CN205398268U - Water, sand and oxide separator - Google Patents
Water, sand and oxide separator Download PDFInfo
- Publication number
- CN205398268U CN205398268U CN201620139295.5U CN201620139295U CN205398268U CN 205398268 U CN205398268 U CN 205398268U CN 201620139295 U CN201620139295 U CN 201620139295U CN 205398268 U CN205398268 U CN 205398268U
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- China
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- sand
- water
- sedimentation tank
- separator
- settling pond
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Abstract
The utility model discloses a water, sand and oxide separator, including spiral water sand separation ware, two -stage sedimentation tank, swirler and magnetic separator, the two -stage sedimentation tank includes one -level sedimentation tank and second grade sedimentation tank, fluid in the one -level sedimentation tank to the overflow of second grade sedimentation tank, the one -level sedimentation tank sets up the overflow mouth of spiral water sand separation ware, the bottom of second grade sedimentation tank sets up the sewage pump, and the sewage pump export is connected with magnetic separator, and the bottom of one -level sedimentation tank sets up the jet pump that is used for spraying the precipitate, and the jet pump export communicates with the entry of swirler, the top overflow mouth and the second grade sedimentation tank intercommunication of swirler. The device can carry out multistage separation reuse to water, sand and hopcalite, and simple structure separation efficiency is high, can realize the zero release of water and sand.
Description
Technical field
This utility model relates to a kind of solid-liquid separation equipment, particularly to a kind of water, sand and oxide segregation apparatus.
Background technology
Adopting wet type anacidity descaling process to process steel and other parts, wherein ball blast slurry includes water and sand, and its medium sand is probably steel sand, glass microballoon or ferrous oxide granule.After carrying out ball blast PROCESS FOR TREATMENT, ball blast slurry is mixed with various metal-oxide and other impurity, there is presently no a kind of device and the ball blast slurry of PROCESS FOR TREATMENT can be effectively separated the purpose purifying and then reaching recycling.
Utility model content
This utility model is in order to solve problem of the prior art, provide a kind of water, sand and oxide segregation apparatus, the ball blast slurry being mixed with various metal-oxide and other impurity is easily separated, so that wherein reusable portion is recycled, emissions-reducing.
Technical solutions of the utility model are as follows: Yi Zhongshui, sand and oxide segregation apparatus, including spiral water sand separator, two-stage sedimentation tank, cyclone and magnetic separator, described two-stage sedimentation tank includes first stage precipitation tank and second-level settling pond, fluid in described first stage precipitation tank is to described second-level settling pond overflow, described first stage precipitation tank is arranged on the overfall of described spiral water sand separator, the bottom of described second-level settling pond arranges sewage pump, the outlet of described sewage pump is connected with magnetic separator, the bottom of described first stage precipitation tank is arranged to the ejector pump of spray precipitation thing, the outlet of described ejector pump connects with the entrance of cyclone, the top overfall of described cyclone connects with described second-level settling pond.
Further, the entrance of described ejector pump is provided with high-pressure hydraulic pump.
Further, described water, sand and oxide segregation apparatus include clear water reserviors, and described high-pressure hydraulic pump entrance is connected with clear water reserviors, and the outlet of described magnetic separator is connected with clear water reserviors.
Further, the outlet of described magnetic separator arranges filter, and the outlet of described filter connects clear water reserviors, to filter non magnetic foreign material further.
Further, described second-level settling pond is provided with degreasing unit, and described degreasing unit is oil removing plate or oil removing band.
Preferably, described first stage precipitation tank and second-level settling pond are disposed adjacent and are separated by overflow plate.
Preferably, described spiral water sand separator becomes 15 °～25 ° to be in tilted layout with horizontal plane.
The advantage of technical scheme provided by the utility model is in that, 1) and utilize multiple existing equipment to be combined by pipeline, simple in construction, good reliability；2) spiral water sand separator and various pump can be equipped with low-power machine to complete separation task, and energy consumption is low；3) carrying out multiple stage separation by spiral water sand separator, cyclone, magnetic separator, separation efficiency is high, can efficiently separate out various metal and nonmetallic substance；4) abrasion solving delivery pump owing to going out the end after adopting ejector pump improves service life；5) coordinate ball blast technique to use and form closed loop cycle separation, environmental protection, it may be achieved zero-emission.
Accompanying drawing explanation
Fig. 1 is this utility model apparatus structure schematic diagram.
Fig. 2 is that ejector pump arranges position view.
Detailed description of the invention
Below in conjunction with embodiment, the utility model is described in further detail, but not as to restriction of the present utility model.
Refer to Fig. 1 and Fig. 2, water disclosed in the present embodiment, sand and oxide segregation apparatus are mainly used in wet type ball blast technique ball blast slurry and reclaim separating recycling, also are adapted for the various solidliquid mixtures containing bulky grain solid impurity and metal impurities are separated and collected simultaneously and are repeated utilizing.This device includes spiral water sand separator 1, two-stage sedimentation tank 2, cyclone 3, magnetic separator 4 and clear water reserviors 5.Spiral water sand separator 1 becomes 15 °～25 ° to be in tilted layout with horizontal plane.Two-stage sedimentation tank 2 includes the adjacent first stage precipitation tank 21 and the second-level settling pond 22 that are separated to form by overflow plate 23, and the fluid in first stage precipitation tank 21 is to second-level settling pond 22 overflow.First stage precipitation tank 21 is arranged on the overfall 11 of spiral water sand separator 1, and the bottom of second-level settling pond 22 arranges bottom valve and sewage pump 6.Sewage pump 6 outlet is connected with magnetic separator 4, and the bottom of first stage precipitation tank 21 is arranged to the ejector pump 7 of spray precipitation thing, and ejector pump 7 outlet connects with the entrance of cyclone 3, and the entrance of ejector pump 7 is provided with high-pressure hydraulic pump 8.The top overfall of cyclone 3 connects with second-level settling pond 22.The outlet of high-pressure hydraulic pump 8 entrance and magnetic separator 4 is all connected with clear water reserviors 5.Second-level settling pond 22 is provided with degreasing unit, and degreasing unit is oil removing plate or oil removing band.
This device and wet type ball blast process equipment with the use of time, solidliquid mixture separating and filtering flow process is such.The mixture of water sand mixed mortar and oxide impurity flows in spiral water sand separator 1 from mortar shot blast room 9 lower exit port, its medium sand and the heavy solid impurity of part sink to bottom and do lifter motion under the promotion of helical blade, the elevated entrance spiral water sand separator 1 of sand exports 12 entrance elevators, and then is admitted to mortar shot blast room 9 and utilizes；Liquid flows out thus realizing water sand first separation in helical blade gap, and efficiency is up to 95%.When the liquid level in spiral water sand separator 1 reaches more than overfall height, the mixed liquor containing oxide, part grit and other impurity enters the first stage precipitation tank 21 of two-stage sedimentation tank 2 by overfall 11.Mixed liquor precipitates in first stage precipitation tank 21.When the liquid level in first stage precipitation tank 21 reaches more than overflow baffle 23, the liquid flooding in first stage precipitation tank 21 is in second-level settling pond 22, precipitates further after the upper strata mixed liquor of first stage precipitation tank 21 enters second-level settling pond 22.Time in mixed liquor containing certain greasy dirt, different degreasing units can be used to be removed by oil slick.Based on the total amount of oil slick, as less in oil mass can using oil removing plate, oil mass is more adopts oil removing band.As adopted vertical rotating oil removing plate, this will rotate disc portion and immerse among liquid.Oil slick can be attracted by rotating disk, is then passed to scraper plate, is removed by oils and fats with scraper plate, and direct plunges into wastebin.The operation principle of oil removing band is similar to the operation principle of oil removing plate, and oils and fats is attracted on oil belt surface, and the motion then as belt is seen off.The oils and fats on oil band removed by scraper plate, direct plunges into wastebin.Mixed liquor after oil removing is undertaken Magnetic Materials separating treatment through bottom valve by sewage pump 6 suction magnetic separator 4, and isolated useless Magnetic Materials solid enters ash can.Liquid after magnetic separator 4 processes carries out overanxious further across considering device 10, removes the non magnetic foreign material in liquid, and the clear liquid after overanxious enters clear water reserviors 5 reuse, and after overanxious, remaining non magnetic foreign material enter ash can.
To the sand aqueous mixtures entered in first stage precipitation tank 21 after precipitation, precipitate flows into ejector pump 7 charging aperture through the bottom valve of first stage precipitation tank 21.Ejector pump 7 entrance connects high-pressure hydraulic pump 8, and the entrance of high-pressure hydraulic pump 8 connects clear water reserviors 5.Under the effect of the water under high pressure provided at high-pressure hydraulic pump 8, when High-Pressure Water is through ejector pump 7, being taken out of by the sand setting mixture of ejector pump 7 charging aperture and enter cyclone 3 by the road and carry out water sand secondary separation, heavy grain moves downward along cyclone 3 inwall and exits into mortar shot blast room 9 bottom cyclone 3 and flow in water sand spiral separator 1 again and further separate.Water and relatively lighter oxide and the useless grit of small part flow out through cyclone 3 top, enter in second-level settling pond 22 through pipeline, then are completed to separate by magnetic separator 4 and filter 10, it is achieved a circulation time process.
Claims (7)
- null1. a water、Sand and oxide segregation apparatus，It is characterized in that: include spiral water sand separator (1)、Two-stage sedimentation tank (2)、Cyclone (3) and magnetic separator (4)，Described two-stage sedimentation tank (2) includes first stage precipitation tank (21) and second-level settling pond (22)，Fluid in described first stage precipitation tank (21) is to described second-level settling pond (22) overflow，Described first stage precipitation tank (21) is arranged on the overfall (11) of described spiral water sand separator (1)，The bottom of described second-level settling pond (22) arranges sewage pump (6)，Described sewage pump (6) outlet is connected with magnetic separator (4)，The bottom of described first stage precipitation tank (21) is arranged to the ejector pump (7) of spray precipitation thing，Described ejector pump (7) outlet connects with the entrance of cyclone (3)，The top overfall of described cyclone (3) connects with described second-level settling pond (22).
- 2. water according to claim 1, sand and oxide segregation apparatus, it is characterised in that: the entrance of described ejector pump (7) is provided with high-pressure hydraulic pump (8).
- 3. water according to claim 2, sand and oxide segregation apparatus, it is characterized in that: include clear water reserviors (5), described high-pressure hydraulic pump (8) entrance is connected with clear water reserviors (5), and the outlet of described magnetic separator (4) is connected with clear water reserviors (5).
- 4. water according to claim 3, sand and oxide segregation apparatus, it is characterized in that: the outlet of described magnetic separator (4) arranges filter (10), the outlet of described filter (10) connects clear water reserviors (5).
- 5. water according to claim 1, sand and oxide segregation apparatus, it is characterised in that: described second-level settling pond (22) is provided with degreasing unit, and described degreasing unit is oil removing plate or oil removing band.
- 6. water according to claim 1, sand and oxide segregation apparatus, it is characterised in that: described first stage precipitation tank (21) and second-level settling pond (22) are disposed adjacent and are separated by overflow plate (23).
- 7. water according to claim 1, sand and oxide segregation apparatus, it is characterised in that: described spiral water sand separator (1) becomes 15 °～25 ° to be in tilted layout with horizontal plane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620139295.5U CN205398268U (en) | 2016-02-25 | 2016-02-25 | Water, sand and oxide separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620139295.5U CN205398268U (en) | 2016-02-25 | 2016-02-25 | Water, sand and oxide separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205398268U true CN205398268U (en) | 2016-07-27 |
Family
ID=56446920
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620139295.5U Withdrawn - After Issue CN205398268U (en) | 2016-02-25 | 2016-02-25 | Water, sand and oxide separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205398268U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105585163A (en) * | 2016-02-25 | 2016-05-18 | 江苏鑫华能环保工程股份有限公司 | Water-sand-oxide separation device |
| CN106194084A (en) * | 2016-09-27 | 2016-12-07 | 西南石油大学 | Pulsed negative pressure vibratory equipment |
| CN106925443A (en) * | 2017-03-20 | 2017-07-07 | 四川大学 | Double helix water and sand separating device |
-
2016
- 2016-02-25 CN CN201620139295.5U patent/CN205398268U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105585163A (en) * | 2016-02-25 | 2016-05-18 | 江苏鑫华能环保工程股份有限公司 | Water-sand-oxide separation device |
| CN106194084A (en) * | 2016-09-27 | 2016-12-07 | 西南石油大学 | Pulsed negative pressure vibratory equipment |
| CN106194084B (en) * | 2016-09-27 | 2019-12-27 | 西南石油大学 | Pulsating negative pressure vibration equipment |
| CN106925443A (en) * | 2017-03-20 | 2017-07-07 | 四川大学 | Double helix water and sand separating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zhao Haiyu Inventor after: He Zhigang Inventor after: Han Xiaowei Inventor before: Zhao Haiyu Inventor before: Gao Zhi Inventor before: He Zhigang Inventor before: Han Xiaowei |
|
| COR | Change of bibliographic data | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160727 Effective date of abandoning: 20180309 |