CN203890149U - Three-phase separator of water system - Google Patents
Three-phase separator of water system Download PDFInfo
- Publication number
- CN203890149U CN203890149U CN201420322056.4U CN201420322056U CN203890149U CN 203890149 U CN203890149 U CN 203890149U CN 201420322056 U CN201420322056 U CN 201420322056U CN 203890149 U CN203890149 U CN 203890149U
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- CN
- China
- Prior art keywords
- water
- separator
- housing
- cyclone separator
- automatic exhaust
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- Expired - Fee Related
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Abstract
The utility model discloses a three-phase separator of a water system and belongs to the field of water treatment technology. A discharging port is formed in the bottom of a shell of the three-phase separator of the water system, wherein a large-discharge automatic exhaust valve and a small-discharge automatic exhaust valve are arranged on the top of the shell; a water inlet and a water outlet are respectively formed in two sides of the shell; a container inner partition plate is arranged in the shell; a cyclone separator and a sintered mesh filter are arranged in the opening of the container inner partition plate. Through the three-phase separator, two processes of discharging gas and removing solid particles in the water treatment technology are combined into a whole, so that the technology is simple; two-stage three-phase separation of water is achieved in the separator, so that the occupied area of equipment facility is reduced, and the field construction cost and the daily operation and maintenance cost are greatly reduced; the three-phase separator of the water system is simple in daily operation and maintenance; other operation management is not required except manual intervention or automatic operation needed for regularly draining sewage, so that the operation cost is extremely low.
Description
Technical field
The utility model relates to a kind of water system triphase separator, belongs to water-treatment technology field.
Background technology
At present, in the water technology of water system, to the water body containing a small amount of gas and a small amount of solid particulate, treatment process is that opened system adopts construction settling tank, natural subsidence solid particulate also discharges gas, and closed system is to adopt to install vent valve additional at the vertex of pipeline, adds strainer etc. in pipeline.Above method technique is outmoded, and installations and facilities floor space is large, and construction cost is high, and line service amount is large.So far go back the succinct and effective treating method of neither one.
Summary of the invention
In order to overcome the deficiencies in the prior art, the utility model provides a kind of water system triphase separator, in an equipment, realize the secondary three phase separation of gas-liquid-solid, can reduce installations and facilities floor space, reduce construction cost, and this equipment is closed operation, to avoid the secondary pollution of open type operation scheme generation and the dissolving of gas.
The technical solution adopted in the utility model is: a kind of water system triphase separator, it comprises housing, the bottom of described housing is provided with slag-drip opening, and the top of housing is provided with large volume automatic exhaust valve and micro-automatic exhaust steam valve, and the both sides of housing are respectively equipped with water inlet and water out.The inside of described housing is provided with the container internal partition that housing is divided into epicoele and cavity of resorption, and the tapping of container internal partition is provided with cyclone separator and sintered meshwork filter.The water inlet pipe of described cyclone separator with the inner chamber of cyclone separator for to be tangentially connected, the pipe core of cyclone separator connects the large volume automatic exhaust valve of hull outside, the outlet at bottom of cyclone separator stretches into the cavity of resorption of container internal partition, and automatic exhaust steam valve is connected with the epicoele of container internal partition.
It is that large cylinder, middle part are that reverse taper is the grading structure that small cylinder is connected with bottom that described cyclone separator adopts top successively.
Adopt technique scheme, the water that contains gas, solid particulate enters into cyclone separator by water inlet, isolating air pocket discharges through large volume automatic exhaust valve, large solid particles sediment is discharged through slag-drip opening to container bottom, through cyclone separator current direction sintered meshwork after treatment filter, carry out secondary three phase separation, micro-bubble is discharged through micro-automatic exhaust steam valve, fine particulate matter is settled down to container bottom and discharges finally by slag-drip opening, and last clean water is discharged by water out.
The beneficial effects of the utility model are: the housing bottom of this water system triphase separator is provided with slag-drip opening, the top of housing is provided with large volume automatic exhaust valve and micro-automatic exhaust steam valve, the both sides of housing are respectively equipped with water inlet and water out, the inside of housing is provided with container internal partition, and the tapping of container internal partition is provided with cyclone separator and sintered meshwork filter.This triphase separator unites two into one the exhaust in water technology and two processes of solid particulate removal, technique is succinct, the secondary three phase separation that realizes water body in this separator, has reduced installations and facilities floor space, has significantly reduced on-the-spot construction cost and daily running maintenance expense.Water system triphase separator regular job easy maintenance, except periodic blow down needs manual intervention or automatic operation, does not need other operational management, and running cost is extremely low.
Brief description of the drawings
Fig. 1 is a kind of structural representation of water system triphase separator.
In figure: 1, large volume automatic exhaust valve, 1a, large discharge capacity venting port, 2, micro-automatic exhaust steam valve, 2a, micro-venting port, 3, cyclone separator, 3a, outlet at bottom, 3b, pipe core, 4, housing, 5, sintered meshwork filter, 6, slag-drip opening, 7, water inlet, 8, water out, 9, container internal partition, 9a, epicoele, 9b, cavity of resorption.
Embodiment
Referring to accompanying drawing, structure of the present invention is described further.
Fig. 1 shows a kind of water system triphase separator.In figure, this water system triphase separator comprises housing 4, and the bottom of housing 4 is provided with slag-drip opening 6, and the top of housing 4 is provided with large volume automatic exhaust valve 1 and micro-automatic exhaust steam valve 2, and the both sides of housing 4 are respectively equipped with water inlet 7 and water out 8.The inside of housing 4 is provided with the container internal partition 9 that housing 4 is divided into epicoele 9a and cavity of resorption 9b, and the tapping of container internal partition 9 is provided with cyclone separator 3 and sintered meshwork filter 5.It is that large cylinder, middle part are that reverse taper is the grading structure that small cylinder is connected with bottom that cyclone separator 3 adopts top successively.The water inlet pipe of cyclone separator 3 with the inner chamber of cyclone separator 3 for to be tangentially connected, the pipe core 3b of cyclone separator 3 connects the large volume automatic exhaust valve 1 of housing 4 outsides, the outlet at bottom 3a of cyclone separator 3 stretches into the cavity of resorption 9b of container internal partition 9, and automatic exhaust steam valve 2 is connected with the epicoele 9a of container internal partition 9.
While adopting technique scheme work, contain the water of a small amount of gas and a small amount of solid particulate under pressure-driven, tangentially enter in the cyclone separator 3 in triphase separator, and around cyclone separator 3 center high speed rotating, produce eddy effect, there is vacuum in the center at cyclone separator 3, overflows the air pocket in water, after the pipe core 3b of cyclone separator 3, automatically discharges from large discharge capacity vent valve 1.Meanwhile, the particle in water, under the effect of centrifugal force, gets rid of to the barrel of cyclone separator 3, is deposited to the bottom of triphase separator along barrel.Through cyclone separator 3 water after treatment, enter into sintered meshwork filter 5 by the bottom of this triphase separator, carry out second-stage treatment, sintered meshwork filter 5 can be tackled 5 microns and above solid particulate, the micro-bubble that is less than 5 microns is separated, micro-bubble is discharged through the micro-automatic exhaust steam valve 2 at triphase separator top simultaneously.Isolated solid particulate, can, according to the solid content of water body regularly by the slag-drip opening 6 of triphase separator bottom, utilize the pressure of water body self, discharges.
Claims (2)
1. a water system triphase separator, it comprises housing (4), it is characterized in that, the bottom of described housing (4) is provided with slag-drip opening (6), the top of housing (4) is provided with large volume automatic exhaust valve (1) and micro-automatic exhaust steam valve (2), and the both sides of housing (4) are respectively equipped with water inlet (7) and water out (8); The inside of described housing (4) is provided with the container internal partition (9) that a housing (4) is divided into epicoele (9a) and cavity of resorption (9b), and the tapping of container internal partition (9) is provided with cyclone separator (3) and sintered meshwork filter (5); The water inlet pipe of described cyclone separator (3) with the inner chamber of cyclone separator (3) for to be tangentially connected, the pipe core (3b) of cyclone separator (3) connects the outside large volume automatic exhaust valve (1) of housing (4), the outlet at bottom (3a) of cyclone separator (3) stretches into the cavity of resorption (9b) of container internal partition (9), and automatic exhaust steam valve (2) is connected with the epicoele (9a) of container internal partition (9).
2. a kind of water system triphase separator according to claim 1, is characterized in that, it is that large cylinder, middle part are that reverse taper is the grading structure that small cylinder is connected with bottom that described cyclone separator (3) adopts top successively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420322056.4U CN203890149U (en) | 2014-06-17 | 2014-06-17 | Three-phase separator of water system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420322056.4U CN203890149U (en) | 2014-06-17 | 2014-06-17 | Three-phase separator of water system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203890149U true CN203890149U (en) | 2014-10-22 |
Family
ID=51716577
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420322056.4U Expired - Fee Related CN203890149U (en) | 2014-06-17 | 2014-06-17 | Three-phase separator of water system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203890149U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106315843A (en) * | 2016-09-23 | 2017-01-11 | 同济大学 | Reactor for efficiently intercepting anaerobic ammonium oxidation bacteria under low-temperature conditions |
| CN114470879A (en) * | 2022-03-02 | 2022-05-13 | 燕山大学 | Gas-liquid-solid three-phase cyclone separation device with automatic exhaust valve and separation method thereof |
-
2014
- 2014-06-17 CN CN201420322056.4U patent/CN203890149U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106315843A (en) * | 2016-09-23 | 2017-01-11 | 同济大学 | Reactor for efficiently intercepting anaerobic ammonium oxidation bacteria under low-temperature conditions |
| CN106315843B (en) * | 2016-09-23 | 2019-09-27 | 同济大学 | The reactor of anaerobic ammonium oxidation bacteria is efficiently retained under a kind of cryogenic conditions |
| CN114470879A (en) * | 2022-03-02 | 2022-05-13 | 燕山大学 | Gas-liquid-solid three-phase cyclone separation device with automatic exhaust valve and separation method thereof |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141022 Termination date: 20180617 |