CN211393942U - Three-phase separator - Google Patents
Three-phase separator Download PDFInfo
- Publication number
- CN211393942U CN211393942U CN201921026276.1U CN201921026276U CN211393942U CN 211393942 U CN211393942 U CN 211393942U CN 201921026276 U CN201921026276 U CN 201921026276U CN 211393942 U CN211393942 U CN 211393942U
- Authority
- CN
- China
- Prior art keywords
- shell
- plate
- outlet
- weir plate
- liquid level
- Prior art date
- 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.)
- Active
Links
Images
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model discloses a three-phase separator, which comprises a shell, a separator inlet, a safety valve, a wire detaching disc, a coalescence plate, a defoaming agent, a gas outlet, a mist catcher, an access hole, an oil outlet, a weir plate, a water outlet, a vortex preventing device, a drain outlet and a deflection plate, wherein the separator inlet is arranged at the left end of the shell, the access hole is arranged at the right end of the shell, the deflection plate, the coalescence plate, the defoaming agent and the mist catcher are arranged at the upper side in the shell according to the sequence, the deflection plate is connected with the separator inlet, the weir plate is arranged below the mist catcher, the weir plate is connected with the bottom inner wall of the shell, the water outlet is arranged at the left side of the weir plate, the oil outlet is arranged at the right side of the weir plate, the water outlet and the oil outlet are connected with the bottom side wall of the shell, the drain outlet is arranged on the bottom inner wall at the left side of the shell, the safety valve, the disconnecting disc and the gas outlet are arranged at the top of the shell.
Description
Technical Field
The utility model relates to a separator especially relates to a three-phase separator.
Background
At present, the wastewater treatment methods are mainly divided into three main types, namely physical treatment methods, chemical treatment methods and biological treatment methods. The physical treatment method is a wastewater treatment method for separating and recovering undecided suspended contaminants (including oil films and oil droplets) in wastewater by physical action, and is classified into a gravity separation method, a centrifugal separation method, a sieve filtration method, and the like. The treating unit of the gravity separation method is a sewage treating method which comprises settling, floating (air floating) and the like, and the correspondingly used treating equipment is a grit chamber, a settling tank, an oil separating tank, an air tank, auxiliary devices thereof and the like, and separates and recovers insoluble suspended pollutants (including oil films and oil drops) in the sewage through physical action.
With the promotion and development of waste gas and waste water treatment methods in the environmental protection industry, the three-phase separator used in the oil field at present is not suitable for waste gas treatment, and the three-phase separator needs to be more attached and improved in the waste water treatment aspect according to the waste water treatment aspect.
SUMMERY OF THE UTILITY MODEL
The to-be-solved technical problem of the utility model is in order to overcome the defect among the prior art, now provide a three-phase separator, divide into hydroecium and grease chamber in the casing, density difference through oil and water makes oil and moisture layering, through the level gauge of weir plate both sides, the oil that accurately detects after the layering enters into grease chamber and water is in succession to be kept the hydroecium, deflector plate and coalescence plate combination make crude oil stage separation handle, the water outlet adopts vortex breaker design, the mode swirl produces and leads to crude oil to appear.
The utility model discloses an above-mentioned technical problem is solved through following technical scheme:
the utility model relates to a three-phase separator, which is characterized in that the three-phase separator comprises a shell, a separator inlet, a safety valve, a wire detaching disc, a coalescence plate, a defoaming agent, a gas outlet, a mist catcher, an access hole, an oil outlet, a weir plate, a water outlet, a vortex breaker, a drain and a deflection plate, wherein the separator inlet is arranged at the left end of the shell, the access hole is arranged at the right end of the shell, the deflection plate, the coalescence plate, the defoaming agent and the mist catcher are arranged at the upper side in the shell according to a sequence, the deflection plate is connected with the separator inlet, the weir plate is arranged below the mist catcher, the weir plate is connected with the bottom inner wall of the shell, the water outlet is arranged at the left side of the weir plate, the oil outlet is arranged at the right side of the weir plate, the water outlet and the oil outlet are connected with the bottom side wall of the shell, the sewage draining outlet is formed in the inner wall of the left bottom of the shell, and the safety valve, the disconnecting disc and the gas outlet are formed in the side wall of the top of the shell.
Preferably, both sides of the weir plate are provided with a first liquid level meter and a second liquid level meter, the first liquid level meter set up in the right side of the weir plate, the second liquid level meter set up in the left side of the weir plate.
Preferably, the positions of the lower pressure taking ports of the first liquid level meter and the second liquid level meter are arranged on the same horizontal plane, and the position of the upper pressure taking port of the first liquid level meter is arranged above the upper pressure taking port of the second liquid level meter
Preferably, the top end of the water outlet is provided with a vortex breaker.
Preferably, the air outlet is arranged above the mist trap.
The utility model discloses an actively advance the effect and lie in:
the utility model discloses a weir plate effectively combines in with the casing for divide into hydroecium and grease chamber in the casing, density difference through oil and water makes oil and moisture layering, through the level gauge of weir plate both sides, and the oil that the accuracy detected after the layering enters into grease chamber and water continues to remain the hydroecium, adopts deflector and coalescence plate combination, makes crude oil stage separation handle, and the water outlet adopts the design of vortex breaker, and the mode swirl produces and leads to crude oil to appear.
Drawings
Fig. 1 is a schematic cross-sectional view of the present invention.
Detailed Description
The present invention is further illustrated by way of the following examples, which are not intended to limit the scope of the invention.
Referring to fig. 1, the utility model relates to a three-phase separator, which comprises a shell 17, a separator inlet 1, a safety valve 2, a disconnecting disc 3, a coalescing plate 4, an antifoaming agent 5, a gas outlet 6, a mist catcher 7, an access opening 8, an oil outlet 9, a weir plate 10, a water outlet 11, a vortex breaker 12, a drain 13 and a deflector plate 14, wherein the separator inlet 1 is arranged at the left end of the shell 17, crude oil flows into the shell 17 from the separator inlet 1, the access opening 8 is arranged at the right end of the shell 17, so that personnel can conveniently enter the inspection, the deflector plate 14, the coalescing plate 4, the antifoaming agent 5 and the mist catcher 7 are arranged at the upper side of the shell 17 in sequence, the deflector plate 14 is connected with the separator inlet 1, crude oil is separated for the first time through the deflector plate 14, crude oil is separated for the second time through the coalescing plate 4 after separation, the antifoaming agent 5 eliminates bubbles on the liquid surface after the second separation, the weir plate 10 is arranged below the mist catcher 7 and is connected with the inner wall at the bottom of the shell 17, the weir plate 10 divides the lower half part of the shell into a left chamber and a right chamber, the right chamber becomes an oil chamber, the left chamber becomes a water chamber, the water outlet 11 is arranged in the left water chamber of the weir plate 10, the oil outlet 9 is arranged in the right oil chamber of the weir plate 10, the water outlet 11 and the oil outlet 9 penetrate through the side wall at the bottom of the shell 17, when crude oil is precipitated and separated in the water chamber, according to the density difference of oil and water, water in the crude oil is separated from oil by precipitation, the density of the water is higher than that of the oil, so that the water is continuously remained in the water chamber on the left side and flows out through the water outlet 11 at the bottom of the water chamber, when the liquid level of the liquid continues to rise, the separated oil enters the oil chamber on the right side of the weir plate 10 and then flows out through the oil outlet 9 by two times of separation, the sewage discharge outlet 13 is arranged on the inner wall of the bottom of the water chamber on the left side of the shell 17, and the safety valve 2, the disconnecting disc 3 and the gas outlet 7 are arranged on the side wall of the top of the shell 17.
Preferably, a first liquid level meter 15 and a second liquid level meter 16 are arranged on two sides of the weir plate 10, the first liquid level meter 15 is arranged in a right oil chamber of the weir plate 10, the second liquid level meter 16 is arranged in a left water chamber of the weir plate 10, lower pressure taking ports of the first liquid level meter 15 and the second liquid level meter 16 are fixed on the same horizontal plane, an upper pressure taking port of the first liquid level meter 15 is arranged higher than an upper pressure taking port of the second liquid level meter 16, the separation condition of oil and water is detected through pressure difference, a vortex breaker 12 is arranged at the top end of the water outlet 11, vortex is generated when water flows out to suck and flow out oil, and the air outlet 6 is arranged on the mist catcher 7.
The utility model discloses a weir plate effectively combines in with the casing for divide into hydroecium and grease chamber in the casing, density difference through oil and water makes oil and moisture layering, through the level gauge of weir plate both sides, and the oil that the accuracy detected after the layering enters into grease chamber and water continues to remain the hydroecium, adopts deflector and coalescence plate combination, makes crude oil stage separation handle, and the water outlet adopts the design of vortex breaker, and the mode swirl produces and leads to crude oil to appear.
The present invention has been described in detail with reference to the embodiments shown in the drawings, and those skilled in the art can make various modifications to the present invention based on the above description. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention. Therefore, certain details of the embodiments should not be construed as limitations of the invention, which are intended to be covered by the following claims.
Claims (3)
1. A three-phase separator is characterized by comprising a shell, a separator inlet, a safety valve, a wire detaching disc, a coalescence plate, a defoaming agent, a gas outlet, a mist catcher, an access hole, an oil outlet, a weir plate, a water outlet, a vortex breaker, a sewage draining outlet and a deflection plate, wherein the separator inlet is arranged at the left end of the shell, the access hole is arranged at the right end of the shell, the deflection plate, the coalescence plate, the defoaming agent and the mist catcher are sequentially arranged at the upper side in the shell, the deflection plate is connected with the separator inlet, the weir plate is arranged below the mist catcher, the weir plate is connected with the inner wall at the bottom of the shell, the water outlet is arranged at the left side of the weir plate, the oil outlet is arranged at the right side of the weir plate, and the water outlet and the oil outlet are connected with the side wall at the bottom of the shell, the sewage draining outlet is arranged on the inner wall of the bottom of the left side of the shell, and the safety valve, the disconnecting disc and the gas outlet are arranged on the side wall of the top of the shell; a first liquid level meter and a second liquid level meter are arranged on two sides of the weir plate, the first liquid level meter is arranged on the right side of the weir plate, and the second liquid level meter is arranged on the left side of the weir plate; the pressure measuring device is characterized in that the positions of lower pressure taking ports of the first liquid level meter and the second liquid level meter are arranged on the same horizontal plane, and the position of an upper pressure taking port of the first liquid level meter is arranged above an upper pressure taking port of the second liquid level meter.
2. The separator of claim 1, wherein the top end of the water outlet is provided with a vortex breaker.
3. The three-phase separator according to claim 1, wherein the gas outlet is provided above the mist trap.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921026276.1U CN211393942U (en) | 2019-07-03 | 2019-07-03 | Three-phase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921026276.1U CN211393942U (en) | 2019-07-03 | 2019-07-03 | Three-phase separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211393942U true CN211393942U (en) | 2020-09-01 |
Family
ID=72225875
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921026276.1U Active CN211393942U (en) | 2019-07-03 | 2019-07-03 | Three-phase separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211393942U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110304687A (en) * | 2019-07-03 | 2019-10-08 | 上海力皇环保工程有限公司 | A kind of three phase separator |
-
2019
- 2019-07-03 CN CN201921026276.1U patent/CN211393942U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110304687A (en) * | 2019-07-03 | 2019-10-08 | 上海力皇环保工程有限公司 | A kind of three phase separator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP2366440B1 (en) | Oil-water separator with self-priming pump | |
| CN201217639Y (en) | Integrated waste water treatment device | |
| CN211393942U (en) | Three-phase separator | |
| CN210400464U (en) | Oil-gas-water three-phase automatic metering device | |
| CN211216044U (en) | Gas-liquid separator | |
| CN207126169U (en) | A kind of Multi-stage oil-water separation facility | |
| CN207175535U (en) | A kind of separator for oily water | |
| CN109553207A (en) | Leak the oily-water seperating equipment in petroleum recovery process | |
| CN110304687A (en) | A kind of three phase separator | |
| CN212894180U (en) | Oily wastewater treatment oil interceptor | |
| US8944256B2 (en) | Filter | |
| CN204874091U (en) | High accuracy aquatic deoiling device | |
| WO2017069170A1 (en) | Suction nozzle and fluid recovery device | |
| CN208603769U (en) | A kind of water-oil separation device | |
| CN205598836U (en) | High -efficient tail gas cleanup unit | |
| CN2688361Y (en) | Natural gas multi-phase separator | |
| CN213803003U (en) | High-temperature high-pressure advection microbubble flotation unit | |
| CN210419362U (en) | Industrial oily wastewater separation and purification device | |
| CN217092189U (en) | Small-size vertical coalescence divides oil machine | |
| CN218968921U (en) | High-efficiency and low-flow-resistance marine oil sewage treatment device | |
| CN203925359U (en) | Under balance pressure drilling anti-block liquid gas separating device | |
| CN212713393U (en) | Natural gas deoiling device | |
| CN118458974A (en) | Airtight multistage air supporting deoiling device of oil field produced water | |
| CN209260029U (en) | A kind of level Four filter separator | |
| CN104828991B (en) | Discharging system for offshore platform |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |