CN202427558U - Differential stirring and centrifugal purifying separator - Google Patents
Differential stirring and centrifugal purifying separator Download PDFInfo
- Publication number
- CN202427558U CN202427558U CN2012200475581U CN201220047558U CN202427558U CN 202427558 U CN202427558 U CN 202427558U CN 2012200475581 U CN2012200475581 U CN 2012200475581U CN 201220047558 U CN201220047558 U CN 201220047558U CN 202427558 U CN202427558 U CN 202427558U
- Authority
- CN
- China
- Prior art keywords
- centrifugal
- stirring
- bearing
- housed
- centrifugal chamber
- 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
Links
- 238000003756 stirring Methods 0.000 title claims abstract description 11
- 238000007599 discharging Methods 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims description 16
- 238000000746 purification Methods 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims 1
- 239000000126 substance Substances 0.000 abstract description 4
- 239000002002 slurry Substances 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 description 4
- 238000007664 blowing Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000001640 fractional crystallisation Methods 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 235000021552 granulated sugar Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229940074869 marquis Drugs 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000011268 mixed slurry Substances 0.000 description 1
- VBUNOIXRZNJNAD-UHFFFAOYSA-N ponazuril Chemical compound CC1=CC(N2C(N(C)C(=O)NC2=O)=O)=CC=C1OC1=CC=C(S(=O)(=O)C(F)(F)F)C=C1 VBUNOIXRZNJNAD-UHFFFAOYSA-N 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Images
Landscapes
- Centrifugal Separators (AREA)
Abstract
The utility model discloses differential stirring and centrifugal purifying separating equipment, which relates to separating equipment. The differential stirring and centrifugal purifying separating equipment mainly comprises a centrifugal unit, a stirring unit, a centrifugal chamber and the like, and is characterized in that: slurry is poured into the centrifugal chamber from a feeding hole, a stirrer is started for stirring, and a centrifuge is started for centrifuging; when the centrifuge reaches a certain rotating speed, primary discharging is started, and a differential stirrer is used for stirring substances which are centrifugally separated primarily; and centrifuging and discharging are performed once again repeatedly, so that a centrifugally-separated substance with high purity is obtained. According to the separating equipment, the utilization ratio is increased, and the purity of a product is increased.
Description
Said technical field
The utility model belongs to a kind of equipment that separates the purification field, particularly relates to the centrifugal purification seperator of a kind of differential stirring-type.
Background technology
Along with expanding economy, science and technology is also more and more flourishing, and in the middle of the 19th century, the 3-foot that weaving dehydration usefulness successively occurred is centrifugal, the upward outstanding centrifuge that general sugar refinery fractional crystallization granulated sugar is used.These centrifuges the earliest all are intermittently operated and artificial deslagging, and it is numerous and diverse to work, and purity is not enough.Now special seperator is the admixture of gas of separable different densities also, for example concentrates, separates the gaseous state hex; Utilize solid particle sinking speed different features in liquid of different densities or granularity, the sedimentation centrifuge that has also can carry out classification by density or granularity to solid particle.These centrifugal separators are widely used in departments such as chemical industry, oil, food, pharmacy, ore dressing, coal, water treatment and boats and ships.But the material of equipment centrifugation now has that much to carry out once the centrifugal purity that obtains be not enough, and mostly is semi-automatic operation, and technology is loaded down with trivial details, and therefore new seperator technology is that present industry, ore dressing aspect are the most indispensable.
Summary of the invention
The utility model provides a kind of stirring-type centrifugal purification seperator, is applicable to all kinds of separation purifications that have the solid, powdery thing slurry of density variation.
Technical scheme below the utility model adopts: a kind of is from the slurry that contains certain metal, to separate purification, main step:
Step 1: raw material is mixed with water, use the differential mixer to stir earlier, re-use centrifuge and separate, obtain the impure more heavy density material of a part earlier, what the most inboard position density was minimum discharges from discharging opening.
Step 2: adopt mixer to stir, make the heavy density material that purity is not enough according to the centrifuge direction of rotation, centrifugal once more, to purify again and separate, the little material of density that then secondary centrifuging is left is discharged from second discharge gate.
Step 3: when reaching the purity that needs, begin to put blowing for the third time, the material that density is maximum, therefore do action can obtain density difference, the higher material of purity.
Step 4: the material air-dry, that storage is required.
The utility model adopts the advantage of the said equipment:
1, mixer plays repeatedly the effect that utilizes, and can make mixing of materials abundant, secondly can make the impure material of centrifugal inwall, and is centrifugal again, obtains the higher material of purity.
2, because of mixer and centrifuge are with wind direction, and be adjustable speed, can reduce friction, reduce the wastage.
3, can layering go out different material, thorough separating substances, convenient utilize once more, also can produce new benefit point simultaneously, other utilities that contain like gold mine etc.
In sum, the cyclic production of the favourable production of the utility model is practiced thrift cost, and separating degree is higher, and no chemical reaction is pollution-free.
Description of drawings
The structural representation sketch of Fig. 1 the utility model
Among Fig. 1,1. stirrer shaft 2. bearing blocks 3. centrifugal chambers 4. stirrer gears 5. centrifugal unit 6. charging apertures 7. bearings one 8. bearings 2 9. discharging opening baffle plates 10. discharging openings 11. bearing block pillars 12. bearings three
Concrete embodiment
A kind of differential stirs centrifugal purification seperator, mainly partly is made up of centrifugal unit 5, agitator, centrifugal chamber 3 etc., and mechanism is that centrifugal unit 5 tops are connected bearing 3 12; Be connected to centrifugal chamber 3, stirrer shaft 1 is housed in the centrifugal chamber 3, stirrer gear 4; Discharging opening baffle plate 9 is equipped with in centrifugal chamber 3 bottoms, and a plurality of discharging openings 10 are housed under the baffle plate, and bearing 28 is equipped with on centrifugal chamber 3 tops; Play the fixedly effect of centrifugal chamber 3, between centrifugal unit 5 and bearing block 2, bearing block pillar 11 is housed, bearing 1 is housed on bearing block 2 tops; Play the fixedly effect of stirrer shaft 1, the first half of stirrer shaft 1 is a feed arrangement, and top is charging aperture 6.
Through throat-fed, get into centrifugal chamber, open mixer, mixed slurry to material; Open centrifugal unit then and begin centrifugally, when reaching rotating speed marquis for the moment, beginning is for the first time centrifugal, and mixing speed begins adjustment simultaneously; Open inboard first drain hole, begin blowing, the material of separating is stirred to return to restart separate; From second discharge gate blowing once more, stir centrifugally again, discharge desired material from last drain hole at last.
Claims (2)
1. the centrifugal purification seperator of differential stirring-type mainly is made up of centrifugal unit, mixer, centrifugal chamber etc.; It is characterized in that centrifugal unit top is connected bearing three, be connected to centrifugal chamber on the bearing, stirrer shaft, stirrer gear are housed in the centrifugal chamber; The discharging opening baffle plate is equipped with in the centrifugal chamber bottom, and a plurality of discharging openings are housed under the baffle plate, and bearing two is equipped with on centrifugal chamber top; The bearing block pillar is housed between centrifugal unit and bearing block; On bearing block top bearing one is housed, the first half of stirrer shaft is a feed arrangement, and top is charging aperture.
2. according to claim 1, its principal character is under the different rotating speeds situation, and mixer is regulated the speed according to the requirement of centrifugal unit, makes the material of first separation stir separation again, thereby each material is progressively successively separated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200475581U CN202427558U (en) | 2012-02-10 | 2012-02-10 | Differential stirring and centrifugal purifying separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200475581U CN202427558U (en) | 2012-02-10 | 2012-02-10 | Differential stirring and centrifugal purifying separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202427558U true CN202427558U (en) | 2012-09-12 |
Family
ID=46777034
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200475581U Expired - Fee Related CN202427558U (en) | 2012-02-10 | 2012-02-10 | Differential stirring and centrifugal purifying separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202427558U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874490A (en) * | 2015-06-08 | 2015-09-02 | 江苏赛德力制药机械制造有限公司 | Vertical settling scraping centrifuge |
| CN107930863A (en) * | 2017-12-28 | 2018-04-20 | 山西三能世纪机械设备有限公司 | A kind of centrifugal separator for solving vinegar precipitation |
| CN110942916A (en) * | 2018-09-21 | 2020-03-31 | 钰冠科技股份有限公司 | Purification system for soluble nanoparticles |
-
2012
- 2012-02-10 CN CN2012200475581U patent/CN202427558U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874490A (en) * | 2015-06-08 | 2015-09-02 | 江苏赛德力制药机械制造有限公司 | Vertical settling scraping centrifuge |
| CN107930863A (en) * | 2017-12-28 | 2018-04-20 | 山西三能世纪机械设备有限公司 | A kind of centrifugal separator for solving vinegar precipitation |
| CN107930863B (en) * | 2017-12-28 | 2023-10-20 | 太原智慧产业园管理有限公司 | Solve centrifuge that vinegar sediment was used |
| CN110942916A (en) * | 2018-09-21 | 2020-03-31 | 钰冠科技股份有限公司 | Purification system for soluble nanoparticles |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 223800 Suqian City, Jiangsu Province Economic Development Zone (West) Sucheng City Road No. 58 Patentee after: Wang Hongju Patentee after: Jiangsu Jinghe New Energy Co., Ltd. Address before: 223800 No. 88 Fumin Road, Suqian Economic Development Zone, Jiangsu, B07 Patentee before: Wang Hongju Patentee before: Jiangsu Jinghe New Energy Co., Ltd. |
|
| DD01 | Delivery of document by public notice |
Addressee: Liu Chun Document name: Notification that Application Deemed not to be Proposed |
|
| ASS | Succession or assignment of patent right |
Free format text: FORMER OWNER: JIANGSU JINGHE NEW ENERGY CO., LTD. Effective date: 20150714 Owner name: SUQIAN ZHISHENG MACHINERY TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: WANG HONGJU Effective date: 20150714 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150714 Address after: 223800, No. 58, Gucheng Road, Su Su Industrial Park, Jiangsu, Suqian Patentee after: Suqian Zhisheng Mechanical Technology Co. Ltd. Address before: 223800 Suqian City, Jiangsu Province Economic Development Zone (West) Sucheng City Road No. 58 Patentee before: Wang Hongju Patentee before: Jiangsu Jinghe New Energy Co., Ltd. |
|
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Suqian Zhisheng Mechanical Technology Co. Ltd. Document name: Notification to Pay the Fees |
|
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Suqian Zhisheng Mechanical Technology Co. Ltd. Document name: Notification of Termination of Patent Right |
|
| 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: 20120912 Termination date: 20170210 |