bubbles. It is something to do.

従来、1万乃至数百万センチポイズ(C,P)
の高粘性の粘体を小売り用などの小容器(充填容
器)に充填するため、例えばピストンとバルブを
組合せたり、ピストンとバルブを兼用した方式
(ロータリーピストン方式)の充填器を用いて一
定容量の粘体を充填することや、計量計の上部に
設けた充填容器中に重量を測定しつつ粘体を滴下
する方法が行なわれている。いずれの方法におい
ても一般に高粘性の粘体を充填する場合、一定量
を精度よく且つ気泡を含まぬように充填すること
が商品価値を高める意味で重要である。特に充填
容器中の粘体に気泡を含まぬようにすることは大
切である。従来、粘体中の気泡を除去(脱泡)す
る方法として、充填器中を真空状態にした後撹拌
することが一般的である。しかしながら、真空下
で単に撹拌を行いつつ粘体を充填するだけでは、
高粘性の粘体中に存在する気泡を充分に取り除く
ことが困難であつた。
Conventionally, 10,000 to several million centipoise (C, P)
In order to fill small containers (filling containers) such as those for retail use with highly viscous viscous substances, for example, a filling device that combines a piston and a valve, or a system that combines a piston and a valve (rotary piston system) is used to fill a fixed volume of viscous material. Methods include filling the container with a viscous material, and dropping the viscous material into a filling container provided at the top of a weighing scale while measuring the weight. In either method, when filling a highly viscous substance, it is important to fill a certain amount accurately and without bubbles in order to increase the commercial value. It is particularly important to ensure that the viscous material in the filled container does not contain air bubbles. Conventionally, as a method for removing air bubbles in a viscous material (defoaming), it is common to create a vacuum state in a filling device and then stir the material. However, simply filling the viscous material while stirring under vacuum will not work.
It was difficult to sufficiently remove air bubbles present in the highly viscous viscous material.

本考案者等は、上記問題に対して特に真空下で
の粘体における脱泡効果について鋭意検討した結
果、容器内部における全ての粘体が液面近くまで
均一にもち上がるような粘体の流れを上下させる
ような撹拌を行うことにより上記問題が解決出来
ることを見出し、本考案を提案するに至つた。
In response to the above problem, the inventors of the present invention have carefully studied the defoaming effect of viscous material under vacuum, and have determined that the flow of the viscous material should be raised and lowered so that all the viscous material inside the container rises uniformly to near the liquid surface. The inventors discovered that the above-mentioned problems could be solved by performing such stirring, and came to propose the present invention.

即ち、本考案は真空容器内に回転軸が回転しな
がら上下動する構造の撹拌機が付設された粘体の
脱泡容器である。
That is, the present invention is a viscous defoaming container in which a stirrer having a rotating shaft that moves up and down while rotating is attached inside the vacuum container.

以下、本考案を図面に基づき詳細に説明する。 Hereinafter, the present invention will be explained in detail based on the drawings.

第1図は、本考案の粘体の脱泡容器の代表的1
例を示す概略図である。即ち、本考案の脱泡容器
は、真空容器1と該容器1内の粘体2を撹拌する
ための特定構造の撹拌機3よりなる。本考案の容
器は、第2図に示すように一般に粘体充填器とし
て好ましく用いられ、この場合真空容器1には粘
体2の取出口4及び該容器1内を吸引する真空手
段5に接続する配管が付設される。このような脱
泡容器を用いた充填器では最初に真空容器1に接
続する真空ポンプ等の真空手段5により、真空容
器1内を真空状態にした後、撹拌機3を作動さ
せ、その後、充填容器を取出口4の下部に設置し
た状態で取出口4の下部のバルブ6を開くこと
で、一定量の粘体が充填される。
Figure 1 shows a typical viscous defoaming container of the present invention.
FIG. 2 is a schematic diagram illustrating an example. That is, the defoaming container of the present invention comprises a vacuum container 1 and a stirrer 3 having a specific structure for stirring the viscous material 2 within the container 1. The container of the present invention is generally preferably used as a viscous filling device, as shown in FIG. is attached. In a filling device using such a defoaming container, first, the inside of the vacuum container 1 is brought into a vacuum state by a vacuum means 5 such as a vacuum pump connected to the vacuum container 1, and then the stirrer 3 is operated, and then the filling is performed. By opening the valve 6 at the bottom of the outlet 4 with the container installed at the bottom of the outlet 4, a certain amount of viscous material is filled.

本考案の特徴は前述の如く、特定な構造の撹拌
機3、即ち、真空下で上下運動と回転運動をする
回転軸(撹拌軸)7を有する撹拌機を用いること
により、真空容器1内の粘体2の流れを上下動さ
せ、脱泡効果を高めることである。
As mentioned above, the feature of the present invention is that by using a stirrer 3 having a specific structure, that is, a stirrer having a rotating shaft (stirring shaft) 7 that moves up and down and rotates under vacuum, The aim is to move the flow of the viscous material 2 up and down to enhance the defoaming effect.

従来、例えば第3図に示すように、先端に螺旋
状の羽根8が接続された回転軸7、或いは第4図
及び第5図(第4図の平面図を示す)のように、
先端に板状の羽根8が斜め下方に向けて接続され
た回転軸7、更に、第6図、第7図(第6図の平
面図)に示すように、斜め下方且つ真空容器1の
内壁に沿つて曲つた形状の羽根8が接続された回
転軸7を有する撹拌機3により粘体2を撹拌する
方法がある。特に第5図に示すような羽根8を有
する撹拌機では粘体2にある程度の上昇流を付与
することもできるが、本考案の撹拌効果は、単に
回転軸7を一定の位置に設置して回転させただけ
では得られないものである。また、超高速度で撹
拌することも考えられるが、該方法では回転軸7
や羽根8の摩耗が激しく且つ高トルクのモーター
が必要である等、実用的でない。
Conventionally, for example, as shown in FIG. 3, a rotating shaft 7 with a spiral blade 8 connected to the tip, or as shown in FIGS. 4 and 5 (a plan view of FIG. 4),
A rotary shaft 7 to which a plate-like blade 8 is connected diagonally downward at the tip thereof, and further, as shown in FIGS. There is a method in which the viscous material 2 is stirred by a stirrer 3 having a rotating shaft 7 to which blades 8 curved along the axis are connected. In particular, with a stirrer having blades 8 as shown in FIG. 5, it is possible to give a certain degree of upward flow to the viscous material 2, but the stirring effect of the present invention is achieved simply by installing the rotating shaft 7 at a fixed position and rotating it. You can't get it just by letting it happen. It is also possible to stir at an ultra-high speed, but in this method, the rotating shaft 7
It is not practical because the blades 8 are severely worn and a high-torque motor is required.

これに対して、本考案は回転軸7が回転しなが
ら上下動する構造の撹拌機3を用いるため、上記
したような問題を全て解決でき、しかも真空下で
の脱泡効果が極めて高くなる。
In contrast, the present invention uses the stirrer 3 having a structure in which the rotary shaft 7 moves up and down while rotating, so all of the above-mentioned problems can be solved, and the degassing effect under vacuum is extremely high.

回転軸7を上下動させる方法は公知の方法が特
に制限なく用いられる。例えば、第2図に示すよ
うに天井に接置されたシリンダー9に撹拌機3本
体を接続させ、シリンダー9の上下動により撹拌
機3を上下させる方法、或いは、第1図に示すよ
うに回転軸7の中間部にネジ切り部10を設け、
撹拌機3の回転方向を変化させることにより回転
軸7の高さ(上下動)及び回転方向を変化させる
方法、更に複数のモーターを用いて、回転軸7を
上下及び回転運動させる方法等がある。
Any known method can be used without particular limitation as to the method of vertically moving the rotating shaft 7. For example, as shown in Fig. 2, the main body of the agitator 3 is connected to a cylinder 9 placed on the ceiling, and the agitator 3 is moved up and down by the vertical movement of the cylinder 9, or as shown in Fig. 1, it is rotated. A threaded part 10 is provided in the middle part of the shaft 7,
There are methods of changing the height (vertical movement) and rotational direction of the rotating shaft 7 by changing the rotating direction of the agitator 3, and methods of vertically and rotationally moving the rotating shaft 7 using a plurality of motors. .

本考案に用いられる真空容器1の形状は特に制
限されないが、一般には第8図に示すような底が
コーン状で他の部分が円筒状の容器が、回転軸7
の回転が容易で粘体2の流れも円滑になるため好
ましく用いられる。
Although the shape of the vacuum container 1 used in the present invention is not particularly limited, generally a container with a cone-shaped bottom and a cylindrical portion as shown in FIG.
It is preferably used because it is easy to rotate and the flow of the viscous material 2 is smooth.

本考案に用いる撹拌機3は、第1図に示すよう
な場合を除いて、一般に回転軸7及び該回転軸7
を回転させるモーターよりなり、回転軸7の先端
には羽根8が接続された構造であれば特に制限な
く用いられる。羽根8の形状は、特に制限されな
いが、真空容器1の側面内壁より20mm以内で内壁
に沿いながら動く形状がよく、また断面の直径が
真空容器1の内径の1/2〜1/4のものは、粘体2が
よく羽根8に付着して上下に動き、且つ回転軸を
回転させた時、断面の大半を通過するため脱泡効
果が良い。羽根8は1本でもよいが2本以上用い
る方が、機械的なバランス上好ましい。
The stirrer 3 used in the present invention generally includes a rotating shaft 7 and a rotating shaft 7, except for the case shown in FIG.
Any structure can be used without any particular restriction as long as it consists of a motor that rotates a rotary shaft 7 and a blade 8 is connected to the tip of the rotary shaft 7. The shape of the blade 8 is not particularly limited, but it is best to have a shape that moves along the inner wall within 20 mm of the side inner wall of the vacuum vessel 1, and whose cross-sectional diameter is 1/2 to 1/4 of the inner diameter of the vacuum vessel 1. In this case, the viscous substance 2 adheres well to the blade 8 and moves up and down, and when the rotating shaft is rotated, it passes through most of the cross section, so the degassing effect is good. Although one blade 8 may be used, it is preferable to use two or more blades from the viewpoint of mechanical balance.

回転軸7の上下間の移動距離は、真空容器1底
部の粘体が粘体の液面近くまでもち上がる程度必
要である。上下の移動速度は0.1〜50回/分、又、
回転数は0.1〜50r.pm程度が好ましい。また、真
空度は、粘体の種類によつても異なるが、一般に
は100mmHg以下で特に10mmHg以下が好ましい。
The vertical movement distance of the rotating shaft 7 is required to be such that the viscous material at the bottom of the vacuum container 1 is lifted close to the liquid level of the viscous material. The vertical movement speed is 0.1 to 50 times/minute, and
The rotation speed is preferably about 0.1 to 50 rpm. Further, the degree of vacuum varies depending on the type of viscous material, but is generally 100 mmHg or less, and preferably 10 mmHg or less.

その他、真空容器1及び撹拌機3を構成する各
部の材質は、粘体に耐食性且つ耐摩耗性を有する
ものであればよく、一般には金属、ガラス樹脂又
はそれらのライニング材が用いられる。又、回転
軸7と真空容器1の気密は、o−リング、オイル
シール、グランドパツキン等を使用すればよい。
In addition, the materials of the parts constituting the vacuum container 1 and the stirrer 3 may be any material as long as it has corrosion resistance and wear resistance in a viscous body, and metals, glass resins, or lining materials thereof are generally used. Further, the rotating shaft 7 and the vacuum container 1 may be airtight by using an O-ring, an oil seal, a gland packing, or the like.

本考案は上記したように真空容器1中に特定な
構造の撹拌機3を設けたことが特徴であつて、該
容器は充填器として好ましく用いられる。この
際、充填される側の容器、或いは充填方法等につ
いては特に制限されるものでないが、第8図のよ
うに真空容器1に撹拌をしない状態で気体圧を加
えで底部から一定量を充填容器11に充填するこ
とは、真空容器1から別の大容器に移しかえる操
作が不要で、真空容器1に残留する量を減ずる
し、移しかえに伴う気泡の混入を防ぐため好まし
い。
As described above, the present invention is characterized in that the agitator 3 of a specific structure is provided in the vacuum container 1, and the container is preferably used as a filling device. At this time, there are no particular restrictions on the container to be filled or the filling method, but as shown in Figure 8, a certain amount is filled from the bottom of the vacuum container 1 by applying gas pressure without stirring. Filling the container 11 is preferable because it eliminates the need for transferring from the vacuum container 1 to another large container, reduces the amount remaining in the vacuum container 1, and prevents air bubbles from being mixed in during transfer.

充填容器11に一定重量の粘体2を充填する場
合、一般に計量計12の上部に充填容器11を設
置した状態で、重量を測定しながらバルブ6を一
定時間開く。この際、粘体2は折り重なりながら
充填器11に入るので気泡を再び含むことになり
好ましくない。これを防止するためには、充填容
器11を真空下(真空雰囲気室13)に置き、真
空中で重量を測定しつつ充填するのがよい。ま
た、充填量の精度を上げるには少量ずつ充填する
のが良いが充填に時間がかかる。逆に時間を短か
くしようとすると充填精度が上らない。これを防
止するため、一般的には大、小弁を設けて制御す
ることが良く行なわれるが、弁内への残留量が問
題となる。そこでバルブ6にコントロール弁(自
動式が好ましい、又、摩耗性粒子を含む場合はダ
イヤフラム弁やピンチ弁が好ましい)を用いて、
充填量を測定しながら初めは弁開度を大きく、希
望充填量に近づくに従つて弁開度を小さくしてい
き、希望充填量の少く前で、たれ落ちる粘体の流
れを糸又はカツターで切つて充填することにより
充填精度を上げることができる。充填中は、粘性
が大きいため弁の出口にぶら下る形で重量を測定
するため予測制御を行なう必要があるためであ
る。バルブ6のコントロールは、制御計14によ
り行なうことができる。その他、粘体の種類等に
ついても特に制限されるものでない。
When filling the filling container 11 with a fixed weight of viscous material 2, the filling container 11 is generally placed above the weighing scale 12, and the valve 6 is opened for a certain period of time while measuring the weight. At this time, the viscous material 2 enters the filling device 11 while folding over itself, which is undesirable because it contains air bubbles again. In order to prevent this, it is preferable to place the filling container 11 under vacuum (vacuum atmosphere chamber 13) and fill the container while measuring the weight in vacuum. In addition, in order to increase the accuracy of the filling amount, it is better to fill in small amounts, but it takes time to fill. On the other hand, if you try to shorten the time, the filling accuracy will not improve. To prevent this, it is generally common practice to provide large and small valves for control, but the amount remaining in the valves poses a problem. Therefore, a control valve (an automatic type is preferable, and a diaphragm valve or a pinch valve is preferable when abrasive particles are included) is used as the valve 6.
While measuring the filling amount, first widen the valve opening, then decrease the valve opening as you approach the desired filling amount. Cut the dripping viscous flow with a thread or cutter just before the desired filling amount. Filling accuracy can be improved by filling the container. This is because during filling, since the viscosity is high, it is necessary to perform predictive control because the weight is measured while hanging from the outlet of the valve. The valve 6 can be controlled by a controller 14. In addition, there are no particular restrictions on the type of viscous material.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本考案の粘体の脱泡容器の概略図で
ある。又、第3図、第4図及び第6図は回転軸の
概略図であり、第5図は第4図の平面図を、又、
第7図は第6図の平面図を夫々示す。また、第2
図及び第8図は本考案の別態様を示す概略図であ
る。 図において、1は真空容器、2は粘体、3は撹
拌機、4は取出口、5は真空手段、6はバルブ、
7は回転軸、8は羽根、9はシリンダー、10
は、ネジ切り部、11は充填容器、12は計量
計、13は真空雰囲気室、14は制御計14であ
る。
FIG. 1 is a schematic diagram of a viscous defoaming container of the present invention. 3, 4, and 6 are schematic diagrams of the rotating shaft, and FIG. 5 is a plan view of FIG. 4, and
FIG. 7 shows a plan view of FIG. 6, respectively. Also, the second
8 and 8 are schematic diagrams showing another embodiment of the present invention. In the figure, 1 is a vacuum container, 2 is a viscous material, 3 is a stirrer, 4 is an outlet, 5 is a vacuum means, 6 is a valve,
7 is the rotating shaft, 8 is the blade, 9 is the cylinder, 10
11 is a filling container, 12 is a weighing meter, 13 is a vacuum atmosphere chamber, and 14 is a control meter 14.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 真空容器内に、回転軸が回転しながら上下動す
る構造の撹拌機が付設された粘体の脱泡容器。
A viscous defoaming container with a stirrer inside the vacuum container that moves up and down while rotating.
JP5726284U 1984-04-20 1984-04-20 Defoaming container for viscous substance Granted JPS60171514U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5726284U JPS60171514U (en) 1984-04-20 1984-04-20 Defoaming container for viscous substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5726284U JPS60171514U (en) 1984-04-20 1984-04-20 Defoaming container for viscous substance

Publications (2)

Publication Number Publication Date
JPS60171514U JPS60171514U (en) 1985-11-13
JPH0213042Y2 true JPH0213042Y2 (en) 1990-04-11

Family

ID=30581622

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5726284U Granted JPS60171514U (en) 1984-04-20 1984-04-20 Defoaming container for viscous substance

Country Status (1)

Country Link
JP (1) JPS60171514U (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2741208B2 (en) * 1988-04-11 1998-04-15 鐘淵化学工業株式会社 Reaction / mixing degassing method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS521505A (en) * 1975-06-24 1977-01-07 Hitachi Ltd Compressor
JPS57159510A (en) * 1980-12-18 1982-10-01 Toshiba Mach Co Ltd Defoaming tank

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS521505A (en) * 1975-06-24 1977-01-07 Hitachi Ltd Compressor
JPS57159510A (en) * 1980-12-18 1982-10-01 Toshiba Mach Co Ltd Defoaming tank

Also Published As

Publication number Publication date
JPS60171514U (en) 1985-11-13

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