CN106423595A - Cyclone separator - Google Patents
Cyclone separator Download PDFInfo
- Publication number
- CN106423595A CN106423595A CN201611198016.3A CN201611198016A CN106423595A CN 106423595 A CN106423595 A CN 106423595A CN 201611198016 A CN201611198016 A CN 201611198016A CN 106423595 A CN106423595 A CN 106423595A
- Authority
- CN
- China
- Prior art keywords
- cylinder
- cone
- separator
- overflow pipe
- drainage trough
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/103—Bodies or members, e.g. bulkheads, guides, in the vortex chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/085—Vortex chamber constructions with wear-resisting arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
Landscapes
- Cyclones (AREA)
Abstract
The invention discloses a cyclone separator. The cyclone separator at least comprises a separator body, and a cone with a drainage tank; the cone with the drainage tank is arranged in the separator body; and when a mixture with internal cyclone upwards moves to reach the cone with the drainage tank, because of stop of the cone, one part of large-particle mixture is forced to guide to external cyclone through the drainage tank of the cone for reseparation, so that the content of large-particle substances in the separated mixture is reduced, and the separation efficiency is improved.
Description
Technical field
The present invention relates to segregation apparatuss technical field, more particularly, to a kind of cyclone separator.
Background technology
How while reducing cost, mixture is more efficiently separated, always oil, chemical industry, medicine,
The industries such as smelting, coking plant problem of interest, the separation efficiency improving fine particle is always the problem of a lot of industry research.
The separation of mixture mainly includes solid-liquid separation, gas solid separation, the gentle solid-liquor separation of gas-liquid separation, a kind of efficient separation of design
Device has great significance for industries such as the energy, chemical industry and medicine.
Content of the invention
The present invention passes through to provide a kind of cyclone separator it is achieved that improving the technique effect of separation efficiency.
The invention provides a kind of cyclone separator, at least include：Separator body and the cone with drainage trough；Described band
The cone of drainage trough is arranged on the inside of described separator body.
Further, described separator body at least includes：Whirl cylinder, cylinder, feed pipe and overflow pipe；Described separation
Cylinder is arranged on the bottom of described whirl cylinder；Through hole is arranged at the bottom of described cylinder；Described overflow pipe is arranged on described whirl cylinder
Top；Described feed pipe is passed through described whirl cylinder with the direction tangent with described whirl cylinder.
Further, also at least include：Threaded rod；The first end of described threaded rod is fixed on described overflow pipe, described
Second end of threaded rod and described cone are threaded connection.
Further, also at least include：Connecting tube；
There is external screw thread in the end of described overflow pipe；There is female thread in the end of described connecting tube；Described overflow pipe and institute
State connecting tube to be threaded connection；
Or,
There is female thread in the end of described overflow pipe；There is external screw thread in the end of described connecting tube；Described overflow pipe and institute
State connecting tube to be threaded connection.
Further, the inwall in described whirl cylinder and/or described cylinder has drainage trough.
Further, the inwall in described whirl cylinder and/or described cylinder has wear-resistant ceramic layer.
Further, the described cone with drainage trough is cone.
The one or more technical schemes providing in the present invention, at least have the following technical effect that or advantage：
Cone with drainage trough is arranged on the inside of separator body, draws when the mixture of inward eddy moves upward to band
When at the cone of chute, due to the stop of cone, the drainage trough guiding that partly oarse-grained mixture is forced through in cone is outer
Eddy flow is separated again, thus decreasing the content of large particulate matter in the mixture isolated, and then improves separation effect
Rate.
Brief description
Fig. 1 is the structural representation of cyclone separator provided in an embodiment of the present invention；
Fig. 2 is the structural representation of the cone with drainage trough in Fig. 1；
Wherein, 1- overflow pipe, 2- whirl cylinder, 3- feed pipe, 4- cylinder, the cone with drainage trough for the 5-, 6- through hole, 7- spiral shell
Rasp bar, 8- end cap, 9- connecting tube.
Specific embodiment
The embodiment of the present invention is passed through to provide a kind of cyclone separator it is achieved that improving the technique effect of separation efficiency.
Technical scheme in the embodiment of the present invention is to solve above-mentioned technical problem, and general thought is as follows：
Cone with drainage trough is arranged on the inside of separator body, draws when the mixture of inward eddy moves upward to band
When at the cone of chute, due to the stop of cone, the drainage trough guiding that partly oarse-grained mixture is forced through in cone is outer
Eddy flow is separated again, thus decreasing the content of large particulate matter in the mixture isolated, and then improves separation effect
Rate.
In order to more fully understand technique scheme, below in conjunction with Figure of description and specific embodiment to upper
State technical scheme to be described in detail.
Referring to Fig. 1 and Fig. 2, cyclone separator provided in an embodiment of the present invention, at least include：Separator body and band drain
The cone 5 of groove；Cone 5 with drainage trough is arranged on the inside of separator body.
The structure of separator body is illustrated, separator body at least includes：Whirl cylinder 2, cylinder 4, feed pipe 3
And overflow pipe 1；Cylinder 4 is arranged on the bottom of whirl cylinder 2；Through hole 6 is arranged at the bottom of cylinder 4；Overflow pipe 1 is arranged on whirl cylinder
2 top；Feed pipe 3 is passed through whirl cylinder 2 with the direction tangent with whirl cylinder 2.
In the present embodiment, the top of whirl cylinder 2 is connected by flange with end cap 8；Overflow pipe 1 is fixed on end cap 8
Center, and be passed through whirl cylinder 2.Feed pipe 3 is arranged on the middle part of whirl cylinder 2.
Depth in order to overflow pipe 1 is passed through with whirl cylinder 2 is adjusted, and also at least includes：Connecting tube 9；
There is external screw thread in the end of overflow pipe 1；There is female thread in the end of connecting tube 9；Overflow pipe 1 is passed through with connecting tube 9
Threaded；
Or,
There is female thread in the end of overflow pipe 1；There is external screw thread in the end of connecting tube 9；Overflow pipe 1 is passed through with connecting tube 9
Threaded.
The structure of the embodiment of the present invention is further described, also at least includes：Threaded rod 7；The first end of threaded rod 7
It is fixed on overflow pipe 1, the second end of threaded rod 7 is threaded connection with the cone 5 with drainage trough.By rotational band drainage trough
Cone 5 its position in separator body can be adjusted.
The structure of the embodiment of the present invention is illustrated further, has in the inwall of whirl cylinder 2 and/or cylinder 4 and draw
Chute.
In order to extend the service life of the embodiment of the present invention, there is wear-resistant ceramic in the inwall of whirl cylinder 2 and/or cylinder 4
Layer.
Need exist for illustrating, all parts in the embodiment of the present invention are all manufactured using anticorrosion material, so that
The embodiment of the present invention can be steady in a long-term under the environment under high pressure containing etchant gas work.
In the present embodiment, whirl cylinder 2 is cylindrical structural, and cylinder 4 is conical structure, the cone 5 with drainage trough
For cone, and the diameter of cone determines according to practical situation between the diameter of overflow pipe 1 is to the diameter of whirl cylinder 2.
The following is the operation principle of the embodiment of the present invention：
When carrying out detached job, it is downward that mixture enters whirl cylinder 2 through feed pipe 3 in tangential direction with certain speed
For the helical movement, the big granule of density is thrown toward wall and moves downward by centrifugal inertial force effect and flows out from bottom through hole 6, little particle
Solid, liquids and gases rise become internal layer eddy flow.When at internal layer eddy flow is up to the cone 5 with drainage trough, granule
By the drainage trough on the conical surface, directed outwards carry out secondary separation to larger portion mixture again.
【Technique effect】
1st, the cone 5 with drainage trough is arranged on the inside of separator body, when the mixture of inward eddy moves upward to
When at the cone 5 with drainage trough, due to the stop of cone, the drainage trough that partly oarse-grained mixture is forced through in cone is led
Being separated again to contour stealth, thus decreasing the content of large particulate matter in the mixture isolated, and then being improve point
From efficiency.
2nd, by threaded rod 7 using it is achieved that tune to the position of the cone 5 with drainage trough according to the actual requirements
Whole, with the desired separated effect required for reaching, further increase the separation efficiency of the embodiment of the present invention.
3rd, by the use to connecting tube 9, actual according to demand the depth that overflow pipe 1 stretches into whirl cylinder 2 can be adjusted.
4th, the inwall in whirl cylinder 2 and/or cylinder 4 have drainage trough such that it is able to guiding entrance mixture more added with
Effect ground, to bottom eddy flow, further improves the separation efficiency of the embodiment of the present invention.
5th, the inwall in whirl cylinder 2 and/or cylinder 4 has wear-resistant ceramic layer, thus extending making of the embodiment of the present invention
Use the life-span.
Embodiment of the present invention structure is simple, both can improve the separation efficiency of finely ground particle substance, can be overflow by adjustment again
The position of position in whirl cylinder 2 for flow tube 1 lower end and cone with the desired separated effect required for reaching, this structure for
The separation efficiency of finely ground particle substance is significantly improved.Additionally, the embodiment of the present invention also has can improve solid-liquid, gas-solid, gas
The advantage of the solid material separation efficiency of liquid, and can run steadily in the long term under high pressure operating mode and strong corrosive environment.
Although preferred embodiments of the present invention have been described, but those skilled in the art once know basic creation
Property concept, then can make other change and modification to these embodiments.So, claims are intended to be construed to including excellent
Select embodiment and fall into being had altered and changing of the scope of the invention.
Obviously, those skilled in the art can carry out the various changes and modification essence without deviating from the present invention to the present invention
God and scope.So, if these modifications of the present invention and modification belong to the scope of the claims in the present invention and its equivalent technologies
Within, then the present invention is also intended to comprise these changes and modification.
Claims (7)
1. a kind of cyclone separator is it is characterised in that at least include：Separator body and the cone with drainage trough；Described band draws
The cone of chute is arranged on the inside of described separator body.
2. separator as claimed in claim 1 is it is characterised in that described separator body at least includes：Whirl cylinder, separation
Cylinder, feed pipe and overflow pipe；Described cylinder is arranged on the bottom of described whirl cylinder；Through hole is arranged at the bottom of described cylinder；Institute
State the top that overflow pipe is arranged on described whirl cylinder；Described feed pipe is passed through described eddy flow with the direction tangent with described whirl cylinder
Cylinder.
3. separator as claimed in claim 2 is it is characterised in that also at least include：Threaded rod；The first end of described threaded rod
It is fixed on described overflow pipe, the second end of described threaded rod and described cone are threaded connection.
4. separator as claimed in claim 3 is it is characterised in that also at least include：Connecting tube；
There is external screw thread in the end of described overflow pipe；There is female thread in the end of described connecting tube；Described overflow pipe and described company
Adapter is threaded connection；
Or,
There is female thread in the end of described overflow pipe；There is external screw thread in the end of described connecting tube；Described overflow pipe and described company
Adapter is threaded connection.
5. separator as claimed in claim 2 is it is characterised in that the inwall in described whirl cylinder and/or described cylinder has
Drainage trough.
6. separator as claimed in claim 2 is it is characterised in that the inwall in described whirl cylinder and/or described cylinder has
Wear-resistant ceramic layer.
7. the separator as any one of claim 1-6 is it is characterised in that the described cone with drainage trough is circular cone
Body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611198016.3A CN106423595A (en) | 2016-12-22 | 2016-12-22 | Cyclone separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611198016.3A CN106423595A (en) | 2016-12-22 | 2016-12-22 | Cyclone separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106423595A true CN106423595A (en) | 2017-02-22 |
Family
ID=58215135
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611198016.3A Pending CN106423595A (en) | 2016-12-22 | 2016-12-22 | Cyclone separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106423595A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107281874A (en) * | 2017-07-27 | 2017-10-24 | 成都川通达科技有限公司 | A kind of New-type Swirl Flow separator |
| CN109488262A (en) * | 2019-01-21 | 2019-03-19 | 常州大学 | A kind of exploitation of gas hydrates silt cyclone separator |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1870947A (en) * | 1930-11-07 | 1932-08-09 | A Neher Van | Dust collector |
| JPS50150875U (en) * | 1974-05-31 | 1975-12-15 | ||
| CN200942363Y (en) * | 2006-09-01 | 2007-09-05 | 辽宁金协机械制造有限公司 | Hydrocyclone |
| CN101590451A (en) * | 2009-02-27 | 2009-12-02 | 太原理工大学 | Coal slime rotational flow reselecting column |
| CN201809458U (en) * | 2010-08-04 | 2011-04-27 | 肇庆市飞南金属有限公司 | Adjustable overflow device |
| CN102350405A (en) * | 2011-08-17 | 2012-02-15 | 中国农业机械化科学研究院呼和浩特分院 | Universal type cyclone separator |
| CN202893541U (en) * | 2012-11-02 | 2013-04-24 | 中交上海航道勘察设计研究院有限公司 | Cyclone separator of tapered overflowing pipe |
| CN204093815U (en) * | 2014-09-30 | 2015-01-14 | 西安科技大学 | Colliery dust collecting |
| CN204134754U (en) * | 2014-08-20 | 2015-02-04 | 宿迁嵘锦信息科技有限公司 | Accelerate cyclone separator |
| CN204746640U (en) * | 2015-06-11 | 2015-11-11 | 揭阳市绿源环保处理有限公司 | Organic matter hydrocyclone separation device |
| CN205392781U (en) * | 2016-03-01 | 2016-07-27 | 山东科技大学 | Easily adjust depth of extended overflow pipe's swirler |
-
2016
- 2016-12-22 CN CN201611198016.3A patent/CN106423595A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1870947A (en) * | 1930-11-07 | 1932-08-09 | A Neher Van | Dust collector |
| JPS50150875U (en) * | 1974-05-31 | 1975-12-15 | ||
| CN200942363Y (en) * | 2006-09-01 | 2007-09-05 | 辽宁金协机械制造有限公司 | Hydrocyclone |
| CN101590451A (en) * | 2009-02-27 | 2009-12-02 | 太原理工大学 | Coal slime rotational flow reselecting column |
| CN201809458U (en) * | 2010-08-04 | 2011-04-27 | 肇庆市飞南金属有限公司 | Adjustable overflow device |
| CN102350405A (en) * | 2011-08-17 | 2012-02-15 | 中国农业机械化科学研究院呼和浩特分院 | Universal type cyclone separator |
| CN202893541U (en) * | 2012-11-02 | 2013-04-24 | 中交上海航道勘察设计研究院有限公司 | Cyclone separator of tapered overflowing pipe |
| CN204134754U (en) * | 2014-08-20 | 2015-02-04 | 宿迁嵘锦信息科技有限公司 | Accelerate cyclone separator |
| CN204093815U (en) * | 2014-09-30 | 2015-01-14 | 西安科技大学 | Colliery dust collecting |
| CN204746640U (en) * | 2015-06-11 | 2015-11-11 | 揭阳市绿源环保处理有限公司 | Organic matter hydrocyclone separation device |
| CN205392781U (en) * | 2016-03-01 | 2016-07-27 | 山东科技大学 | Easily adjust depth of extended overflow pipe's swirler |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107281874A (en) * | 2017-07-27 | 2017-10-24 | 成都川通达科技有限公司 | A kind of New-type Swirl Flow separator |
| CN109488262A (en) * | 2019-01-21 | 2019-03-19 | 常州大学 | A kind of exploitation of gas hydrates silt cyclone separator |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170222 |