JPH0450523B2 - - Google Patents

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Publication number
JPH0450523B2
JPH0450523B2 JP2336339A JP33633990A JPH0450523B2 JP H0450523 B2 JPH0450523 B2 JP H0450523B2 JP 2336339 A JP2336339 A JP 2336339A JP 33633990 A JP33633990 A JP 33633990A JP H0450523 B2 JPH0450523 B2 JP H0450523B2
Authority
JP
Japan
Prior art keywords
rotation speed
pump
size liquid
liquid
metering pump
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2336339A
Other languages
Japanese (ja)
Other versions
JPH03233323A (en
Inventor
Yasuhiro Osada
Sadaichi Nagai
Takeshi Takada
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.)
Kanebo Ltd
Original Assignee
Kanebo 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 Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP33633990A priority Critical patent/JPH03233323A/en
Publication of JPH03233323A publication Critical patent/JPH03233323A/en
Publication of JPH0450523B2 publication Critical patent/JPH0450523B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) 本発明は、高粘度液を一定量計量する装置に関
するものである。 (従来の技術とその問題点) 捺染における色糊の作成は捺染製品の色品質を
決定する重要な作業である。通常、この色糊は染
料粉末或いは染料粉末を溶解した染料液と糊材を
水及び助剤で溶解した糊液とを一定比率で混合
し、撹拌して作られる。又、印捺方法によつては
この色糊に抜染剤或いは防染剤等の助剤を添加し
再度撹拌混合される。 この色糊の作成量は印捺量、印捺面積、印捺付
着量等により各色糊ごとに異なる。それ故、各色
糊ごとに、染料、糊液、助剤を都度計量しなけれ
ばならず、色糊作成作業の大半はこの計量作業に
費やされている。特に糊液、抜染剤、及び防染剤
の計量は量的に多くかつ粘度が高く取扱いが困難
である。 従来、この糊液或いは抜染剤、防染剤等の助剤
(以下これらを総称して糊液と云う)の計量は、
混合撹拌する容器を台秤り上に置き、所要糊液量
に計量目盛を設定し、糊液貯蔵タンクより、手動
でバルブを開け容器に投入する方法、或いは糊液
容器より柄杓にて汲み取り投入する方法で、台秤
り指示が所要量に到達したことを目視により判断
し投入を停止する方法で行なわれている。しかし
この方法は人手作業であるため細心の配慮が必要
であり、人的誤差が生じやすくかつ労力を要する
欠点がある。 又他の方法として、糊液を定容量ポンプにて送
糊投入し、所要投入量に相当するポンプ運転時間
をタイマーにて設定し投入量を制御する方法がと
られている。しかしこの方法は糊液粘度、定容量
ポンプの回転数変動等により誤差が生じやすく、
かつ投入量から時間に換算する作業が必要である
などの欠点がある。 さらに他の方法として、実公昭46−23614号公
報には、糊液を定容量ポンプにて送糊投入し、所
要投入量に相当する累計回転数に達した時、モー
ターとポンプ間の電磁クラツチによりポンプの回
転を瞬間的に停止し投入量を制御する装置が提案
されている。しかしこの装置は高粘度の糊液の計
量ポンプに応用した場合、機構的に複雑でコスト
アツプの要因ともなり、また吐出圧とヘツド圧の
逆転による配管内への空気の流入の要因となり、
次回計量時の誤差発生並びに糊液の固化によるつ
まり発生につながるという欠点がある。 (問題点を解決するための手段) 本発明はこれ等の欠点を除去し高粘度液を一定
量計量することを目的とし、糊液タンクの下流側
に設けた容積計量ポンプと、該計量ポンプの出口
側配管に設けたストツプ弁および多数の細孔を備
えたノズルと、糊液の密度、計量ポンプの単位回
転数当りの吐出量、計量ポンプの惰性回転数およ
び必要計量重量値を設定する設定器と、該設定器
からの情報を基にして前記計量ポンプの回転数を
演算し制御するコンピユーターより成り、且つ前
記ノズルの細孔の断面積の総和を前記配管の断面
積以上に構成したことを特徴とする糊液の計量装
置を要旨とするものである。 次に本発明を図示の例によつてさらに詳細に説
明する。第1図において、タンク1〜1nは、溶
解した糊液を貯蔵するタンク、タンク4〜4nは
中間ストレージタンクであり、液レベルを制御す
るための制御機構としてのレベル検出端11〜1
1n,12〜12n及び、レベルコントローラ1
0〜10nが取付けられている。 前記中間ストレージタンク4〜4nには定量ポ
ンプ7〜7nが連通されており、さらに該ポンプ
7〜7nの吐出側にノズル8〜8nが取付けられ
ている。容器13は糊作成量に合せた大きさの小
分け容器であり、おのおのの糊を定量収容し、染
料及び水を添加混合するものである。添加する水
を計量する計量計16、バルブ17は小分け容器
13に水を供給する導管に設置されている。制御
盤15は所定値に設定される各糊量、水量を制御
するものであり、各検出端からの信号により定量
ポンプ7〜7nの起動停止制御と、バルブ17の
開閉を行うよう構成されている。 第2図及び第3図は、定量ポンプ7〜7nの吐
出側に取付けるノズル8〜8nを示すもので、2
0はフレーム、21は多孔ノズル22を有する吐
出部、23はストツプ弁、24は逆止用スプリン
グ、25,27は前記ストツプ弁23及びスプリ
ング24を保持する金具及びネジ、26はシール
用Oリングパツキンである。 次に第1図により本発明方法の過程を説明す
る。捺染に必要な糊種に対応して設置した糊液貯
蔵タンク1〜1nには数日分の使用量の糊が貯蔵
されている。該タンク1〜1nの糊液は落差或い
はポンプにより中間ストレージタンク4〜4nへ
パイプ3、弁2を経て送られる。中間ストレージ
タンク4〜4nは定量ポンプ7〜7nの吸引量を
安定するために設置しており、該タンク4〜4n
の排出口と定量ポンプ7〜7nの吸引口とは極力
短かい距離で接続することが好ましい。又該タン
ク4〜4n内の液レベルを一定に保つためにレベ
ル計5、レベルコントローラ10、及びレベル検
出端11,12を中間ストレージタンク4〜4n
に付設し、液レベルが検出端11以下に下ると弁
2を開き液を供給し、レベル検出端12の位置で
供給を停止し、該検出端11と12の間に液レベ
ルを制御する。定量ポンプ7〜7nは制御盤15
からの制御信号により起動・停止し糊液は所定量
容器13に供給される。定量ポンプ7〜7nから
配管14〜14nの先端に取付けられたノズル8
〜8nは定量ポンプ7〜7nを停止した際に配管
14内の糊液が滴下することを防止するためのも
のである。 すなわち高粘度液を移送する際の配管圧力損失
を極力少なくし定量ポンプの定量精度を高めるた
めには配管14は極力管径の大きいパイプにする
必要がある。該管径の大きいパイプでは糊液が高
粘度であつても、供給停止後パイプ先端より順次
滴下する現象が発生し計量精度が低下する。糊粘
度に応じた滴下現象の発生しない限界径以下の径
の細孔を複数個もうけ、該細孔の断面積の総和が
配管14の断面積以上となるようにした多孔のノ
ズル8〜8nを配管14の先端に取付けることに
より滴下を防止する。さらに第2図に示すスプリ
ング24により圧接されるストツプ弁23を設
け、糊液供給停止時に配管14〜14n内の残留
圧力により糊液がノズル8〜8nより押出される
ことを防止する。このように滴下防止の多孔ノズ
ル8〜8n及びストツプ弁23を吐出管の先端に
設けることにより吐出管への空気の流入が防止さ
れ、次回の計量においてポンプ起動と同時にポン
プ計量吐出量に等しい糊液が吐出口から排出さ
れ、定量ポンプから吐出口までの送液管の長さに
関係なく定量供給が可能となる。 第4図は制御操作をブロツク図で示したもので
ある。計量値設定盤34にて必要計量重量値
(W)を設定し、定量ポンプ7の必要回転数を演
算する。回転数設定演算部33(コンピユータ
ー)にて計量重量値をポンプ回転数に変換する。
この回転数設定演算部33では計量する糊液の特
性に合せ、糊液の密度(w)、計量ポンプ7の単
位回転数当りの吐出量(v)をあらかじめ計測し
密度回転数当り吐出量設定盤35にて設定された
設定値及び定量ポンプ7の惰性回転数(n)をあ
らかじめ計測し、ポンプ惰性回転数設定盤36に
設定された設定値(n)をもとに次式により必要
回転数(N)の演算を行なう。 N=W/w・v−n 以上の演算が終了後起動ボタン37にて起動・
停止操作器32(電磁開閉器)を起動し計量を開
始する。計量ポンプ7の回転に合せ回転数を計測
する回転パルス発信器9より回転パルス信号を回
転数カウンター30に送り回転数をカウントす
る。設定値・カウンター比較回路31では回転数
が必要回転数設定値(N)に到達したかを判定
し、設定値とカウント値が一致した時停止信号を
発し計量ポンプを停止する。回転数を精度よく制
御するために、計量ポンプの回転パルス発信器は
ポンプ1回転当り6〜30パルスの信号を発信する
機構が好ましく、これは計量ポンプの機構、ポン
プ吐出量、回転速度及び計量要求精度により選択
される。 尚色糊は捺染柄、被捺染布帛、印捺方法によつ
て糊特性を選択して使用されるのが通常であり、
そのために色糊作成は数種の特性の糊液を混合し
て行う場合がある。 この糊液混合作成に際しては、あらかじめ糊液
の混合比率レサイプを回転数設定演算部33のコ
ンピユーターに記憶せしめ、計量値設定盤34上
にレサイプ選択ボタンを設け、計量値設定時にレ
サイプの選択を行ない演算部では該当レサイプの
混合比率に従つて各糊液の計量値を算出し前記の
演算式に従い、各糊液ごとの必要回転数(N1
(Industrial Application Field) The present invention relates to an apparatus for measuring a fixed amount of high viscosity liquid. (Prior art and its problems) Preparation of colored paste in textile printing is an important operation that determines the color quality of printed products. Usually, this color paste is made by mixing a dye powder or a dye liquid containing a dye powder dissolved therein and a size liquid containing a sizing material dissolved in water and an auxiliary agent in a fixed ratio and stirring the mixture. Further, depending on the printing method, an auxiliary agent such as a discharge printing agent or a dye resisting agent is added to the colored paste and the mixture is stirred and mixed again. The amount of colored paste to be produced differs for each colored paste depending on the amount of printing, the area of printing, the amount of adhesion of printing, etc. Therefore, it is necessary to measure the dye, size liquid, and auxiliary agent each time for each color paste, and most of the color paste production work is spent on this measuring work. In particular, the size liquid, discharge printing agent, and dye resisting agent have to be measured in large quantities and have high viscosity, making them difficult to handle. Conventionally, the measurement of this size liquid or auxiliary agents such as discharge printing agent and dye resisting agent (hereinafter collectively referred to as size liquid) is as follows:
Place the container to be mixed and stirred on a platform scale, set the measuring scale to the required amount of size liquid, and pour the size liquid into the container by manually opening the valve from the size liquid storage tank, or scoop the size liquid from the size liquid container with a ladle and pour it into the container. In this method, it is determined visually that the required amount has been reached according to the platform scale instruction, and the feeding is stopped. However, this method requires careful consideration because it is a manual process, and has the disadvantage of being prone to human error and requiring labor. Another method is to feed the size liquid using a fixed volume pump and control the amount of injection by setting the pump operation time corresponding to the required amount of injection using a timer. However, this method is prone to errors due to factors such as the viscosity of the glue and fluctuations in the rotational speed of the fixed displacement pump.
Another disadvantage is that it requires work to convert the amount of input into time. As yet another method, Japanese Utility Model Publication No. 46-23614 discloses that the size liquid is fed into the paste using a constant volume pump, and when the cumulative number of revolutions corresponding to the required amount of injection is reached, an electromagnetic clutch between the motor and the pump is used. A device has been proposed that instantly stops the rotation of the pump and controls the input amount. However, when this device is applied to a metering pump for high-viscosity paste liquid, it becomes mechanically complex and causes an increase in costs, and also causes air to flow into the piping due to the reversal of the discharge pressure and head pressure.
There are disadvantages in that errors occur during the next measurement and clogging occurs due to solidification of the paste. (Means for Solving the Problems) The present invention aims to eliminate these drawbacks and measure a certain amount of high viscosity liquid. Set the stop valve installed on the outlet side piping and the nozzle with numerous pores, the density of the size liquid, the discharge amount per unit rotation speed of the metering pump, the inertia rotation speed of the metering pump, and the required weighing weight value. It consists of a setting device and a computer that calculates and controls the rotation speed of the metering pump based on information from the setting device, and the total cross-sectional area of the pores of the nozzle is larger than the cross-sectional area of the piping. The gist of the present invention is to provide a measuring device for glue liquid, which is characterized by the following. Next, the present invention will be explained in more detail using illustrated examples. In FIG. 1, tanks 1 to 1n are tanks for storing dissolved glue, tanks 4 to 4n are intermediate storage tanks, and level detection ends 11 to 1 are used as control mechanisms for controlling the liquid level.
1n, 12 to 12n and level controller 1
0 to 10n are attached. Metering pumps 7-7n are connected to the intermediate storage tanks 4-4n, and nozzles 8-8n are attached to the discharge side of the pumps 7-7n. The container 13 is a subdivided container of a size corresponding to the amount of glue to be prepared, and is used to store a fixed amount of each glue, and add and mix dye and water. A meter 16 for measuring the amount of water to be added and a valve 17 are installed in a conduit that supplies water to the subdividing container 13. The control panel 15 controls each amount of glue and water to be set to a predetermined value, and is configured to control the start/stop of the metering pumps 7 to 7n and open/close the valve 17 based on signals from each detection end. There is. 2 and 3 show nozzles 8 to 8n attached to the discharge side of metering pumps 7 to 7n.
0 is a frame, 21 is a discharge part having a multi-hole nozzle 22, 23 is a stop valve, 24 is a check spring, 25 and 27 are metal fittings and screws that hold the stop valve 23 and spring 24, and 26 is an O-ring for sealing. It's Patsukin. Next, the process of the method of the present invention will be explained with reference to FIG. The size liquid storage tanks 1 to 1n, which are installed according to the type of paste required for textile printing, store the amount of paste used for several days. The size liquid in the tanks 1 to 1n is sent via a pipe 3 and a valve 2 to intermediate storage tanks 4 to 4n by a head or a pump. The intermediate storage tanks 4 to 4n are installed to stabilize the suction amount of the metering pumps 7 to 7n.
It is preferable that the discharge port and the suction port of the metering pumps 7 to 7n be connected by as short a distance as possible. In order to keep the liquid level in the tanks 4 to 4n constant, the level meter 5, level controller 10, and level detection terminals 11 and 12 are connected to the intermediate storage tanks 4 to 4n.
When the liquid level falls below the detection end 11, the valve 2 is opened to supply liquid, and the supply is stopped at the level detection end 12 to control the liquid level between the detection ends 11 and 12. Control panel 15 for metering pumps 7 to 7n
The paste is started and stopped by a control signal from the controller, and a predetermined amount of paste is supplied to the container 13. Nozzle 8 attached to the tip of piping 14-14n from metering pump 7-7n
-8n is for preventing the paste liquid in the pipe 14 from dripping when the metering pumps 7-7n are stopped. That is, in order to minimize piping pressure loss when transferring a high viscosity liquid and to improve the metering accuracy of the metering pump, the piping 14 needs to be a pipe with as large a diameter as possible. Even if the size liquid has a high viscosity in a pipe with a large diameter, a phenomenon occurs in which the size liquid drips from the tip of the pipe after the supply is stopped, resulting in a decrease in measurement accuracy. A multi-hole nozzle 8 to 8n is provided with a plurality of pores having a diameter below the limit diameter at which a dripping phenomenon does not occur depending on the viscosity of the glue, and the total cross-sectional area of the pores is greater than or equal to the cross-sectional area of the pipe 14. By attaching it to the tip of the pipe 14, dripping is prevented. Furthermore, a stop valve 23 which is pressed by a spring 24 shown in FIG. 2 is provided to prevent the size liquid from being pushed out from the nozzles 8 to 8n due to the residual pressure in the pipes 14 to 14n when the size liquid supply is stopped. In this way, by providing the multi-hole nozzles 8 to 8n and the stop valve 23 to prevent dripping at the tip of the discharge pipe, air is prevented from entering the discharge pipe, and the next time the pump is started, the glue equal to the pump metered discharge amount is removed. The liquid is discharged from the discharge port, and a fixed amount can be supplied regardless of the length of the liquid pipe from the metering pump to the discharge port. FIG. 4 shows a block diagram of the control operation. The required measured weight value (W) is set on the measured value setting board 34, and the required number of revolutions of the metering pump 7 is calculated. The measured weight value is converted into a pump rotation speed by a rotation speed setting calculation unit 33 (computer).
This rotation speed setting calculation unit 33 measures the density (w) of the size liquid and the discharge amount (v) per unit rotation speed of the metering pump 7 in advance according to the characteristics of the size liquid to be measured, and sets the discharge amount per density rotation speed. The set value set on the panel 35 and the inertia rotation speed (n) of the metering pump 7 are measured in advance, and the required rotation is determined by the following formula based on the set value (n) set on the pump inertia rotation speed setting board 36. Calculate the number (N). N=W/w・v−n After the above calculations are completed, press the start button 37 to start.
The stop operation device 32 (electromagnetic switch) is activated to start measuring. A rotation pulse signal is sent to a rotation speed counter 30 from a rotation pulse transmitter 9 which measures the rotation speed according to the rotation of the metering pump 7, and the rotation speed is counted. The set value/counter comparison circuit 31 determines whether the rotation speed has reached the required rotation speed set value (N), and when the set value and the count value match, a stop signal is issued to stop the metering pump. In order to accurately control the rotation speed, it is preferable that the rotation pulse transmitter of the metering pump has a mechanism that transmits a signal of 6 to 30 pulses per pump rotation. Selected according to required accuracy. Normally, colored pastes are used by selecting the adhesive properties depending on the printing pattern, the fabric to be printed, and the printing method.
For this reason, colored pastes may be prepared by mixing several types of paste liquids with different characteristics. When creating this size liquid mixture, the size liquid mixture ratio recipe is stored in advance in the computer of the rotation speed setting calculation unit 33, and a recipe selection button is provided on the measurement value setting board 34, and the recipe is selected when setting the measurement value. The calculation section calculates the measured value of each size liquid according to the mixing ratio of the corresponding recipe, and calculates the required number of rotations for each size liquid (N 1 ~

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】 (発明の効果) 本発明によれば糊液計量に要する労力が大幅に
低減され、かつ人的誤差を減少させ高度の計量精
度が得られ優れた捺染品質を確保することが出来
る。
[Table] (Effects of the Invention) According to the present invention, the labor required for measuring the size solution can be significantly reduced, human error can be reduced, a high degree of measurement accuracy can be obtained, and excellent printing quality can be ensured.

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

第1図は本発明装置の全体を示す説明図、第2
図はノズルの縦断面図、第3図はノズルの底面
図、第4図は制御操作フロートのブロツク図であ
る。 1〜1n……タンク、2〜2n……弁、4〜4
n……中間ストレージタンク、6〜6n……管、
7〜7n……定量ポンプ、8〜8n……ノズル。
FIG. 1 is an explanatory diagram showing the entire device of the present invention, and FIG.
3 is a bottom view of the nozzle, and FIG. 4 is a block diagram of the control operation float. 1~1n...Tank, 2~2n...Valve, 4~4
n...Intermediate storage tank, 6~6n...Pipe,
7~7n...metering pump, 8~8n...nozzle.

Claims (1)

【特許請求の範囲】[Claims] 1 糊液タンクの下流側に設けた容積計量ポンプ
と、該計量ポンプの出口側配管に設けたストツプ
弁および多数の細孔を備えたノズルと、糊液の密
度、計量ポンプの単位回転数当りの吐出量、計量
ポンプの惰性回転数および必要計量重量値を設定
する設定器と、該設定器からの情報を基にして前
記計量ポンプの回転数を演算し制御するコンピユ
ーターより成り、且つ前記ノズルの細孔の断面積
の総和を前記配管の断面積以上に構成したことを
特徴とする糊液の計量装置。
1. A volumetric measuring pump installed downstream of the size liquid tank, a nozzle equipped with a stop valve and a large number of pores installed on the outlet side piping of the measuring pump, the density of the size liquid, and the per unit rotation speed of the measuring pump. a setting device for setting the discharge amount of the metering pump, an inertial rotation speed of the metering pump, and a required weighing weight value, and a computer that calculates and controls the rotation speed of the metering pump based on information from the setting device; A size liquid measuring device characterized in that the sum of the cross-sectional areas of the pores is larger than the cross-sectional area of the piping.
JP33633990A 1990-11-29 1990-11-29 Metering device for size liquid Granted JPH03233323A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33633990A JPH03233323A (en) 1990-11-29 1990-11-29 Metering device for size liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33633990A JPH03233323A (en) 1990-11-29 1990-11-29 Metering device for size liquid

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP14971980A Division JPS5773630A (en) 1980-10-24 1980-10-24 Method and device for metering paste liquid

Publications (2)

Publication Number Publication Date
JPH03233323A JPH03233323A (en) 1991-10-17
JPH0450523B2 true JPH0450523B2 (en) 1992-08-14

Family

ID=18298101

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33633990A Granted JPH03233323A (en) 1990-11-29 1990-11-29 Metering device for size liquid

Country Status (1)

Country Link
JP (1) JPH03233323A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015036660A (en) * 2013-08-15 2015-02-23 株式会社▲吉▼本製作所 Liquid mixing apparatus

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0674200A (en) * 1992-08-25 1994-03-15 Kubota Corp Noise/water power eliminating structure for pump discharge water
JP4953505B2 (en) * 1998-07-09 2012-06-13 コンティネンタル・テーベス・アクチエンゲゼルシヤフト・ウント・コンパニー・オッフェネ・ハンデルスゲゼルシヤフト Method and apparatus for brake pressure regulation and inlet valve opening

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5224184Y2 (en) * 1975-04-01 1977-06-01
JPS5318898A (en) * 1976-08-06 1978-02-21 Keiichirou Ishida Caterpillar lumber conveying device in band sawing machine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015036660A (en) * 2013-08-15 2015-02-23 株式会社▲吉▼本製作所 Liquid mixing apparatus

Also Published As

Publication number Publication date
JPH03233323A (en) 1991-10-17

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