CN202155273U - Built-in cyclone separator device - Google Patents
Built-in cyclone separator device Download PDFInfo
- Publication number
- CN202155273U CN202155273U CN2011202594557U CN201120259455U CN202155273U CN 202155273 U CN202155273 U CN 202155273U CN 2011202594557 U CN2011202594557 U CN 2011202594557U CN 201120259455 U CN201120259455 U CN 201120259455U CN 202155273 U CN202155273 U CN 202155273U
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- CN
- China
- Prior art keywords
- crystallizing evaporator
- return pipe
- cyclone separator
- liquid
- cylindrical shell
- 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 - Fee Related
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Abstract
The utility model relates to a built-in cyclone separator device which belongs to the technical field of manufacturing of mechanical equipment and comprises a liquid return pipe, a lower conic body, a barrel, a gas return pipe, a spiral plate, a washing pipe and a fixed plate, wherein the barrel is internally provided with the gas return pipe; the lower conic body is welded with the liquid return pipe; the upper end of the barrel is fixedly connected with the fixed plate; and the fixed plate is welded with an upper end enclosure of a crystallizing evaporator. In the device, the manufacturing cost of a whole crystallizing evaporator system can be reduced, the space for arranging the crystallizing evaporator system in a workshop can be reduced, and the manufacturing cost is low; the air flowing direction is controlled through the guiding function of the a spiral plate; and liquid can be prevented from accumulating in the liquid return pipe, and the temperature of the liquid is in accordance with that of the crystallizing evaporator, so that material crystallization caused by temperature reduction can be avoided, the separator can be cleaned irregularly through the annular washing pipe, and blockage of the liquid return pipe is further avoided.
Description
Technical field
The utility model relates to a kind of vapor-liquid separating device, specifically is used for the vapor-liquid separation of crystallizing evaporator system, belongs to biofermentation, chemical mechanical equipment manufacturing technology field.
Background technology
The effect of cyclone separator in the crystallizing evaporator system is the material of carrying secretly in the separated secondary steam.In traditional prior art, cyclone separator generally all is the outside that is placed on crystallizing evaporator, can take the space that entire equipment is arranged usually; Simultaneously,, to thicken during the design of separator tank skin, make whole cost of manufacture to promote because whole system is the negative pressure operation; Cyclone separator generally all arranges in a high position, when heavier, needs to give the separator designs support to bear deadweight like this body weight of separator; Crystallizing evaporator has crystal and produces, and makes cyclone separator liquid back pipe (U type pipe) easy blocking, promptly uses hot water also to be difficult to clean, and loses separating effect.
Summary of the invention
The purpose of the utility model is to overcome above-mentioned weak point; Thereby a kind of built-in cyclone separator means is provided; Can reduce the spatial placement of whole evaporation and crystallization system, reduce the cost of whole workshop and cyclone separator body, solve the liquid back pipe blocking problem.
According to the technical scheme that the utility model provides, built-in cyclone separator means comprises liquid back pipe, lower cone, cylindrical shell, muffler, spiral plate, jet water spout and fixed head, is provided with muffler in the said cylindrical shell; Between muffler and cylindrical shell, be furnished with spiral plate; Jet water spout is connected with muffler, and said cylindrical shell lower end is provided with lower cone, and lower cone and liquid back pipe are welded to connect; Said cylindrical shell upper end is fixedly connected fixed head, and fixed head and the welding of crystallizing evaporator upper cover are fixing.
Said liquid back pipe is a straight tube.The spiral angle of said spiral plate is: between 30 ° to 45 °.
Said jet water spout is annular jet water spout.
The utility model is simple, compact and reasonable for structure; Can reduce the cost of whole crystallizing evaporator system, save the space that whole crystallizing evaporator system workshop is arranged, low preparation cost; Control the flow direction of air-flow through the guide effect of spiral plate; Simultaneously, because liquid back pipe is straight tube, avoided liquid accumulating in liquid back pipe; And temperature is consistent with crystallizing evaporator; Avoided causing the material crystallization because of temperature drop, again can be through jet water spout not timing separator is cleaned, thus avoided the obstruction of liquid back pipe; Liquid back pipe outlet design is avoided air-flow in liquid back pipe, to form short circuit and is reduced separating effect when crystallizing evaporator moves below the liquid level.
Description of drawings
Fig. 1 is the utility model structural front view.
Fig. 2 is the utility model structure vertical view.
The specific embodiment
Following the utility model will combine the embodiment in the accompanying drawing to further describe:
As shown in Figure 1, comprising: liquid back pipe 1, lower cone 2, cylindrical shell 3, muffler 4, spiral plate 5, jet water spout 6 and fixed head 7 etc.
Be provided with muffler 4 in the utility model cylindrical shell 3, between muffler 4 and cylindrical shell 3, be furnished with spiral plate 5, the spiral angle of said spiral plate 5 is: between 30 ° to 45 °, jet water spout 6 is connected with muffler 4, and said jet water spout 6 is annular jet water spout.Said cylindrical shell 3 lower ends are provided with lower cone 2, and lower cone 2 is welded to connect with liquid back pipe 1, and said liquid back pipe 1 is a straight tube.Said cylindrical shell 3 upper ends are fixedly connected fixed head 7, and fixed head 7 is fixing with the welding of crystallizing evaporator upper cover.
The utility model is confirmed the diameter of muffler 4 and the clearance distance of cylindrical shell to crystallizing evaporator upper cover (top) according to the evaporation capacity (indirect steam vapour amount) of crystallizing evaporator; And then the diameter of definite cylindrical shell 3, confirm the angle of spiral plate 5 according to the indirect steam flow velocity.After whole cyclone separator completes separately, be welded to connect completion to jet water spout 6 and crystallizing evaporator upper cover preformed hole earlier, again muffler 4 and crystallizing evaporator top preformed hole implemented to be welded to connect; In welding process, to keep whole cyclone separator vertical with the angle of evaporative crystallization, fixing through 3 fixed heads 7 then with the welding of crystallizing evaporator upper cover.At last liquid back pipe 1 and cone 2 are welded to connect.
The operation principle of the utility model and the course of work:
No matter be which kind of material, in the crystallizing evaporator evaporation process, always carry a certain amount of material secretly in the indirect steam and escape outward.Through cyclone separator the time; Indirect steam revolves the branch separator through the gap entering of cyclone separator and crystallizing evaporator earlier; Get into then between muffler 4 and the cylindrical shell 3, flow according to the angle rotation of spiral plate 5 then, produce centrifugal force; Make the heavier material of proportion flow down, be back to crystallizing evaporator through liquid back pipe then along cylindrical shell and cone inwall.Indirect steam then can flow to next body or the condenser of imitating through muffler.
Crucial effect is played in the setting of the utility model spiral plate and angle thereof in work; Reach the flows at angles of forcing indirect steam to envision according to design through it, in the whole flow process of air-flow, the centrifugal force of generation is with the fluid separation applications of carrying secretly in the air-flow to separator inwall; Thereby flow to liquid back pipe along inwall; Gas is then overflowed from muffler fast, produces certain centrifugal force, thereby has reached the purpose that makes gas and fluid separation applications.Simultaneously be provided with annular jet water spout, can be used to clean whole separator by external hot water on separator top.
The points for attention of the utility model:
1, to polish whole cyclone separator, reduce the material wall cling phenomenon.2, regularly through jet water spout to the cleaning of washing by water of cyclone separator inside.When 3, whole crystallizing evaporator is shut down maintenance, check whether liquid back pipe has clogging.
Claims (4)
1. built-in cyclone separator means; It is characterized in that: comprise liquid back pipe (1), lower cone (2), cylindrical shell (3), muffler (4), spiral plate (5), jet water spout (6) and fixed head (7); Be provided with muffler (4) in the said cylindrical shell (3), between muffler (4) and cylindrical shell (3), be furnished with spiral plate (5), jet water spout (6) is connected with muffler (4); Said cylindrical shell (3) lower end is provided with lower cone (2); Lower cone (2) is connected with liquid back pipe (1), and said cylindrical shell (3) upper end is fixedly connected fixed head (7), and fixed head (7) is fixing with the welding of crystallizing evaporator upper cover.
2. built-in cyclone separator means as claimed in claim 1 is characterized in that: said liquid back pipe (1) is a straight tube.
3. built-in cyclone separator means as claimed in claim 1 is characterized in that: the spiral angle of said spiral plate (5) is: 30 ° to 45 °.
4. built-in cyclone separator means as claimed in claim 1 is characterized in that: said jet water spout (6) is annular jet water spout.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202594557U CN202155273U (en) | 2011-07-21 | 2011-07-21 | Built-in cyclone separator device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202594557U CN202155273U (en) | 2011-07-21 | 2011-07-21 | Built-in cyclone separator device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202155273U true CN202155273U (en) | 2012-03-07 |
Family
ID=45762923
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202594557U Expired - Fee Related CN202155273U (en) | 2011-07-21 | 2011-07-21 | Built-in cyclone separator device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202155273U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102284385A (en) * | 2011-07-21 | 2011-12-21 | 无锡荣丰生物工程有限公司 | Built-in cyclone separator device |
-
2011
- 2011-07-21 CN CN2011202594557U patent/CN202155273U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102284385A (en) * | 2011-07-21 | 2011-12-21 | 无锡荣丰生物工程有限公司 | Built-in cyclone separator device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120307 Termination date: 20180721 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |