JPS60120219A - Flow-rate measuring device for clean draft - Google Patents

Flow-rate measuring device for clean draft

Info

Publication number
JPS60120219A
JPS60120219A JP22858183A JP22858183A JPS60120219A JP S60120219 A JPS60120219 A JP S60120219A JP 22858183 A JP22858183 A JP 22858183A JP 22858183 A JP22858183 A JP 22858183A JP S60120219 A JPS60120219 A JP S60120219A
Authority
JP
Japan
Prior art keywords
flow rate
clean
exhaust duct
fluid resistance
pressure
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
JP22858183A
Other languages
Japanese (ja)
Other versions
JPS6338647B2 (en
Inventor
Shigeharu Hanajima
花島 重春
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.)
DAN KAGAKU KK
Original Assignee
DAN KAGAKU KK
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 DAN KAGAKU KK filed Critical DAN KAGAKU KK
Priority to JP22858183A priority Critical patent/JPS60120219A/en
Publication of JPS60120219A publication Critical patent/JPS60120219A/en
Publication of JPS6338647B2 publication Critical patent/JPS6338647B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01FMEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F1/00Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow
    • G01F1/05Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects
    • G01F1/34Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by using mechanical effects by measuring pressure or differential pressure

Abstract

PURPOSE:To enhance reliability and to reduce cost, by providing a measuring part comprising a specified resistance bridge between a blower discharge port and an exhaust duct, detecting static pressure and total pressure in the exhaust duct and the discharge pressure of the blower, and guiding the values to the measuring part. CONSTITUTION:A blower-discharge-pressure detecting pipe 12 is connected to one end of a fluid resistance bridge 11 and attached in the vicinity of a discharge port 10 of an upper blower (not shown) of an air filter 2 of an etching tank 1 in a clean draft 9. The pipe 12 is branched into pipes 15 and 16 through the bridge 11. The end parts thereof are coupled to static pressure and total pressure detecting pipes 13 and 14 which are arranged in an exhaust duct 4. Fluid resistors ra, rc, rb and rd are provided in the pipes 15 and 16, respectively. A point A between the resistors ra and rc and a point B between the resistors rb and rd are connected by a branch pipe 17 having a fluid resistor rg. A flow speed sensor 18 is provided in the pipe 17. Thus mixing of corrosive vapor and mist into the bridge 11 can be prevented.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明はクリーンドラフトの排気状態を管理するクリー
ンドラフトの流量計測装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a clean draft flow rate measuring device for managing the exhaust state of a clean draft.

〔発明の背景〕[Background of the invention]

半導体装置の製造工程では、強酸、強アルカリまたは弗
化水素酸などの薬品による化学エツチング加工がしばし
ば使用される。これらの加工工程は当然激しい腐蝕性蒸
気やミストの発散を伴うので、上記腐蝕性蒸気やミスト
な安全かつ確実に排出しなければならない。しかも作業
空間は極めて清浄な空気で満されている必要があるため
に、通常、いわゆるクリーンドラフトが使用される。
In the manufacturing process of semiconductor devices, chemical etching using chemicals such as strong acids, strong alkalis, or hydrofluoric acid is often used. Since these processing steps naturally involve the emission of intense corrosive vapor and mist, the corrosive vapor and mist must be safely and reliably discharged. Moreover, since the work space must be filled with extremely clean air, a so-called clean draft is usually used.

クリーンドラフトは第1図の構成図に示すように、エツ
チング槽1の上部に高性能のエアフィルタ2を設け、清
浄空気送風ブロア3によって送り込まれ上記エアフィル
タ2を通過した清浄空気を絶えず供給しつつ、工7チン
グ槽1から発生ずる腐蝕性蒸気やミストなりジー/ドラ
フト後面の排気ダクト4からダンパ5およびp過装置6
を経て排気ブロアマにより強制排気する。上記クリーン
ドラフトの排気流量が適正である場合には、第2図に示
すようにエアフィルタ2を通過した清浄空気の一部はク
リーンドラフトの前面にエアカーテン8を形成し、かつ
エツチング槽1から発生する腐蝕性蒸気やミスト(図中
に破線で示す)はすべて排気ダクト4から排出される。
As shown in the block diagram of FIG. 1, the clean draft is equipped with a high-performance air filter 2 above an etching tank 1, and constantly supplies clean air that is sent by a clean air blower 3 and passed through the air filter 2. At the same time, corrosive steam and mist are generated from the cooling tank 1 and the exhaust duct 4 on the rear surface of the gee/draft to the damper 5 and the filtration device 6.
After that, the air is forcibly exhausted by an exhaust blower. When the exhaust flow rate of the clean draft is appropriate, a part of the clean air that has passed through the air filter 2 forms an air curtain 8 in front of the clean draft, as shown in FIG. All of the generated corrosive vapor and mist (indicated by broken lines in the figure) are exhausted from the exhaust duct 4.

もし上記排気流量が過小である場合には、第3図に示す
ようにエツチング槽1からの腐蝕性蒸気やミストの一部
は清浄空気流に混入して工場内に拡散し極めて危険であ
る。またクリーンドラフトの排気流量が過大である場合
は、第4図に示すように工場内の塵埃が多い空気をクリ
ーンドラフトの前面開口部から導入し、この塵埃が多い
空気が混入した清浄空気がエツチング槽1に流入するた
め、製品に欠陥を生じ著しく生産性が低下することにな
る。
If the exhaust flow rate is too small, some of the corrosive vapor and mist from the etching bath 1 will mix with the clean air flow and spread into the factory, as shown in FIG. 3, which is extremely dangerous. In addition, if the exhaust flow rate of the clean draft is excessive, as shown in Figure 4, the dusty air from inside the factory is introduced through the front opening of the clean draft, and the clean air mixed with this dusty air is used for etching. Since it flows into the tank 1, it causes defects in the product and significantly reduces productivity.

上記のようにクリーンドラフトを使用するに際し排気流
量の適正化が最重要であるが、多量の強腐蝕性蒸気やミ
ストを取扱う排気流量の計測には、従来信頼性が大きく
しかも安価な設備が得られなかった。
As mentioned above, optimization of the exhaust flow rate is most important when using a clean draft, but conventionally reliable and inexpensive equipment has been used to measure the exhaust flow rate when handling large amounts of highly corrosive steam and mist. I couldn't.

〔発明の目的〕[Purpose of the invention]

本発明は適正な排気状態を維持管理するため、信頼性が
大きく安価なりリーンドラフトの流量計測装置を得るこ
とを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a lean draft flow rate measuring device that is highly reliable and inexpensive in order to maintain and manage appropriate exhaust conditions.

〔発明の概要〕[Summary of the invention]

上記目的を達成するために本発明によるクリーンドラフ
トの流量計測装置は、クリーンドラフトの排気ダクト内
の静圧および全圧、ならびに清浄空気送風ブロアの吐出
圧とをそれぞれ検出して計測部に導く配管系と、上記清
浄空気送風ブロアの吐出口と排気ダクトとの間に設けた
流体抵抗と流速センサとで構成される流体抵抗ブリッジ
よりなる計測部とを備えたものである。
In order to achieve the above object, the clean draft flow rate measuring device according to the present invention detects the static pressure and total pressure in the exhaust duct of the clean draft, and the discharge pressure of the clean air blower, and leads the piping to the measuring section. and a measuring section consisting of a fluid resistance bridge constituted by a fluid resistance and a flow rate sensor provided between the discharge port of the clean air blower and the exhaust duct.

〔発明の実施例〕[Embodiments of the invention]

つぎに本発明の実施例を図面とともに説明する第5図は
本発明によるクリーンドラフトの流量計測装置の一実施
例の構成を示す図、第6図は排気ダクト内のアスピレー
ション吸引圧(負の動圧)リーンドラフト9内のエツチ
ング槽1の上部に高性能のエアフィルタ2を設け、該エ
アフィルタ2の上部に位置する送風ブロア(図示せず)
からの空気の吐出口10付近に流体抵抗ブリッジ11の
一端に連結された送風ブロア吐出圧検出管12を取付は
上記流体抵抗プリンジ11の他端はそれぞれ静圧検出管
13および全圧検出管14と連結し、クリーンドラフト
9の後部から導かれた排気ダクト4内に導入されている
Next, an embodiment of the present invention will be explained with drawings. Figure 5 is a diagram showing the configuration of an embodiment of the clean draft flow rate measuring device according to the present invention, and Figure 6 is a diagram showing the aspiration suction pressure (negative Dynamic pressure) A high-performance air filter 2 is provided above the etching tank 1 in the lean draft 9, and a blower (not shown) is located above the air filter 2.
A blower discharge pressure detection tube 12 connected to one end of the fluid resistance bridge 11 is installed near the air discharge port 10 from the fluid resistance bridge 11.The other end of the fluid resistance bridge 11 is connected to a static pressure detection tube 13 and a total pressure detection tube 14, respectively. and is introduced into the exhaust duct 4 led from the rear of the clean draft 9.

上記流体抵抗ブリッジ11は送風ブロア吐出圧検出管1
2から、静圧検出管13に連結する流体抵抗rlLとr
。とを有する配管15および全圧検出管14に連結する
流体抵抗rbとrdとを有する配管16に分れ、上記2
つの配管15および16における流体抵抗raとroと
の間のA点と流体抵抗rbとrdとの間のB点とは流体
抵抗rgを有する枝管17で結ばれ、該枝管17内には
流速センサ18が設けられている。
The fluid resistance bridge 11 is the blower discharge pressure detection tube 1
2, the fluid resistances rlL and r connected to the static pressure detection tube 13
. and a pipe 16 having fluid resistances rb and rd connected to the total pressure detection pipe 14.
A point A between fluid resistances ra and ro and a point B between fluid resistances rb and rd in the two pipes 15 and 16 are connected by a branch pipe 17 having a fluid resistance rg. A flow rate sensor 18 is provided.

上記クリーンドラフト9の流量計測装置において最も空
気の圧力が高(・のは送風ブロア吐出圧検出管12の送
風ブロア吐出圧である。従って空気の流れは送風ブロア
検出管12から流体抵抗プリノジ■■を経て静圧検出管
13および全圧検出管14へと流れる。流体抵抗raが
rbに等しく、流体抵抗r。がrdに等しくて排気流量
がゼロの場合は、上記静圧検出管13の圧力と全圧検出
管14の圧力とは等しくなり、流体抵抗ブリッジ11は
平衡状態となり上記枝管17に空気の流れはなく、上記
吐出圧検出管12を通過した空気が静圧検出管13と全
圧検出管14とから排気ダクト4内に流れる。
In the flow measuring device of the clean draft 9, the highest air pressure (・ is the blower discharge pressure of the blower discharge pressure detection tube 12. Therefore, the air flow is from the blower detection tube 12 to the fluid resistance pre-noise. to the static pressure detection tube 13 and the total pressure detection tube 14. When the fluid resistance ra is equal to rb, the fluid resistance r is equal to rd, and the exhaust flow rate is zero, the pressure in the static pressure detection tube 13 is and the pressure in the total pressure detection tube 14 become equal, the fluid resistance bridge 11 becomes in an equilibrium state, and there is no air flow in the branch pipe 17, and the air that has passed through the discharge pressure detection tube 12 reaches the static pressure detection tube 13 and the total pressure. It flows from the pressure detection pipe 14 into the exhaust duct 4.

排気ブロア(図示せず)が動作して排気ダクト4内に第
5図の矢印で示す方向に流量が存在する場合には、全圧
検出管14の圧力は静圧検出管13の圧力より動圧だけ
高くなり、前記枝管17にはB点からA点に向う空気の
流れを生じ、排気ダクト4中の流量に関連した通常の空
気の流量が流速センサ18によって検出される。
When the exhaust blower (not shown) operates and a flow exists in the exhaust duct 4 in the direction indicated by the arrow in FIG. The pressure increases, causing an air flow in the branch pipe 17 from point B to point A, and the normal air flow rate related to the flow rate in the exhaust duct 4 is detected by the flow rate sensor 18.

もし送風ブロア吐出圧検出管12の圧力よりも排気ダク
ト4内の排気全圧力の方が高くなるような場合には、全
圧検出管I4がら静圧検出管】3へ向う空気の流れが発
生し、流体抵抗ブリッジ110枝管17においてはA点
からB点に空気が流れるおそれがある。このようなおそ
れがある場合には、第6図に示すように排気ダクト4内
における全圧検出管14′の先端を排気ダクト4の下流
の方向に曲げ、アスピレーション吸引圧(負の動圧)を
利用するようにすれば、クリーンドラフト9内のエツチ
ング槽1で発生した腐蝕性蒸気やミストが混入した空気
を流体抵抗ブリッジ11が吸引するのを防ぐことができ
る。上記のアスビレーション吸引圧を利用する場合には
、流体抵埃ブリッジ11の枝管17にA点からB点に向
う適正運転時とは逆の方向に通常の空気が流れる。
If the total exhaust pressure in the exhaust duct 4 becomes higher than the pressure in the blower discharge pressure detection tube 12, air flows from the total pressure detection tube I4 toward the static pressure detection tube 3. However, in the fluid resistance bridge 110 branch pipe 17, there is a possibility that air may flow from point A to point B. If there is such a possibility, bend the tip of the total pressure detection tube 14' in the exhaust duct 4 in the downstream direction of the exhaust duct 4 as shown in FIG. ), it is possible to prevent the fluid resistance bridge 11 from sucking in air mixed with corrosive vapor or mist generated in the etching tank 1 in the clean draft 9. When using the above-mentioned asvilation suction pressure, normal air flows through the branch pipe 17 of the fluid resistance bridge 11 in the opposite direction from point A to point B during proper operation.

なお第7図は計測部における流体抵抗ブリッジ11の一
具体例を示した断面図であるが、各流体抵抗ra、rb
、r0、r6はそれぞれニードル弁を用いて抵抗値の調
整ができるようにしている。(枝管17の流体抵抗rg
は省略しである。)同図における19、加、21はそれ
ぞれ吐出圧検出管、静圧検出管、全圧検出管の連結口で
ある。
Note that FIG. 7 is a sectional view showing a specific example of the fluid resistance bridge 11 in the measurement section, and each fluid resistance ra, rb
, r0, and r6 each use a needle valve so that the resistance value can be adjusted. (Fluid resistance rg of branch pipe 17
is omitted. ) Reference numerals 19, 21, and 21 in the figure are connection ports for the discharge pressure detection tube, static pressure detection tube, and total pressure detection tube, respectively.

上記のように実施例に示すクリーンドラフト9の流体計
測装置は計測部の流体抵抗ブリッジ11に腐蝕性蒸気や
ミストが混入した空気が流入するおそれがないため、上
記流体抵抗ブリッジ11の枝管17に挿入する流速セン
サ18はその耐蝕性を考慮する必要がなく、排気ダクト
4および排気ダクト4内に挿入される配管だけを耐蝕性
があるものにすればよい。
As described above, in the clean draft 9 fluid measuring device shown in the embodiment, there is no risk of air mixed with corrosive vapor or mist flowing into the fluid resistance bridge 11 of the measurement section. There is no need to consider the corrosion resistance of the flow rate sensor 18 inserted into the exhaust duct 4, and it is sufficient to make only the exhaust duct 4 and the piping inserted into the exhaust duct 4 corrosion resistant.

なお排気ダクト4の全圧が常に大気圧より負圧であるな
らば、(はとんどの場合はこの条件が成立する)第5図
および第6図における送風ブロア吐出圧検出管12を送
風ブロア吐出口10近傍に接続することなく、大気中に
開放してもよい。
Note that if the total pressure of the exhaust duct 4 is always negative than atmospheric pressure (this condition holds in most cases), the blower discharge pressure detection pipe 12 in FIGS. 5 and 6 is connected to the blower. It may be opened to the atmosphere without being connected to the vicinity of the discharge port 10.

〔発明の効果〕〔Effect of the invention〕

上記のように本発明によるクリーンドラフトの流量計測
装置は、クリーンドラフトの排気ダクト内の静圧および
全圧、ならびに清浄空気送風ブロアの吐出圧とをそれぞ
れ検出して計測部に導く配管系と、上記清浄空気送風ブ
ロアの吐出口と排気ダクトとの間に設けた流体抵抗と流
速センサとで構成される流体抵抗ブリッジよりなる計測
部とを備えたことにより、腐蝕性蒸気やミストが混入し
1こ空気を上記流体抵抗ブリッジ内に流さないため排気
ダクトおよび排気ダクト内に挿入された配管だけを耐蝕
性があるものにすれば、通常の流速センサを用いて排気
状態を維持管理することができ極めて信頼性が高く、か
つ安価なりリーンドラフトの流量計測装置を得ることが
できる。
As described above, the clean draft flow rate measuring device according to the present invention includes a piping system that detects the static pressure and total pressure in the exhaust duct of the clean draft, and the discharge pressure of the clean air blower and guides them to the measurement section. By providing a measuring section consisting of a fluid resistance bridge consisting of a fluid resistance and a flow velocity sensor provided between the discharge port of the clean air blower and the exhaust duct, corrosive vapor and mist can be mixed in. In order to prevent this air from flowing into the fluid resistance bridge, if only the exhaust duct and the piping inserted into the exhaust duct are made corrosion-resistant, the exhaust condition can be maintained and managed using a normal flow rate sensor. It is possible to obtain a lean draft flow rate measuring device that is extremely reliable and inexpensive.

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

第1図は従来のクリーンドラフトの構成図、第2図はク
リーンドラフトの排気流量が適正な場合の空気の流れを
示す説明図、第3図は上記排気流量が過小な場合の空気
の流れを示す説明図、第4図は上記排気流量が過大な場
合の空気の流れを示す説明図、第5図は本発明によるク
リーンドラフトの流量計測装置の一実施例の構成を示す
図、第6図は上記実施例における排気ダクト内のアスピ
レーション吸引圧を利用した配管系と計測部を示す構成
図、第7図は計測部の一具体例を示す断面図である。 4°・排気ダクト、9・・クリーンドラフト、10・・
清浄空気送風ブロアの吐出口、11・・・流体抵抗ブリ
ッジ、12・・・送風ブロア吐出圧検出管、13・・・
静圧検出管、14・・全圧検出管、17・・・枝管、1
8・・・流速センサ、ra 、 rb、 re 、 r
(1、rg ”’流体抵抗代理人弁理士 中 村 純之
助 第1 図 才2図 才3図 矛4図 才5図
Figure 1 is a configuration diagram of a conventional clean draft, Figure 2 is an explanatory diagram showing the air flow when the exhaust flow rate of the clean draft is appropriate, and Figure 3 is an illustration of the air flow when the exhaust flow rate is too low. FIG. 4 is an explanatory diagram showing the air flow when the exhaust flow rate is excessive, FIG. 5 is a diagram showing the configuration of an embodiment of the clean draft flow rate measuring device according to the present invention, and FIG. 7 is a configuration diagram showing a piping system and a measuring section that utilize aspiration suction pressure in the exhaust duct in the above embodiment, and FIG. 7 is a sectional view showing a specific example of the measuring section. 4°・Exhaust duct, 9.・Clean draft, 10.
Clean air blower discharge port, 11... Fluid resistance bridge, 12... Blower discharge pressure detection tube, 13...
Static pressure detection tube, 14... Total pressure detection tube, 17... Branch pipe, 1
8...Flow rate sensor, ra, rb, re, r
(1, rg ”'Fluid resistance agent patent attorney Junnosuke Nakamura 1st figure 2nd figure 3rd figure 4th figure 5th figure

Claims (5)

【特許請求の範囲】[Claims] (1) クリーンドラフトの排気ダクト内の静圧および
全圧、ならびに清浄空気送風ブロアの吐出圧とをそれぞ
れ検出して計測部に導く配管系と、上記清浄空気送風ブ
ロアの吐出口と排気ダクトとの間に設けた、流体抵抗と
流速センサとで構成される流体抵抗ブリッジよりなる計
測部とを備えたクリーンドラフトの流量計測装置。
(1) A piping system that detects the static pressure and total pressure in the exhaust duct of the clean draft and the discharge pressure of the clean air blower and leads them to the measurement unit, and the discharge port of the clean air blower and the exhaust duct. A clean draft flow rate measurement device comprising a measurement section consisting of a fluid resistance bridge, which is provided between fluid resistance and a flow velocity sensor.
(2) 上記流体抵抗ブリッジは、流体抵抗ra、rb
、 rc 、rd、rgと流速センサとよりなり、ra
−rb、、ro:= rdとし、raとr。およびrb
とrdをそれぞれ直列に接続し、上記raの他端とrb
の他端とを清浄空気送風ブロアの吐出口に接続し、ro
およびrdの他端を排気ダクトの静圧側および全圧側に
それぞれ接続し、かつraとr。どの間およびrI)と
rdとの間を流体抵抗r、を有する枝管で連結して、該
枝管の中の流量を計測する流速センサを上記枝管中に設
けたことを特徴とする特許請求の範囲第1項に記載され
たクリーンドラフトの流量計測装置。
(2) The fluid resistance bridge has fluid resistances ra and rb.
, rc, rd, rg and a flow rate sensor, and ra
-rb,,ro:=rd, and ra and r. and r.b.
and rd are connected in series, and the other end of the above ra and rb
Connect the other end to the outlet of a clean air blower, and
The other ends of and rd are connected to the static pressure side and the total pressure side of the exhaust duct, respectively, and ra and r. A patent characterized in that a branch pipe having a fluid resistance r connects between (rI) and rd, and a flow velocity sensor for measuring the flow rate in the branch pipe is provided in the branch pipe. A clean draft flow rate measuring device according to claim 1.
(3) 上記流体抵抗は接続用管の流体抵抗であること
を特徴とする特許請求の範囲第1項または第2項に記載
されたクリーンドラフトの流量計測装置。
(3) The clean draft flow measuring device according to claim 1 or 2, wherein the fluid resistance is fluid resistance of a connecting pipe.
(4) 上記流速センサはサーミスタを用いた熱伝導形
の風速セ/すであることを特徴とする特許請求の範囲第
1項乃至第3項のいずれかに記載されたクリーンドラフ
トの流量計測装置。
(4) The clean draft flow rate measuring device according to any one of claims 1 to 3, wherein the flow rate sensor is a thermally conductive type wind speed sensor using a thermistor. .
(5) 上記全圧は、排気ダクトの下流方向に向けて開
口した圧力検出管により検出されるアスピレーション圧
であることを特徴とする特許請求の範囲第1項乃至第4
項のいずれかに記載されたクリーンドラフトの流量計測
装置。
(5) Claims 1 to 4, characterized in that the total pressure is an aspiration pressure detected by a pressure detection tube opened toward the downstream direction of the exhaust duct.
A clean draft flow rate measuring device described in any of the paragraphs.
JP22858183A 1983-12-05 1983-12-05 Flow-rate measuring device for clean draft Granted JPS60120219A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22858183A JPS60120219A (en) 1983-12-05 1983-12-05 Flow-rate measuring device for clean draft

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22858183A JPS60120219A (en) 1983-12-05 1983-12-05 Flow-rate measuring device for clean draft

Publications (2)

Publication Number Publication Date
JPS60120219A true JPS60120219A (en) 1985-06-27
JPS6338647B2 JPS6338647B2 (en) 1988-08-01

Family

ID=16878602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22858183A Granted JPS60120219A (en) 1983-12-05 1983-12-05 Flow-rate measuring device for clean draft

Country Status (1)

Country Link
JP (1) JPS60120219A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107631765A (en) * 2017-09-05 2018-01-26 合肥科迈捷智能传感技术有限公司 A kind of differential pressure flowmeter method for treating water
WO2018230043A1 (en) * 2017-06-14 2018-12-20 株式会社日立産機システム Safety cabinet

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53143361A (en) * 1977-05-20 1978-12-13 Oval Eng Co Ltd Flow meter for von k*arman*s vortex street
JPS5633565U (en) * 1979-08-23 1981-04-02

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4083649A (en) * 1976-05-05 1978-04-11 Carrier Corporation Cooling system for turbomachinery

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53143361A (en) * 1977-05-20 1978-12-13 Oval Eng Co Ltd Flow meter for von k*arman*s vortex street
JPS5633565U (en) * 1979-08-23 1981-04-02

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018230043A1 (en) * 2017-06-14 2018-12-20 株式会社日立産機システム Safety cabinet
US11273438B2 (en) 2017-06-14 2022-03-15 Hitachi Industrial Equipment Systems Co., Ltd. Safety cabinet
CN107631765A (en) * 2017-09-05 2018-01-26 合肥科迈捷智能传感技术有限公司 A kind of differential pressure flowmeter method for treating water
CN107631765B (en) * 2017-09-05 2020-07-07 合肥科迈捷智能传感技术有限公司 Differential pressure flowmeter water treatment method

Also Published As

Publication number Publication date
JPS6338647B2 (en) 1988-08-01

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