CN2391871Y - Three-phase separator - Google Patents
Three-phase separator Download PDFInfo
- Publication number
- CN2391871Y CN2391871Y CN99228910U CN99228910U CN2391871Y CN 2391871 Y CN2391871 Y CN 2391871Y CN 99228910 U CN99228910 U CN 99228910U CN 99228910 U CN99228910 U CN 99228910U CN 2391871 Y CN2391871 Y CN 2391871Y
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- China
- Prior art keywords
- triphase separator
- cylindrical shell
- district
- reaction device
- flow
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- 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
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- Y02W10/12—
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model relates to a novel three-phase separator, which fully utilizes a hydraulics principle. The three-phase separation effect is enhanced through arranging an adjustable flow guide plate on an inlet section, and water draining speed can be conveniently controlled to accommodate fluctuation of a hydraulic load.
Description
The utility model relates to a kind of tripping device, particularly relates to a kind of novel triphase separator.
Triphase separator mainly is to utilize hydraulic principle to realize gas, the triphasic effective separation of solid, liquid, thereby reaches that branch is dried up, the purpose of mud and methane gas.Triphase separator has been widely used in the anaerobism waste disposal plant such as outer-flowing type anaerobic reactor (UASB), anaerobic grain bed (EGSB) at present.Core as the anaerobic biochemical reaction device one of is constructed, and the separating effect of triphase separator directly determines the quality of anaerobic reaction device performance.Traditional triphase separator mainly is to utilize the variation of water flow section to cause the difference of gas-solid liquid three-phase fluid speed, thereby realizes the purpose of three phase separation.Generally all do not add any guiding device in its ingress, only rely on single water flow section to change, therefore traditional triphase separator is all existing the halfway defective of three phase separation effect in varying degrees.In actual mechanical process, also often run into sewage flooding quantity instability, the bigger phenomenon that fluctuates, this just needs to seek a kind of effective means and controls the adaptability of reaction unit to the hydraulic load fluctuation, and does not see also that in traditional triphase separator effective device is arranged.
The purpose of this utility model is to overcome the shortcoming of traditional triphase separator, designs a kind ofly can effectively improve the three phase separation effect, can conveniently adjust water speed again, thereby adapts to the triphase separator of hydraulic load fluctuation.
The technical scheme that realizes the utility model purpose is as follows: triphase separator has the triphase separator cylindrical shell, its top is the non-air-gathering zone venting port, the lower end is the triphase separator inlet section, triphase separator cylindrical shell inner side-wall is provided with effluent weir, effluent weir communicates with the triphase separator water outlet in the triphase separator cylindrical shell outside, triphase separator cylindrical shell below socket anaerobic reaction device up-flow district cylindrical shell, and the triphase separator inlet section is stretched in the anaerobic reaction device up-flow district cylindrical shell, cylindrical shell lower end, anaerobic reaction device up-flow district is a water-in, anaerobic reaction device up-flow district cylindrical shell upper side wall is provided with the gas collection district venting port that is in triphase separator inlet section top, be provided with flow deflector in anaerobic reaction device up-flow district cylindrical shell, flow deflector is connected with the triphase separator inlet section by governor lever.
As further technical measures of the present utility model, above-mentioned flow deflector is symmetric streamline contour plate.
Advantage of the present utility model is to make full use of hydraulic principle, by an adjustable flow deflector is set, has both improved the three phase separation effect, can control out water speed easily again, to adapt to the fluctuation of hydraulic load.
Fig. 1 is the utility model structural representation.
Below in conjunction with accompanying drawing embodiment of the present utility model is described further:
Each mark is as follows among Fig. 1: the A district is the triphase separator non-air-gathering zone, and the B district is the triphase separator settling region, and the C district is triphase separator gas collection district, and the D district is anaerobic reaction device up-flow district; 1-flow deflector; 2-governor lever; 3-triphase separator inlet section; 4-triphase separator water outlet; 5-non-air-gathering zone venting port; 6-effluent weir; 7-triphase separator cylindrical shell; 8-gas collection district venting port; 9-anaerobic reaction device up-flow district cylindrical shell; 10-water-in.
When the utility model uses, anaerobic reaction device up-flow district, D district when fluid enters anaerobic reaction device up-flow district cylindrical shell 9 from water-in 10 in, during the tabular flow deflector 1 of the symmetric streamline contour made according to hydraulic performance of flowing through, stream, because the difference of triphasic hydraulic performance, must cause the certain velocity contrast of three alternate formation, thereby being taken the lead in, separates gas, spill into C district, triphase separator gas collection district after gas collection district venting port 8 is discharged, when the fluctuation of generation hydraulic load is big, can regulate governor lever 2 easily, adjust the distance between triphase separator inlet section 3 and the flow deflector 1, thereby reach the purpose of controlling out water speed, to adapt to the fluctuation of hydraulic load.Remaining fluid enters triphase separator settling region, B district in the triphase separator cylindrical shell 7 from triphase separator inlet section 3, liquid enters effluent weir 6 after triphase separator water outlet 4 is discharged, remaining gas is discharged from non-air-gathering zone venting port 5 through A district triphase separator non-air-gathering zone, and solid then precipitates.
Claims (2)
1, a kind of novel triphase separator, has triphase separator cylindrical shell (7), its top is non-air-gathering zone venting port (5), the lower end is triphase separator inlet section (3), triphase separator cylindrical shell (7) inner side-wall is provided with effluent weir (6), effluent weir (6) communicates with the triphase separator water outlet (4) in the triphase separator cylindrical shell outside, triphase separator cylindrical shell (7) below socket anaerobic reaction device up-flow district's cylindrical shell (9), and triphase separator inlet section (3) is stretched in the anaerobic reaction device up-flow district cylindrical shell (9), anaerobic reaction device up-flow district cylindrical shell (9) lower end is water-in (10), anaerobic reaction device up-flow district cylindrical shell (9) upper side wall is provided with the gas collection district venting port (8) that is in triphase separator inlet section (3) top, it is characterized in that: be provided with flow deflector (1) in anaerobic reaction device up-flow district cylindrical shell (9), flow deflector (1) is connected with triphase separator inlet section (3) by governor lever (2).
2, triphase separator according to claim 1 is characterized in that: described flow deflector (1) is symmetric streamline contour plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99228910U CN2391871Y (en) | 1999-07-14 | 1999-07-14 | Three-phase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99228910U CN2391871Y (en) | 1999-07-14 | 1999-07-14 | Three-phase separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2391871Y true CN2391871Y (en) | 2000-08-16 |
Family
ID=34018211
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99228910U Expired - Fee Related CN2391871Y (en) | 1999-07-14 | 1999-07-14 | Three-phase separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2391871Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104368208A (en) * | 2014-11-13 | 2015-02-25 | 常熟市高压容器制造有限公司 | Combined bubble cap type three-phase separator |
| CN113504150A (en) * | 2021-07-07 | 2021-10-15 | 巨翊医疗科技(苏州)有限公司 | Dynamic liquid specific gravity detector and dynamic detection method |
-
1999
- 1999-07-14 CN CN99228910U patent/CN2391871Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104368208A (en) * | 2014-11-13 | 2015-02-25 | 常熟市高压容器制造有限公司 | Combined bubble cap type three-phase separator |
| CN113504150A (en) * | 2021-07-07 | 2021-10-15 | 巨翊医疗科技(苏州)有限公司 | Dynamic liquid specific gravity detector and dynamic detection method |
| CN113504150B (en) * | 2021-07-07 | 2024-03-15 | 巨翊医疗科技(苏州)有限公司 | Dynamic detector for specific gravity of liquid and dynamic detection method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |