CN110976288A - Energy-saving environment-friendly efficient powder concentrator - Google Patents
Energy-saving environment-friendly efficient powder concentrator Download PDFInfo
- Publication number
- CN110976288A CN110976288A CN201911376383.1A CN201911376383A CN110976288A CN 110976288 A CN110976288 A CN 110976288A CN 201911376383 A CN201911376383 A CN 201911376383A CN 110976288 A CN110976288 A CN 110976288A
- Authority
- CN
- China
- Prior art keywords
- barrel
- cylinder body
- cylindricality
- cylindrical cylinder
- air
- 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
- 239000000843 powder Substances 0.000 title claims abstract description 45
- 239000002893 slag Substances 0.000 claims abstract description 25
- 230000004888 barrier function Effects 0.000 claims description 5
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 2
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 2
- 241001330002 Bambuseae Species 0.000 claims description 2
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 2
- 239000011425 bamboo Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 11
- 238000000926 separation method Methods 0.000 description 11
- 239000002245 particle Substances 0.000 description 10
- 239000008187 granular material Substances 0.000 description 5
- 230000005484 gravity Effects 0.000 description 3
- 230000001174 ascending effect Effects 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000009700 powder processing Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force
- B07B7/086—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force generated by the winding course of the gas stream
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/06—Jet mills
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/02—Arrangement of air or material conditioning accessories
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
The invention discloses an energy-saving environment-friendly high-efficiency powder concentrator, wherein a separating cylinder comprises an upper cylindrical cylinder body I and a lower inverted cone-shaped cylinder body I, an air inlet pipe is installed on the cylindrical cylinder body I, a feed inlet is formed in the cylindrical cylinder body I above the air inlet pipe, a qualified powder discharge outlet in the top of the cylindrical cylinder body I is communicated with a negative pressure exhaust pipe, a rotor is arranged in the cylindrical cylinder body I below the qualified powder discharge outlet, a bottom end opening of the inverted cone-shaped cylinder body I is a slag outlet I, an inner separating cylinder is arranged in the separating cylinder and comprises an upper cylindrical cylinder body II and a lower inverted cone-shaped cylinder body II, the cylindrical cylinder body II is arranged in the cylindrical cylinder body I and is positioned below the rotor, an annular cavity is formed between the cylindrical cylinder body II and the cylindrical cylinder body I, an air deflector is arranged in the annular cavity above the feed inlet, a. The invention can separate three materials with different diameters, effectively reduce black slag and ensure that the yield of qualified powder can reach 10-12 tons per hour.
Description
Technical Field
The invention relates to powder processing equipment, in particular to an energy-saving environment-friendly high-efficiency powder concentrator.
Background
The powder concentrator is widely applied in the powder processing industry, and the first powder concentrator produced in 1885 is a centrifugal powder concentrator which separates materials by utilizing the difference of centrifugal force and gravity of particles; the second generation powder concentrator, namely a cyclone type powder concentrator, appears in 1960, and the problems of low powder concentration efficiency, low powder concentration precision and the like of the first generation powder concentrator are solved; in 1979, a high-efficiency powder concentrator was produced, and a cage type powder concentrator represented by a 0-SEPA powder concentrator is called the high-efficiency powder concentrator, overcomes the defects of uneven material scattering, uneven flow distribution air field and the like of a centrifugal type powder concentrator and a cyclone type powder concentrator, and is the most efficient and advanced powder concentrator on the market at present.
However, the efficient powder concentrator still has the following problems when in use:
1. low separation rate and low productivity. The medium coarse particles which cannot meet the fineness requirement of the finished product and cannot pass through the grading device are suspended in the air to block an ascending channel of the finished product meeting the fineness requirement due to the fact that downward gravity and upward conveying wind power collide to form airflow disorder, and the medium coarse particles reduce the capacity and increase the energy consumption.
2. The energy consumption is high. The powder selecting machine on the market is generally used for feeding from the top of the machine, and the feeding height and the feeding amount are both at the cost of electric energy loss.
3. Easily produces black slag and has low separation purity. The materials to be separated often contain black slag, the existing powder selecting device generally uses mechanical force to disperse and break up at high speed in the powder selecting process, so that the black slag is secondarily ground, the black slag meeting the fineness requirement is separated out and mixed into finished products, and the purity of the finished products is influenced.
Disclosure of Invention
Aiming at the defects of the prior art, the invention aims to provide the energy-saving environment-friendly high-efficiency powder concentrator which can improve the material separation efficiency, reduce the generation of black slag and improve the separation purity.
The energy-saving environment-friendly high-efficiency powder concentrator capable of solving the technical problems comprises a separating cylinder, wherein the separating cylinder comprises an upper cylindrical cylinder I and a lower inverted cone cylinder I, an air inlet pipe is installed on the cylindrical cylinder I in an oriented mode, a feed inlet is formed in the cylindrical cylinder I above the air inlet pipe, a qualified powder discharge port coaxially formed in the top of the cylindrical cylinder I is communicated with a negative pressure exhaust pipe, a rotor driven by an external motor is coaxially arranged in the cylindrical cylinder I below the qualified powder discharge port, a bottom end opening of the inverted cone cylinder I is a slag outlet I, the difference is that an inner separating cylinder is arranged in the separating cylinder and comprises an upper inverted cone II and a lower inverted cone II, the cylindrical cone II is coaxially arranged in the cylindrical cylinder I and is positioned below the rotor, and an annular cavity with the inner ring diameter larger than the rotor diameter is formed between the cylindrical cylinder II and the cylindrical cylinder I, the annular cavity above the feeding hole is internally provided with air deflectors which are uniformly distributed on the circumference and can control the air speed by adjusting the angle, the bottom opening of the inverted cone II is a slag outlet II, and a fence plate with the functions of upward air guiding and downward blanking is arranged in the annular cavity and is parallel and level to the bottom position of the air inlet pipe.
In order to obtain a longer air course, the air inlet pipe is arranged at the lower part of the cylindrical barrel I, the air deflector is arranged at the upper part of the annular cavity, and the feed inlet is arranged on the cylindrical barrel I at the top position of the air inlet pipe.
The barrier panels are preferably in the form of louvres.
Furthermore, slag notch II communicates the oblique unloading pipe that sets up on the back taper barrel I.
The invention has the beneficial effects that:
the energy-saving environment-friendly high-efficiency powder concentrator realizes the technology of simultaneously and effectively separating three types of particles, effectively reduces black slag, has the yield of qualified powder which can reach 10-12 tons per hour, is approximately doubled compared with the yield of the prior powder concentrator, and consumes only two fifths of the energy per hour compared with the energy of the traditional equipment.
Drawings
Fig. 1 is a schematic structural diagram of an embodiment of the present invention.
And (3) identifying the figure number: 1. a separation cylinder; 2. an air inlet pipe; 3. a negative pressure exhaust pipe; 4. a slag outlet I; 5. a rotor; 6. an inner separation barrel; 7. an air deflector; 8. a slag outlet II; 9. a discharging pipe; 10. a feed inlet; 11. a motor; 12. a fence plate.
Detailed Description
The technical solution of the present invention will be further explained with reference to the embodiments shown in the drawings.
The invention relates to an energy-saving environment-friendly high-efficiency powder concentrator, which comprises a separating cylinder 1, an air inlet pipe 2, a rotor 5, an inner separating cylinder 6, a negative pressure exhaust pipe 3 and an air deflector 7.
The separating cylinder 1 comprises a cylindrical cylinder body I on the upper portion and a reverse taper cylinder body I on the lower portion, a qualified powder discharge port is coaxially formed in the top of the cylindrical cylinder body I, a negative pressure exhaust pipe 3 is arranged on the top of the qualified powder discharge port communicated with the cylindrical cylinder body I, a rotor 5 driven by an outer cylinder motor 11 is coaxially arranged in the cylindrical cylinder body I below the qualified powder discharge port, and a bottom cylinder opening of the reverse taper cylinder body I is a slag outlet I4 and is shown in figure 1.
The lower part of the cylindricality barrel I of the knockout drum 1 is located to air-supply line 2 (connection fan) level (the bottom parallel and level of air-supply line 2 is in the lower extreme tube socket of cylindricality barrel I), and air-supply line 2 communicates knockout drum 1 with the tangent mode with cylindricality barrel I, has seted up feed inlet 10 on the cylindricality barrel I at air-supply line 2 top, as shown in fig. 1.
In interior separation cylinder 3 coaxial locating separation cylinder 1, interior separation cylinder 3 includes the cylindricality barrel II on upper portion and the back taper barrel II of lower part, II coaxial locating cylindricality barrels in I, the upper end nozzle of cylindricality barrel II is in rotor 5 below and the diameter of diameter more than rotor 5, and the lower extreme nozzle parallel and level of cylindricality barrel II forms the annular chamber between II and the cylindricality barrel I in the lower extreme nozzle of cylindricality barrel, the lower extreme nozzle department of annular chamber is equipped with shutter form's fence board 12 (has the function of last wind-guiding and downward blanking), the bottom nozzle of back taper barrel II is slag notch II 8, slag notch II 8 link to each other unloading pipe 9, unloading pipe 9 leads to down back taper barrel I to one side, as shown in figure 1.
The air deflectors 7 are uniformly distributed on the upper part (higher than the feeding hole 10) of the annular cavity at the circumference, and the angles of the air deflectors 7 can be synchronously adjusted so as to control the air speed passing through the annular cavity, as shown in figure 1.
The operation mode of the invention is as follows:
the fan starts, the material gets into from feed inlet 10, blow in the gas of annular chamber from air-supply line 2 and break up the material for the first time, the wind of entering has upwards and two kinds of motion trends down, barrier plate 12 has blockked the trend of wind direction downstream, consequently, the air inlet forms ascending spiral shell whirlwind in the annular chamber, the granule of partly material diameter between 50 meshes ~ 5mm is owing to gravity and centrifugal force effect directly through barrier plate 12 or accumulate to the section of thick bamboo wall landing again and drop to the back taper barrel I of separator 1 and follow slag notch I4 discharge collection through barrier plate 12.
The gas carries particles to rise in the annular cavity in a rotating mode, when the gas passes through the air inlet of the air inlet pipe 2, materials are scattered for the second time, like the first scattering, through the adjustment of the air deflector 7 on the rotating direction and the rotating speed, most of large particles with the diameter of 50 meshes-5 mm are accumulated on the wall of the cylinder under the action of centrifugal force before entering the powder selecting area, fall off through the fence plate 12 and are discharged from the slag outlet I4 for collection, and the rest particles are carried by the gas to rise in a rotating mode.
When the gas rises to the position of the air deflector 7, the speed of the gas passing through is adjusted by adjusting the angle of the air deflector 7, when the wind speed is increased, small particles can reach the position near the rotor 5 through the air deflector 7, and large particles which do not pass through the air deflector 7 are thrown onto the wall of the cylindrical barrel I, stacked and slide down, discharged through the slag outlet I4 and collected.
The rotor 5 screens the particles passing through the air deflector 7, qualified materials of about 300 meshes are sucked into the negative pressure exhaust pipe 3 and collected, and medium-diameter particles of 200-50 meshes are not sucked into the negative pressure exhaust pipe 3 due to insufficient particle size, fall into the cylindrical barrel II of the inner separation barrel 6 after being accumulated at the lower end of the rotor 5, and are discharged and collected from a slag outlet II 8 at the bottom of the inverted conical barrel II through the discharging pipe 9.
Because the whole course of operation does not have any mechanical force to act on the material granule, consequently can not cause the regrinding to the granule, just can not smash black granule yet, black granule is collected at slag notch I4 and slag notch II 8, and the black sediment in the qualified powder just significantly reduces to separation purity has been improved.
The above-mentioned embodiments are only used for explaining the technical solution of the present invention, and do not limit the same. It will be appreciated by those skilled in the art that various modifications and alternatives to those embodiments can be developed without departing from the principles of the invention.
Claims (4)
1. Energy-concerving and environment-protective high-efficient selection powder machine, including knockout drum (1), knockout drum (1) is including cylindricality barrel I on upper portion and the back taper barrel I of lower part, surely to installing air-supply line (2) on cylindricality barrel I, feed inlet (10) have been seted up on the cylindricality barrel I of air-supply line (2) top, and qualified powder discharge gate intercommunication negative pressure blast pipe (3) that I tops of cylindricality barrel were coaxial to be seted up, coaxial rotor (5) that are driven by motor (11) outside the section of thick bamboo are equipped with in the cylindricality barrel I of qualified powder discharge gate below, the bottom nozzle of back taper barrel I is slag notch I (4), its characterized in that: be equipped with interior separator (6) in separator (1), interior separator (6) are including the cylindricality barrel II on upper portion and the back taper barrel II of lower part, cylindricality barrel II is coaxial to be located in cylindricality barrel I and be in rotor (5) below, forms the annular chamber that inner ring diameter is greater than rotor (5) diameter between cylindricality barrel II and the cylindricality barrel I, be equipped with circumference equipartition aviation baffle (7) that accessible angle regulation and control wind speed in the annular chamber of feed inlet (10) top, the bottom nozzle of back taper barrel II is slag notch II (8), sets up barrier (12) that have upwards wind-guiding and downward blanking function in the annular chamber with the bottom position parallel and level of air-supply line (2).
2. The energy-saving environment-friendly high-efficiency powder concentrator as claimed in claim 1, wherein: the air inlet pipe (2) is arranged on the lower portion of the cylindrical barrel body I, the feed inlet (10) is arranged on the cylindrical barrel body I at the top of the air inlet pipe (2), and the air deflector (7) is arranged on the upper portion of the annular cavity.
3. The energy-saving environment-friendly high-efficiency powder concentrator as claimed in claim 1, wherein: the fence panel (12) is in the form of a louvre.
4. An energy-saving environment-friendly efficient powder concentrator as claimed in any one of claims 1 to 3, wherein: slag notch II (8) intercommunication back taper barrel I goes up oblique blanking pipe (9) that set up.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911376383.1A CN110976288A (en) | 2019-12-27 | 2019-12-27 | Energy-saving environment-friendly efficient powder concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911376383.1A CN110976288A (en) | 2019-12-27 | 2019-12-27 | Energy-saving environment-friendly efficient powder concentrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110976288A true CN110976288A (en) | 2020-04-10 |
Family
ID=70077863
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911376383.1A Pending CN110976288A (en) | 2019-12-27 | 2019-12-27 | Energy-saving environment-friendly efficient powder concentrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110976288A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112264152A (en) * | 2020-11-10 | 2021-01-26 | 湖南嘉力亚新材料有限公司 | Prebaked anode manufacturing powder grinding device with quick discharging function |
| CN114428032A (en) * | 2021-12-24 | 2022-05-03 | 中电建河南万山绿色建材有限公司 | Online quick detection device of advection formula mechanism sand grain composition analysis |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200954502Y (en) * | 2006-09-30 | 2007-10-03 | 江苏科行环境工程技术有限公司 | Wind-intaking device of superfine powder sorting machine special for industrial waste dregs |
| CN201102015Y (en) * | 2007-10-18 | 2008-08-20 | 刘怀平 | Cataract type air separator |
| CN204035032U (en) * | 2014-07-22 | 2014-12-24 | 中材装备集团有限公司 | A kind of wind formula of sweeping is association of activity and inertia high efficiency dust separator |
| WO2016031636A1 (en) * | 2014-08-29 | 2016-03-03 | 株式会社日清製粉グループ本社 | Cyclone device and classification method |
| CN211587521U (en) * | 2019-12-27 | 2020-09-29 | 桂林矿山机械有限公司 | Energy-saving environment-friendly efficient powder concentrator |
-
2019
- 2019-12-27 CN CN201911376383.1A patent/CN110976288A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200954502Y (en) * | 2006-09-30 | 2007-10-03 | 江苏科行环境工程技术有限公司 | Wind-intaking device of superfine powder sorting machine special for industrial waste dregs |
| CN201102015Y (en) * | 2007-10-18 | 2008-08-20 | 刘怀平 | Cataract type air separator |
| CN204035032U (en) * | 2014-07-22 | 2014-12-24 | 中材装备集团有限公司 | A kind of wind formula of sweeping is association of activity and inertia high efficiency dust separator |
| WO2016031636A1 (en) * | 2014-08-29 | 2016-03-03 | 株式会社日清製粉グループ本社 | Cyclone device and classification method |
| CN211587521U (en) * | 2019-12-27 | 2020-09-29 | 桂林矿山机械有限公司 | Energy-saving environment-friendly efficient powder concentrator |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112264152A (en) * | 2020-11-10 | 2021-01-26 | 湖南嘉力亚新材料有限公司 | Prebaked anode manufacturing powder grinding device with quick discharging function |
| CN114428032A (en) * | 2021-12-24 | 2022-05-03 | 中电建河南万山绿色建材有限公司 | Online quick detection device of advection formula mechanism sand grain composition analysis |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102397841B (en) | Bidirectional airflow submicron powder sorting machine | |
| CN202778960U (en) | Vertical purification efficient airflow grader | |
| WO2020048278A1 (en) | Cement roller press finish grinding system and working method | |
| CN206286201U (en) | Wood chip sorting unit | |
| CN106669888A (en) | Efficient roller pressing grinding station and technique thereof | |
| CN110976288A (en) | Energy-saving environment-friendly efficient powder concentrator | |
| CN104984910A (en) | High-dispersibility vortex powder selecting machine | |
| CN106824452A (en) | Fluidized bed airflow grinding machine intelligence change system | |
| CN102784757B (en) | Efficient airflow classification fine-coal remover for power coal before selecting | |
| CN211587521U (en) | Energy-saving environment-friendly efficient powder concentrator | |
| CN209715344U (en) | A kind of grinding system of processing | |
| CN215878794U (en) | Novel powder selecting device | |
| CN106975609A (en) | A kind of sorting grid and the powder concentrator sorted using sorting grid | |
| WO2007145207A1 (en) | Air flow classifier, and classifying plant | |
| CN204892373U (en) | High dispersivity vortex selection powder machine | |
| CN206229684U (en) | A kind of air selects powder system and its powder concentrator | |
| CN214077294U (en) | Gas-phase powder grading equipment | |
| CN213792245U (en) | Comprehensive raise dust formula circulation piece-rate system | |
| CN209577389U (en) | Powder raw material sorting machine | |
| CN211756859U (en) | Pneumatic vortex separator | |
| CN211964482U (en) | Special ceramic refining equipment | |
| CN107755258A (en) | A kind of material weight particle sorting apparatus | |
| CN109746105B (en) | Grinding system | |
| CN202725501U (en) | Fines removal all-in-one machine used for dry-method classification before steam coal preparation | |
| CN202343456U (en) | Coarse powder separator for lightweight particle materials |
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 |