JPH03233323A - Metering device for size liquid - Google Patents

Metering device for size liquid

Info

Publication number
JPH03233323A
JPH03233323A JP33633990A JP33633990A JPH03233323A JP H03233323 A JPH03233323 A JP H03233323A JP 33633990 A JP33633990 A JP 33633990A JP 33633990 A JP33633990 A JP 33633990A JP H03233323 A JPH03233323 A JP H03233323A
Authority
JP
Japan
Prior art keywords
metering
piping
size
size liquid
pumps
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
Application number
JP33633990A
Other languages
Japanese (ja)
Other versions
JPH0450523B2 (en
Inventor
Yasuhiro Osada
長田 泰礼
Sadaichi Nagai
長井 定一
Takeshi Takada
健 高田
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

Links

Abstract

PURPOSE:To obtain a high degree of metering accuracy and to assure printing quality by constituting nozzles in such a manner that the sum total of the sectional areas of the fine holes thereof is larger than the sectional area of a piping, thereby drastically lessening the labor for metering and decreasing human errors. CONSTITUTION:The perforated nozzles 8 to 8n which are provided with the fine holes of the diameter below the threshold diameter at which the dropping according to size viscosities does not arise and are formed to have the total sum of the section areas thereof larger than the sectional area of the piping 14 are mounted to the front end of the piping 14 to prevent the dropping. Further, stop valves 23 which are brought into pressurized contact by springs 24 prevent the size liquids from being extruded from the nozzles 8 to 8n by the pressures remaining in the piping 14 to 14n at the time the supply of the size liquids stops. The size liquids equal to the discharge quantity of the pumps by metering are discharged from discharge ports simultaneously with the start of the pumps at the next metering so that the supply at the constant rate is possible regardless of the length of the liquid feed pipes from the metering pumps to the liquid feed pipes. Since plural sizes of the size liquids are simultaneously metered, the metering is executed in a short period of time and the remarkable improvement in productivity is made.

Description

【発明の詳細な説明】 (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。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to an apparatus for measuring a fixed amount of a high viscosity liquid.

(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0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梅林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
捺方法によっ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。
(Conventional technology and its problems) The preparation of colored paste in textile printing is an important task that determines the color quality of printed products.Normally, this colored paste is made by mixing dye powder or a dye liquid containing dissolved dye powder with umerin in water. It is made by mixing and stirring in a fixed ratio a paste solution dissolved with an auxiliary agent. 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.

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。
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. Especially the glue,
Discharging agents and resisting agents have to be measured in large quantities and have high viscosity, making them difficult to handle.

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、手動でパルプを開は容器に投入す
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
、人的誤差が生しやすくかつ労力を要する欠点がある。
Conventionally, to measure the size liquid or auxiliary agents such as discharge printing agent and dye resisting agent (hereinafter collectively referred to as size liquid), the container to be mixed and stirred was placed on a table scale, and the measuring scale was set at the required amount of size liquid. and set
Either manually open the pulp from the size liquid storage tank and pour it into the container, or scoop it up from the size liquid container with a ladle and pour it in. Feeding is stopped when it is determined visually that the required amount has been reached according to the platform scale instructions. It is done in this way. However, this method requires careful consideration because it is a manual process, and has the drawbacks of being prone to human error and requiring labor.

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
誤差が生しやすく、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。
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 changes in the viscosity of the paste liquid, the rotational speed of the fixed displacement pump, etc., and has drawbacks such as the need to convert the input amount into time.

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1ttti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amでコストア・ノブの要因と
もなり、また吐出圧とヘッ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。
Furthermore, as another method, Japanese Utility Model Publication No. 46-23614 discloses that the size liquid is fed by a constant volume pump, and when the total number of revolutions corresponding to the required amount of injection is reached, a 1ttti clutch between the motor and the pump is connected. 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 a cause of the coster knob due to the am mechanism, 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.

(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ッ
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ューターより成り、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。
(Means for Solving the Problems) The present invention aims to eliminate these drawbacks and measure a fixed amount of high viscosity liquid. A stop valve and a nozzle equipped with numerous pores are installed on the outlet side piping, and the density of the size liquid,
A setting device for setting the discharge amount per unit rotational speed of the metering pump, the inertia rotational speed of the metering pump, and the required weighing weight value, and calculating and controlling the rotational speed of the metering pump based on information from the setting device. The gist of the present invention is to provide a size liquid metering device comprising a computer, and characterized in that the total cross-sectional area of the pores of the nozzle is larger than the cross-sectional area of the piping.

次に本発明を図示の例によってさらに詳細に説明する。The invention will now be explained in more detail by way of illustrated examples.

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11御するため
の制御機構としてのレベル検出端(11) 〜(llr
i) 、(12) 〜(12n)及び、レベルコントロ
ーラ(10)〜(10n)が取付けられている。
In Figure 1, tanks (1> to (1n) are tanks for storing dissolved paste liquid, and tanks (4) to (4n) are intermediate storage tanks, which are used as a control mechanism to control the liquid level. level detection terminal (11) ~(llr
i) , (12) to (12n) and level controllers (10) to (10n) are attached.

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
大きさの小分は容器であり、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) 、パルプ(17)は小分は容
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置ポンプ(
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。
Metering pumps (7) to (7n) are connected to the intermediate storage tanks (4) to (4n), and nozzles (8) to (8n) are connected to the discharge sides of the pumps (7) to (7n).
is installed. The container (13) is a small container of a size corresponding to the amount of glue to be prepared, and is used to store a certain amount of each glue, and add and mix dye and water. A meter (16) for measuring the water to be added and the pulp (17) are installed in the conduit supplying the water to the container (13). The control panel (15) controls the amount of glue and water set to predetermined values, and the stationary pump (15) is controlled by the signals from each detection end.
7) to (7n), and the valve (17) is opened and closed.

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、
(20)はフレーム、(21〉は多孔ノズル(22)を
有する吐出部、(23)はストップ弁、(24)は逆止
用スプリング、(25)、 (27)は前記ストップ弁
(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○リングパツキンである。
Figures 2 and 3 show nozzles (8) to (8n) attached to the discharge side of metering pumps (7) to (7n),
(20) 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 the stop valves (23). and metal fittings and screws for holding the spring (24), and (26) is a sealing ring packing.

次に第1図により本発明方法の過程を説明する。Next, the process of the method of the present invention will be explained with reference to FIG.

捺染に必要な糊量に対応して設置した糊液貯蔵タンク(
1)〜(In)には数日分の使用量の糊が貯蔵されてい
る。該タンク(1)〜(in)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(1
0)、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
ポンデ(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。
A size liquid storage tank (
1) to (In) store glue to be used for several days. The paste in the tanks (1) to (in) is sent to intermediate storage tanks (4> to (4n) via pipes (3) and valves (2) by head or pump. 4n) are metering pumps (7) to (7n
) is installed to stabilize the suction amount of the tank (
4) - (4n) outlet and metering pump (7) - (7n)
It is preferable to connect it to the suction port at a distance as short as possible. In addition, in order to keep the liquid level in the tanks (4) to (4n) constant, a level meter (5) and a level controller (1) are installed.
0), and level detection ends (11) and (12) are attached to the intermediate storage tanks (4) to (4n), and when the liquid level falls below the detection end (11), the valve (2) is opened to supply liquid. Then, the supply is stopped at the level detection end (12), and the liquid level is controlled between the detection ends (11) and (12). The metering pumps (7) to (7n) are started and stopped by control signals from the control panel (15), and a predetermined amount of the paste is supplied to the container (13).

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(1
4)内の糊液が滴下することを防止するためのものであ
る。
From metering pump (7) ~ (7n) to piping (14) ~ (
Nozzles (8) to (8n) attached to the tip of 14n)
When the metering pumps (7) to (7n) are stopped, the piping (1
4) This is to prevent the glue inside from dripping.

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
なくし定置ポンプの定量精度を高めるためには配管(1
4)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っても、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。糊粘度に応し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ップ弁(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)7ブ弁(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。
In other words, in order to minimize piping pressure loss when transferring high viscosity liquids and improve the quantitative accuracy of stationary pumps, piping (1
For 4), it is necessary to use 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 sequentially drips from the tip of the pipe after the supply is stopped, resulting in a decrease in measurement accuracy. A porous nozzle (8) having a plurality of pores having a diameter below the limit diameter at which no dripping phenomenon occurs according to the viscosity of the glue, and the total cross-sectional area of the pores being greater than or equal to the cross-sectional area of the pipe (14). ) to (8n) are attached to the tip of the pipe (14) to prevent dripping. Furthermore, a stop valve (23) which is pressed by a spring (24> shown in FIG. ).In this way, by providing the porous nozzles (8) to (8n) and the valve (23) to prevent dripping at the tip of the discharge pipe, air can flow into the discharge pipe. In the next measurement, when the pump is started, a size liquid equal to the pump metered discharge amount is discharged from the discharge port, and a fixed amount of liquid can be supplied regardless of the length of the liquid pipe from the metering pump to the discharge port.

第4図はIIIIIII操作をブロック図で示したもの
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) (コンピューター)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)をあらかし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)をあらかしめ計測し、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。
FIG. 4 shows a block diagram of the IIIIII operation. Enter the required weight value (W) on the weight value setting panel (34).
) and calculate the required rotation speed of the metering pump (7). The rotation speed setting calculation unit (33) (computer) converts the measured weight value into the pump rotation speed. This rotation speed setting calculation unit (33) roughly measures the density (W) of the size liquid and the discharge amount (V) per unit rotation speed of the metering pump (7) according to the characteristics of the size liquid to be measured, and then performs the density rotation. Setting value set on the discharge amount setting panel (35) and metering pump (7)
The inertia rotation speed (n) of the pump is roughly measured, and the required rotation speed (N) is calculated using the following formula based on the setting value (n) set on the pump inertia rotation speed setting board (36).

N=                 −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(3
2) (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(3
0)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
待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。
After N = -n or more calculations are completed, press the start button (37) to turn on the start/stop operation device (3).
2) Start the (electromagnetic switch) and start weighing. The rotation pulse signal is sent to the rotation speed counter (3) from the rotation pulse transmitter (9) that measures the rotation speed according to the rotation of the metering pump (7).
0), count the number of feed revolutions. In the set value/counter comparison circuit (31), the number of revolutions is determined as the required number of revolutions set value (N).
It is determined whether the count value has been reached, and a wait stop signal is issued when the set value and the count value match, and the metering pump is stopped. 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 rotation of the pump.
Selected depending on rotation speed and required measurement accuracy.

尚色糊は捺染柄、被捺染布帛、印捺方法によって糊特性
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。
Normally, colored pastes are used by selecting the properties of the paste depending on the printing pattern, the fabric to be printed, and the printing method, and for this reason colored pastes are sometimes created by mixing paste liquids with several different properties. be.

この糊液混合作成に際しては、あらかしめ糊液の混合比
率レサイブを回転数設定演算部(33)のコンピュータ
ーに記憶せしめ、計量値設定盤(34)上にレサイブ選
択ボタンを設け、計量値設定時にレサイブの選択を行な
い演算部では該当レサイプの混合比率に従って各糊液の
計量値を算出し前記の演算式に従い、各糊液ご乙の必要
回転数(Nl 〜〜Nn)を設定し、定量ポンプを同時
に起動し各糊液の回転パルスカウント数が一致した定量
ポンプから停止し全ての糊液の計量が終った時点で計量
が終了する。
When creating this size liquid mixture, the mixing ratio recipe of the rough size liquid is stored in the computer of the rotation speed setting calculation unit (33), and a recipe selection button is provided on the weighing value setting board (34), and when setting the weighing value, After selecting the recipe, the calculation section calculates the measured value of each size liquid according to the mixing ratio of the corresponding recipe, sets the required rotation speed (Nl ~ ~Nn) of each size liquid according to the above calculation formula, and then starts the metering pump. are started at the same time, and the metering pump whose rotational pulse count number for each size liquid matches is stopped, and the measurement ends when all the size liquids have been measured.

従来の台秤りで計量する方法では、複数個の糊液を順次
計量して行くため1つの色糊を計量するのに長時間を要
したが、本発明によれば複数個の糊液を同時に計量する
ため、短時間で計量することが出来、生産性が大幅に向
上される。
In the conventional weighing method using a platform scale, it took a long time to weigh one color glue because multiple size liquids were weighed in sequence, but with the present invention, multiple size liquids can be weighed at the same time. Because it weighs, it can be measured in a short time, greatly improving productivity.

以下、実施例にて更に詳細に説明する。This will be explained in more detail in Examples below.

(実施例) 第1図の貯蔵タンク(1)を4基、中間ストレージタン
ク(4)を4基、計量ポンプ(7)を4基及び流量計(
16)、バルブ(17)を含む水計量ライン1基を基本
構成とする装置にて、糊量4種と水を計量した。第1表
に糊の種類及び特性を示す、第2表はm混合レサイプで
あり混合後の重量を100とし百分率で表わしている。
(Example) 4 storage tanks (1), 4 intermediate storage tanks (4), 4 metering pumps (7), and flow meters (
16) Four types of glue amounts and water were measured using an apparatus basically consisting of one water measuring line including a valve (17). Table 1 shows the types and properties of the glue, and Table 2 shows the m-mix recipe, which is expressed as a percentage with the weight after mixing as 100.

第3表は計量ポンプ特性である。中間ストレージタンク
は2001のタンクとし液面レベル計にてレベル変動を
30cm以内に設定した。糊液吐出口は各糊液ともに2
83mmφの穴170個を有する多孔ノズルと背圧Q、
 5 k g / c m ”で作動するストップ弁を
取付けた。定量ポンプ回転数パルス発信器は光電式信号
発信器とポンプ1回転当り20パルス発生する光遮断回
転板により構成した。水流量はtM1流量計を用い10
cc/パルスの発信により計量した。
Table 3 shows the metering pump characteristics. The intermediate storage tank was a 2001 tank, and the level fluctuation was set to within 30 cm using a liquid level meter. Each size liquid has two discharge ports.
A multi-hole nozzle with 170 holes of 83 mmφ and a back pressure Q,
A stop valve that operates at 5 kg/cm" was installed. The metering pump rotation speed pulse transmitter was composed of a photoelectric signal transmitter and a light cutoff rotary plate that generates 20 pulses per pump revolution. The water flow rate was tM1. 10 using a flow meter
Weighing was done by sending cc/pulse.

以上の条件のもとで色糊量10kg、20kg30kg
、40kg、50kgを各レサイプにつき計量した結果
各糊量(A、B、C,D)及び水の各所要量に対する精
度は1%以内であり色糊量全体に対する精度は2%以内
であった。又該糊料に比例した量の染料を添加後撹拌し
印捺発色後測色し色比較を行った結果色差1.5 N 
B S以下であった。
Under the above conditions, the amount of colored glue is 10kg, 20kg, and 30kg.
, 40 kg, and 50 kg for each recipe, the accuracy for each amount of glue (A, B, C, D) and each required amount of water was within 1%, and the accuracy for the total amount of colored glue was within 2%. . In addition, a proportionate amount of dye was added to the paste, stirred, and after the color was printed, the color was measured and the color was compared. As a result, the color difference was 1.5 N.
It was below B.S.

第 図 第 図 第 図 (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。
(Effects of the Invention) According to the present invention, the labor required for measuring size liquid is significantly reduced, human error is reduced, a high degree of measurement accuracy is obtained, and excellent printing quality is ensured. I can do it.

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

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ック図である。 l〜In・・・タンク、   2〜2n・・・弁、4〜 4n・・・中間ス トレージタンク、 6n・・・管、 7n・・・定量ポンプ、 n・・・ノズル。 第 1 図 第 図
FIG. 1 is an explanatory diagram showing the entire apparatus of the present invention, FIG. 2 is a longitudinal sectional view of the nozzle, FIG. 3 is a bottom view of the nozzle, and FIG. 4 is a block diagram of the control operation float. 1~In...tank, 2~2n...valve, 4~4n...intermediate storage tank, 6n...pipe, 7n...metering pump, n...nozzle. Figure 1 Figure

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ップ弁および多
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
るコンピューターより成り、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 pump installed downstream of the size liquid tank,
A stop valve provided on the outlet side piping of the metering pump and a nozzle equipped with a large number of pores, the density of the size liquid, the discharge amount per unit rotation speed of the metering pump, the inertial rotation speed of the metering pump, and the required weighing weight value. and a computer that calculates and controls the rotational 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 greater than or equal to the cross-sectional area of the piping. A size liquid measuring device characterized in that it is configured as follows.
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 true JPH03233323A (en) 1991-10-17
JPH0450523B2 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 (3)

* 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
JP2015036660A (en) * 2013-08-15 2015-02-23 株式会社▲吉▼本製作所 Liquid mixing apparatus

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51129130U (en) * 1975-04-01 1976-10-19
JPS5318898A (en) * 1976-08-06 1978-02-21 Keiichirou Ishida Caterpillar lumber conveying device in band sawing machine

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51129130U (en) * 1975-04-01 1976-10-19
JPS5318898A (en) * 1976-08-06 1978-02-21 Keiichirou Ishida Caterpillar lumber conveying device in band sawing machine

Cited By (3)

* 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
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
JPH0450523B2 (en) 1992-08-14

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