JPH0423730B2 - - Google Patents

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Publication number
JPH0423730B2
JPH0423730B2 JP59281267A JP28126784A JPH0423730B2 JP H0423730 B2 JPH0423730 B2 JP H0423730B2 JP 59281267 A JP59281267 A JP 59281267A JP 28126784 A JP28126784 A JP 28126784A JP H0423730 B2 JPH0423730 B2 JP H0423730B2
Authority
JP
Japan
Prior art keywords
measuring
pipe
liquid
discharge
mixing container
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
JP59281267A
Other languages
Japanese (ja)
Other versions
JPS61159116A (en
Inventor
Atsuki Wada
Seiichi Numata
Hitoo 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.)
Kurashiki Spinning Co Ltd
Original Assignee
Kurashiki Spinning 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 Kurashiki Spinning Co Ltd filed Critical Kurashiki Spinning Co Ltd
Priority to JP28126784A priority Critical patent/JPS61159116A/en
Publication of JPS61159116A publication Critical patent/JPS61159116A/en
Publication of JPH0423730B2 publication Critical patent/JPH0423730B2/ja
Granted legal-status Critical Current

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  • Weight Measurement For Supplying Or Discharging Of Specified Amounts Of Material (AREA)
  • Accessories For Mixers (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、例えばシリコン等のウエハーの洗浄
液、エツチング液を調製する薬液等、種々の液体
の計量及び混合に供される計量・混合装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a measuring/mixing device used for measuring and mixing various liquids, such as a cleaning liquid for silicon wafers and a chemical liquid for preparing an etching liquid. .

[従来技術] 例えば、シリコンウエハー等の表面処理(洗
浄、エツチング等)のための処理液には、アンモ
ニア、硫酸、塩酸等の洗浄剤と過酸化水素水等の
酸化剤とを所定の比率で混合した混合液が使用さ
れている。このような処理液によつて良好な処理
効果を得るためには混合比を正確に調整する必要
がある。
[Prior art] For example, a processing solution for surface treatment (cleaning, etching, etc.) of silicon wafers, etc. contains a cleaning agent such as ammonia, sulfuric acid, or hydrochloric acid and an oxidizing agent such as hydrogen peroxide in a predetermined ratio. A mixed solution is used. In order to obtain good processing effects using such processing liquids, it is necessary to accurately adjust the mixing ratio.

ところで、洗浄液等の調合に使用される原液に
は腐食性の高いものが多いので、このような原液
を汎用の流量計によつて計量する場合は、流量計
材質から液中に金属イオン等が溶出して液が劣化
を起こすこという問題がある。
By the way, many of the undiluted solutions used to prepare cleaning solutions are highly corrosive, so when measuring such undiluted solutions with a general-purpose flowmeter, metal ions etc. may be present in the solution due to the material of the flowmeter. There is a problem that the solution deteriorates due to elution.

又、各原液を混合する混合容器に原液を一定の
流速で供給し、供給時間を調節することにより各
原液の供給量を制御する方法もあるが、その場合
は、液温(粘度)によつて流速が変化しやすいの
で、正確な計量は期し難い。
There is also a method of supplying each stock solution at a constant flow rate to a mixing container in which each stock solution is mixed, and controlling the supply amount of each stock solution by adjusting the supply time. Since the flow rate tends to change easily, accurate measurement is difficult.

そこで、従来から原液の供給量を重量によつて
計量することが試みられており、その一例として
第3図aに示す如く、台秤1と、該台秤1上に載
置された計量容器2と、送液配管3に接続される
入口管4とを備え、薬液の送給前と送給後の計量
容器2の重量変化量によつて送給された薬液の重
量を計量するようにしたものが知られている。
Therefore, attempts have been made to measure the supply amount of the stock solution by weight, and as an example, as shown in FIG. , and an inlet pipe 4 connected to the liquid feeding pipe 3, and the weight of the fed chemical solution is measured based on the amount of change in the weight of the measuring container 2 before and after the feeding of the chemical solution. It has been known.

ところが、上記の計量装置において、薬液の送
液速度が一定であれば、第3図b中に仮想線で示
す如く、送液開始後、薬液が計量溶器2内の貯留
液5の液面に達する時刻T1以降は、計量容器2
の重量が直線的に増加する筈であるが、実際には
薬液の動荷重及び落下荷重FMが台秤1に作用す
るため、実線で示すように、台秤1によつて測定
される計量容器2の見かけの重量変化量が現実の
重量変化量より大きくなり、しかも重量変化量が
目標地W0に達した時点で開閉バルブ6を閉じて
も、既に入口管4を離れた薬液はそのまま計量容
器2内に落下するので、充分な計量精度が得られ
ないという問題がある。
However, in the above-mentioned measuring device, if the feeding speed of the chemical solution is constant, as shown by the imaginary line in FIG. From time T 1 onwards, measuring container 2
The weight of the weighing container 2 should increase linearly, but in reality, the dynamic load and falling load F M of the chemical solution act on the platform scale 1, so the weight of the weighing container 2 measured by the platform scale 1 increases as shown by the solid line. Even if the on-off valve 6 is closed when the apparent weight change becomes larger than the actual weight change and the weight change reaches the target point W0 , the chemical solution that has already left the inlet pipe 4 remains in the measuring container. There is a problem in that sufficient measurement accuracy cannot be obtained because the sample falls into the container.

又、第4図aに示す如く、密閉式の計量容器7
に固定した入口管8を、送液配管3に接続してな
る計量装置も考えられ、かかる構成は計量容器7
内へのダストの混入を防止する上で好ましい。
Moreover, as shown in FIG. 4a, a closed measuring container 7
It is also possible to consider a metering device in which an inlet pipe 8 fixed to
This is preferable in order to prevent dust from entering the inside.

ところが、第4図aの計量装置においては、第
4図bに示す如く、送液開始後、薬液が液面に到
達する時刻T1以降には、薬液の噴出に伴つて入
口管8に加わる反力FRと、上記した薬液等の動
荷重及び落下荷重FMとが平衡して一時的に重量
変化量に対する影響はなくなるが、目標値W0
達した時点で開閉バルブ6を閉じても上述と同様
に既に入口管8を離れた薬液が計量容器7内に落
下して薬液の供給量が増し、計量値をくるわせる
といつた問題があり、やはり良好な計量精度は得
られない。又、第4図aの計量装置においては、
送液中に台秤1の下方への変位に伴つて、送液配
管3から計量容器7に大きな引張荷重が加わり、
それが台秤1に負荷重として作用して計量精度が
一層低下するという問題がある。
However, in the metering device of FIG. 4a, as shown in FIG. 4b, after the start of liquid feeding, after the time T1 when the chemical liquid reaches the liquid surface, the amount of liquid applied to the inlet pipe 8 as the chemical liquid is jetted out is The reaction force F R and the above-mentioned dynamic load such as the chemical liquid and falling load F M are balanced and temporarily have no effect on the amount of weight change, but when the target value W 0 is reached, the on-off valve 6 is closed. Similarly to the above, there is a problem in that the chemical liquid that has already left the inlet pipe 8 falls into the measuring container 7, increasing the amount of chemical liquid supplied and distorting the measured value, so that good measuring accuracy cannot be obtained. do not have. Furthermore, in the measuring device shown in Fig. 4a,
As the platform scale 1 is displaced downward during liquid feeding, a large tensile load is applied from the liquid feeding pipe 3 to the measuring container 7.
There is a problem in that this acts as a load on the platform scale 1, further reducing measurement accuracy.

[発明の目的] 本発明は上述の問題に鑑みてなされたものであ
つて、台秤を使用して液体を重量によつて計量す
るタイプの計量装置の計量精度を向上させるとと
もに、精度よく計量された液体を効率よく混合し
て必要な成分比を有する液体を調製できるように
することを目的としている。
[Object of the Invention] The present invention has been made in view of the above-mentioned problems, and it improves the measuring accuracy of a type of measuring device that uses a platform scale to measure liquid by weight, and also improves the measuring accuracy of a measuring device that measures liquid by weight using a platform scale. The purpose of this invention is to efficiently mix liquids that have been mixed together to prepare a liquid having the required component ratio.

[発明の構成] このため、本発明では、上部が蓋部材によつて
密閉された計量・混合容器と、固定台上に載置さ
れ、計量・混合容器を載置支持した台秤と、複数
の送液配管に夫々一端が接続され、各他端が計
量・混合容器内の底部に挿入され、各送液配管か
ら送給される液体を計量・混合容器内に流入させ
る複数の入口管と、一端が計量・混合容器内に挿
入され、計量・混合容器内の液体を排出するため
の出口管と、出口管の他端に吸込側が連結された
吐出・循環ポンプと、吐出・循環ポンプの吐出側
に連結され、途中に開閉弁が介設された吐出配管
と、吐出配管の開閉弁により上流側から分岐して
計量・混合容器に至り、途中に開閉弁を介設した
復流配管と、計量・混合容器内の流体の増減にと
もなつて空気を計量・混合容器内に流入もしくは
排出させる手段とを備え、上記複数の入口管、出
口管及び復流配管は、計量・混合容器の上方にお
いて鉛直に配管され、鉛直部の途中は上下方向に
伸縮可能な螺旋管部として形成されるとともに、
各鉛直部は、螺旋管部の上方で固定フレームに固
定支持される一方、螺旋管部の下方で計量・混合
容器の蓋部材に設けた管継手で支持されており、
各入口管から液を供給しつつ台秤によつて供給量
を計量し、各液の供給量が予め設定した量に達し
たときに各液の供給を停止したのち、吐出・循環
ポンプを作動させ、吐出配管の開閉弁を閉じ、復
流配管の開閉弁を開いて、出口管、復流配管の経
路で計量・混合容器内の液を循環させて混合する
ようにしたことを特徴とする液体計量・混合装置
を提供するものである。
[Structure of the Invention] Therefore, in the present invention, a weighing/mixing container whose upper part is sealed by a lid member, a platform scale placed on a fixed stand and supporting the weighing/mixing container, and a plurality of weighing/mixing containers are provided. a plurality of inlet pipes each having one end connected to the liquid feeding pipe and each other end inserted into the bottom of the measuring/mixing container to allow the liquid fed from each liquid feeding pipe to flow into the measuring/mixing container; An outlet pipe whose one end is inserted into the measuring/mixing container and for discharging the liquid in the measuring/mixing container, a discharge/circulation pump whose suction side is connected to the other end of the outlet pipe, and a discharge pipe of the discharge/circulation pump. A discharge pipe that is connected to the side and has an on-off valve interposed in the middle, and a return pipe that branches from the upstream side by the on-off valve of the discharge pipe and reaches the measuring/mixing container, and has an on-off valve interposed in the middle. The plurality of inlet pipes, outlet pipes, and return piping are arranged above the measuring/mixing container, and includes means for causing air to flow into or out of the measuring/mixing container as the fluid in the measuring/mixing container increases or decreases. The pipe is vertically piped, and the middle of the vertical part is formed as a spiral pipe part that can be expanded and contracted in the vertical direction.
Each vertical section is fixedly supported by a fixed frame above the spiral tube section, and supported below the spiral tube section by a pipe joint provided on the lid member of the measuring/mixing container,
While supplying liquid from each inlet pipe, the supply amount is measured using a platform scale, and when the supply amount of each liquid reaches a preset amount, the supply of each liquid is stopped, and then the discharge/circulation pump is activated. A liquid characterized in that the on-off valve of the discharge pipe is closed, the on-off valve of the return flow pipe is opened, and the liquid in the measuring/mixing container is circulated and mixed through the route of the outlet pipe and the return flow pipe. It provides measuring and mixing equipment.

なお、上記台秤としては、例えば電磁力自動平
衡形電子天秤又は、ロードセル形天秤を使用する
ことが好ましい。
As the platform balance, it is preferable to use, for example, an electromagnetic force self-balancing electronic balance or a load cell type balance.

[発明の効果] 本発明によると、各入口管の下端が常時計量・
混合容器内の液に浸漬されるので、薬液等の液体
の落下荷重はなくなり、又各入口管の下端から噴
出される液体の動荷重は、各入口管に加わる反力
と常に平衡するようになる。しかも液体の送給を
停止した後に余分の液体が計量・混合容器に供給
されることがなくなるので、計量・混合容器への
液体の供給量を正確に計量できるようになる。
[Effects of the Invention] According to the present invention, the lower end of each inlet pipe is
Since it is immersed in the liquid in the mixing container, the falling load of liquids such as chemical solutions is eliminated, and the dynamic load of the liquid spouted from the lower end of each inlet pipe is always balanced with the reaction force applied to each inlet pipe. Become. Moreover, since excess liquid is not supplied to the measuring/mixing container after the supply of liquid is stopped, the amount of liquid supplied to the measuring/mixing container can be accurately measured.

又、各入口管、出口管および復流配管の蓋部材
より上方の部分に、計量・混合容器内の液体の増
減に伴う台秤上での計量・混合容器の上下動に追
随して伸縮する螺旋管部を形成するとともに、該
螺旋管部の上方側を固定フレームによつて支持し
たので、入口管の重量を固定フレームで受け合う
ことができ、台秤の変動に伴つて計量・混合容器
が上下動しても螺旋管部の伸縮によつて上下動を
吸収することができるので、多数の管を連結した
場合にも計量・混合容器に大きな引張荷重又は、
圧縮荷重が作用するようなことはなく、従つて計
量精度を一層向上させることができる。
In addition, above the lid member of each inlet pipe, outlet pipe, and return pipe, there is a spiral that expands and contracts as the measuring/mixing container moves up and down on the platform scale as the liquid in the measuring/mixing container increases or decreases. In addition to forming a pipe part, the upper side of the spiral pipe part is supported by a fixed frame, so the weight of the inlet pipe can be received by the fixed frame, and the weighing/mixing container can move up and down as the platform scale changes. Even when moving, the vertical movement can be absorbed by the expansion and contraction of the spiral tube section, so even when many tubes are connected, there is no need to apply large tensile loads to the weighing/mixing container.
No compressive load is applied, and therefore measurement accuracy can be further improved.

更に又、計量・混合容器を密閉式としたので、
計量・混合容器内の液中のダスト等の異物の混入
が防止されるようになり、それにより計量に際し
て液が劣化することがなくなる。
Furthermore, since the measuring and mixing container is a closed type,
This prevents foreign matter such as dust from entering the liquid in the measuring/mixing container, thereby preventing the liquid from deteriorating during measuring.

一方、出口管、吐出・循環ポンプ・復流配管に
よつて循環系を構成したので、計量が終了すると
直ちに液の循環混合が行え、必要な混合比の液を
精度よく調製することができる。
On the other hand, since the circulation system is configured by the outlet pipe, the discharge/circulation pump, and the return piping, the liquid can be circulated and mixed immediately after measurement is completed, and the liquid with the required mixing ratio can be prepared with high precision.

[実施例] 以下、実施例を説明する。[Example] Examples will be described below.

第1図には、シリコン等のウエハーの洗浄液を
調製するための調合装置が示されており、該装置
はアンモニア11を貯留する密閉式の第1貯留容
器12と、該第1貯留容器12にアンモニア11
を補充する密閉式で移動可能な第1補充容器13
と、過酸化水素水を貯留する第2貯留容器(不図
示)と、第2貯留容器に過酸化水素水を補充する
第2補充容器(不図示)と、固定台19上に載置
された台秤14(電磁力自動平衡形電子天秤又は
ロードセル形天秤)上に密閉式の計量・混合容器
15を載置してなり、上記第1貯留容器12、第
2貯留容器及び純水供給口16から供給されるア
ンモニア11、過酸化水素水および純水を夫々計
量して混合する計量・混合装置17と、計量・混
合容器15内で調製された洗浄液18を貯留する
密閉式の第3貯留容器20とから構成されてい
る。なお、計量・混合容器15からウエハーの洗
浄槽(不図示)に直接洗浄液18を供給するよう
にしても良い。
FIG. 1 shows a compounding device for preparing a cleaning solution for wafers such as silicon. Ammonia 11
A sealed and movable first replenishment container 13 for replenishing
, a second storage container (not shown) for storing the hydrogen peroxide solution, a second replenishment container (not shown) for replenishing the second storage container with the hydrogen peroxide solution, and a second storage container (not shown) placed on the fixed base 19. A closed weighing/mixing container 15 is placed on a platform scale 14 (electromagnetic force self-balancing electronic balance or load cell type balance), and the first storage container 12, the second storage container and the pure water supply port 16 are connected to each other. A measuring/mixing device 17 that measures and mixes the supplied ammonia 11, hydrogen peroxide solution, and pure water, respectively, and a third sealed storage container 20 that stores the cleaning liquid 18 prepared in the measuring/mixing container 15. It is composed of. Note that the cleaning liquid 18 may be directly supplied from the measuring/mixing container 15 to a wafer cleaning tank (not shown).

上記第1貯留容器12には、予め設定されたア
ンモニア11の液面の上限レベルL1と下限レベ
ルL2とを検出する検知装置21,22が設置さ
れ、アンモニア11の液面が常時上限レベルL1
と下限レベルL2との間に位置するように、第1
補充容器13から、アンモニア11の流通状況を
検出する液体検出器23を有する送液配管24を
通して、送液ポンプ25(空気駆動式のベローズ
ポンプ)によつてアンモニア11が供給されるよ
うになつている。該送液ポンプ25は、駆動用空
気供給口26から圧力調節器27及び圧力計28
が介設された空気配管30を通して供給される圧
縮空気により駆動される。
Detectors 21 and 22 are installed in the first storage container 12 to detect a preset upper limit level L 1 and lower limit level L 2 of the ammonia 11 liquid level, so that the ammonia 11 liquid level is always at the upper limit level. L 1
and the lower limit level L2 .
Ammonia 11 is now supplied from the replenishment container 13 by a liquid feeding pump 25 (air-driven bellows pump) through a liquid feeding pipe 24 having a liquid detector 23 for detecting the distribution status of ammonia 11. There is. The liquid feeding pump 25 connects a driving air supply port 26 to a pressure regulator 27 and a pressure gauge 28.
It is driven by compressed air supplied through an air pipe 30 with an interposed air pipe.

又、第1貯留容器12内のアンモニア11は、
圧送用ガス供給口31から、圧力調節器32、ガ
スフイルタ33及び圧力計34が介設されたガス
配管35を通して送給される高圧ガス(空気、窒
素等)により、送液配管36及び入口管37を通
して計量・混合容器15に供給されるようになつ
ている。
Moreover, the ammonia 11 in the first storage container 12 is
High-pressure gas (air, nitrogen, etc.) is supplied from the pressurized gas supply port 31 through a gas pipe 35 in which a pressure regulator 32, a gas filter 33, and a pressure gauge 34 are installed, and the liquid supply pipe 36 and the inlet pipe 37 are It is designed to be supplied to the measuring/mixing container 15 through the pipe.

上記入口管37は、計量・混合容器15の上部
を密閉する蓋部材38の上方に設けられた螺旋管
40の下端と計量・混合容器15内に配設された
直管41の上端とを蓋部材38に固定した管継手
42で接続してなるもので、上記螺旋管40は計
量・混合容器15内の液の増減による台秤14上
での計量・混合容器15の上下動を吸収し得るよ
うに、テフロン等の樹脂で伸縮可能に形成されて
いる。
The inlet pipe 37 connects the lower end of a spiral pipe 40 provided above a lid member 38 that seals the upper part of the measuring/mixing container 15 and the upper end of a straight pipe 41 disposed inside the measuring/mixing container 15. The spiral pipe 40 is connected to a member 38 by a pipe joint 42 fixed to the member 38, and the spiral pipe 40 is designed to absorb vertical movement of the weighing/mixing container 15 on the platform scale 14 due to increase or decrease of liquid in the weighing/mixing container 15. It is made of resin such as Teflon so that it can expand and contract.

上記螺旋管40の長手方向の中心線は鉛直方向
を向けられており、該螺旋管40の上端は、前記
固定台19の台秤14の両側方位置に立設した固
定フレーム43,43間に横架されたバー44上
の管継手45を介して送液配管36に接続される
とともに、螺旋管40の上、下端は上記中心線上
に位置している。
The longitudinal center line of the spiral tube 40 is oriented in the vertical direction, and the upper end of the spiral tube 40 is located between the fixed frames 43, 43, which are erected on both sides of the platform scale 14 of the fixed table 19. It is connected to the liquid feeding pipe 36 via a pipe joint 45 on the suspended bar 44, and the upper and lower ends of the spiral pipe 40 are located on the center line.

一方、噴射ノズルを形成する直管41の下端
は、常時計量・混合容器15内の液中に浸漬され
るように、計量・混合容器15の底部15a近傍
に位置している。すなわち計量・混合容器15に
は、入口管37の直管41の下端より高い下限レ
ベルL3が設定され、計量・混合容器15内の液
面レベルが下限レベルL3以下にならないように、
台秤14の出力信号、つまり計量・混合容器15
の重量に基づいて、計量・混合容器15からの液
の吐出量が制限される。
On the other hand, the lower end of the straight pipe 41 forming the injection nozzle is located near the bottom 15a of the measuring/mixing container 15 so as to be immersed in the liquid in the measuring/mixing container 15 at all times. That is, a lower limit level L 3 higher than the lower end of the straight pipe 41 of the inlet pipe 37 is set in the metering/mixing container 15 so that the liquid level in the metering/mixing container 15 does not fall below the lower limit level L 3 .
The output signal of the platform scale 14, that is, the weighing/mixing container 15
Based on the weight of the liquid, the amount of liquid discharged from the measuring/mixing container 15 is limited.

第1貯留容器12から計量・混合容器15への
アンモニア11の供給量は、アンモニア11の供
給前と供給後の計量・混合容器15の重量変化量
として台秤14により測定される。本実施例で
は、入口管37の直管41の下端が常時計量・混
合容器15内の液に浸漬されるので、アンモニア
11の供給時に、アンモニア11の落下荷重はな
くなり、又アンモニア11の動荷重と直管41に
加わる反力とが相殺されるので、例えばアンモニ
ア11の送液速度が一定であれば、計量・混合容
器15の重量は第2図に示す如く直線的に増加
し、計量・混合容器15の重量変化量が目標値
W0に達した時点で送液配管36に介設した開閉
バルブ46を閉じると、計量・混合容器15への
アンモニア11の供給は直ちに停止されるように
なり、供給量を正確に測定することができる。
The amount of ammonia 11 supplied from the first storage container 12 to the measuring/mixing container 15 is measured by the platform scale 14 as the amount of change in the weight of the measuring/mixing container 15 before and after the ammonia 11 is supplied. In this embodiment, since the lower end of the straight pipe 41 of the inlet pipe 37 is constantly immersed in the liquid in the metering/mixing container 15, the falling load of the ammonia 11 is eliminated when the ammonia 11 is supplied, and the dynamic load of the ammonia 11 is eliminated. Since the reaction force applied to the straight pipe 41 is canceled out by the reaction force applied to the straight pipe 41, for example, if the feeding speed of the ammonia 11 is constant, the weight of the measuring/mixing container 15 increases linearly as shown in FIG. The amount of weight change of the mixing container 15 is the target value
When the on-off valve 46 installed in the liquid supply pipe 36 is closed when W 0 is reached, the supply of ammonia 11 to the measuring/mixing container 15 is immediately stopped, making it possible to accurately measure the supply amount. I can do it.

一方、過酸化水素水は、前記第2貯留容器から
送液用配管47及び螺旋管48と直管49からな
る入口管50を介して、また純水は、純水供給口
16から圧力調節器51を有する純水配管52及
び螺旋管53と直管54からなる入口管55を介
して夫々計量・混合容器15に供給され、上述と
同様の方法で夫々計量されたアンモニア11と、
過酸化水素水と、純水とが所定の混合比で混合さ
れる。上記両直管49,54の下端は、直管41
と同様、下限レベルL3より下方に位置している。
On the other hand, the hydrogen peroxide solution is supplied from the second storage container via the liquid supply pipe 47 and the inlet pipe 50 consisting of a spiral pipe 48 and a straight pipe 49, and pure water is supplied from the pure water supply port 16 to the pressure regulator. 51 and an inlet pipe 55 consisting of a spiral pipe 53 and a straight pipe 54, respectively, to the metering/mixing container 15, and each metered ammonia 11 in the same manner as described above;
Hydrogen peroxide and pure water are mixed at a predetermined mixing ratio. The lower ends of both the straight pipes 49 and 54 are connected to the straight pipe 41.
Similarly, it is located below the lower limit level L3 .

上述の混合液は、直管56と螺旋管57からな
る出口管58に連続して計量・混合容器15と第
3貯留容器20とを連絡する吐出配管60の一部
と、螺旋管61に接続される復流配管62とによ
り形成される計量・混合容器15を含む循環路6
3内で、循環・吐出ポンプ(ベローズポンプ)6
4の吸引力と吐出力によつて循環されて撹拌さ
れ、均一な組成の洗浄液18が調製される。な
お、吐出管60と復流配管62には、分岐部の下
流に夫々開閉弁71,72を介設し、循環時に
は、開閉弁71を閉、開閉弁72を開とする。
又、循環中に流体フイルタ65によつて洗浄液1
8か濾過されて不純物が除去されると共に、熱交
換器66により洗浄液18の液温が調整される。
そして充分に撹拌、濾過された洗浄液18が吐出
配管60を通して第3貯留容器20もしくは前述
の洗浄槽に移送される。計量・混合容器15から
第3貯留容器20又は洗浄槽への洗浄液18の供
給量は台秤14によつて計量される。
The above-mentioned liquid mixture is connected to a spiral pipe 61 and a part of a discharge pipe 60 that connects the measuring/mixing container 15 and the third storage container 20 continuously to an outlet pipe 58 consisting of a straight pipe 56 and a spiral pipe 57. A circulation path 6 including a measuring/mixing container 15 formed by a return flow pipe 62
3, circulation/discharge pump (bellows pump) 6
The washing liquid 18 is circulated and stirred by the suction force and discharge force of No. 4, and a cleaning liquid 18 having a uniform composition is prepared. Note that the discharge pipe 60 and the return flow pipe 62 are provided with on-off valves 71 and 72, respectively, downstream of the branch part, and during circulation, the on-off valve 71 is closed and the on-off valve 72 is opened.
Also, during the circulation, the cleaning liquid 1 is removed by the fluid filter 65.
The cleaning liquid 18 is filtered to remove impurities, and the temperature of the cleaning liquid 18 is adjusted by a heat exchanger 66.
The thoroughly stirred and filtered cleaning liquid 18 is then transferred to the third storage container 20 or the aforementioned cleaning tank through the discharge pipe 60. The amount of cleaning liquid 18 supplied from the measuring/mixing container 15 to the third storage container 20 or the cleaning tank is measured by the platform balance 14.

上記計量・混合容器15には、通気フイルタ6
7が介設された給排気管68が備えられ、計量・
混合容器15への液の給排に伴つて計量・混合容
器15に空気が供給又は、排出されるようになつ
ている。
The measuring/mixing container 15 is equipped with a ventilation filter 6.
7 is provided with an air supply and exhaust pipe 68 for measuring and
Air is supplied to or discharged from the measuring/mixing container 15 as liquid is supplied to or discharged from the mixing container 15.

なお、計量・混合容器15への液の給排による
台秤14の上下変位量は、計量・混合容器15の
容量にもよるが、台秤14として電磁力自動平衡
形電子天秤、ロードセル形天秤のいずれを使用す
る場合も通常高々数mmと僅かであり(電磁力自動
平衡形電子天秤は基準高さを有し、常時この高さ
となるように制御されるが、大きな荷重変動があ
つた場合には、平衡に達するまでに若干の変動を
繰返す。)、しかもこの上下変位に際して、各送液
配管36,47、純水配管52、吐出配管60及
び復流配管62から計量・混合容器15に引張又
は、圧縮荷重が作用することはなく、各螺旋管4
0,48,53,57,61から微弱な引張又は
圧縮荷重が作用するのみであるので、台秤14の
上下変位の計量精度への影響は極めて僅かであ
る。
The amount of vertical displacement of the platform scale 14 due to the supply and discharge of liquid to and from the weighing/mixing container 15 depends on the capacity of the weighing/mixing container 15, but the platform scale 14 may be either an electromagnetic force automatic balance type electronic balance or a load cell type balance. (Electromagnetic force self-balancing electronic balances have a reference height and are always controlled to this height, but if there is a large load fluctuation, , some fluctuations are repeated until equilibrium is reached), and during this vertical displacement, tension or , no compressive load acts, and each helical tube 4
Since only a weak tensile or compressive load is applied from 0, 48, 53, 57, and 61, the vertical displacement of the platform scale 14 has very little effect on the measurement accuracy.

その場合、上部支持バー44の支持高さは、各
管に液を流したときの螺旋管部の伸びを含んだ各
管の自然長(即ち、上部支持バー44から蓋部材
38までの長さ)に等しく設定することが好まし
く、その場合には、各管は液を流した状態で平衡
状態となるので、計量時において、計量・混合容
器の上下動に伴なう引張・圧縮力以外に余分な力
が螺旋管部に発生することはない。
In that case, the support height of the upper support bar 44 is the natural length of each tube (i.e., the length from the upper support bar 44 to the lid member 38 ) is preferable. In that case, each tube will be in an equilibrium state with liquid flowing, so when measuring, there will be no force other than the tensile and compressive forces associated with the vertical movement of the measuring and mixing container. No extra forces are generated in the helical tube section.

そのうえ、上記の如き電子天秤やロードセル形
天秤を用いた場合、計量・混合容器の上下動はご
く微小で無視できる程度であり、全体として、よ
り一層計量精度の向上を図ることができる。
Furthermore, when an electronic balance or a load cell type balance as described above is used, the vertical movement of the weighing/mixing container is extremely small and can be ignored, making it possible to further improve the weighing accuracy as a whole.

なお、上記の実施例では、計量・混合装置17
によりアンモニア11と過酸化水素水と純水とを
混合してシリコンウエハーの表面の洗浄液を調合
する場合を説明したが、計量・混合装置17はシ
リコンウエハーの処理液の調合に限らずその他の
各種の薬液等の調合にも使用でき、又、複数の薬
液等を混合する場合のみならず、単一の薬液等の
計量装置としても使用しうることは言うまでもな
い。
In addition, in the above embodiment, the measuring/mixing device 17
Although the case where ammonia 11, hydrogen peroxide solution, and pure water are mixed to prepare a cleaning liquid for the surface of a silicon wafer has been explained, the measuring/mixing device 17 is not limited to mixing a processing liquid for silicon wafers, but can also be used for various other purposes. Needless to say, it can be used not only for mixing a plurality of medicinal solutions, but also as a measuring device for a single medicinal solution.

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

第1図は本発明に係る計量・混合装置を備えた
シリコンウエハーの洗浄液の調合装置の全体説明
図、第2図は第1図中の計量・混合装置における
計量開始後の時間と計量容器の重量変化量との関
係を示すグラフ、第3図aは第1従来例の説明
図、第3図bは第1従来例の第2図に対応するグ
ラフ、第4図aは第2従来例の説明図、第4図b
は第2従来例の第2図に対応するグラフである。 11……アンモニア(液体)、14……台秤、
15……計量・混合容器、15a……底部、19
……固定台、36,47,52……送液配管、3
7,50,55……入口管、38……蓋部材、4
0,48,53……螺旋管部、43……固定フレ
ーム、58……出口管、60……吐出配管、62
……復流配管、63……循環路、64……吐出・
循環ポンプ、68……給排気管、71,72……
開閉弁。
Fig. 1 is an overall explanatory diagram of a silicon wafer cleaning liquid preparation device equipped with a measuring/mixing device according to the present invention, and Fig. 2 shows the time after the start of measurement in the measuring/mixing device shown in Fig. 1 and the time of measuring containers. Graph showing the relationship with the amount of weight change, Figure 3a is an explanatory diagram of the first conventional example, Figure 3b is a graph corresponding to Figure 2 of the first conventional example, Figure 4a is the second conventional example Explanatory diagram of Figure 4b
is a graph corresponding to FIG. 2 of the second conventional example. 11... Ammonia (liquid), 14... Platform scale,
15...Measuring/mixing container, 15a...Bottom, 19
...Fixing stand, 36, 47, 52...Liquid delivery piping, 3
7, 50, 55... Inlet pipe, 38... Lid member, 4
0, 48, 53...Spiral tube part, 43...Fixed frame, 58...Outlet pipe, 60...Discharge piping, 62
...Return piping, 63...Circulation path, 64...Discharge/
Circulation pump, 68... Supply/exhaust pipe, 71, 72...
Open/close valve.

Claims (1)

【特許請求の範囲】 1 上部が蓋部材によつて密閉された計量・混合
容器と、 固定台上に載置され、計量・混合容器を載置支
持した台秤と、 複数の送液配管に夫々一端が接続され、各他端
が計量・混合容器内の底部に挿入され、各送液配
管から送給される液体を計量・混合容器内に流入
させる複数の入口管と、 一端が計量・混合容器内に挿入され、計量・混
合容器内の液体を排出するための出口管と、 出口管の他端に吸込側が連結された吐出・循環
ポンプと、吐出・循環ポンプの吐出側に連結さ
れ、途中に開閉弁が介設された吐出配管と、 吐出配管の開閉弁により上流側から分岐して計
量・混合容器に至り、途中に開閉弁を介設した復
流配管と、 計量・混合容器内の流体の増減にともなつて空
気を計量・混合容器内に流入もしくは排出させる
手段とを備え、 上記複数の入口管、出口管及び復流配管は、計
量・混合容器の上方において鉛直に配管され、鉛
直部の途中は上下方向に伸縮可能な螺旋管部とし
て形成されるとともに、各鉛直部は、螺旋管部の
上方で固定フレームに固定支持される一方、螺旋
管部の下方で計量・混合容器の蓋部材に設けた管
継手で支持されており、 各入口管から液を供給しつつ台秤によつて供給
量を計量し、各液の供給量が予め設定した量に達
したときに各液の供給を停止したのち、吐出・循
環ポンプを作動させ、吐出配管の開閉弁を閉じ、
復流配管の開閉弁を開いて、出口管、復流配管の
経路で計量・混合容器内の液を循環させて混合す
るようにしたことを特徴とする液体の計量・混合
装置。 2 上記台秤が電磁力自動平衡形電子天秤又はロ
ードセル形天秤であることを特徴とする特許請求
の範囲第1項記載の液体の計量・混合装置。
[Scope of Claims] 1. A measuring/mixing container whose upper part is sealed by a lid member, a platform scale placed on a fixed stand and supporting the measuring/mixing container, and a plurality of liquid feeding pipes, respectively. A plurality of inlet pipes, each of which is connected at one end and inserted into the bottom of the metering/mixing vessel at the other end, allows the liquid delivered from each liquid delivery pipe to flow into the metering/mixing vessel; An outlet pipe inserted into the container to discharge the liquid in the measuring/mixing container, a discharge/circulation pump whose suction side is connected to the other end of the outlet pipe, and a discharge/circulation pump connected to the discharge side of the discharge/circulation pump. A discharge pipe with an on-off valve in the middle, a return pipe that branches from the upstream side using the on-off valve in the discharge pipe and reaches the measuring/mixing container, and a return pipe with an on-off valve in the middle, and inside the measuring/mixing container. The plurality of inlet pipes, outlet pipes, and return piping are vertically piped above the measuring and mixing container. The middle part of the vertical part is formed as a spiral pipe part that can be expanded and contracted in the vertical direction, and each vertical part is fixedly supported by a fixed frame above the spiral pipe part, while measuring and mixing is carried out below the spiral pipe part. It is supported by a pipe joint installed on the lid of the container, and while supplying liquid from each inlet pipe, the supply amount is measured using a platform scale, and when the supply amount of each liquid reaches a preset amount, each After stopping the supply of liquid, operate the discharge/circulation pump, close the on-off valve of the discharge piping,
A liquid measuring/mixing device characterized in that an on-off valve of a return flow pipe is opened to circulate and mix the liquid in a measuring/mixing container through an outlet pipe and a return flow pipe route. 2. The liquid measuring and mixing device according to claim 1, wherein the platform scale is an electromagnetic force self-balancing electronic balance or a load cell type balance.
JP28126784A 1984-12-28 1984-12-28 Weighing equipment for liquid Granted JPS61159116A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28126784A JPS61159116A (en) 1984-12-28 1984-12-28 Weighing equipment for liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28126784A JPS61159116A (en) 1984-12-28 1984-12-28 Weighing equipment for liquid

Publications (2)

Publication Number Publication Date
JPS61159116A JPS61159116A (en) 1986-07-18
JPH0423730B2 true JPH0423730B2 (en) 1992-04-23

Family

ID=17636688

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28126784A Granted JPS61159116A (en) 1984-12-28 1984-12-28 Weighing equipment for liquid

Country Status (1)

Country Link
JP (1) JPS61159116A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5705615B2 (en) * 2011-03-30 2015-04-22 株式会社Screenホールディングス Coating apparatus and coating liquid coating method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5979815A (en) * 1982-10-29 1984-05-09 Toyota Motor Corp Measuring apparatus for engine oil consumption

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5979815A (en) * 1982-10-29 1984-05-09 Toyota Motor Corp Measuring apparatus for engine oil consumption

Also Published As

Publication number Publication date
JPS61159116A (en) 1986-07-18

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