CN110304687A - A kind of three phase separator - Google Patents
A kind of three phase separator Download PDFInfo
- Publication number
- CN110304687A CN110304687A CN201910595910.1A CN201910595910A CN110304687A CN 110304687 A CN110304687 A CN 110304687A CN 201910595910 A CN201910595910 A CN 201910595910A CN 110304687 A CN110304687 A CN 110304687A
- Authority
- CN
- China
- Prior art keywords
- shell
- weir plate
- liquid level
- level gauge
- plate
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 239000003595 mist Substances 0.000 claims abstract description 14
- 239000002518 antifoaming agent Substances 0.000 claims abstract description 9
- 239000010865 sewage Substances 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims description 28
- 238000010079 rubber tapping Methods 0.000 claims description 9
- 239000003921 oil Substances 0.000 description 27
- 239000004519 grease Substances 0.000 description 11
- 239000010779 crude oil Substances 0.000 description 10
- 238000000926 separation method Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 4
- 238000004065 wastewater treatment Methods 0.000 description 4
- 238000013517 stratification Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000004587 chromatography analysis Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 210000005241 right ventricle Anatomy 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Removal Of Floating Material (AREA)
Abstract
The invention discloses a kind of three phase separators, including shell, separator inlet, safety valve, it takes out stitches disk, coalescing-plate, defoaming agent, gas vent, mist eliminator, access hole, oil export, weir plate, water out, vortex breaker, sewage draining exit and deflecting plates, the separator inlet is set to the left end of the shell, the access hole is set to the right end of the shell, the deflecting plates, coalescing-plate, defoaming agent and mist eliminator are according to being sequentially arranged in the intracorporal upside of the shell, the deflecting plates is connected with the separator inlet, the weir plate is set to below the mist eliminator, the weir plate is connected with the bottom interior wall of the shell, the water out is set to the left side of the weir plate, the oil export is set to the right side of the weir plate, the water out and oil export are connected with the bottom sidewall of the shell, the blowdown It mouthful is set in the bottom interior wall on the left of the shell, the safety valve takes out stitches disk and gas vent is set to the top of the shell.
Description
Technical field
The present invention relates to a kind of separator more particularly to a kind of three phase separators.
Background technique
Physical treatment process, method of chemical treatment and biological treatment three categories are broadly divided into wastewater treatment method at present.Object
Reason facture is the pollutant (including oil film and oil droplet) in suspended state by not understanding in physical action separation, recycling waste water
Waste water treatment process, be divided into gravitational separation process, centrifugal separation and sieving retention method etc..Belong to the processing unit of gravitational separation process
Have: precipitating floats (air bearing) etc., and the processing equipment accordingly used is setting pot, sedimentation basin, oil separator, gas pond and its attached dress
It sets, passes through the undissolved pollutant in suspended state in physical action separation, recycling waste water (including oil film and oil droplet)
Waste water treatment process.
With the propulsion and development of environmental protection industry (epi) exhaust gas method for treating wastewater, currently used for the three phase separator in oil field,
Not enough it is suitble to above waste gas pollution control and treatment, at this moment it is necessary to according in terms of waste water treatment, being more bonded three phase separator and waste water
Aspect is administered to improve.
Summary of the invention
The technical problem to be solved by the present invention is in order to overcome the defects of the prior art, now provide a kind of three phase separation
Device is divided into water chamber and grease chamber in shell, makes oil and water stratification by the density difference of oil and water, passes through the liquid level of weir plate two sides
Meter, the oil after accurately detecting layering enters grease chamber and water continues to maintain water chamber, and deflecting plates and coalescing-plate combine so that former
Oil grade separating treatment, water out are designed using vortex breaker, and mode whirlpool generates and crude oil is caused to be precipitated.
The present invention is to solve above-mentioned technical problem by following technical proposals:
A kind of three phase separator of the present invention, it is characterized in that, the three phase separator includes shell, separator inlet, peace
Full valve, disk of taking out stitches, coalescing-plate, defoaming agent, gas vent, mist eliminator, access hole, oil export, weir plate, water out, vortex breaker, row
Dirty mouth and deflecting plates, the separator inlet are set to the left end of the shell, and the access hole is set to the right side of the shell
End, the deflecting plates, coalescing-plate, defoaming agent and mist eliminator according to being sequentially arranged in the intracorporal upside of the shell, it is described partially
Rotating plate is connected with the separator inlet, and the weir plate is set to below the mist eliminator, the weir plate and the shell
Bottom interior wall be connected, the water out is set to the left side of the weir plate, and the oil export is set to the right side of the weir plate
Side, the water out and oil export are connected with the bottom sidewall of the shell, and the sewage outfalls setting is on the left of the shell
Bottom interior wall on, the safety valve takes out stitches disk and gas vent is set on the side wall of the case top.
Preferably, the two sides of the weir plate are provided with first liquid level gauge and second liquid level gauge, the first liquid level gauge setting
In the right side of the weir plate, the second liquid level gauge is set to the left side of the weir plate.
Preferably, the position of the lower pressure tappings of the first liquid level gauge and second liquid level gauge is set as same level, institute
The position for stating the upper pressure tappings of first liquid level gauge is set as above the upper pressure tappings of second liquid level gauge
Preferably, the top of the water out is provided with vortex breaker.
Preferably, the gas outlet is set to the upper surface of described mist eliminator.
The positive effect of the present invention is that:
The present invention is closed using effect is had in weir plate and shell, so that being divided into water chamber and grease chamber in shell, passes through oil and water
Density difference makes oil and water stratification, by the liquidometer of weir plate two sides, the oil after accurately detecting layering enter grease chamber and
Water continues to maintain water chamber, is combined using deflecting plates and coalescing-plate, so that crude oil is classified separating treatment, water out uses vortex breaker
Design, mode whirlpool generate and crude oil are caused to be precipitated.
Detailed description of the invention
Fig. 1 is diagrammatic cross-section of the invention.
Specific embodiment
The present invention is further illustrated below by the mode of embodiment, but does not therefore limit the present invention to the reality
It applies among a range.
Referring to Figure 1, a kind of three phase separator of the present invention, including shell 17, separator inlet 1, safety valve 2, disk of taking out stitches
3, coalescing-plate 4, defoaming agent 5, gas vent 6, mist eliminator 7, access hole 8, oil export 9, weir plate 10, water out 11, vortex breaker 12,
Sewage draining exit 13 and deflecting plates 14, separator inlet 1 are mounted on the left end of shell 17, and crude oil is flowed into shell from separator inlet 1
In 17, access hole 8 is mounted on the right end of shell 17, and personnel is facilitated to enter maintenance, deflecting plates 14, coalescing-plate 4, defoaming agent 5 and catches
Day with fog 7 is connected according to the upside being mounted in shell 17, deflecting plates 14 is sequentially arranged with separator inlet 1, and crude oil passes through inclined
Rotating plate 14 carries out first time detached job, and crude oil carries out second of separation again by coalescing-plate 4 after separation, and defoaming agent 5 is right
Liquid surface bubble after second of separation is eliminated, and weir plate 10 is mounted below mist eliminator 7, the bottom interior wall phase with shell 17
Shell lower half portion is cut into left and right room by connection, weir plate 10, and right ventricle becomes grease chamber, and left room becomes water chamber, and water out 11 is mounted on
The left side water chamber of weir plate 10, oil export 9 are mounted on the right side grease chamber of weir plate 10, the bottom of water out 11 and oil export 9 and shell 17
Portion's side wall runs through, when crude oil in water chamber precipitation and separation, according to the density variation of grease, water and oily chromatography in crude oil,
The density of water is greater than oil, so that water continues to stay in the water chamber in left side, then is flowed out by the water out 11 of water chamber bottom, when liquid
Liquid level continues to rise, and by separating twice, the oil separated enters the grease chamber on 10 right side of weir plate, then is flowed by oil export 9
Out, sewage draining exit 13 is mounted in the bottom interior wall of 17 left side water chamber of shell, and safety valve 2 takes out stitches disk 3 and gas vent 7 is mounted on
On the side wall at 17 top of shell.
Preferably, the two sides of weir plate 10 are equipped with first liquid level gauge 15 and second liquid level gauge 16, and first liquid level gauge 15 is mounted on
In the right side grease chamber of weir plate 10, second liquid level gauge 16 is mounted in the left side water chamber of weir plate 10, first liquid level gauge 15 and the second liquid
The position of the lower pressure tappings of position meter 16 is fixed on same level, and the upper pressure tappings installation of first liquid level gauge 15 is higher than the second liquid level
The upper pressure tappings of meter 16, by the separation situation of pressure difference detection oil and water, the top of water out 11 is equipped with vortex breaker 12, prevents
Whirlpool is generated when sealing flows out by oil sucking outflow, gas outlet 6 is mounted on the upper surface of mist eliminator 7.
The present invention is closed using effect is had in weir plate and shell, so that being divided into water chamber and grease chamber in shell, passes through oil and water
Density difference makes oil and water stratification, by the liquidometer of weir plate two sides, the oil after accurately detecting layering enter grease chamber and
Water continues to maintain water chamber, is combined using deflecting plates and coalescing-plate, so that crude oil is classified separating treatment, water out uses vortex breaker
Design, mode whirlpool generate and crude oil are caused to be precipitated.
The present invention has been described in detail with reference to the accompanying drawings, those skilled in the art can be according to upper
It states and bright many variations example is made to the present invention.All within the spirits and principles of the present invention, it is made it is any modification, equally replace
It changes, improve, should all be included in the protection scope of the present invention.Thus, certain details in embodiment should not be constituted to this
The restriction of invention, the present invention will be using the ranges that the appended claims define as protection scope of the present invention.
Claims (5)
1. a kind of three phase separator, which is characterized in that the three phase separator includes shell, separator inlet, safety valve, takes out stitches
Disk, coalescing-plate, defoaming agent, gas vent, mist eliminator, access hole, oil export, weir plate, water out, vortex breaker, sewage draining exit and partially
Rotating plate, the separator inlet are set to the left end of the shell, and the access hole is set to the right end of the shell, described inclined
Rotating plate, coalescing-plate, defoaming agent and mist eliminator according to being sequentially arranged in the intracorporal upside of the shell, the deflecting plates with it is described
Separator inlet is connected, and the weir plate is set to below the mist eliminator, the bottom interior wall of the weir plate and the shell
It is connected, the water out is set to the left side of the weir plate, and the oil export is set to the right side of the weir plate, and the water goes out
Mouth and oil export are connected with the bottom sidewall of the shell, bottom interior wall of the sewage outfalls setting on the left of the shell
On, the safety valve takes out stitches disk and gas vent is set on the side wall of the case top.
2. three phase separator according to claim 1, which is characterized in that the two sides of the weir plate are provided with first liquid level gauge
And second liquid level gauge, the first liquid level gauge are set to the right side of the weir plate, the second liquid level gauge is set to the weir plate
Left side.
3. three phase separator according to claim 2, which is characterized in that under the first liquid level gauge and second liquid level gauge
The position of pressure tappings is set as same level, and the position of the upper pressure tappings of the first liquid level gauge is set as second liquid level gauge
The upper surface of upper pressure tappings.
4. three phase separator according to claim 1, which is characterized in that the top of the water out is provided with vortex breaker.
5. three phase separator according to claim 1, which is characterized in that the gas outlet is set to the upper of the mist eliminator
Face.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910595910.1A CN110304687A (en) | 2019-07-03 | 2019-07-03 | A kind of three phase separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910595910.1A CN110304687A (en) | 2019-07-03 | 2019-07-03 | A kind of three phase separator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN110304687A true CN110304687A (en) | 2019-10-08 |
Family
ID=68078956
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910595910.1A Pending CN110304687A (en) | 2019-07-03 | 2019-07-03 | A kind of three phase separator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110304687A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112899023A (en) * | 2021-02-01 | 2021-06-04 | 江苏华普泰克石油装备有限公司 | Three-phase separator for petroleum processing |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1593418A1 (en) * | 2004-05-06 | 2005-11-09 | Services Petroliers Schlumberger | A gravity separator for a multi-phase effluent |
CN202289572U (en) * | 2011-11-06 | 2012-07-04 | 吉林大学 | Horizontal-type oil-gas-water triphase separator |
CN205297510U (en) * | 2015-12-22 | 2016-06-08 | 中国石油天然气股份有限公司 | three-phase separator |
CN205603358U (en) * | 2016-05-13 | 2016-09-28 | 陈丽亭 | Oil gas - water separation equipment |
KR101666603B1 (en) * | 2015-04-09 | 2016-10-14 | 태경중공업주식회사 | 3-phase seperator with high thermal efficiency |
CN211393942U (en) * | 2019-07-03 | 2020-09-01 | 上海力皇环保工程有限公司 | Three-phase separator |
-
2019
- 2019-07-03 CN CN201910595910.1A patent/CN110304687A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1593418A1 (en) * | 2004-05-06 | 2005-11-09 | Services Petroliers Schlumberger | A gravity separator for a multi-phase effluent |
CN202289572U (en) * | 2011-11-06 | 2012-07-04 | 吉林大学 | Horizontal-type oil-gas-water triphase separator |
KR101666603B1 (en) * | 2015-04-09 | 2016-10-14 | 태경중공업주식회사 | 3-phase seperator with high thermal efficiency |
CN205297510U (en) * | 2015-12-22 | 2016-06-08 | 中国石油天然气股份有限公司 | three-phase separator |
CN205603358U (en) * | 2016-05-13 | 2016-09-28 | 陈丽亭 | Oil gas - water separation equipment |
CN211393942U (en) * | 2019-07-03 | 2020-09-01 | 上海力皇环保工程有限公司 | Three-phase separator |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112899023A (en) * | 2021-02-01 | 2021-06-04 | 江苏华普泰克石油装备有限公司 | Three-phase separator for petroleum processing |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20191008 |