CN107670838A - A kind of spiral-shaped cyclone - Google Patents
A kind of spiral-shaped cyclone Download PDFInfo
- Publication number
- CN107670838A CN107670838A CN201711069639.5A CN201711069639A CN107670838A CN 107670838 A CN107670838 A CN 107670838A CN 201711069639 A CN201711069639 A CN 201711069639A CN 107670838 A CN107670838 A CN 107670838A
- Authority
- CN
- China
- Prior art keywords
- spiral
- cavity
- ore deposit
- ore
- outlet
- 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
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/48—Washing granular, powdered or lumpy materials; Wet separating by mechanical classifiers
- B03B5/52—Spiral classifiers
Abstract
Proposed by the present invention is a kind of spiral-shaped cyclone.By being fixedly connected with spiral cavity centered on support column, spiral cavity is made up of the second circular cavity of inner side and first circular cavity in outside, spiral cavity opening is provided with ore inlet port, first circular cavity and the second circular cavity are exported by triangular chamber and coarse grain ore deposit, intermediate particle outlet and particulate ore deposit outlet.The present invention is simple in construction, and floor space is small, and ore dressing is high with classification efficiency.Suitably it is used as preparation equipment application.
Description
Technical field
The present invention relates to preparation equipment technical field, particularly a kind of spiral-shaped cyclone.
Background technology
At present, in the classification and sorting process technology of mineral processing at home and abroad, big-and-middle-sized ore dressing plant is substantially all using rotation
Stream device is classified, and uses the techniques such as spiral chute to carry out reselection operation.
Cyclone is formed by connecting by hollow cylinder and circular cone, inserts an overflow pipe at the center of cylinder, tangentially side
To mineral-feeding pipe is connected to, dirt sand mouth is left in the bottom of cone.Its operation principle is:Ore pulp enters along mineral-feeding pipe under pressure
After entering cyclone, make gyration under the limitation of cylindrical wall.Under the influence of centrifugal force, coarse granule is thrown near wall,
And as external spiral stream is discharged by bottom；Fine grained is trapped in inside spin stream, arranged by overflow pipe because centrifugal sedimentation speed is small
Go out.External spiral stream constantly expands in flowing downward, and is full of overflow pipe lower periphery whole region, and a portion is directly entered
Enter into overflow pipe, turn into short-circuit flow.Coarse granule can be brought directly in overflow by short-circuit flow, reduce classification efficiency.It, which has, divides
Stage efficiency is high, and floor space is small, does not have the advantages that moving component, but be the shortcomings that cyclone：Fluctuation of service, due to its knot
The defects of structure, there is short-circuit flow phenomenon, cause to be mingled with coarse granule in overflow fine grained product, reduce classification efficiency.
One narrow and long open slot is bent into curl around vertical axis, just forms spiral chute.Its main body work
It is a spiral shaped openings cell body as part.Spiral chute is that choosing point is carried out to ore pulp by gravity, after ore pulp is fed from top, in weight
Under power effect, during being flowed downward along chute, particle swarm is layered in ore pulp, the transverse direction of the heavy suite of bottom along bottom land
The gradient is moved to the inner edge of groove, and final concentrate is formed in cell body end；Light mineral particle positioned at upper strata is then with revolution flowing
Ore pulp is moved downward along on the outside of groove, and mine tailing discharge is finally formed in the end of groove.Its advantage is movement-less part, operation letter
Single, cost is cheap；But its beneficiating efficiency is low, disposal ability is small, long flow path, and floor space is big, can only handle relatively crude
Grade mineral, application are narrower etc..
The content of the invention
The shortcomings that in order to overcome existing preparation equipment to exist, the present invention propose a kind of spiral-shaped cyclone.The eddy flow
Device carries out ore dressing by setting spiral cavity on the support columns, by spiral cavity, solves the technical problem of Mineral Classification.
Scheme is used by the present invention solves technical problem：
By being fixedly connected with spiral cavity centered on support column, spiral cavity is by the second circular cavity of inner side and first circle in outside
Shape chamber forms, spiral cavity opening be provided with ore inlet port, the first circular cavity and the second circular cavity by triangular chamber with it is thick
The outlet of grain ore deposit, intermediate particle outlet and particulate ore deposit outlet.
Good effect, the present invention is simple in construction, and floor space is small, and ore dressing is high with classification efficiency.Suitably it is used as preparation equipment
Using.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention.
In figure, 1. support columns, 2. spiral cavities, 3. ore inlet ports, 4. first circular cavities, 5. second circular cavities, 6. triangles
Chamber, the outlet of 7. coarse grain ore deposits, the outlet of 8. intermediate particles, the outlet of 9. particulate ore deposits.
Embodiment
Illustrate the embodiment of the present invention below in conjunction with the accompanying drawings.
As illustrated, by being fixedly connected with spiral cavity 2 centered on support column 1, spiral cavity is second circular by inner side
Chamber 5 and first circular cavity 4 in outside form, and spiral cavity opening is provided with ore inlet port 3, the first circular cavity and the second circle
Chamber is connected by triangular chamber 6 and coarse grain ore deposit outlet 7, intermediate particle outlet 8 with particulate ore deposit outlet 9.
The ore inlet port is connected by adpting flange with mineral-feeding pipe, and ore inlet port is arranged on the top, close of spiral cavity
Position at support column；
The intermediate particle outlet and the outlet of coarse grain ore deposit are arranged on the bottom of spiral cavity, close to the edge position of spiral cavity
Put；
Described particulate goes out mine mouth and is connected by flange with particulate ore deposit efferent duct；
Described intermediate particle ore deposit outlet is connected by flange with intermediate particle ore deposit efferent duct；
Described coarse grain ore deposit outlet is connected by flange with coarse grain ore deposit efferent duct.
Operation principle：
When ore pulp to be separated is entered in spiral cavity with certain pressure from the ore inlet port of spiral cyclone, then it is forced to make
Gyration.Because the centrifugal force that it is subject to is of different sizes, the coarse granule in ore pulp overcomes the resistance of water to enter cross section for circle
The intermediate particle enrichment region and coarse granule enrichment region of shape chamber, decline along the cavity wall spiral of this circular cavity, until under spiral cavity
Portion, is exported by intermediate particle ore deposit respectively and intermediate particle ore deposit efferent duct and the outlet of coarse grain ore deposit and coarse grain ore deposit efferent duct enter lower road
Process.Centrifugal force is smaller suffered by fine grained, is similar triangular chamber in cross section under the collective effect of gravity and water flow pressure
Fine grained enrichment region inside spin decline, until spiral cavity bottom, exported by particulate ore deposit and particulate ore deposit efferent duct enter
Next procedure, so as to reach the purpose of classification.
The present invention can not only be used for classifying equipoment, but also as sorting equipment.During as classifying equipoment, compared with cyclone,
Short-circuit flow is thoroughly avoided, improves effectiveness of classification, increases graded product, classification efficiency is high.During as sorting equipment, slipped with spiral
Groove is compared, and floor space is small, and disposal ability is stronger, and processing grade is wide, can handle micro-size fraction mineral.
Feature：
Its structure integrates the design feature of cyclone and spiral chute, i.e. ore pulp is entered by ore inlet port under the effect of the pressure
In spiral cavity, it is forced to do gyration.During spiral declines, because the centrifugal force that it is subject to is of different sizes, ore pulp
In coarse granule overcome water resistance enter most edge cross section be circular cavity coarse granule enrichment region, along the chamber of this circular cavity
Wall spiral declines, until the bottom of spiral cavity, is exported by coarse grain ore deposit and coarse grain ore deposit efferent duct enters next procedure.In ore pulp
Intermediate particle overcome water resistance enter near-end cross section be circular cavity intermediate particle enrichment region, along the chamber of this circular cavity
Wall spiral declines, until the bottom of spiral cavity, is exported by intermediate particle ore deposit and intermediate particle grain ore deposit efferent duct enters lower road
Process.Centrifugal force is smaller suffered by fine grained, is subtriangular chamber in cross section under the collective effect of gravity and water flow pressure
Fine grained enrichment region inside spin decline, until spiral cavity bottom, exported by particulate ore deposit and particulate ore deposit efferent duct enter
Next procedure, so as to reach the purpose of classification.
The present invention can not only be used for classifying equipoment, but also as sorting equipment.During as classifying equipoment, compared with cyclone,
Short-circuit flow phenomenon is thoroughly avoided, improves effectiveness of classification, increases graded product, classification efficiency is high；During as sorting equipment, with spiral shell
Rotation chute is compared, and floor space is small, and disposal ability is stronger, and processing grade is wide, can handle micro-size fraction mineral, application
Extensively.
Claims (6)
1. a kind of spiral-shaped cyclone, it is characterized in that：By support column（1）Centered on be fixedly connected with spiral cavity（2）, spiral
Cavity by inner side the second circular cavity（5）With first circular cavity in outside（4）Composition, is provided with into ore deposit in spiral cavity opening
Mouthful（3）, the first circular cavity and the second circular cavity pass through triangular chamber（6）Exported with coarse grain ore deposit（7）, intermediate particle outlet（8）With
Particulate ore deposit exports（9）Connection.
2. a kind of spiral-shaped cyclone according to claim 1, it is characterized in that：The ore inlet port by adpting flange with
Mineral-feeding pipe is connected, and ore inlet port is arranged on the top of spiral cavity, close to position at support column.
3. a kind of spiral-shaped cyclone according to claim 1, it is characterized in that：The intermediate particle outlet and coarse grain ore deposit
Outlet is arranged on the bottom of spiral cavity, close to the edge position of spiral cavity.
4. a kind of spiral-shaped cyclone according to claim 1, it is characterized in that：Described particulate goes out mine mouth and passes through flange
It is connected with particulate ore deposit efferent duct.
5. a kind of spiral-shaped cyclone according to claim 1, it is characterized in that：Described intermediate particle ore deposit outlet passes through
Flange is connected with intermediate particle ore deposit efferent duct.
6. a kind of spiral-shaped cyclone according to claim 1, it is characterized in that：Described coarse grain ore deposit outlet passes through flange
It is connected with coarse grain ore deposit efferent duct.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711069639.5A CN107670838A (en) | 2017-11-03 | 2017-11-03 | A kind of spiral-shaped cyclone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711069639.5A CN107670838A (en) | 2017-11-03 | 2017-11-03 | A kind of spiral-shaped cyclone |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107670838A true CN107670838A (en) | 2018-02-09 |
Family
ID=61146087
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711069639.5A Pending CN107670838A (en) | 2017-11-03 | 2017-11-03 | A kind of spiral-shaped cyclone |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107670838A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113560029A (en) * | 2020-04-28 | 2021-10-29 | 张术军 | Apparatus and method for separating particles from a particulate suspension |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4324334A (en) * | 1979-02-05 | 1982-04-13 | Inheed Pty Ltd. | Spiral separators |
| CN102553704A (en) * | 2012-01-16 | 2012-07-11 | 鞍钢集团矿业公司 | Spiral cyclone |
| CN105370313A (en) * | 2015-07-29 | 2016-03-02 | 深圳市工勘岩土集团有限公司 | Rock static blasthole drilling dust reduction device |
| CN205926062U (en) * | 2016-08-25 | 2017-02-08 | 安徽纽亚达科技有限责任公司 | Separate mining swirler |
| CN205975844U (en) * | 2016-07-26 | 2017-02-22 | 周忠 | Single riser swirler of jam is prevented to leak protection water |
-
2017
- 2017-11-03 CN CN201711069639.5A patent/CN107670838A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4324334A (en) * | 1979-02-05 | 1982-04-13 | Inheed Pty Ltd. | Spiral separators |
| CN102553704A (en) * | 2012-01-16 | 2012-07-11 | 鞍钢集团矿业公司 | Spiral cyclone |
| CN105370313A (en) * | 2015-07-29 | 2016-03-02 | 深圳市工勘岩土集团有限公司 | Rock static blasthole drilling dust reduction device |
| CN205975844U (en) * | 2016-07-26 | 2017-02-22 | 周忠 | Single riser swirler of jam is prevented to leak protection water |
| CN205926062U (en) * | 2016-08-25 | 2017-02-08 | 安徽纽亚达科技有限责任公司 | Separate mining swirler |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113560029A (en) * | 2020-04-28 | 2021-10-29 | 张术军 | Apparatus and method for separating particles from a particulate suspension |
| US11541332B2 (en) | 2020-04-28 | 2023-01-03 | Shujun Zhang | Apparatus for separating particles from a particulate suspension |
| CN113560029B (en) * | 2020-04-28 | 2024-01-09 | 张术军 | Apparatus and method for separating particles from a particulate suspension |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203425904U (en) | Bottom cone spiral flow impeller type water supply magnetic separation column | |
| CN204769192U (en) | Hydraulic cyclone that unshorting is flowed | |
| CN205731673U (en) | A kind of multi-product cyclone | |
| CN109046743A (en) | A kind of compound force field sorting machine and its method for separating for magnetic iron ore sorting | |
| CN204412476U (en) | Gas phase classifying equipoment | |
| CN201002058Y (en) | Mining slurry grading swirler | |
| CN107670838A (en) | A kind of spiral-shaped cyclone | |
| CN104624405A (en) | High-efficiency hydrocyclone | |
| CN102430485A (en) | Spiral-flow type separator | |
| US2655263A (en) | Ore pulp concentrator | |
| CN201815153U (en) | Graded overflow device for concentrator | |
| CN206199509U (en) | A kind of product cyclone of scalping four | |
| CN204122265U (en) | A kind of four-product efficient separation cyclone | |
| CN207169971U (en) | A kind of fine graded special hydrocyclone of magnetizing roast | |
| CN102553704B (en) | Spiral cyclone | |
| CN103586128B (en) | Cyclonic magnetic separation column | |
| CN207204402U (en) | Mining swirler | |
| CN205815949U (en) | A kind of arrangement of cyclone | |
| CN206965950U (en) | A kind of concentration-type cyclone | |
| CN202427547U (en) | Spiral cyclone | |
| CN108970798A (en) | A kind of novel spiral chute | |
| CN205361641U (en) | It throws tail and thickness three hierarchical product magnet separators to have preliminary election concurrently | |
| CN108311295A (en) | A kind of compound force field step reinforcing centrifugal ore separator | |
| CN206924886U (en) | The device of coal in being extracted in a kind of gangue | |
| CN106890733A (en) | Double middle coal fecund product swirlers and its application method are selected in a kind of underflow again |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180209 |
|
| RJ01 | Rejection of invention patent application after publication |