CN201552069U - Cyclone separator for manufacturing spherical graphite - Google Patents
Cyclone separator for manufacturing spherical graphite Download PDFInfo
- Publication number
- CN201552069U CN201552069U CN2009202585531U CN200920258553U CN201552069U CN 201552069 U CN201552069 U CN 201552069U CN 2009202585531 U CN2009202585531 U CN 2009202585531U CN 200920258553 U CN200920258553 U CN 200920258553U CN 201552069 U CN201552069 U CN 201552069U
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- separator
- primary
- cyclone
- spherical graphite
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Abstract
The utility model provides a cyclone separator for manufacturing spherical graphite, which relates to a cyclone separator, and is provided with a support and a material storage, the upper end of the material storage is provided with a primary separator and a secondary separator, the bottom ends of the primary separator and the secondary separator are respectively connected with the material storage, the top parts of the primary separator and the secondary separator are provided with a cyclone distribution cylinder which connects the top parts of the primary separator and the secondary separator together in series, the secondary separator is formed by connecting two cylinder bodies together in parallel, the primary separator is provided with a feed connecting opening, the secondary separator is provided with an air exhaust connecting opening, and the cyclone distribution cylinder comprises a primary separation delivery cylinder and a secondary separation delivery cylinder which are respectively sheathed on top centers of the primary separator and the secondary separator. The benefits are as follows: the cyclone separator has fast speed, high separation rate, good sealing performance of equipment and no pollution, reduces loss by more than 30%, increases yield by more than 80% and can realize zero emission of dust.
Description
Technical field
The utility model relates to a kind of cyclone separator, a kind of specifically cyclone separator that is used to produce spherical graphite.
Background technology
Cyclone separator in the graphite preparation, its major function is the thickness particle of further isolating by in the graphite powder after the refinement, and the quality of separating effect directly influences the quality of product.In the prior art, separation method to graphite powder is, adopt a cylinder, for this reason, graphite powder after the pulverizing can not thoroughly separate refinement, and the dust that should not collect confuses graphite powder particle and is collected in together together, and the graphite powder particle that should collect and dust confuse together and be discharged, waste material, also reduced the quality of product.In the prior art, also the defective of Cun Zaiing is, separator is behind long time continuous working, and dust is easily piled up in the separator, has had a strong impact on and restricted the normal operation of whole production system.
Summary of the invention
The deficiency that the utility model purpose is intended to solve the problems of the technologies described above effectively improve graphite powder separation in process of production, and speed is fast, the separation rate height, the equipment good airproof performance, pollution-free, cut down the consumption of energy more than 30%, improve productive rate more than 80%, can realize dust zero discharge.
The technical scheme that the utility model adopted is: be provided with support and material holder, be provided with primary separator and second-stage separator in the upper end of material holder, the bottom of primary separator and second-stage separator is connected with the material holder respectively, be provided with a whirlwind distribution drum at the top of primary separator and second-stage separator, the whirlwind distribution drum is with the top serial connection of primary separator and second-stage separator.
The utility model, described second-stage separator are two and the cylindrical shell that connects.
The utility model, described whirlwind distribution drum is provided with one-level separation transport tube and separates transport tube with secondary.
The utility model is provided with the charging connector on primary separator, be provided with the air draft connector on second-stage separator.
The utility model, described one-level is separated transport tube and is separated transport tube with secondary, is set in the center, last top of primary separator and second-stage separator.
The utility model, the junction of described primary separator and material holder also is provided with blast volume controller, junction at second-stage separator and material holder also is provided with funnel, the funnel junction is to adopt to be tightly connected, the setting of funnel is for the i.e. material rectification normalizing of the whereabouts of two and the cylindrical shell that connects of second-stage separator, junction between funnel and the material holder also is provided with a blast volume controller, is more conducive to material collection in the material holder.
The utility model, the bottom of described material holder is provided with material outlet, is provided with hand-operated valve on material outlet, and the whereabouts amount that the interior material of adjusting holder that can be manual is set of hand-operated valve avoids material to block discharging opening.
Described primary separator and second-stage separator all are to be provided with charging aperture on sidewall, can make so more that the spiral rotation separates under the effect of the material air-flow in separator that enters, the diameter of primary separator is greater than the diameter of second-stage separator, second-stage separator is two and the cylindrical shell that connects, the whirlwind distribution drum is attempted by the charging connector of two cylindrical shells, having guaranteed like this can be to the air intake feeding simultaneously of two cylindrical shells, secondary separates the center, last top that transport tube is sleeved on these two and the cylindrical shell that connects and that is to say that secondary separation transport tube is to be sleeved on center, top on the second-stage separator, because two cylindrical shells are and connect setting, so it also is to separate transport tube by two to connect together that the secondary on two cylindrical shells separates transport tube, the separation process that can guarantee whole material so all is incremental carrying out in airtight separator, has also avoided dust pollution in the time of with the more effective separation of material.
Described blast volume controller is an airlock, is made of motor, impeller and seal bootr, and impeller is arranged in the seal bootr, relies on driven by motor to produce active force material will be transported to subordinate.Be installed in the material outlet place of the material holder of working under the negative pressure, material in the material holder, play the effect of convey materials by the impeller in the airlock, airlock is being undertaken the effect of sealing again simultaneously, prevent to suck air from material outlet in the process of air delivery, guaranteed the normal discharge of material holder.
The whirlwind distribution drum is with the top serial connection of primary separator and second-stage separator, and described serial connection is meant that the air inducing connector of one-level separation transport tube is connected in series with the air intake feeding port of second-stage separator.
The beneficial effects of the utility model are:
The utility model compact overall structure is convenient to install; It all is to be provided with air inlet on sidewall for primary separator and second-stage separator, and the position of air inlet setting all is lower than the whirlwind distribution drum, makes like this that material is easier to be rotated separation in separator, effectively improves graphite powder separation in process of production; Adopted a plurality of separators, the good airproof performance of equipment after twice separation, had both solved the halfway problem of feed separation of a separator, had avoided material through the waste that first separation does not thoroughly cause, and had saved cost, improved productive rate more than 80%; Dust is difficult for piling up, thereby has increased the stream time of separator, has improved the efficient of material production; Separation process of the present utility model all is to carry out in airtight relatively space, both can well classification cycle separate also difficult by dust pollution, environment friendly and pollution-free; The separation rate height separates hastening to cut down the consumption of energy more than 30% soon, can realize dust zero discharge.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is a schematic top plan view of the present utility model;
Mark is among the figure: 1, support, 2, the material holder, 3, primary separator, 4, second-stage separator, 5, the whirlwind distribution drum, 6, one-level separates transport tube, 7, secondary separates transport tube, and 8, the charging connector, 9, the air draft connector, 10, blast volume controller, 11, funnel, 12, material outlet, 13, hand-operated valve, 14, air intake feeding port, 15, the air inducing connector, 16, combination Blowing stopper I.
The specific embodiment
As shown in Figure 1, support 1 below is provided with material holder 2, support 1 top is provided with primary separator 3 and second-stage separator 4, above material holder 2, be provided with primary separator 3 and second-stage separator 4, the bottom of primary separator 3 and second-stage separator 4 is connected with material holder 2 respectively, on primary separator 3, be provided with the charging connector, whirlwind distribution drum 5 is with the top serial connection of primary separator 3 and second-stage separator 4, the center, top is respectively equipped with one-level and separates transport tube 6 and separate transport tube 7 with secondary on primary separator 3 and second-stage separator 4, on secondary separation transport tube 7, be provided with air draft connector 9, the air inducing connector 15 that one-level is separated transport tube 6 is connected in series with the air intake feeding port 14 of second-stage separator 4, primary separator 3 also is provided with blast volume controller 10 with the junction of material holder 2, junction at second-stage separator 4 and material holder 2 also is provided with funnel 11, be provided with combination Blowing stopper I 16 between funnel 11 and the material holder 2, the bottom of material holder 2 is provided with material outlet 12, is provided with hand-operated valve 13 on material outlet 12.
The graphite material is admitted in the primary separator 3 from the charging connector, material rotates with flow spiral at primary separator 3 inwalls, one-level separation this moment transport tube 6 provides one air inducing, the light smaller particles of primary separator 3 inwalls rotation is attracted primary separator 3, big heavier particle is sent into material holder 2 through blast volume controller, the granule that attracts in the primary separator 3 sent into two of second-stage separator 4 respectively with air inducing suction and the cylindrical shell that connects in, material rotates with flow spiral at two and the cylinder inboard wall that connects, secondary separation this moment transport tube 7 provides air inducing power by air draft connector 9, light smaller particles in two of second-stage separator 4 and the cylindrical shell that connects is attracted two and the cylindrical shell that connects, big heavier particle is through funnel rectification normalizing, send into material holder 2, the material of collecting in the material holder 2 is discharged through material outlet 12.
The utility model is to adopt gas actuation power, so good airproof performance of device, the charging connector 8 of cyclone separator is connected with air-flow vortex powder refinement machine, if use the nodularization grader in the production procedure, then charging connector 8 is connected with the nodularization grader, after material enters cyclone separator, under the interaction of centrifugal force and negative pressure gravitation, descend along the barrel rotation than coarse dust, fall into material holder 2, discharging from material outlet 12 in the material holder 2 than coarse dust, be transported to the air-flow vortex powder refinement machine of next working group, described air-flow vortex powder refinement machine can be a kind of QWJ-60 type air-flow vortex pulverizing mill, and the gas that contains thin dirt is discharged by air draft connector 9, enters the pulse device for recovering powder and is collected once more.
It all is to be provided with charging aperture on sidewall for primary separator 3 and second-stage separator 4, make like this that material is easier to be rotated separation in separator, from primary separator 3 isolated materials, a part falls to collecting, and another part enters second-stage separator 4 with air-flow, after twice separation, can guarantee separated more thorough of material, avoided material through the waste that first separation does not thoroughly cause, saved cost, the quality of material is also better simultaneously; Separation process of the present utility model all is to carry out in airtight relatively space, adopts gas to do power, both can well classification cycle separate also difficult by dust pollution; Adopted a plurality of separators, improved the efficient of material production, dust also is difficult for piling up, thereby has increased the stream time of separator, and the separation rate height separates hastening to cut down the consumption of energy more than 30% soon, improves productive rate more than 80%, can realize dust zero discharge.
Claims (7)
1. cyclone separator that is used to produce spherical graphite, be provided with support (1) and material holder (2), it is characterized in that: be provided with primary separator (3) and second-stage separator (4) in the upper end of material holder (2), the bottom of primary separator (3) and second-stage separator (4) is connected with material holder (2) respectively, top at primary separator (3) and second-stage separator (4) is provided with a whirlwind distribution drum (5), and whirlwind distribution drum (5) is with the top serial connection of primary separator (3) and second-stage separator (4).
2. a kind of cyclone separator that is used to produce spherical graphite according to claim 1 is characterized in that: described second-stage separator (4) is two and the cylindrical shell that connects.
3. a kind of cyclone separator that is used to produce spherical graphite according to claim 1 is characterized in that: described whirlwind distribution drum (5) is provided with one-level separation transport tube (6) and separates transport tube (7) with secondary.
4. a kind of cyclone separator that is used to produce spherical graphite according to claim 1 is characterized in that: be provided with charging connector (8) on primary separator (3), be provided with air draft connector (9) on second-stage separator (4).
5. a kind of cyclone separator that is used to produce spherical graphite according to claim 3, it is characterized in that: described one-level is separated transport tube (6) and is separated transport tube (7) with secondary, is set in the center, last top of primary separator (3) and second-stage separator (4).
6. a kind of cyclone separator that is used to produce spherical graphite according to claim 1, it is characterized in that: described primary separator (3) also is provided with blast volume controller (10) with the junction of material holder (2), also is provided with funnel (11) in the junction of second-stage separator (4) and material holder (2).
7. a kind of cyclone separator that is used to produce spherical graphite according to claim 1 is characterized in that: the bottom of described material holder (2) is provided with material outlet (12), is provided with hand-operated valve (13) on material outlet (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202585531U CN201552069U (en) | 2009-11-27 | 2009-11-27 | Cyclone separator for manufacturing spherical graphite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202585531U CN201552069U (en) | 2009-11-27 | 2009-11-27 | Cyclone separator for manufacturing spherical graphite |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201552069U true CN201552069U (en) | 2010-08-18 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202585531U Expired - Fee Related CN201552069U (en) | 2009-11-27 | 2009-11-27 | Cyclone separator for manufacturing spherical graphite |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201552069U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109292462A (en) * | 2018-10-12 | 2019-02-01 | 吉林市新大科机电技术有限责任公司 | A kind of twin-stage gas-solid separating device for air-transport system |
| CN110339927A (en) * | 2019-06-18 | 2019-10-18 | 江阴鑫久机械制造有限公司 | A kind of high speed vortex mill with modified function |
-
2009
- 2009-11-27 CN CN2009202585531U patent/CN201552069U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109292462A (en) * | 2018-10-12 | 2019-02-01 | 吉林市新大科机电技术有限责任公司 | A kind of twin-stage gas-solid separating device for air-transport system |
| CN109292462B (en) * | 2018-10-12 | 2023-12-15 | 吉林市新大科机电技术有限责任公司 | Double-stage gas-solid separation device for pneumatic conveying system |
| CN110339927A (en) * | 2019-06-18 | 2019-10-18 | 江阴鑫久机械制造有限公司 | A kind of high speed vortex mill with modified function |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100818 Termination date: 20171127 |