JPH0580249B2 - - Google Patents

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Publication number
JPH0580249B2
JPH0580249B2 JP61011114A JP1111486A JPH0580249B2 JP H0580249 B2 JPH0580249 B2 JP H0580249B2 JP 61011114 A JP61011114 A JP 61011114A JP 1111486 A JP1111486 A JP 1111486A JP H0580249 B2 JPH0580249 B2 JP H0580249B2
Authority
JP
Japan
Prior art keywords
emulsion
stirring
water
heavy oil
viscosity
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
JP61011114A
Other languages
Japanese (ja)
Other versions
JPS62171746A (en
Inventor
Takashi Ueda
Kan Iwaki
Kyoji Kubo
Hajime Iwao
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP1111486A priority Critical patent/JPS62171746A/en
Publication of JPS62171746A publication Critical patent/JPS62171746A/en
Publication of JPH0580249B2 publication Critical patent/JPH0580249B2/ja
Granted legal-status Critical Current

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  • Colloid Chemistry (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明はエマルジヨンの製造方法に関し、特に
重質油のパイプライン輸送、船舶輸送等において
重質油の低粘度化を目的としたエマルジヨンを連
続して製造する方法に関する。 〔従来の技術〕 従来、重質油は高粘性かつ高流動性であるがた
めに、そのままでは輸送困難であり、種々の方法
が講じられてきた。 ここで言う重質油とは、タールサンド、ビチユ
ーメン、シエールオイル等を指す。 輸送方法には、ヒーターで加熱し、粘性を下げ
る加熱法、灯軽油等の軽質油を添加し、粘性を下
げる希釈法、及び界面活性剤を使用し、水と混合
し、W/O型エマルジヨンにする水エマルジヨン
法等がある。 加熱法及び希釈法は実用的であるが、輸送コス
トの点で問題がある。一方、水エマルジヨン法は
先の二つの方法と比較し、経済的であるという理
由で、技術開発が鋭意進められている。 水エマルジヨン法は、重質油と水を界面活性剤
の力を借りて均一なW/O型エマルジヨンにし、
粘性を大幅に下げることによりポンプで輸送可能
にするものである。界面活性剤としては、HLB
(親水性−疎水性バランス)値が8〜18のノニル
フエニルエーテル系、グリセロール酸化エチレン
系等が使用されている。混合撹拌方法は、これま
でプロペラ式のホモジナイザー、すり混ぜ式のコ
ロイドミル等が使用されているが、大半が一定条
件下での撹拌方式が採用されている。 〔発明が解決しようとする問題点〕 従来の水エマルジヨン化技術では、前述の通り
一定条件下での撹拌方法が採用されているため、
高粘性の重質油と水を撹拌する場合、均一なエマ
ルジヨンを製造することは困難であつた。これ
は、重質油と水の粘性が極端に異なるためであ
り、どちらか一方が選択的に撹拌せん断される結
果になる。 従つて、例えば、このような方法で生成したエ
マルジヨン中の油粒子の直径は数μ〜数千μmと
幅広く、大粒子は容易に沈降し、油と水の分離が
起こる。従つて、この方法ではエマルジヨンの安
定性の点で問題があつた。 〔問題点を解決するための手段〕 本発明は、前記問題点を、従来の一定条件下で
の混合撹拌方法の代わりに、撹拌条件を変化させ
た複数個の撹拌槽で、最初の撹拌槽は撹拌動力の
小さいもの、次の撹拌槽は撹拌動力を前よりも大
きくしたものというように順次撹拌動力を大きく
したものを使用して、エマルジヨンを製造するこ
とにより解決するものである。 〔作用〕 本発明では、重質油と水の混合物を徐々に撹拌
することにより均一なO/W型エマルジヨンを形
成することが可能である。即ち、重質油は高粘性
であるため、水に比べせん断されにくい。従つ
て、最初、緩やかな撹拌を行うことにより重質油
は一部せん断され、粒径の大きなエマルジヨンを
形成する。次に、この一部エマルジヨン化したも
のを、更に撹拌動力の強いもので撹拌すると、既
にエマルジヨン化したものは更に小粒子化し、エ
マルジヨン化していなかつた重質油もせん断によ
り小粒子化するようになる。このような撹拌を必
要に応じて二回以上続けることにより均一なO/
W型エマルジヨンを形成することが可能である。 このように本発明では、撹拌動力を変えた複数
個の撹拌槽に、順次、重質油と水の混合物を連続
的に大量に通すことにより、均一で、安定性の高
いエマルジヨンを大量に連続製造することができ
る。 また、本発明において、重質油と水の混合割合
は、重質油が75重量%以上になると極端にエマル
ジヨンの粘度が上昇し、輸送困難になるため、重
質油/水(重量比)で75/25以下とすることが望
ましい。なお、水の割合が増すほど粘度は下がる
が、カロリー低下による経済性の面で問題がある
ため、斯る面を考慮して水の割合の上限を定める
ことが望ましい。 〔実施例〕 使用した重質油の性状を第1表に示す。70℃に
加熱した重質油と25℃の蒸留水を重量比で7:3
の割合で混合し、更に市販のノニルフエニルエー
テル系界面活性剤(HLB=14)を油−水混合物
に対し0.3重量パーセント添加した。 撹拌槽の撹拌機はプロペラ式ホモジナイザー
(容量500ml)を使用した。上記の重質油−水混合
物は、ホモジナイザーにより所定時間、所定回転
数で撹拌した。撹拌後のエマルジヨンは二重円筒
型回転粘度計で粘度を測定し、同時に、光学顕微
鏡観察によりエマルジヨン中の油粒子の平均直径
を求めた。第2表に結果を示す。 第2表から明らかなように、従来の単一の撹拌
方法の場合(RUN1〜5)、エマルジヨンの粘度
は高く、油粒子の平均直径も大きい。これは、エ
マルジヨン化が不充分であり、油層と水層が分離
しているためである。一方、本発明の段階的に混
合する方法(RUN6〜8)では、エマルジヨンの
粘度は非常に低下し、均一なエマルジヨンにでき
ることが判明した。また、油粒子の平均直径も数
10〜100μmと小さく、充分油粒子がせん断され
ていることがわかる。
[Industrial Field of Application] The present invention relates to a method for producing an emulsion, and particularly to a method for continuously producing an emulsion for reducing the viscosity of heavy oil in pipeline transportation, ship transportation, etc. [Prior Art] Conventionally, heavy oil has high viscosity and high fluidity, so it is difficult to transport it as it is, and various methods have been used. The heavy oil referred to here refers to tar sand, bitumen, sierre oil, etc. Transportation methods include heating with a heater to lower the viscosity, dilution by adding light oil such as kerosene to lower the viscosity, and surfactants and mixing with water to create a W/O emulsion. There are methods such as water emulsion method. Although the heating method and the dilution method are practical, there are problems in terms of transportation costs. On the other hand, the technology of the water emulsion method is being actively developed because it is more economical than the previous two methods. In the water emulsion method, heavy oil and water are made into a uniform W/O emulsion with the help of surfactants.
By significantly lowering the viscosity, it can be transported by pump. As a surfactant, HLB
Nonylphenyl ether type, glycerol oxide ethylene type, etc. having a (hydrophilicity-hydrophobicity balance) value of 8 to 18 are used. Up to now, propeller-type homogenizers, grinding-type colloid mills, etc. have been used as mixing and stirring methods, but most of them employ stirring methods under certain conditions. [Problems to be solved by the invention] In the conventional water emulsion technology, as mentioned above, a stirring method under certain conditions is adopted;
When stirring highly viscous heavy oil and water, it is difficult to produce a uniform emulsion. This is because the viscosity of heavy oil and water is extremely different, resulting in either one being selectively stirred and sheared. Therefore, for example, the diameter of oil particles in an emulsion produced by such a method is wide ranging from several micrometers to several thousand micrometers, and large particles easily settle, causing separation of oil and water. Therefore, this method had a problem with the stability of the emulsion. [Means for Solving the Problems] The present invention solves the above problems by using a plurality of stirring tanks with varying stirring conditions, instead of the conventional mixing and stirring method under constant conditions. This problem can be solved by producing an emulsion using a tank with a lower stirring power, followed by a stirring tank with a higher stirring power than the previous one, and so on. [Operation] In the present invention, it is possible to form a uniform O/W type emulsion by gradually stirring a mixture of heavy oil and water. That is, since heavy oil has high viscosity, it is less likely to be sheared than water. Therefore, by performing gentle stirring at first, the heavy oil is partially sheared and an emulsion with a large particle size is formed. Next, when this partially emulsified material is further stirred with something with a strong stirring power, the material that has already been emulsified becomes even smaller particles, and the heavy oil that has not been emulsified is also reduced to smaller particles by shearing. Become. By continuing such stirring two or more times as necessary, uniform O/
It is possible to form a W-type emulsion. In this way, in the present invention, a large amount of a mixture of heavy oil and water is continuously passed through a plurality of stirring tanks with varying stirring power, thereby producing a uniform and highly stable emulsion in large quantities. can be manufactured. In addition, in the present invention, the mixing ratio of heavy oil and water is heavy oil/water (weight ratio) because if the heavy oil exceeds 75% by weight, the viscosity of the emulsion will increase extremely and transportation will be difficult. It is desirable that the ratio be 75/25 or less. Note that as the proportion of water increases, the viscosity decreases, but since there is a problem in terms of economy due to a decrease in calories, it is desirable to set an upper limit for the proportion of water in consideration of this aspect. [Example] Table 1 shows the properties of the heavy oil used. Heavy oil heated to 70℃ and distilled water at 25℃ in a weight ratio of 7:3.
Furthermore, a commercially available nonyl phenyl ether surfactant (HLB=14) was added in an amount of 0.3% by weight based on the oil-water mixture. A propeller-type homogenizer (capacity: 500 ml) was used as the stirrer in the stirring tank. The above heavy oil-water mixture was stirred by a homogenizer for a predetermined period of time at a predetermined rotation speed. The viscosity of the emulsion after stirring was measured using a double cylindrical rotational viscometer, and at the same time, the average diameter of oil particles in the emulsion was determined by observation with an optical microscope. Table 2 shows the results. As is clear from Table 2, in the case of the conventional single stirring method (RUN1-5), the viscosity of the emulsion is high and the average diameter of the oil particles is also large. This is because emulsion is insufficient and the oil layer and water layer are separated. On the other hand, it was found that in the stepwise mixing method of the present invention (RUN 6 to 8), the viscosity of the emulsion was significantly reduced and a uniform emulsion could be obtained. In addition, the average diameter of oil particles is also several
It can be seen that the oil particles are as small as 10 to 100 μm and are sufficiently sheared.

【表】【table】

【表】【table】

〔発明の効果〕〔Effect of the invention〕

本発明によれば、高粘性であるがために輸送上
問題があつた重質油に水を加え、段階的に混合撹
拌することにより、重質油は水中に均一な小粒子
で分散し、安定性のあるO/W型エマルジヨンと
なり、大幅な粘度低下を達成することができる。
According to the present invention, by adding water to heavy oil, which poses transportation problems due to its high viscosity, and mixing and stirring in stages, the heavy oil is dispersed in water as uniform small particles. It becomes a stable O/W type emulsion and can achieve a significant reduction in viscosity.

Claims (1)

【特許請求の範囲】[Claims] 1 重質油と水から構成されるエマルジヨンの製
造方法において、撹拌動力を順次大きくした撹拌
機を有する複数個の撹拌槽を設け、撹拌動力の小
さな撹拌機を有する撹拌槽から撹拌動力の大きい
撹拌機を有する撹拌槽に該重質油と水との混合物
を逐次通過させることを特徴とするエマルジヨン
の製造方法。
1. In a method for producing an emulsion composed of heavy oil and water, a plurality of stirring tanks each having a stirrer with successively increased stirring power are provided, and a stirring tank with a stirrer with a lower stirring power is used, followed by a stirring tank with a higher stirring power. 1. A method for producing an emulsion, which comprises sequentially passing the mixture of heavy oil and water through a stirring tank equipped with a stirrer.
JP1111486A 1986-01-23 1986-01-23 Production of emulsion Granted JPS62171746A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1111486A JPS62171746A (en) 1986-01-23 1986-01-23 Production of emulsion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1111486A JPS62171746A (en) 1986-01-23 1986-01-23 Production of emulsion

Publications (2)

Publication Number Publication Date
JPS62171746A JPS62171746A (en) 1987-07-28
JPH0580249B2 true JPH0580249B2 (en) 1993-11-08

Family

ID=11768980

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1111486A Granted JPS62171746A (en) 1986-01-23 1986-01-23 Production of emulsion

Country Status (1)

Country Link
JP (1) JPS62171746A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012061446A (en) * 2010-09-17 2012-03-29 Lion Corp Method for producing emulsion which contains encapsulated particle

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5810127A (en) * 1981-07-09 1983-01-20 Toyota Motor Corp Calculation for intake-air flow rate in electronically controlled fuel injection engine

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5810127A (en) * 1981-07-09 1983-01-20 Toyota Motor Corp Calculation for intake-air flow rate in electronically controlled fuel injection engine

Also Published As

Publication number Publication date
JPS62171746A (en) 1987-07-28

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