CN201510803U - High-efficiency solid-liquid separation system - Google Patents
High-efficiency solid-liquid separation system Download PDFInfo
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- CN201510803U CN201510803U CN2009201077715U CN200920107771U CN201510803U CN 201510803 U CN201510803 U CN 201510803U CN 2009201077715 U CN2009201077715 U CN 2009201077715U CN 200920107771 U CN200920107771 U CN 200920107771U CN 201510803 U CN201510803 U CN 201510803U
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- solid
- liquid separation
- separation system
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Abstract
The utility model relates to a high-efficiency solid-liquid separation system which comprises a cyclone separator and a high-efficiency settler. The high-efficiency solid-liquid separation system is characterized in that the separated liquid outlet of the cyclone separator is connected with the to-be-separated liquid inlet of the high-efficiency settler, a front centrifugal pump is arranged in front of the cyclone separator, a buffer tank is arranged behind the high-efficiency settler, and a rear centrifugal pump is arranged between the high-efficiency settler and the buffer tank. With the reasonable connection and combination of multiple components, the high-efficiency solid-liquid separation system achieves the continuous processes of the solid-liquid mixture, including grading and screening, particle washing, degassing and impunity removal, solid-liquid separation, liquid-liquid separation and liquid clarification, according to the technological requirements. The high-efficiency solid-liquid separation system achieves the purposes of high efficiency, complete separation, low cost and continuous operation; is applied to the treatment of both industrial and domestic sewage; and is also applied to the screening, the impurity removal and the rinsing processes in the mining and ore dressing industry and the fine chemical industry.
Description
Technical field
The utility model relates to a kind of efficient solid-liquid separation system, is applicable to that the liquid liquid of Separation of Solid and Liquid such as screening in sewage disposal and digging ore dressing, the fine chemistry industry, removal of impurities, cleaning or different physical characteristics separates.
Background technology
Existing Separation of Solid and Liquid adopts spinning liquid separator method, swash plate pipe sedimentation and sedimentation basin method etc. substantially, this several method is because of being subjected to limitation separately, exist defectives such as separation is unclean, process is slow, floor space is big respectively, restricted to industrialization, the high-quality that becomes more meticulous, high-efficient development.
The utility model content
For overcoming the above-mentioned defective of prior art, the utility model provides a kind of efficient solid-liquid separation system, this piece-rate system is utilized the reasonable combination of multiple separator, can make solidliquid mixture carry out flow processs such as sizing screening, particle washing, degasification removal of impurities, Separation of Solid and Liquid, the separation of liquid liquid, liquid clarification continuously according to technological requirement, reach efficient, meticulous, industrialization, solidliquid mixture fully handled the purpose of recycling.
The utility model realizes that the technical scheme of above-mentioned purpose is: a kind of efficient solid-liquid separation system, comprise cyclone separation device and efficient sedimentation device, it is characterized in that liquid outlet after the separation of described cyclone separation device connects the pending liquid-inlet of described efficient sedimentation device.
Described piece-rate system can also be provided with preceding centrifugal pump, and described preceding centrifugal delivery side of pump connects the pending liquid-inlet of described cyclone separation device.
Described piece-rate system also is provided with surge tank, and the liquid-inlet of described surge tank connects liquid outlet after the separation of described efficient sedimentation device.
The separating the back liquid outlet and can directly be connected by fluid passage of the liquid-inlet of described surge tank and described efficient sedimentation device, described fluid passage is normally managed or groove.
Also can be provided with the back centrifugal pump after the liquid-inlet of described surge tank and the separation of described efficient sedimentation device between the liquid outlet, the import of described back centrifugal pump connects liquid outlet after the separation of described efficient sedimentation device, and the centrifugal delivery side of pump in described back connects the liquid-inlet of described surge tank.
Described efficient sedimentation device can be inclined plate sedimentation device or inclined tube sedimentation device.
Described cyclone separation device can adopt barrel formula structure or pencil formula structure.
Described cyclone separation device adopts vertical structure usually, and is located at the top of efficient sedimentation device.
Described cyclone separation device and described efficient sedimentation device are equipped with sewage draining exit.
Described surge tank can be the tank body of sealing, and the top is provided with port, and the bottom is provided with sewage draining exit.
The beneficial effects of the utility model are: because the separator of cyclone separation device and efficient two kinds of different characteristics of sedimentation device is joined together, given full play to usefulness separately, both improved oarse-grained separating rate, guaranteed short grained thorough separation again; Owing to be provided with preceding centrifugal pump, for system provides power; Owing to can directly connect by fluid passage between surge tank and the efficient sedimentation device, also can connect by the back centrifugal pump, can be adapted to different system architectures and liquid flow characteristics; Owing to be provided with surge tank, make separation back liquid be stored stand-by.Configuration of this piece-rate system and connected mode are reasonable, reached raise the efficiency, separate thoroughly, reduce floor space, reduce disposal cost, make things convenient for the technology adjustment, the purpose of continuous automatic job.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
Referring to Fig. 1, the separation equipment of described solid-liquid separation system comprises interconnective cyclone separation device 2 and efficient sedimentation device 3, the front of cyclone separation device is provided with preceding centrifugal pump 1, so that pending liquid is sent into described cyclone separation device with certain flow and pressure, realize that liquid is carried and the purpose of rotational flow separation, cyclone separation device adopts bucket formula structure or pencil formula structure, usually can be vertical, be positioned at the top of the efficient sedimentation device of postorder, make the liquid after the processing just can flow into efficient sedimentation device smoothly not needing to increase under the situation of power thus, described efficient sedimentation device adopts swash plate or inclined tube sedimentation device, to reduce volume, improve settling efficiency, improve effect of settling, its outlet that separates back liquid directly connects the surge tank 5 of postorder by fluid passages such as pipe or grooves, also can back centrifugal pump 4 be set between in case of necessity, so that power to be provided, guarantee the conveying of liquid.As required, can on the pipeline that liquid is carried, necessary control valve etc. be set, so that control flow and pressure.Described cyclone separation device and described efficient sedimentation device all should be provided with sewage draining exit, be used to discharge the dope or the mud that contain impurity after the separation, described surge tank can be the tank body of sealing, it also can be the tank body of open-top, when adopting closed tank, its top is provided with port, and the bottom of various tank bodies generally can be provided with sewage draining exit, is used to discharge the mud that is precipitated out or washes sewage etc.
Claims (10)
1. efficient solid-liquid separation system comprises cyclone separation device and efficient sedimentation device, it is characterized in that liquid outlet after the separation of described cyclone separation device connects the pending liquid-inlet of described efficient sedimentation device.
2. efficient solid-liquid separation system as claimed in claim 1 is characterized in that also being provided with preceding centrifugal pump, and described preceding centrifugal delivery side of pump connects the pending liquid-inlet of described cyclone separation device.
3. efficient solid-liquid separation system as claimed in claim 2 is characterized in that also being provided with surge tank, and the liquid-inlet of described surge tank connects liquid outlet after the separation of described efficient sedimentation device.
4. efficient solid-liquid separation system as claimed in claim 3 is characterized in that the liquid-inlet of described surge tank directly is connected by fluid passage with the back liquid outlet that separates of described efficient sedimentation device, and described fluid passage is pipe or groove.
5. efficient solid-liquid separation system as claimed in claim 3, it is characterized in that being provided with the back centrifugal pump between the liquid outlet after the separation of the liquid-inlet of described surge tank and described efficient sedimentation device, the import of described back centrifugal pump connects liquid outlet after the separation of described efficient sedimentation device, and the centrifugal delivery side of pump in described back connects the liquid-inlet of described surge tank.
6. as claim 1,2,3,4 or 5 described efficient solid-liquid separation systems, it is characterized in that described efficient sedimentation device is inclined plate sedimentation device or inclined tube sedimentation device.
7. efficient solid-liquid separation system as claimed in claim 6 is characterized in that described cyclone separation device adopts bucket formula structure or pencil formula structure.
8. as efficient solid-liquid separation system as described in the claim 7, it is characterized in that described cyclone separation device adopts vertical structure, and be located at the top of efficient sedimentation device.
9. as efficient solid-liquid separation system as described in the claim 8, it is characterized in that described cyclone separation device and described efficient sedimentation device are equipped with sewage draining exit.
10. as efficient solid-liquid separation system as described in the claim 3, it is characterized in that the tank body of described surge tank for sealing, the top is provided with port, and the bottom is provided with sewage draining exit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201077715U CN201510803U (en) | 2009-04-30 | 2009-04-30 | High-efficiency solid-liquid separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201077715U CN201510803U (en) | 2009-04-30 | 2009-04-30 | High-efficiency solid-liquid separation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201510803U true CN201510803U (en) | 2010-06-23 |
Family
ID=42482199
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009201077715U Expired - Fee Related CN201510803U (en) | 2009-04-30 | 2009-04-30 | High-efficiency solid-liquid separation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201510803U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104117255A (en) * | 2013-04-26 | 2014-10-29 | 中国石油天然气股份有限公司 | Oil, gas, water and silt tetra-phase separation device |
-
2009
- 2009-04-30 CN CN2009201077715U patent/CN201510803U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104117255A (en) * | 2013-04-26 | 2014-10-29 | 中国石油天然气股份有限公司 | Oil, gas, water and silt tetra-phase separation device |
| CN104117255B (en) * | 2013-04-26 | 2016-01-06 | 中国石油天然气股份有限公司 | A kind of oil, gas, water, silt four phase-separating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100623 Termination date: 20130430 |