JPS6014140A - Method and apparatus for measuring gas content containing in liquid - Google Patents

Method and apparatus for measuring gas content containing in liquid

Info

Publication number
JPS6014140A
JPS6014140A JP12202983A JP12202983A JPS6014140A JP S6014140 A JPS6014140 A JP S6014140A JP 12202983 A JP12202983 A JP 12202983A JP 12202983 A JP12202983 A JP 12202983A JP S6014140 A JPS6014140 A JP S6014140A
Authority
JP
Japan
Prior art keywords
liquid
pressure
gas
flow path
flow
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
JP12202983A
Other languages
Japanese (ja)
Other versions
JPH0326786B2 (en
Inventor
Yoji Miyoshi
三好 洋二
Sumio Sato
佐藤 澄夫
Hiroshi Ooya
博 大矢
Motoki Kiyozawa
清沢 基紀
Kunio Naganami
長南 国男
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.)
Niigata Engineering Co Ltd
AGC Inc
Original Assignee
Niigata Engineering Co Ltd
Asahi Glass 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 Niigata Engineering Co Ltd, Asahi Glass Co Ltd filed Critical Niigata Engineering Co Ltd
Priority to JP12202983A priority Critical patent/JPS6014140A/en
Publication of JPS6014140A publication Critical patent/JPS6014140A/en
Publication of JPH0326786B2 publication Critical patent/JPH0326786B2/ja
Granted legal-status Critical Current

Links

Classifications

    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N7/00—Analysing materials by measuring the pressure or volume of a gas or vapour

Landscapes

  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Sampling And Sample Adjustment (AREA)
  • Measuring Volume Flow (AREA)

Abstract

PURPOSE:To measure a gas content contg. in a liquid by varying a pressure of the liquid while flowing the liquid through a liquid flow passage with maintaining a flow rate per unit time constant, and measuring pressures and flow velocities at high and low pressures respectively. CONSTITUTION:The liquid flow passage 2 for circulating liquid in a containing tank 1 is provided with a ball valve 5, a liquid pump 6, a pressure gauge 7, a change-over valve 8, a pressure detector 9, a current meter 10, a change-over valve 11, a gas mixing apparatus 12, a check valve 13 and a ball valve 14. A variable throttle valve 15 is controlled so that a quantity per unit time of liquid sent out from the pump 6 becomes constant independently of the liquid pressure variation in case the gas content is measured. Next, the apparatus 12 is operated to mix the gas into liquid. The pressure and the flow velocity at high pressure are detected by the detector 9 and the meter 10 respectively. Next, the valves 8, 11 are changed over, the pressure and the flow velocity at low pressure are detected, and the mixing rate of gas in liquid is measured by a controlling device 27.

Description

【発明の詳細な説明】 本発明はプラスチック液状成分等に混入された気体の含
有量を測定する気体含有量の測定方法及びその装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gas content measuring method and apparatus for measuring the gas content mixed in a plastic liquid component or the like.

互いに反応する少なくとも二種以上のプラスチック液状
成分を衝突混合させ、成形品を製造する反応射出成形に
おいては、成形品内部の発泡組織を緻密にし、物性及び
外観を良くして商品価値を高める目的から、プラスチッ
ク液状成分中に空気を微細な気泡として混入することが
行なわfyて0る。そして従来においては、プラスチッ
ク液状成分の流れを止めて気体含有量を測定してしする
1fi(特開昭56−21036号)、測定中は、循環
を停止しなければならないという欠点があった。
In reaction injection molding, in which molded products are produced by colliding and mixing at least two plastic liquid components that react with each other, the purpose of this is to make the foam structure inside the molded product denser, improve its physical properties and appearance, and increase its commercial value. In this case, air is mixed into the plastic liquid component as fine bubbles. Conventionally, 1fi (Japanese Unexamined Patent Publication No. 56-21036), in which the flow of the plastic liquid component is stopped and the gas content is measured, has the disadvantage that circulation must be stopped during the measurement.

本発明は、液体の流路に、液体ポンプと、気体混入装置
、圧力切換え装置、圧力検出器及び流速計を設け、単位
時間当りの流量を一定に保つ−C液体流路に液体を流し
ながら、その液体の液圧を変化させ、高圧時の圧力と流
速、及び低圧時の圧力と流速を目測J°ることによって
液体内の気体含有量を測定するようにして上記従来の欠
点を解消したもので、プラスチック液状成分等の液体の
流れを止めることなく、液体を連続して流しながら気体
含有量を測定することができる気体含有量の測定方法と
測定装置を提供することを目的とする。
The present invention provides a liquid pump, a gas mixing device, a pressure switching device, a pressure detector, and a current meter in a liquid flow path, and maintains a constant flow rate per unit time. The above-mentioned drawbacks of the conventional method were solved by measuring the gas content in the liquid by changing the pressure of the liquid and visually measuring the pressure and flow rate at high pressure and the pressure and flow rate at low pressure. It is an object of the present invention to provide a gas content measuring method and a measuring device capable of measuring the gas content while continuously flowing a liquid such as a plastic liquid component without stopping the flow of the liquid.

以下本発明を図面に基いて説明する。The present invention will be explained below based on the drawings.

図面は本発明の気体含有量測定装置を用いたRIM高圧
反応成形装置の概要を示すもので、図中1はプラスブッ
ク液状成分(液体)を収容する収容タンクである。るこ
の収容タンク1にはパイプよりなる液体流路2の両端2
a、2bが接続され、また内部にはモータ3によって回
転させられる撹拌羽根4が設けられている。上記液体流
路2は収容タンク1内の液体を循環させるもので、これ
には、ボールバルブ5、液体ポンプ6、圧力817、切
換バルブ8、圧JJ検出器9、流速it 10 、切換
えバルブ11、気体混入装置12、チェツギバルブ13
、ボールバルブ14が上記の順に設けられている。そし
て上記二つの切換えバルブ8.11の部分からは可変絞
り15.16を備えた液体流路17.18が分岐され、
それら流路17.18の他端は、切換えバルブ8と圧力
検出器9の間、及び切換えバルブ11と気体混入装置1
2の間の液体流路2にそれぞれ連結されている。
The drawing shows an outline of a RIM high-pressure reaction molding apparatus using the gas content measuring device of the present invention, and in the drawing, 1 is a storage tank for storing a plus book liquid component (liquid). This storage tank 1 has both ends 2 of a liquid flow path 2 made of a pipe.
a and 2b are connected, and a stirring blade 4 rotated by a motor 3 is provided inside. The liquid flow path 2 circulates the liquid in the storage tank 1, and includes a ball valve 5, a liquid pump 6, a pressure 817, a switching valve 8, a pressure JJ detector 9, a flow rate it10, and a switching valve 11. , gas mixing device 12, Chetsugi valve 13
, ball valves 14 are provided in the above order. A liquid flow path 17.18 equipped with a variable throttle 15.16 is branched from the two switching valves 8.11.
The other ends of these channels 17 and 18 are located between the switching valve 8 and the pressure detector 9, and between the switching valve 11 and the gas entrainment device 1.
2 are respectively connected to the liquid flow paths 2 between them.

また、上記気体混入装置12にはパイプ19を介して気
体供給源20が連結され、このパイプ19には、気体供
給源20から順に、エアーレギュレーター21、エアー
圧力計22、エアー流量調節弁23、エアー流量計24
、エアー電磁弁25、エアーヂエツキバルブ26が設け
られ、液体ポンプ6の作動によって液体流路2を循環ゼ
しめられる液体に希望する量の気体を混入させることが
できるようになっている。
Further, a gas supply source 20 is connected to the gas mixing device 12 via a pipe 19, and this pipe 19 is connected to an air regulator 21, an air pressure gauge 22, an air flow rate control valve 23, Air flow meter 24
, an air solenoid valve 25, and an air pump valve 26 are provided so that a desired amount of gas can be mixed into the liquid that is circulated through the liquid flow path 2 by the operation of the liquid pump 6.

さらにまた、上記の圧力検出器9と流速計10及びエア
ー電磁弁25には制御l装置27が連Nされている。こ
の制御装置27は、圧力検出器って測定された液体圧力
と、流速計10により測定された液体の流速から、液体
流N2を流れる液体内に含有されている気体の量を算出
する計棹部28と、この計算部28により算出された気
体含有量の°実測値と予め記憶部33に記憶された気体
含有量の設定値とを比較し、実測値が設定値より小であ
る場合にエアー電磁弁25を開かせ、等しいか大である
場合にエアー電磁弁25を閉じさせる比較指令部29を
備えている。
Furthermore, a control device 27 is connected to the pressure detector 9, flow meter 10, and air solenoid valve 25. This control device 27 is a meter that calculates the amount of gas contained in the liquid flowing in the liquid stream N2 from the liquid pressure measured by the pressure detector and the liquid flow rate measured by the current meter 10. The unit 28 compares the actual measured value of the gas content calculated by the calculating unit 28 with the set value of the gas content stored in advance in the storage unit 33, and if the actual measured value is smaller than the set value, A comparison command section 29 is provided which opens the air solenoid valve 25 and closes the air solenoid valve 25 when the two are equal or larger.

しかして上記収容タンク1には、周知のように計量シリ
ンダ30とミキシングヘッド31が連結され、収容タン
ク1から供給されたプラスチック液状成分をミキシング
ヘッド31に送って、図示されていない他の計量シリン
ダ等から送られてきた他のプラスチック液状成分と混合
し、量液状成分の反応により成形品を得ることができる
ようになっている。なお、32は気体含有量の実測値が
設定値に対して大きいか、小さいか、或いは等しいかを
表示する表示部、34は2個の切換えバルブ8,11を
相互に同期して切り換える切換用アクヂコ:[ターであ
る。流速計10の代りに流量計を用いることができる。
As is well known, a measuring cylinder 30 and a mixing head 31 are connected to the storage tank 1, and the plastic liquid component supplied from the storage tank 1 is sent to the mixing head 31, and is then connected to another measuring cylinder (not shown). By mixing with other plastic liquid components sent from other companies, molded products can be obtained by reaction of the liquid components. In addition, 32 is a display unit that displays whether the measured value of the gas content is larger than, smaller than, or equal to the set value, and 34 is a switching unit that switches the two switching valves 8 and 11 in synchronization with each other. Akujiko: [That's it. A flow meter can be used instead of the current meter 10.

切換えバルブ11と可変絞り16は圧力切換え装置を構
成する。
The switching valve 11 and the variable throttle 16 constitute a pressure switching device.

次に上記のように構成された気体含有量測定装置の作用
を説明する。
Next, the operation of the gas content measuring device configured as described above will be explained.

この装置による気体含有量の測定に当っては、液体ポン
プ6から送り出される液体の単位1間当りの量が、圧力
検出器9の部分における液体の圧力変動に関係なく一定
に保1cれるように、可変絞り15を調節する。
When measuring the gas content using this device, the amount of liquid sent out from the liquid pump 6 per unit time is kept constant regardless of the pressure fluctuation of the liquid at the pressure detector 9. , adjust the variable aperture 15.

すなわち、液体ポンプ6から吐出された液体が液体流路
17を通らずに切換えバルブ8を直進し、また流速計1
9の部分を通った液体が切換えバルブ11で流れ方向を
切り換えられて液体流路18に流れる図の状態において
、液体を循環させ圧力泪7の圧力を読み取る。次いで切
換えバルブ8゜11を切換え、液体ポンプ6から吐出さ
れた液体を液体流路17に流し、また流速計10を通っ
た液体を可変絞り16を通さずに直進させて液体を循環
させながら、圧力計7が前回と同一の圧力を示すにうに
可変絞り15を調節する。この操作により、液体ポンプ
6の吐出圧は下流のバルブの切換状態に関係なく、常に
同一であるから、吐出流量も均一となる、。
That is, the liquid discharged from the liquid pump 6 does not pass through the liquid flow path 17 but goes straight through the switching valve 8, and the flow rate meter 1
In the state shown in the figure in which the flow direction of the liquid that has passed through the section 9 is switched by the switching valve 11 and flows into the liquid flow path 18, the liquid is circulated and the pressure of the pressure drop 7 is read. Next, the switching valve 8° 11 is switched, and the liquid discharged from the liquid pump 6 is made to flow into the liquid flow path 17, and the liquid that has passed through the flow meter 10 is made to go straight without passing through the variable throttle 16, thereby circulating the liquid. The variable throttle 15 is adjusted so that the pressure gauge 7 shows the same pressure as before. By this operation, the discharge pressure of the liquid pump 6 is always the same regardless of the switching state of the downstream valve, so the discharge flow rate also becomes uniform.

上記の調節が済/υだら、液体ポンプ6を作動させて液
体を液体流路2に循環させながら気体混入装置12を作
動させ、液体内に気体を微細な気泡として混入させる。
When the above adjustment is completed/υ, the liquid pump 6 is operated to circulate the liquid through the liquid flow path 2, while the gas mixing device 12 is operated to mix gas into the liquid as fine bubbles.

図の場合は、液体ポンプ6から送り出された液体は切換
えバルブ8を直進し、次の切換えバルブ11で液体流路
18に流れて可変絞り16を通過し気体混入装置12に
流れるが、可変絞り16を通過する際に大きな抵抗を受
けるため、液体の圧力が高まり、その圧力に応じて液体
内の気泡が圧縮されることになる。この際の圧力と流速
は圧力検出器9と流速計10によって検出される。
In the case shown in the figure, the liquid sent out from the liquid pump 6 goes straight through the switching valve 8, flows into the liquid flow path 18 at the next switching valve 11, passes through the variable throttle 16, and flows to the gas mixing device 12, but the variable throttle 16, the pressure of the liquid increases, and air bubbles within the liquid are compressed in accordance with the pressure. The pressure and flow rate at this time are detected by a pressure detector 9 and a current meter 10.

高圧時の圧ノJと流速を検出し終ったら、切換え )(
a“用アクチュエータ34の作用で2個の切換えバルブ
8.11を同時に切り換え、それまで切換えバルブ8の
部分を直進していた液体を液体流路17に流して可変絞
り15を通過させ、またそれまで液体流路18に流れて
いた液体を直進させて気体混入装置12に流す。この場
合は、液体流路17から液体流路2に戻された液体はそ
のまま抵抗なく流れるので、液体圧ツノは低くなり、そ
れに応じて液体中の気泡が膨張する。圧力検出器9と流
速計10は前と同様に圧力と流速を検出する。]−記の
ように圧力検出器9の部分の流体圧力が変っても、可変
絞り15の調整で液体全体の循環抵抗が等しくされてい
るので、単位時間当りの液体流切が変ることはない。
After detecting pressure J and flow velocity at high pressure, switch )(
The two switching valves 8.11 are simultaneously switched by the action of the actuator 34 for "a", and the liquid that had previously flowed straight through the switching valve 8 is caused to flow into the liquid flow path 17 and pass through the variable throttle 15. The liquid that has been flowing into the liquid channel 18 until now is made to go straight and flows into the gas mixing device 12. In this case, the liquid returned from the liquid channel 17 to the liquid channel 2 flows without resistance, so the liquid pressure horn is The pressure sensor 9 and the flow meter 10 detect the pressure and flow rate as before.] - As shown, the fluid pressure at the pressure sensor 9 is Even if it changes, the circulation resistance of the entire liquid is made equal by adjusting the variable throttle 15, so the liquid flow rate per unit time will not change.

高圧時と低圧時の圧力と流速の検出結果は直ちに制御装
置27に送られる。制御装置27は、圧力検出器9と流
速計10によって検出された圧力と流速をもとに、次の
ようにして割り出された式%式%) ) を4算して液体に対する気体の混入率(Xa )を算出
する。
The detection results of pressure and flow velocity at high pressure and low pressure are immediately sent to the control device 27. Based on the pressure and flow velocity detected by the pressure detector 9 and the current meter 10, the control device 27 calculates the amount of gas mixed into the liquid by calculating the formula % (%) calculated as follows. Calculate the ratio (Xa).

なお、計算は次の三点を条件としている。The calculation is subject to the following three conditions.

(1) 液体ポンプ6から送り出される液体の流量は一
定である。
(1) The flow rate of the liquid sent out from the liquid pump 6 is constant.

〈2) 空気状態式(P V =一定)が、液体に対す
る混入状態においても成立1゛る。
(2) The air state equation (PV = constant) holds true even when mixed with liquid.

(3) 液体は非圧縮性である。(3) Liquids are incompressible.

1)a:大気圧(1,033kg/cm2>Pl :第
1圧力条件kGl/d(絶対圧)P2 :第2圧力条件
kQ/cm2(絶対圧)Vm:l休の休M4d Va:Pa下の混入気体の体積 d V+:P+下の混入気イホの体積 d V2:P2下の混入気体の体積 d S+:P+下の液体の速度 CTII / 5ecS2
:P2下の液体の速度 cyn / 5ecA:液体流
路2の断面積 d 単位時間当りの液体の通過体積を考えると、Va xl
、033=V+ P+ =V2 P2V2 = Va 
xl、033/P2 ・・・・・・・・・(1) Vl =Va X 1 、033/P+ −・・=・=
= (2)V2 −Vl =Va X 1.033/P
2−Va xl、033/P+ =1.033Va (1/P2 − .1/P+ )・
・・・・・・・・・・・・・・ (3)Vl +VII
l =Sz XA Vlll =S+ A−V+’ =S+ A −1,0
33Va /P ・・・・・・・・・(4) Vz +Vm =S2 XA ・・・・・・・・・(5
)(4)、(5)式より V2 +S+ A−Vl =82 A Vz Vl =S2 A−8t A =A (S2−8t > ・・・・・・ (6)(3)
、(6)式より 1.033Va (1/P2 −1/P+ )=A (
32−8+ ) 1.033Va (PI P2 )/PI P2=A 
<82 −8+ ) 、’、Va’=A (S2 −8t > ・ PI P
2 / ((PI−P2 )Xl、033) ・・・・
・・・・・ (7)混入率 Xa == Va / (
Vm→−Va )(4)式より Xa =Va/ (St A−1,033Va /P+
4−Va) −Va/(S+△十Va (1−1,033)/P+)
) (7)式より (以下余白) どなる。
1) a: Atmospheric pressure (1,033 kg/cm2>Pl: First pressure condition kGl/d (absolute pressure) P2: Second pressure condition kQ/cm2 (absolute pressure) Vm: L holiday M4d Va: Under Pa Volume of entrained gas under P+ d V+: Volume of entrained gas under P+ d V2: Volume of entrained gas under P2 d S+: Velocity of liquid under P+ CTII/5ecS2
:Velocity of liquid under P2 cyn/5ecA: Cross-sectional area of liquid flow path 2 d Considering the volume of liquid passing per unit time, Va xl
, 033=V+ P+ =V2 P2V2 = Va
xl, 033/P2 ・・・・・・・・・(1) Vl = Va X 1 , 033/P+ −・・=・=
= (2) V2 - Vl = Va X 1.033/P
2-Vaxl, 033/P+ = 1.033Va (1/P2 - .1/P+)・
・・・・・・・・・・・・・・・ (3) Vl +VII
l =Sz XA Vllll =S+ A-V+' =S+ A-1,0
33Va /P ・・・・・・・・・(4) Vz +Vm =S2 XA ・・・・・・・・・(5
) (4), from formulas (5), V2 +S+ A-Vl = 82 A Vz Vl = S2 A-8t A = A (S2-8t > ...... (6) (3)
, from formula (6), 1.033Va (1/P2 -1/P+ )=A (
32-8+ ) 1.033Va (PI P2 )/PI P2=A
<82 -8+),', Va'=A (S2 -8t>・PI P
2/((PI-P2)Xl,033)...
... (7) Mixing rate Xa == Va / (
Vm→-Va) From formula (4), Xa = Va/ (St A-1,033Va /P+
4-Va) -Va/(S+△10Va (1-1,033)/P+)
) From equation (7), (below in the margins), there is a roar.

上式の計算は目算部28が行なうが、その1粋結果は記
憶部33に予め記憶されている気体の混入設定値と比較
され、実測定値と設定値が等しい場合にはそのままの状
態で運転が継続され、また実測値が設定値より小さい時
は、比較指令部29から出される指令によりTアー電磁
弁25が聞かれて気体混入装置12から液体内に気体が
混入されるとともに、実測定が設定値より大きい時はそ
のままの状態を保ち、必要ならば気体が混入されていな
い液体を収容タンク7に補充する。
Calculation of the above equation is performed by the calculation section 28, and the first result is compared with the set value of gas mixture stored in advance in the storage section 33, and if the actual measured value and the set value are equal, the operation is continued in that state. continues, and when the actual measured value is smaller than the set value, the T-ar solenoid valve 25 is activated by a command issued from the comparison command unit 29, and gas is mixed into the liquid from the gas mixing device 12, and the actual measurement is performed. When is larger than the set value, the condition is maintained as it is, and if necessary, the storage tank 7 is replenished with liquid that is not mixed with gas.

なJ3、RIM高圧反応成形においては、プラスチック
液状成分中にガラス繊維等の各種フィラーを゛混合ザる
場合すある。流速計としては配管の外周にセンサーを取
り刊ける方式で、しかも液内部に気泡、ガラス繊維等の
フィラーが混入していても、計測精度に影響が出ない形
式のものを選定ダベきで、これを満足するものどじて、
超音波ドツプラー底流m系を挙げることができる。
In J3 and RIM high-pressure reaction molding, various fillers such as glass fibers are sometimes mixed into the plastic liquid component. The current meter should be of a type that has a sensor mounted around the outer circumference of the pipe, and that does not affect measurement accuracy even if fillers such as air bubbles or glass fibers are mixed into the liquid. Those who satisfy this,
One example is the ultrasonic Doppler underflow m system.

以し説明したように、本発明においては、気体混入装置
によって気体を混入された液体を、単位時間当りの流m
を一定に保って液体流路に流しながら、上記液体の圧力
を変化させ、その液体の高圧a4の圧力と流速(流量)
、及び定圧時の圧力と流速(流量)をC1測りることに
よって液体内に混入されている気体の但を測定するもの
であるから、液状成分をシリンダー等に導い−(その流
れを止める必要のあった従来の測定方法と違って、成形
作業を■害づることなく、能率的に気体の含有量を測定
づることができる。その上、装置が簡単で−゛答性よく
、正確かつ迅速に気1ホ含有量を測定ることができる。
As explained above, in the present invention, the liquid mixed with gas by the gas mixing device is
The pressure of the liquid is changed while keeping it constant and flowing through the liquid flow path, and the pressure and flow rate (flow rate) of the high pressure a4 of the liquid are changed.
Since the gas mixed in the liquid is measured by measuring the pressure and flow rate (flow rate) at constant pressure C1, it is necessary to introduce the liquid component into a cylinder etc. and stop the flow. Unlike conventional measuring methods, it is possible to efficiently measure gas content without harming the molding operation.In addition, the device is simple, responsive, accurate, and quick. Qi 1 Ho content can be measured.

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

図面は本発明の気体含有最測定装置の一実施例を示すブ
ロック図である。 2・・・・・・液体流路、6・・・・・・液体ポンプ、
9・・・・・・圧力検出器、10・・・・・・流速計、
11・・・・・・切換えバルブ、12・・・・・・気体
混入装置、16・・・・・・可変絞り。 出願人 株式会社 新潟鉄工所 旭硝子株式会社
The drawing is a block diagram showing an embodiment of the gas-containing measuring device of the present invention. 2...Liquid channel, 6...Liquid pump,
9...Pressure detector, 10... Current velocity meter,
11...Switching valve, 12...Gas mixing device, 16...Variable throttle. Applicant Niigata Iron Works Co., Ltd. Asahi Glass Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] (1) 気体混入装置によって気体を混入された液体を
、単位時間当りの流量を一定に保って液体流路に流しな
がら、上記液体の圧力を変化させ、その液体の高圧時の
圧力と流速、及び低圧時の圧力と流速を計測することに
よって液体内に混入されている気体の但を測定づること
を特徴とする液体に含まれる気体含有量の1Ill]定
方法。
(1) While the liquid mixed with gas by the gas mixing device is kept flowing through the liquid flow path at a constant flow rate per unit time, the pressure of the liquid is changed, and the pressure and flow rate of the liquid at high pressure, A method for determining the gas content of a liquid, characterized by measuring the amount of gas mixed in the liquid by measuring the pressure and flow rate at low pressure.
(2) 液体流路に、単位時間当りの流路を一定に保っ
て液体を液体流路に流す液体ポンプと、液体流路を流れ
る液体に気体を混入さゼる気体混入装置と、上記液体流
路を流れる液体の圧力を切り換える圧力切換えil置と
、上記液体流路を流れる液体の圧力を31測する圧力検
出器と、液体流路を流れる液体の流速を81測する流速
計とが設りられて成ることを特徴とザる液体に含まれる
気体含有量の測定装置。
(2) A liquid pump that flows the liquid into the liquid flow path while keeping the flow rate constant per unit time, a gas mixing device that mixes gas into the liquid flowing through the liquid flow path, and a gas mixing device that mixes gas into the liquid flowing through the liquid flow path; A pressure switching device for switching the pressure of the liquid flowing through the flow path, a pressure detector that measures the pressure of the liquid flowing through the liquid flow path, and a current meter that measures the flow velocity of the liquid flowing through the liquid flow path are designed. A device for measuring the gas content contained in a liquid.
JP12202983A 1983-07-05 1983-07-05 Method and apparatus for measuring gas content containing in liquid Granted JPS6014140A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12202983A JPS6014140A (en) 1983-07-05 1983-07-05 Method and apparatus for measuring gas content containing in liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12202983A JPS6014140A (en) 1983-07-05 1983-07-05 Method and apparatus for measuring gas content containing in liquid

Publications (2)

Publication Number Publication Date
JPS6014140A true JPS6014140A (en) 1985-01-24
JPH0326786B2 JPH0326786B2 (en) 1991-04-11

Family

ID=14825825

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12202983A Granted JPS6014140A (en) 1983-07-05 1983-07-05 Method and apparatus for measuring gas content containing in liquid

Country Status (1)

Country Link
JP (1) JPS6014140A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61193019U (en) * 1985-05-22 1986-12-01

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61193019U (en) * 1985-05-22 1986-12-01

Also Published As

Publication number Publication date
JPH0326786B2 (en) 1991-04-11

Similar Documents

Publication Publication Date Title
US4050896A (en) Method and apparatus for the production of reaction mixtures from liquid reaction components
EP0584052B1 (en) System and method for producing and maintaining predetermined proportionate mixtures of fluids
US20100031825A1 (en) Blending System
US4195527A (en) Method of and apparatus for producing a foam-forming reaction mixture
US4062373A (en) Method and apparatus for mixing gases
JPH0220306A (en) Method and device for continuously filling at least one kind of fluid reaction component with gas in order to manufacture fluid reaction mixture forming form material
AU2010229111B2 (en) Electronic proportioner using continuous metering and correction
US3762428A (en) Volumetric gas mixing system
US5567885A (en) Measuring fluid flow rate
US2707964A (en) Measurement and control of the compositions of flowing streams of fluid mixtures
JPS6348550B2 (en)
KR100908583B1 (en) Oxygen Concentrator
CN107063413A (en) The static criteria weighing device and method of a kind of high-pressure sealed system fluid medium
AU2019323687B2 (en) Device for producing foamed construction materials
CN103644456A (en) Sound velocity nozzle volume automatic air distributing system and control method thereof
US4526907A (en) Process and device for the preparation of a reaction mixture of at least two components for the production of foams
JPH0326786B2 (en)
US6182503B1 (en) On-line rheological measurement for process control
JP3181072B2 (en) Carbonated water production equipment
JPH02502447A (en) Production control device and production control method for bubble-containing materials
JPS60201918A (en) Device for mixing gas with liquid
JP2545751Y2 (en) Air-blast equipment
JPS61277030A (en) Apparatus for calibrating vacuum gauge
US3599668A (en) Liquid blending apparatus
JPS6125809A (en) Controlling method of gas quantity mixed in liquid