CN2912804Y - Poly-column-awl combined type liquid-liquid separation cyclone - Google Patents
Poly-column-awl combined type liquid-liquid separation cyclone Download PDFInfo
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- CN2912804Y CN2912804Y CN 200520087364 CN200520087364U CN2912804Y CN 2912804 Y CN2912804 Y CN 2912804Y CN 200520087364 CN200520087364 CN 200520087364 CN 200520087364 U CN200520087364 U CN 200520087364U CN 2912804 Y CN2912804 Y CN 2912804Y
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Abstract
The utility model discloses a multi-column-cone combining type liquid-liquid separating swirler which is composed of a plurality of column sections and conic sections which are alternately connected with each other and a tail pipe. The utility model has the advantages of that: the flowing loss in the swirler is decreased, and the energy consumption is reduced; the processing is less difficult, and the processing precision is easier to ensure. The utility model is applicable to the liquid-solid and liquid-liquid separations field in industries such as petroleum, chemical engineering, environmental protection, medicine, and foods.
Description
Technical field
The utility model is applicable to liquid-liquid separation hydrocyclone of industries such as oil, chemical industry, environmental protection, medicine, food.
Background technology
Liquid-liquid separates and generally is made up of charging aperture, overflow pipe, cylinder, cone and tail pipe etc. with hydrocyclone, and wherein cone structure is generally single awl or bipyramid form.It is generally acknowledged, its main centrifugation of the cone of cyclone, for the flow field situation of improving cyclone inside, improve its separative efficiency, the optimization of cone structure is modified into the important research target into people.Developed at present have third hand tap, liquid-liquid of cone form such as curved surface awl separates and uses hydrocyclone.
But the following problems of cone structure form ubiquity such as single awl, bipyramid, third hand tap and curved surface awl:
1. taper hole is long, the conical surface is too complicated, and feasible processing, assembly difficulty with cyclone of this class formation increases, and the assembly precision of joining place is difficult to guarantee between the cone, and the processing charges of cyclone also can increase therefore and to some extent.
2. cone changes when remedying the inner rotation function consumption of cyclone, strengthening the centrifugation field of force continuously, has increased unnecessary turbulence energy consumption, has improved the shear action of fluid to dispersed phase drop.
Summary of the invention
The purpose of this utility model is to provide the poly-column-awl combined type liquid that a kind of processing technology is simple, easy to assembly and assembly precision guarantees easily, separative efficiency is high-liquid to separate and uses cyclone.
Order of the present utility model is realized by following measure.
The said Liquid-Liquid Separation Hydrocyclone of the utility model be is characterized in that by charging aperture 1, overflow pipe 2, cylinder 3, cone 4, cylinder 5, cone 6, tail pipe 7: described hydrocyclone structure is connected and composed at interval by at least 2 straight pilaster bodies and 2 cones at least; The tail pipe end of Liquid-Liquid Separation Hydrocyclone can connect a cone; The cone angle that connects cone at interval is identical or inequality.
Description of drawings
Fig. 1 is the structural representation of the cyclone of tail pipe band one cone that proposes according to the utility model;
Fig. 2 is that the tail pipe that proposes according to the utility model is not with the hydrocyclone structure schematic diagram of cone.
The specific embodiment
Below in conjunction with drawings and Examples structure of the present utility model and work characteristics are further described:
As shown in Figure 1 and Figure 2, the utility model is connected successively by charging aperture 1, overflow pipe 2, cylinder 3, cone 4, cylinder 5, cone 6, tail pipe 7 etc. and constitutes.During work, mixed liquor enters cyclone by charging aperture 1, forms a centrifugal force field of rotating at a high speed in cyclone.Wherein heavy is descending at the effect lower edge of centrifugal force field and axial compressive force cylinder 3, cone 4, cylinder 5, cone 6, discharges via tail pipe 7, cone 8 (Fig. 1), perhaps directly discharges (Fig. 2) via tail pipe 7, and lightweight is then discharged by overflow pipe 2 mutually.
The design of this multistage cylinder has reduced the turbulence intensity of interior flow field, stablizes separated space for heterogeneous fluid provides multistage; The multistage taper designs makes internal flow anglec of rotation momentum in time to obtain to replenish, and improves swirl strength, has strengthened separation process.
Because liquid-liquid rotational flow separation device tail pipe is longer, center lightweight phase fluid column tail end spin intensity significantly weakens, the angular momentum deficiency, usually " wagging the tail " phenomenon occurs, influences separative efficiency.The terminal awl section that increases of tail pipe can remedy angular momentum, stable center lightweight phase fluid column, thereby improves separative efficiency.
Major advantage of the present utility model is:
1. cone is shorter, processing, installs simple and conveniently, and post cone joining place assembly precision guarantees easily.
2. reduced owing to cone changes the part turbulence energy consumption that produces continuously, the cyclone energy consumption decreases.
3. the poly-column-awl combination is so that rotational flow field is stable in the cyclone inside, balanced energy consumption distributes, the shearing of fluid Fragmentation reduces, and separative efficiency improves.
Claims (3)
1. a poly-column-awl combined type liquid-liquid separates and uses cyclone, comprise charging aperture (1), overflow pipe (2), cylinder (3), cone (4), cylinder (5), cone (6), tail pipe (7), it is characterized in that: described hydrocyclone structure is connected and composed at interval by at least 2 straight pilaster bodies and 2 cones at least.
2. poly-column-awl combined type liquid as claimed in claim 1-liquid separates uses cyclone, it is characterized in that said tail pipe end can connect a cone.
3. poly-column-awl combined type liquid as claimed in claim 1-liquid separates use cyclone, and it is identical or inequality to it is characterized in that the interval connects the cone angle of cone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN 200520087364 CN2912804Y (en) | 2005-09-23 | 2005-09-23 | Poly-column-awl combined type liquid-liquid separation cyclone |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN 200520087364 CN2912804Y (en) | 2005-09-23 | 2005-09-23 | Poly-column-awl combined type liquid-liquid separation cyclone |
Publications (1)
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CN2912804Y true CN2912804Y (en) | 2007-06-20 |
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CN 200520087364 Expired - Fee Related CN2912804Y (en) | 2005-09-23 | 2005-09-23 | Poly-column-awl combined type liquid-liquid separation cyclone |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102424444A (en) * | 2011-10-25 | 2012-04-25 | 华东理工大学 | Method and device for removing oil from desalted water of crude electrostatic desalting apparatus |
CN102847606A (en) * | 2012-09-01 | 2013-01-02 | 山东科技大学 | Coarse slime separation process |
CN103396830A (en) * | 2013-08-14 | 2013-11-20 | 中国石油大学(华东) | Device and method for dehydrating heavy sump oil |
CN103641070A (en) * | 2013-12-31 | 2014-03-19 | 中国石油化工股份有限公司 | Method of supplementing hydrogen gas in Szorb device to remove moisture |
CN108778517A (en) * | 2015-12-18 | 2018-11-09 | 美卓矿物工业公司 | The broken stream of controlled turbulence |
CN113226558A (en) * | 2018-12-21 | 2021-08-06 | 乌尔可公司 | Hydraulic cyclone |
-
2005
- 2005-09-23 CN CN 200520087364 patent/CN2912804Y/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102424444A (en) * | 2011-10-25 | 2012-04-25 | 华东理工大学 | Method and device for removing oil from desalted water of crude electrostatic desalting apparatus |
CN102424444B (en) * | 2011-10-25 | 2013-06-12 | 华东理工大学 | Method and device for removing oil from desalted water of crude electrostatic desalting apparatus |
CN102847606A (en) * | 2012-09-01 | 2013-01-02 | 山东科技大学 | Coarse slime separation process |
CN103396830A (en) * | 2013-08-14 | 2013-11-20 | 中国石油大学(华东) | Device and method for dehydrating heavy sump oil |
CN103396830B (en) * | 2013-08-14 | 2015-05-20 | 中国石油大学(华东) | Device and method for dehydrating heavy sump oil |
CN103641070A (en) * | 2013-12-31 | 2014-03-19 | 中国石油化工股份有限公司 | Method of supplementing hydrogen gas in Szorb device to remove moisture |
CN108778517A (en) * | 2015-12-18 | 2018-11-09 | 美卓矿物工业公司 | The broken stream of controlled turbulence |
CN113226558A (en) * | 2018-12-21 | 2021-08-06 | 乌尔可公司 | Hydraulic cyclone |
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Legal Events
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |