JPH0679011B2 - Method and apparatus for continuously measuring PH of non-aqueous sample - Google Patents

Method and apparatus for continuously measuring PH of non-aqueous sample

Info

Publication number
JPH0679011B2
JPH0679011B2 JP61091686A JP9168686A JPH0679011B2 JP H0679011 B2 JPH0679011 B2 JP H0679011B2 JP 61091686 A JP61091686 A JP 61091686A JP 9168686 A JP9168686 A JP 9168686A JP H0679011 B2 JPH0679011 B2 JP H0679011B2
Authority
JP
Japan
Prior art keywords
aqueous
aqueous sample
sample
measuring
mixing
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
JP61091686A
Other languages
Japanese (ja)
Other versions
JPS62247245A (en
Inventor
徳幸 武田
令文 市倉
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.)
Mitsui Petrochemical Industries Ltd
Original Assignee
Mitsui Petrochemical Industries 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 Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Priority to JP61091686A priority Critical patent/JPH0679011B2/en
Publication of JPS62247245A publication Critical patent/JPS62247245A/en
Publication of JPH0679011B2 publication Critical patent/JPH0679011B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
  • Sampling And Sample Adjustment (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

発明の目的 Purpose of the invention

【産業上の利用分野】[Industrial applications]

本発明は、非水性の試料とくに油類のpHを、プロセスの
運転中に連続的に測定する方法に関し、その方法の実施
に使用する装置をも包含する。
The present invention relates to a method for continuously measuring the pH of non-aqueous samples, especially oils, during the operation of the process, and also includes the equipment used to carry out the method.

【従来の技術】[Prior art]

製造プロセスの迅速、適確な制御を行なう手段の一つと
して、反応生成物や回収された未反応物質のpHの測定が
行なわれる。 たとえば、オレフィン系炭化水素の水和によりアルコー
ルを製造した場合、反応混合物から分離したアルコール
および未反応オレフィン中には、合成に使用した水や反
応の媒体として用いた有機酸が不純物として含有されて
いる。有機酸は、製品アルコールにとっては不純物であ
るから、規格により許容限度が定められるが、それ以外
の問題として、貯蔵容器や反応装置の腐食の原因ともな
るから、可能な限り除去する必要がある。有機酸の含有
量を知り、プロセスを制御するためには、pHを迅速、適
確に知ることが重要である。 このpH測定は、試料が水溶液である場合にはとくに問題
はないが、非水性の試料を対象とするときは面倒であ
る。 ここで「非水性の試料」とは、非水溶媒の溶液のほか
に、固体試料をも包含する語である。 pHは、本来は水溶液中の水素イオン濃度指数として定義
されたものであるが、非水性の媒質中においても水素イ
オン濃度を観念することができる。たとえば、その試料
を水性媒質中に移したときに発生し得る潜在的な水素イ
オンの濃度レベルとしてこれを把握することもできよ
う。このような意味での水素イオン濃度を、ここでは便
宜上、従来からあるpHの語に意義に包含させて用いる。
このような意味でのpHは、反応生成物や未反応原料の性
状を示すものとして役立つことが多く、従ってその測定
が必要かつ有意義なことは、しばしばある。 しかし、従来はその実用的な測定技術が確立されていな
かった。これまで行なわれてきた方法は、たとえば試料
が油性のものであるときは、この油性試料を分液ロート
に入れ、これに純水を等容量加えて振とうすることによ
り、油中に含まれている水溶液の電気的特性を寄与する
物質を抽出し、浮遊、分散する油滴をろ過して得られた
水層のpHを、たとえばガラス電極式のpH計で測定する、
といったものである。 しかし、このような方法では、(1)pHを連続的に測定
することができず、時々刻々変化する工程の状態を迅
速、的確に把握できない、(2)大気の影響を受けやす
い、すなわち、大気中のCO2,NOX,SOX,NH3,HClなどの酸
性、アルカリ性物質の汚染によりpH測定値にバラツキが
出る、(3)測定にかなりの人手を要する、などの問題
点があった。
The pH of reaction products and recovered unreacted substances is measured as one of means for performing rapid and appropriate control of the production process. For example, when an alcohol is produced by hydration of an olefinic hydrocarbon, the alcohol separated from the reaction mixture and the unreacted olefin contain the water used in the synthesis and the organic acid used as a reaction medium as impurities. There is. The organic acid is an impurity for product alcohol, and therefore the permissible limit is set by the standard. However, as another problem, it causes corrosion of the storage container and the reaction device, and therefore it should be removed as much as possible. In order to know the content of organic acids and control the process, it is important to know the pH quickly and accurately. This pH measurement is not a problem when the sample is an aqueous solution, but is troublesome when a non-aqueous sample is used. As used herein, the term “non-aqueous sample” includes a solid sample as well as a solution of a non-aqueous solvent. The pH is originally defined as a hydrogen ion concentration index in an aqueous solution, but the hydrogen ion concentration can be considered even in a non-aqueous medium. This could be understood, for example, as the potential hydrogen ion concentration level that can occur when the sample is transferred into an aqueous medium. For the sake of convenience, the hydrogen ion concentration in such a meaning is used here by being included in the meaning of the conventional pH.
The pH in this sense often serves as an indicator of the properties of the reaction products and unreacted raw materials, and therefore its measurement is often necessary and meaningful. However, the practical measurement technique has not been established so far. The method that has been carried out so far is, for example, when an oily sample is used, the oily sample is placed in a separating funnel, and an equal volume of pure water is added to the oily funnel to shake the oily sample so that it is contained in the oil. The substance that contributes to the electrical characteristics of the aqueous solution is extracted, and the pH of the aqueous layer obtained by filtering the suspended and dispersed oil droplets is measured by, for example, a glass electrode type pH meter,
And so on. However, in such a method, (1) it is not possible to continuously measure the pH, and the state of the process that changes from moment to moment cannot be grasped quickly and accurately, and (2) it is easily affected by the atmosphere, that is, There is a problem that pH measurement value varies due to the pollution of acidic and alkaline substances such as CO 2 , NO X , SO X , NH 3 and HCl in the air, and (3) requires a considerable amount of manual labor. It was

【発明が解決しようとする問題点】[Problems to be Solved by the Invention]

本発明の目的は、このような問題点を解決し、非水性試
料のpHをインラインで、すなわちプロセスの運転中に、
大気汚染によるバラツキのおそれや人手を要することな
く、連続的に測定できる方法を提供し、これにより製造
プロセスの迅速、的確な制御をできるようにすることに
ある。 本発明は、そのような方法の実施に使用するための装置
を提供することも、その目的に含んでいる。 発明の構成
The object of the present invention is to solve these problems and to bring the pH of non-aqueous samples in-line, i.e. during the operation of the process,
It is an object of the present invention to provide a method capable of continuous measurement without fear of variations due to air pollution or requiring human labor, thereby enabling rapid and accurate control of the manufacturing process. The invention also includes for that purpose the provision of an apparatus for use in carrying out such a method. Structure of the invention

【問題点を解決するための手段】[Means for solving problems]

本発明の非水性試料のpHの連続的測定方法は、プロセス
ラインから抜き出した非水性試料に純水および必要な希
釈剤を混合して非水性試料中のpHに寄与する物質を抽出
する工程、混合液を適宜の滞留時間を与える分離部に導
いて水層と非水層とに分離する工程、および分離された
水層のpHを連続的に測定する工程からなる。 上記の方法を実施するために用いる本発明の非水性試料
のpHの連続的測定装置は、プロセスラインの一部に接続
された、流量計を有する非水性試料の抜き出しライン、
およびこの抜き出しラインの出口側に接続された、それ
ぞれ流量計を有する純水供給ラインおよび必要な希釈剤
の供給ラインからなる非水性試料中のpHに寄与する物質
を抽出するための混合抽出部、この混合抽出部に接続さ
れ、混合液を適宜の時間滞留させて水層と非水層とに分
離する分離部、ならびにこの分離部に接続され、分離さ
れた水層のpHを測定する計器を有する測定部から構成さ
れ、水層のpHを連続的に測定できるようにしたものであ
る。
The method for continuously measuring the pH of a non-aqueous sample of the present invention comprises a step of extracting pure water and a necessary diluent into a non-aqueous sample extracted from a process line to extract a substance contributing to pH in the non-aqueous sample, It comprises a step of guiding the mixed solution to a separation section that gives an appropriate residence time to separate it into an aqueous layer and a non-aqueous layer, and a step of continuously measuring the pH of the separated aqueous layer. The apparatus for continuously measuring the pH of a non-aqueous sample of the present invention used for carrying out the above method comprises a non-aqueous sample withdrawal line having a flow meter connected to a part of the process line,
And a mixing and extracting unit for extracting a substance contributing to pH in a non-aqueous sample, which is connected to the outlet side of this extraction line, and comprises a pure water supply line having a flow meter and a supply line of a necessary diluent, respectively. Connected to this mixing and extracting section, a separation section for allowing the mixed solution to stay for an appropriate time to separate it into an aqueous layer and a non-aqueous layer, and an instrument connected to this separating section for measuring the pH of the separated aqueous layer It is composed of a measuring unit which is provided so that the pH of the aqueous layer can be continuously measured.

【作用】[Action]

非水性試料のpHの測定は、そのプロセスラインに接続さ
れた抜き出しライン中で、従って密閉した系内で行なわ
れる。このため、試料を系外にとり出すことにより圧力
が下ってpHに寄与する成分が揮散したり、大気中のCO2
やNOX,SOX,NH3などで汚染されたりすることなく、安定
した測定値が得られる。しかも、これらの測定は、水層
−非水層分離に要する時間を必要とするだけで、系内で
連続的に行なわれるから、迅速かつ適確なプロセス制御
が可能となり、省力化を図ることができる。
The measurement of the pH of non-aqueous samples is carried out in the extraction line connected to the process line and thus in a closed system. For this reason, when the sample is taken out of the system, the pressure decreases and the components that contribute to pH are volatilized, and CO 2 in the atmosphere is removed.
And NO X, SO X, without or contaminated with such NH 3, stable measurement value is obtained. Moreover, since these measurements are performed continuously within the system by only requiring the time required for separation of the water layer and the non-aqueous layer, rapid and accurate process control is possible, and labor saving is achieved. You can

【実施態様】Embodiment

代表的な例については、図面を参照して説明すると、1
は反応器、蒸留塔、洗浄装置などの各種処理装置から非
水性の液が流れるプロセスラインであって、このライン
1に試料抜き出しのための、面積式流量計2Aを有する抜
き出しライン3が接続されている。 この抜き出しライン3の出口側には、純水供給ライン4
および希釈剤の供給ライン5が接続され、ライン4,5に
は同様に面積式流量計2B,2Cが設けてある。 6は試料である非水性の媒質と純水および必要な希釈剤
とを混合し、非水性試料中のpH寄与物質を純水で抽出す
るための混合抽出物である。この混合抽出物6は、混合
液の流れが乱流となるようにする。配管内での混合も、
そこでの流れが乱流状態であるならば、十分な抽出効果
を期待できる。ただし、あまり強い乱流は、後の油水分
離部7において分離に要する時間を不相応に長くするこ
ともあるから、レイノルズ数が4,000〜6,000程度になる
よう、試料および純水の流量および配管径を選定する。 つまり、通常は特別の混合装置を必要としないわけであ
るが、試料の性状によって、たとえば試料が高粘度の液
である場合とか、配管内の圧力損失が過大になる場合に
は、必要に応じ、ラインミキサーを用い、または管内に
バッフルを設ける。 ライン内混合の場合の滞留時間は、通常2〜4秒間で足
りる。 混合の一例をあげれば、ベンゼンが測定対象試料であっ
て、純水とベンゼンとを各々50/hrの割合で混合する
場合、混合抽出部は内径6mmとし、長さを3mとすれば十
分である。混合抽出部は、管をコイル状に巻いておく
と、混合効果がさらに高くなり、かつ設置スペースが小
さくなるので好ましい。 図に戻って、7は抽水分離部であって、混合抽出部6に
おける混合液が所定時間滞留し、油層と水層とが分離で
きる容量とする。 8は油水分離部7で分離された水層のpHを測定するpH測
定部で、工業用pH計9を備えている。このpH測定部8に
は、油水分離部7における界面レベルが変動しても油層
が流れ込まないように、水層の供給量を一定に保つ手段
を設けることが好ましい。 被測定試料である非水性媒質の密度が純水のそれとかな
り異なる場合には、油水分離部7で所定時間滞留させる
ことにより、油層と水分が良好に分離する。しかし、両
者の密度差が0.05g/cm3以下と小さいか、または被測定
試料が多少の親水性を有する場合には、コアレッサーを
使用すればよい。被測定試料の混合、抽出に際し、pH測
定値に影響せず、かつ試料の性質を実質的に変化させな
い炭化水素のような希釈剤を、前記供給ライン5から連
続的に添加することも有効である。 非水性試料の性状に応じたpHの具体的測定方法を示せ
ば、次のとおりである。 (1) BTX(ベンゼン、トルエン、キシレン)類の場
合: この場合には、油水分離が静置により迅速に行なわれる
から、希釈剤の使用は不要であり、油水分離部は筒状な
どの簡単な装置でよい。分離水を油水分離部の底部から
抜き出し、pH測定部に導く。 (2) 親水性を有する油類、およびその密度が1に近
い場合: これらの試料では油水分離が困難であるから、 イ)pH寄与物質を含まないBTX類、パラフィン系炭化水
素などを希釈剤として使用する、 ロ)混合抽出部において激しい混合を避ける、 ハ)油水分離部として前記のコアレッサーを用いる、な
どの手段を併用する。 (3) 粘度の高い試料の場合: 上記(2)と同様に、希釈剤を用いるなどの手段を併用
する。 (4) 水と完全混和する試料の場合: 低級アルコール、グリコール、ケトン類などの水と完全
に混和する試料の混合には、油水分離工程を省き、混合
液の全量をpH測定部に導入すればよい。 発明の効果 本発明の方法および装置により、非水性試料とくに油類
のpHをインラインで、大気中の成分による汚染を受ける
ことなく、連続的に測定することができるから、化学プ
ロセスの迅速かつ適確な制御が可能となる。また、測定
試料として抜き出し、油水分離により分離された油層
は、全量プロセスへ戻すことができるから、ロスがな
く、別途処理する必要も生じない。
A typical example will be described with reference to the drawings.
Is a process line in which a non-aqueous liquid flows from various processing devices such as a reactor, a distillation column, and a washing device, and a withdrawal line 3 having an area flow meter 2A for withdrawing a sample is connected to the line 1. ing. On the outlet side of this extraction line 3, a pure water supply line 4
And diluent supply line 5 are connected, and area type flowmeters 2B and 2C are similarly provided in lines 4 and 5. Reference numeral 6 is a mixed extract for mixing a non-aqueous medium as a sample with pure water and a necessary diluent to extract a pH contributing substance in the non-aqueous sample with pure water. This mixed extract 6 makes the flow of the mixed liquid turbulent. Mixing in piping
If the flow there is turbulent, a sufficient extraction effect can be expected. However, too strong turbulence may disproportionately lengthen the time required for separation in the oil-water separation unit 7 after that, so that the Reynolds number is about 4,000 to 6,000, and the flow rate of the sample and pure water and the pipe diameter are set. Select. In other words, it does not usually require a special mixing device, but depending on the properties of the sample, for example, when the sample is a highly viscous liquid or when the pressure loss in the pipe becomes excessive, it may be necessary. , Use a line mixer, or install a baffle inside the tube. The residence time in the case of in-line mixing is usually 2 to 4 seconds. As an example of mixing, when benzene is the sample to be measured and pure water and benzene are mixed at a ratio of 50 / hr, it is sufficient to set the mixing extraction section to an inner diameter of 6 mm and a length of 3 m. is there. It is preferable that the mixing / extracting section has a tube wound in a coil shape because the mixing effect is further enhanced and the installation space is reduced. Returning to the figure, reference numeral 7 denotes a water extraction / separation unit, which has a capacity such that the mixed liquid in the mixing / extracting unit 6 stays for a predetermined time and can separate the oil layer and the water layer. Reference numeral 8 denotes a pH measuring unit for measuring the pH of the aqueous layer separated by the oil / water separating unit 7, which comprises an industrial pH meter 9. It is preferable that the pH measuring unit 8 is provided with means for keeping the supply amount of the water layer constant so that the oil layer does not flow even if the interface level in the oil / water separating unit 7 changes. When the density of the non-aqueous medium, which is the sample to be measured, is considerably different from that of pure water, the oil layer and the water are favorably separated by allowing the non-aqueous medium to stay in the oil / water separation unit 7 for a predetermined time. However, when the density difference between the two is as small as 0.05 g / cm 3 or less, or when the sample to be measured has some hydrophilicity, a coalescer may be used. When mixing and extracting the sample to be measured, it is also effective to continuously add a diluent such as a hydrocarbon that does not affect the measured pH value and does not substantially change the properties of the sample from the supply line 5. is there. The specific method for measuring pH according to the properties of the non-aqueous sample is as follows. (1) In the case of BTX (benzene, toluene, xylene): In this case, the oil-water separation is performed quickly by standing, so no diluent is required, and the oil-water separation part is simple, such as a cylinder. Any device will do. The separated water is extracted from the bottom of the oil / water separation section and led to the pH measurement section. (2) Hydrophilic oils and their densities close to 1: a) It is difficult to separate oil / water from these samples, so a) BTXs that do not contain pH-contributing substances, paraffin hydrocarbons, etc. are used as diluents. And (b) avoiding vigorous mixing in the mixing / extracting section, and (c) using the coalescer as the oil / water separating section. (3) In the case of a highly viscous sample: As in the case of (2) above, a means such as using a diluent is also used. (4) For samples that are completely miscible with water: To mix samples that are completely miscible with water, such as lower alcohols, glycols, and ketones, omit the oil-water separation step and introduce the entire mixture into the pH measurement unit. Good. EFFECTS OF THE INVENTION The method and apparatus of the present invention allow the pH of a non-aqueous sample, particularly oils, to be continuously measured in-line and without being contaminated by atmospheric constituents. Precise control is possible. Further, since the oil layer separated as a measurement sample and separated by oil-water separation can be returned to the whole process, there is no loss and no separate treatment is required.

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

図面は本発明の装置の代表例を示すフローチャートであ
る。 1……プロセスライン 2A,2B,2C……面積式流量計 3……抜き出しライン 4……純水供給ライン 5……希釈剤の供給ライン 6……混合抽出部 7……油水分離部 8……pH測定部 9……工業用pH計
The drawing is a flow chart showing a typical example of the apparatus of the present invention. 1 ... Process line 2A, 2B, 2C ... Area type flow meter 3 ... Extraction line 4 ... Pure water supply line 5 ... Diluent supply line 6 ... Mixing extraction part 7 ... Oil-water separation part 8 ... … PH measuring part 9 …… Industrial pH meter

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】プロセスラインから抜き出した非水性試料
に純水および必要な希釈剤を混合して非水性試料中のpH
に寄与する物質を抽出する工程、混合液を適宜の滞留時
間を与える分離部に導いて水層と非水層とに分離する工
程、および分離された水層のpHを連続的に測定する工程
からなる非水性試料のpHを連続的に測定する方法。
1. The pH in a non-aqueous sample obtained by mixing pure water and a necessary diluent with a non-aqueous sample extracted from a process line.
A step of extracting a substance that contributes to, a step of guiding the mixed solution to a separation section that gives an appropriate residence time, and separating into a water layer and a non-aqueous layer, and a step of continuously measuring the pH of the separated water layer. A method for continuously measuring the pH of a non-aqueous sample consisting of.
【請求項2】プロセスラインの一部に接続された、流量
計を有する非水性試料の抜き出しライン、およびこの抜
き出しラインの出口側に接続された、それぞれ流量計を
有する純水供給ラインおよび必要な希釈剤の供給ライン
からなる非水性試料中のpHに寄与する物質を抽出するた
めの混合抽出部、この混合抽出部に接続され、混合液を
適宜の時間滞留させて水層と非水層とに分離する分離
部、ならびにこの分離部に接続され、分離された水層の
pHを測定する計器を有する測定部から構成され、水層の
pHを連続的に測定できるようにしたことを特徴とする非
水性試料のpHを連続的に測定する装置。
2. A non-aqueous sample withdrawal line having a flow meter, which is connected to a part of the process line, and a pure water supply line, each having a flow meter, which is connected to the outlet side of the withdrawal line, and the necessary Mixing and extracting section for extracting substances that contribute to pH in a non-aqueous sample consisting of a diluent supply line, connected to this mixing and extracting section, and a mixed solution is retained for an appropriate time to form an aqueous layer and a non-aqueous layer. Of the separated water layer that is connected to this separation part and the separation part
Comprised of a measuring unit with a measuring instrument for measuring pH,
An apparatus for continuously measuring the pH of a non-aqueous sample, which is characterized in that the pH can be continuously measured.
JP61091686A 1986-04-21 1986-04-21 Method and apparatus for continuously measuring PH of non-aqueous sample Expired - Lifetime JPH0679011B2 (en)

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JP61091686A JPH0679011B2 (en) 1986-04-21 1986-04-21 Method and apparatus for continuously measuring PH of non-aqueous sample

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JP61091686A JPH0679011B2 (en) 1986-04-21 1986-04-21 Method and apparatus for continuously measuring PH of non-aqueous sample

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JPS62247245A JPS62247245A (en) 1987-10-28
JPH0679011B2 true JPH0679011B2 (en) 1994-10-05

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Publication number Priority date Publication date Assignee Title
JP2563232Y2 (en) * 1990-11-09 1998-02-18 三菱重工業株式会社 Automatic pH measurement device
JP2002016621A (en) 2000-06-30 2002-01-18 Haamorinku:Kk Control/supervisory signal transmitting system

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