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JPS5935247B2 - Light liquid/heavy liquid mixing device - Google Patents
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JPS5935247B2 - Light liquid/heavy liquid mixing device - Google Patents

Light liquid/heavy liquid mixing device

Info

Publication number
JPS5935247B2
JPS5935247B2 JP56099891A JP9989181A JPS5935247B2 JP S5935247 B2 JPS5935247 B2 JP S5935247B2 JP 56099891 A JP56099891 A JP 56099891A JP 9989181 A JP9989181 A JP 9989181A JP S5935247 B2 JPS5935247 B2 JP S5935247B2
Authority
JP
Japan
Prior art keywords
liquid
container
fixed partition
heavy
partition wall
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
Application number
JP56099891A
Other languages
Japanese (ja)
Other versions
JPS583628A (en
Inventor
勝昭 松本
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP56099891A priority Critical patent/JPS5935247B2/en
Publication of JPS583628A publication Critical patent/JPS583628A/en
Publication of JPS5935247B2 publication Critical patent/JPS5935247B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/625Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis the receptacle being divided into compartments, e.g. with porous divisions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/72Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Description

【発明の詳細な説明】 不発明は水と油、A−B−C重油等の如く比重差のある
二種以上の重液、重液あるいは二種以上の液体を混合撹
拌して混和する装置に関する。
Detailed Description of the Invention The invention is a device for mixing and agitating two or more types of heavy liquids, heavy liquids, or two or more types of liquids with different specific gravities, such as water and oil, A-B-C heavy oil, etc. Regarding.

特に水と重油のエマルジョン装置として有益な利用用途
がある。従来の重液、重液の混和装置は単に羽根を回転
させて撹拌混合するものであり、羽根の回転に伴つて液
体に回転流が発生し、逆にその回転の遠心力によつて液
体が遠心分離して混和が阻害され、完全な混和が行えず
、且つ時間がかかるという欠点があり、又ミクロン単位
の微粒状態で混和することが出来ず、完全なエマルジョ
ン化ができず、通常乳化剤を添加しなければならないと
いう欠点があつた。
It is particularly useful as an emulsion device for water and heavy oil. Conventional equipment for mixing heavy liquids and heavy liquids simply rotates blades to stir and mix the liquid, and as the blades rotate, a rotational flow is generated in the liquid, and conversely, the centrifugal force of that rotation causes the liquid to mix. There is a disadvantage that mixing is inhibited by centrifugation, complete mixing cannot be achieved, and it takes time.Also, it is impossible to mix in the form of fine particles on the micron scale, making complete emulsion impossible, and emulsifiers are usually not used. The disadvantage was that it had to be added.

本発明はかかる欠点を解消し、極めて短時間で且つミク
ロン単位の微粒子状態で完全な混和が行えるという優れ
た重液重液混和装置を提供せんとするものである。特許
請求の範囲第1項に記載する発明(以下第1発明という
)の要旨は、筒状容器1に所要数の多孔質の固定隔壁2
を設け、同固定隔壁2を設け、同固定隔壁の両側それぞ
れに同固定隔壁に向う対向流を引起す多孔質の回転羽根
3を設け、更に容器1の一方端に重液及び重液の導入口
5、6を又容器の他方端に、混和液の吐出口Tを設けて
なる重液重液混和装置にある。
The present invention aims to eliminate such drawbacks and provide an excellent heavy liquid/heavy liquid mixing device that can completely mix fine particles in the micron scale in an extremely short time. The gist of the invention described in claim 1 (hereinafter referred to as the first invention) is that a cylindrical container 1 is provided with a required number of porous fixed partition walls 2.
A fixed partition wall 2 is provided, a porous rotary vane 3 is provided on each side of the fixed partition wall to cause a counterflow toward the fixed partition wall, and a heavy liquid and a heavy liquid are introduced into one end of the container 1. The heavy liquid/heavy liquid mixing apparatus is provided with ports 5 and 6 and a discharge port T for mixed liquid at the other end of the container.

特許請求の範囲第2項記載の発明(以下第2発明という
)の要旨は第1発明の構成に、更に容器1内の所要個所
に同容器内周壁付近の外側液分を容器1内部中心側に移
動せしめる求心流発生用羽根4を設ける構成を付加した
ものである。第1|2いずれの発明とも比重差のある二
種以上の液体の混和ばかりでなく、化学的、物理的性質
を異にする二種以上の液体の混和あるいは単なる混合撹
拌装置としても使用できるものである。又回転羽根3は
スクリュー羽根、軸流翼いずれの形式の羽根構造でもよ
い。ここで固定隔壁2、これに対向する一対の回転羽根
3及び求心流発生用羽根4を一組として筒状容器1内に
多段にわたつて設けることが、より完全な混和にとつて
望ましい。求心流発生用羽根4は回転駆動されるもので
も又、固定羽根でも構わないが回転、駆動される方が好
ましい。又固定隔壁2、回転羽根3の「多孔質」とは壁
板・羽根板に’5、前後の透孔を多数穿孔したものでも
、あるいはメッシュで構成してもよい。要はこれら壁・
羽根の構成部材に5%前後の液体の流通、空隙が多数存
在すればよい。重液、重液の導入口5、6は別個の導入
口を設けても、又同一導入管によつて供給されてもよい
。な卦、図中2′は固定隔壁2に多数穿設した透孔、3
′は回転羽根3に多数穿設した透孔、8は回転羽根3・
求心流発生用羽根4とを軸着した回転軸、9は同回転軸
の駆動モータ、10は軽液導入管、11は重液導入管、
12は固定隔壁2の取付ボルト、13は求心流発生用羽
根4の中央側に穿設した連通口である。
The gist of the invention recited in claim 2 (hereinafter referred to as the second invention) is that in addition to the structure of the first invention, the outer liquid near the inner circumferential wall of the container 1 is placed at a required location in the container 1 on the inner center side of the container 1. This is an additional configuration in which a centripetal flow generation vane 4 is provided to move the blade. No. 1 | 2 Both inventions can be used not only for mixing two or more liquids with different specific gravity, but also for mixing two or more liquids with different chemical and physical properties, or as a simple mixing and stirring device. It is. Further, the rotating blade 3 may have a blade structure of either a screw blade or an axial flow blade. Here, it is desirable to provide the fixed partition wall 2, the pair of rotating blades 3 facing the fixed partition wall 2, and the centripetal flow generating blades 4 as a set in multiple stages in the cylindrical container 1 for more complete mixing. The centripetal flow generating blades 4 may be rotationally driven or fixed blades, but it is preferable that they be rotated and driven. Furthermore, the "porous" material of the fixed partition wall 2 and the rotary blade 3 may be one in which a large number of through holes are punched in the wall plate or blade plate, or may be made of a mesh. The point is these walls.
It is only necessary that there be a large number of voids and a flow of liquid of around 5% in the components of the blade. The heavy liquid and heavy liquid inlets 5 and 6 may be provided with separate inlets or may be supplied by the same inlet pipe. In the figure, 2' indicates a large number of through holes drilled in the fixed partition wall 2, and 3
' is a large number of through holes drilled in the rotating blade 3, 8 is a hole in the rotating blade 3.
a rotating shaft on which the centripetal flow generating blade 4 is attached; 9 a drive motor for the same rotating shaft; 10 a light liquid introduction pipe; 11 a heavy liquid introduction pipe;
Reference numeral 12 indicates a mounting bolt for the fixed partition wall 2, and reference numeral 13 indicates a communication port bored in the center of the centripetal flow generating blade 4.

この発明では、導入口5,6から軽液、重液が容器1内
に送られれば、各固定隔壁2の左右両側の液体は両側そ
れぞれK設けた多孔質の回転羽根3によつて、互いに固
定隔壁2に向つて流れ、固定隔壁2との衝突及び対向流
同志の衝突によつて液体が撹拌混合されると同時に回転
羽根3の対向流と伴に発生する回転成分が相殺され、遠
心分離が発生するのを防いでいる。
In this invention, when light liquid and heavy liquid are sent into the container 1 from the inlets 5 and 6, the liquids on both the left and right sides of each fixed partition wall 2 are mutually separated by the porous rotary blades 3 provided on both sides. The liquid flows toward the fixed partition wall 2, and the liquid is stirred and mixed by the collision with the fixed partition wall 2 and the collision between the countercurrents, and at the same time, the rotation component generated with the counterflow of the rotating blades 3 is canceled out, resulting in centrifugal separation. is prevented from occurring.

更に重要なことは、回転羽根3、固定隔壁2を通過、衝
突の際に多数の透孔2′,3′によつて液体が剪断され
、液体が容易にミクロン単位程度に微粒化され、水、油
等の混和をより完全に出来ることとなる。このような剪
断、衝突をくりかえして軽液、重液を混合撹拌して完全
な混和状態とするものである。更に第2発明では多少の
回転力の存在によつて容器1の外側に遠心分離された容
器1内周壁付近の液分又は比重分離した液分は求心流発
生用羽根4によつて容器1内部中央に強制的に引戻し、
回転羽根3、固定隔壁2によつて剪断、衝突をくりかえ
させるとともに、一部は連通口13から次段の固定隔壁
2、回転羽根3に送られ、前述の混和過程をくりかえさ
せるものであり、混和が完全となつた段階で吐出口7よ
り混和液が吐出されるものである。以上の様に、本第1
,2の発明によれば多孔質の固定隔壁2をはさんで対向
流を発生させる一対の多孔質の回転羽根3Kよつて、液
体を対向衝突させ、混和撹拌能力が著しく高まるととも
に、回転成文を相殺して回転による遠心分離を避け、し
かも多数の透孔2′,3′によつて液体を充分に剪断し
て、ミクロン単位の微粒子状態に容易にでき、よつて軽
液、重液等の二種以上の液体をミクロン単位の微粒状態
に完全に且つ短時間でしかも何ら乳化剤等の添加剤を加
えることなく、混和できるという優れた効果を得ること
ができるものである。更に第2発明では多少残在する回
転によつて遠心分離された、あるいは比重分離した容器
1内周壁の外側に滞留した液分を求心流発生用羽根4に
よつて容器1内部中央に戻して液体の分離、非混和が発
生しない様にするとともに、強制的に回転羽根3、固定
隔壁2による混合撹拌、衝突剪断の混和過程に移行させ
るもので、よつて1分程度の短時間で水、油等、軽液、
重液を完全に混和できるものであり、何ら乳化剤を添加
する必要もなく、更に完全に且つ迅速に混和状態にする
ことができるという優れた効果を得ることができる。
More importantly, when the liquid passes through the rotating blade 3 and the fixed partition wall 2 and collides with it, the liquid is sheared by the numerous through holes 2' and 3', and the liquid is easily atomized to the order of microns, and the liquid is , oil, etc. can be mixed more completely. By repeating such shearing and collision, the light liquid and heavy liquid are mixed and stirred to achieve a completely mixed state. Furthermore, in the second invention, the liquid near the inner circumferential wall of the container 1 that is centrifuged to the outside of the container 1 due to the presence of some rotational force or the liquid that has been separated by specific gravity is transferred to the inside of the container 1 by the centripetal flow generating blades 4. Forcibly pull back to the center,
Shearing and collision are repeated by the rotating blades 3 and the fixed partition wall 2, and a portion is sent from the communication port 13 to the next stage of the fixed partition wall 2 and the rotating blades 3, thereby repeating the above-mentioned mixing process. The mixed liquid is discharged from the discharge port 7 when the mixing is complete. As mentioned above, book 1
According to the invention of , 2, a pair of porous rotary blades 3K that generate counterflows across the porous fixed partition wall 2 cause the liquid to collide with each other in opposite directions, thereby significantly increasing the mixing and stirring ability and achieving rotational composition. This offsets the need for centrifugal separation due to rotation, and the large number of through holes 2' and 3' sufficiently shear the liquid, making it easy to form fine particles on the micron scale. It is possible to obtain the excellent effect of being able to mix two or more types of liquids into micron-sized particles completely and in a short time without adding any additives such as emulsifiers. Furthermore, in the second invention, the liquid remaining on the outside of the inner circumferential wall of the container 1, which has been centrifuged or separated by specific gravity due to some remaining rotation, is returned to the center inside the container 1 by the centripetal flow generating blades 4. This system prevents liquid separation and immiscibility from occurring, and forcibly transitions to the mixing process of mixing agitation and collision shear using the rotating blades 3 and fixed partition walls 2. Therefore, water and water can be mixed in a short time of about 1 minute. Oil etc., light liquid,
The heavy liquid can be completely miscible, and there is no need to add any emulsifier, and an excellent effect can be obtained in that the mixture can be completely and quickly mixed.

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

第1図は本発明軽液重液混和装置の実施例を示す一部切
欠正面図、第2図は第1図1−1線に卦ける縦断面図、
第3図は第1図−線にち・ける縦断面図である。 1:容器、2:固定隔壁、2′,3′:透孔、3:回転
羽根、4:求心流発生用羽根、5,6:導入口、7:吐
出口。
Fig. 1 is a partially cutaway front view showing an embodiment of the light liquid/heavy liquid mixing device of the present invention, Fig. 2 is a longitudinal sectional view taken along the line 1-1 in Fig. 1;
FIG. 3 is a longitudinal sectional view taken along the line of FIG. 1. 1: Container, 2: Fixed partition, 2', 3': Through hole, 3: Rotating blade, 4: Centripetal flow generating blade, 5, 6: Inlet, 7: Discharge port.

Claims (1)

【特許請求の範囲】 1 筒状容器1に所要数の多孔質の固定隔壁2を設け、
同固定隔壁の両側それぞれに同固定隔壁に向う対向流を
引起す多孔質の回転羽根3を設け、又容器1の一方端に
軽液及び重液の導入口5、6を又容器の他方端に混和液
の吐出口7を設けてなる軽液重液混和装置。 2 筒状容器1に所要数の多孔質の固定隔壁2を設け、
同固定隔壁の両側それぞれに同固定隔壁に向う対向流を
引起す多孔質の回転羽根3を設け、又容器1内の所要個
所に同容器内周壁付近の外側液分を容器1内部中心側に
移動せしめる求心流発生用羽根4を設け、更に容器1の
一方端に軽液及び重液の導入口5、6を又容器の他方端
に混和液の吐出口7を設けてなる軽液重液混和装置。
[Claims] 1. A cylindrical container 1 is provided with a required number of porous fixed partition walls 2,
Porous rotary vanes 3 are provided on both sides of the fixed partition wall to induce counterflow toward the fixed partition wall, and inlets 5 and 6 for light liquid and heavy liquid are provided at one end of the container 1 and at the other end of the container. A light liquid/heavy liquid mixing device which is provided with a discharge port 7 for mixed liquid. 2. A required number of porous fixed partition walls 2 are provided in the cylindrical container 1,
Porous rotary vanes 3 are provided on each side of the fixed partition wall to cause a counterflow toward the fixed partition wall, and the outer liquid near the inner circumferential wall of the container 1 is directed to the center side inside the container 1 at required locations in the container 1. A light liquid/heavy liquid which is provided with a vane 4 for generating a centripetal flow for movement, and further provided with inlets 5 and 6 for light liquid and heavy liquid at one end of the container 1, and an outlet 7 for a mixed liquid at the other end of the container. Mixing device.
JP56099891A 1981-06-26 1981-06-26 Light liquid/heavy liquid mixing device Expired JPS5935247B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56099891A JPS5935247B2 (en) 1981-06-26 1981-06-26 Light liquid/heavy liquid mixing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56099891A JPS5935247B2 (en) 1981-06-26 1981-06-26 Light liquid/heavy liquid mixing device

Publications (2)

Publication Number Publication Date
JPS583628A JPS583628A (en) 1983-01-10
JPS5935247B2 true JPS5935247B2 (en) 1984-08-28

Family

ID=14259392

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56099891A Expired JPS5935247B2 (en) 1981-06-26 1981-06-26 Light liquid/heavy liquid mixing device

Country Status (1)

Country Link
JP (1) JPS5935247B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6365791A (en) * 1986-09-05 1988-03-24 Sharp Corp Picture information offering device
JPS6384633A (en) * 1986-09-26 1988-04-15 Nobuo Koyama Device for emitting electron into liquid
JP2004161943A (en) * 2002-11-15 2004-06-10 Kyoto Tool Co Ltd Emulsion production equipment
CN108126604A (en) * 2017-12-28 2018-06-08 郑州游爱网络技术有限公司 The mixing apparatus that a kind of feed processing is stirred with multistage

Also Published As

Publication number Publication date
JPS583628A (en) 1983-01-10

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