CN203899771U - Vertical settling centrifugal dehydrator - Google Patents
Vertical settling centrifugal dehydrator Download PDFInfo
- Publication number
- CN203899771U CN203899771U CN201420165758.6U CN201420165758U CN203899771U CN 203899771 U CN203899771 U CN 203899771U CN 201420165758 U CN201420165758 U CN 201420165758U CN 203899771 U CN203899771 U CN 203899771U
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- separation chamber
- solid
- separation
- chamber
- liquid
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Abstract
The utility model belongs to centrifugal solid-liquid separation machinery equipment. The equipment comprises the structure that a motor drives an upper separation chamber and a lower separation chamber through a belt wheel and a bearing chamber to horizontally rotate at high speed; an upper material-separating pipe and a lower material-separating pipe are arranged in the upper separation chamber and the lower separation chamber; an upper electromagnetic valve material-discharging opening and a lower electromagnetic valve material-discharging opening are formed in the material-discharging ends of the upper separation chamber and the lower separation chamber; a conduction slide ring provides a control power supply to the upper electromagnetic valve material-discharging opening and the lower electromagnetic valve material-discharging opening; a material inlet, a material-feeding pipe and a liquid overflow pipe are arranged at the top end of the upper separation chamber; suspension liquid enters the upper separation chamber and the lower separation chamber through the material inlet, the material-feeding pipe, the upper material-separating pipe and the lower material-separating pipe; through two-grade centrifugal separation, the solid material passes through the upper electromagnetic valve material-discharging opening and the lower electromagnetic valve material-discharging opening and then is discharged from a solid discharging groove to a solid discharging opening, the clarified liquid material flows through the liquid overflow pipe and a water tank and is finally discharged from a water outlet. By the equipment, the aim of effective solid-liquid separation is fulfilled. The equipment has the advantages of automatic control, stable operation, low cost, low energy consumption, large treatment amount, durability, advanced technical index and the like.
Description
Technical field
The utility model relates to a kind of vertical settling centrifugal dewatering machine equipment, be particularly related to a kind of continuous solid-liquid separating equipment, according to centrifugal sedimentation principle, when suspension enters after vertical settling centrifugal dehydrator, at machinery, drive separation chamber to horizontally rotate at a high speed under the huge centrifugal action of generation, utilize density of solid particles to be greater than the character of fluid density, make solid particle deposit to the solid exhaust end of separation chamber, liquid material arrives the other end of separation chamber, thereby realizes Separation of Solid and Liquid.The utility model is applicable to environmental protection Wu mud Tuo Shui ﹑ tailing dry and gets rid of the multiple fields such as Shui ﹑ coal slime dewatering and Kuang Ye ﹑ chemical industry.
Background technology
Solid-liquid separating equipment has two large classes: a kind equipment is filtering type dehydration equipment, and filter dewatering equipment has filter press, vacuum filter, ceramic filter, band filter, high-frequency dewatering screen etc.All filter dewatering equipments are all used filter medium, and when filter medium filter opening is thicker, filtrate is muddy, filtration difficulty when filter medium filter opening is thinner, and energy consumption increases.Also there is the problems such as recoil washing in filter medium simultaneously.Another kind of equipment is decanter type dehydration equipment, and wherein a kind of decanter type dehydration equipment is concentrator, and concentrator is that natural subsidence mode thereby equipment are huge, and equipment manufacturing cost is high, inefficiency.Another kind of decanter type dehydration equipment is horizontal screw centrifugal dewaterer, and this equipment adopts centrifugal Separation of Solid and Liquid operation principle, and its solid deposits adopts differential spiral to discharge mode, and therefore sleeping spiral shell dewaterer energy consumption is large, cost is high, wearing and tearing are large, treating capacity is little.All there is some problems in above-mentioned solid-liquid separating equipment as can be seen here, and the utility model has made up the deficiency of above-mentioned solid-liquid separating equipment.
Utility model content
The purpose of this utility model is to provide a kind of vertical settling centrifugal dehydrator, the deficiency existing to solve current solid-liquid separating equipment.
The technical solution of the utility model is: utilize solids in suspension grain density to be greater than the character of fluid density, in mechanical high-speed rotation, produce under the effect of huge centrifugal force, by the lower separation chamber horizontally rotating, make solid particle deposit to lower magnetic valve discharge gate and discharge.Through first separation rear suspension liquid, by upper sub-feed tube, enter upper separation chamber, separated through secondary centrifuging in Shang separation chamber, solid material is discharged after again depositing to the upper magnetic valve discharge gate of separation chamber continuously.The solid material that once solid material of centrifugal discharge and secondary centrifuging are discharged is discharged through solid drain tank and solid discharging opening.Liquid after clarification is through liquid overflow pipe, tank, finally discharge from delivery port.
The utility model includes: charging aperture, feed pipe, upper sub-feed tube, upper separation chamber, upper magnetic valve discharge gate, lower sub-feed tube, lower separation chamber, lower magnetic valve discharge gate, the dish that is in transmission connection, motor, tank, frame, belt pulley, conducting slip ring, solid drain tank, solid discharging opening, delivery port, hood, bearing chamber, liquid overflow pipe.
The utility model is by bearing chamber is installed in frame, in the upper end of bearing chamber, is connected with the dish that is in transmission connection.The Pan Yuxia separation chamber that is in transmission connection is connected, and there is lower magnetic valve discharge gate one end of lower separation chamber, and there is lower sub-feed tube at the center of Xia separation chamber, the You Shang separation chamber, top of Xia separation chamber.There is upper magnetic valve discharge gate one end of Shang separation chamber, and there is upper sub-feed tube at the center of Shang separation chamber.There is feed pipe on the top of Shang separation chamber, and feed pipe upper end is provided with charging aperture, and there is liquid overflow pipe side top in Shang separation chamber.Below bearing chamber, have belt pulley, belt pulley is connected with motor, and motor is connected with frame, in the lower end of bearing chamber, has conducting slip ring.In frame, be provided with tank and delivery port, frame is connected with hood, and hood is provided with solid drain tank and solid discharging opening.Separation chamber is for being horizontally disposed with, and the centrifugal force that it horizontally rotates at a high speed generation, makes suspension carry out centrifugation, and deposition of solid is to exhaust end, and the liquid of clarification is to the other end of separation chamber.Upper and lower separation chamber is upper and lower two-layer setting, suspension enters upper separation chamber and carries out secondary centrifuging separation after the centrifugation in lower separation chamber, makes solid material still less moisture, and liquid material containing solid still less, this centrifugal dehydrator is twice centrifugation, or twice above centrifugation.The exhaust end of upper and lower separation chamber is provided with magnetic valve discharge gate, and the solid material of deposition is discharged from upper and lower magnetic valve discharge gate.In upper and lower separation chamber, be provided with upper and lower sub-feed tube, so that suspension uniform distribution.
Feature of the present utility model is: suspension enters in the lower separation chamber of High Rotation Speed and carries out horizontal centrifugal separation, and solid material deposits to the lower magnetic valve discharge gate end of lower separation chamber, from lower magnetic valve discharge gate, discharges continuously.Suspension through first separation enters upper separation chamber by upper sub-feed tube, solid material Shang separation chamber back warp in first separation rear suspension liquid is crossed secondary centrifuging separation, solid material deposits to the upper magnetic valve discharge gate end of separation chamber again, and magnet valve discharge gate is discharged continuously from power on.The solid material that once solid material of centrifugal discharge and secondary centrifuging are discharged is discharged through solid drain tank and solid discharging opening.Liquid material after clarification flows out from liquid overflow pipe, by tank and delivery port, discharges.Feature of the present utility model is that suspension adopts horizontal centrifugal separated separated with secondary centrifuging, and energy consumption of the present utility model is little as can be seen here, and solid material is moisture few, and liquid material is few containing solid, therefore can obtain better economic indicator and technical indicator.
Accompanying drawing explanation
If Fig. 1 is the utility model schematic diagram.
The specific embodiment
As shown in drawings, the utility model has 1. charging apertures, and 2. feed pipe, 3. goes up sub-feed tube, 4.Shang separation chamber, 5. goes up magnetic valve discharge gate, 6. descends sub-feed tube, 7.Xia separation chamber, 8. descend magnetic valve discharge gate, the dish that is 9. in transmission connection, 10. motor, 11. tanks, 12. frames, 13. belt pulleys, 14. conducting slip rings, 15. solid drain tanks, 16. solid discharging openings, 17. delivery ports, 18. hoods, 19. bearing chambers, 20. liquid overflow pipes.
When work, suspension enters feed pipe 2 by charging aperture 1 and arrives in lower separation chamber 7 through lower sub-feed tube 6, suspension carries out horizontal centrifugal separation in the lower separation chamber 7 of mechanical high-speed rotation, solid material deposits to 7 times, lower separation chamber magnetic valve discharge gate end, from lower magnetic valve discharge gate 8, is discharged to continuously solid drain tank 15.Suspension after first separation enters upper separation chamber 4 by upper sub-feed tube 3, in solid material Shang separation chamber 4 in first separation suspension, carry out secondary levels centrifugation, solid material deposits to the upper magnetic valve discharge gate end of separation chamber 4 again, the solid material that magnet valve discharge gate 5 is discharged to 15, twice discharges of solid drain tank continuously is from power on discharged by solid discharging opening 16 in the lump through solid drain tank 15.Supernatant liquid material through twice centrifugation is discharged to tank 11 from liquid overflow pipe 20, finally by delivery port 17, discharges.Thereby realize Separation of Solid and Liquid.Control power supply by conducting slip ring 14 for upper magnetic valve discharge gate 5 and lower magnetic valve discharge gate 8 provide control power supply, be seated in motor 10 in frame 12 and provide rotary power by belt pulley 13 and bearing chamber 19 and the dish 9 that is in transmission connection for complete machine.At frame 12 peripheral hardwares, there is hood 18, on hood 18, be provided with solid drain tank 15 and solid discharging opening 16.In frame 12, be provided with tank 11 and delivery port 17.
Claims (6)
1. a vertical settling centrifugal dehydrator, be applicable to the Separation of Solid and Liquid of suspension, it is characterized in that: bearing chamber is installed in frame, upper end at bearing chamber is connected with the dish that is in transmission connection, the Pan Yuxia separation chamber that is in transmission connection is connected, there is lower magnetic valve discharge gate one end of lower separation chamber, there is lower sub-feed tube at the center of Xia separation chamber, the You Shang separation chamber, top of Xia separation chamber, there is upper magnetic valve discharge gate one end of Shang separation chamber, there is upper sub-feed tube at the center of Shang separation chamber, there is feed pipe on the top of Shang separation chamber, feed pipe is provided with charging aperture, there is liquid overflow pipe side top, Shang separation chamber, below bearing chamber, there is belt pulley to be connected with motor, motor is connected with frame, there is conducting slip ring lower end at bearing chamber, in frame, be provided with tank and delivery port, frame is connected with hood, hood is provided with solid drain tank and solid discharging opening.
2. vertical settling centrifugal dehydrator according to claim 1, it is characterized in that: separation chamber is for being horizontally disposed with, it horizontally rotates at a high speed the centrifugal force of generation, secondary centrifuging separation makes suspension carry out centrifugation, solid material deposits to magnetic valve discharge gate end, and the liquid material of clarification is to the other end of separation chamber.
3. vertical settling centrifugal dehydrator according to claim 1, it is characterized in that: upper and lower separation chamber is upper and lower two-layer setting, separation chamber is tapered design, suspension enters upper separation chamber and carries out secondary centrifuging separation after the centrifugation in lower separation chamber, make solid material still less moisture, containing solid still less, this centrifugal dehydrator is twice centrifugation to liquid material, or twice above centrifugation.
4. vertical settling centrifugal dehydrator according to claim 1, is characterized in that: one end of upper and lower separation chamber is provided with magnetic valve discharge gate, and the solid material of deposition is discharged from upper and lower magnetic valve discharge gate.
5. vertical settling centrifugal dehydrator according to claim 1, is characterized in that: in upper and lower separation chamber, be provided with upper and lower sub-feed tube, so that suspension uniform distribution.
6. vertical settling centrifugal dehydrator according to claim 1, is characterized in that: conducting slip ring provides control power supply for upper and lower magnetic valve discharge gate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420165758.6U CN203899771U (en) | 2014-04-08 | 2014-04-08 | Vertical settling centrifugal dehydrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420165758.6U CN203899771U (en) | 2014-04-08 | 2014-04-08 | Vertical settling centrifugal dehydrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203899771U true CN203899771U (en) | 2014-10-29 |
Family
ID=51774062
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420165758.6U Expired - Fee Related CN203899771U (en) | 2014-04-08 | 2014-04-08 | Vertical settling centrifugal dehydrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203899771U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113603926A (en) * | 2021-09-17 | 2021-11-05 | 曲航 | Equipment for preparing chitosan micro-bracket material |
| CN114733654A (en) * | 2022-06-10 | 2022-07-12 | 胜利油田新邦石油科技有限责任公司 | Curing centrifugal device for preparing polyaluminium chloride medicament composition |
-
2014
- 2014-04-08 CN CN201420165758.6U patent/CN203899771U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113603926A (en) * | 2021-09-17 | 2021-11-05 | 曲航 | Equipment for preparing chitosan micro-bracket material |
| CN114733654A (en) * | 2022-06-10 | 2022-07-12 | 胜利油田新邦石油科技有限责任公司 | Curing centrifugal device for preparing polyaluminium chloride medicament composition |
| CN114733654B (en) * | 2022-06-10 | 2022-08-26 | 胜利油田新邦石油科技有限责任公司 | Curing centrifugal device for preparing polyaluminium chloride medicament composition |
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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 |
Granted publication date: 20141029 Termination date: 20170408 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |