CN203513592U - Recovered oil sedimentation and dehydration device - Google Patents
Recovered oil sedimentation and dehydration device Download PDFInfo
- Publication number
- CN203513592U CN203513592U CN201320658321.1U CN201320658321U CN203513592U CN 203513592 U CN203513592 U CN 203513592U CN 201320658321 U CN201320658321 U CN 201320658321U CN 203513592 U CN203513592 U CN 203513592U
- Authority
- CN
- China
- Prior art keywords
- tank body
- oil
- feed liquor
- disengaging zone
- water
- 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.)
- Expired - Lifetime
Links
- 230000018044 dehydration Effects 0.000 title abstract description 5
- 238000006297 dehydration reaction Methods 0.000 title abstract description 5
- 238000004062 sedimentation Methods 0.000 title abstract 2
- 239000007788 liquid Substances 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000012856 packing Methods 0.000 claims abstract description 6
- 230000008021 deposition Effects 0.000 claims description 13
- 239000012530 fluid Substances 0.000 claims description 12
- 239000004744 fabric Substances 0.000 claims description 9
- 239000004519 grease Substances 0.000 claims description 9
- 239000010865 sewage Substances 0.000 claims description 8
- 239000000945 filler Substances 0.000 claims description 4
- 239000000919 ceramic Substances 0.000 claims description 3
- 238000013022 venting Methods 0.000 claims description 3
- 238000000926 separation method Methods 0.000 abstract description 9
- 238000004581 coalescence Methods 0.000 abstract description 5
- 239000003921 oil Substances 0.000 description 30
- 230000000694 effects Effects 0.000 description 6
- 239000000839 emulsion Substances 0.000 description 5
- 230000032683 aging Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002569 water oil cream Substances 0.000 description 1
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- Removal Of Floating Material (AREA)
Abstract
The utility model relates to a recovered oil sedimentation and dehydration device, which is mainly used for solving the problem in the prior art that the existing dehydration system is unstable in running and the dehydrated water is poor in quality. The device is characterized in that a liquid inlet pipeline (15) is connected with a liquid distribution box (1) in a tank body at one opposite side of a liquid inlet; an inner cavity in the tank body (2) is divided into three areas, respectively a liquid inlet area, a first separation area and a second separation area from left to right, through a first coalescence packing section (3) and a second coalescence packing section (5); the liquid distribution box (1) is positioned in the liquid inlet area; an oil room (12) and a water room (13) are respectively arranged at the right end of the tank body in the second separation area up and down and are respectively provided with an oil outlet (9) and a water outlet (11). As the device is used, the running stability of the dehydration system is improved; and the quality of the dehydrated water is effectively improved.
Description
Technical field
The utility model relates to a kind of deposition dehydrating device in crude oil dehydration field, particularly a kind of refiltered oil deposition dehydrating device.
Background technology
Along with the use of tertiary oil production in oil field technology, the crude oil that major part is exploited out is existed with form of emulsion, and emulsification is serious.Water-oil emulsion in the equipment such as sewage precipitation tank, at certain condition and stable gradually in the time, forms ageing oil, along with the prolongation of time, forms certain thickness, and the existence of ageing oil has brought series of problems to normal production the in oil field.Refiltered oil milk sap complicated component, contains the mechanical impuritys such as clay that much electroconductibility is stronger and FeS, often can cause dewatering system self-cleaning oil moisture exceed standard or de-after sewage quality exceed standard.Meanwhile, because the electroconductibility of these impurity is stronger, tend to cause apparatus for electrodewatering to occur Frequent trip, the electric field that even collapses, causes dewatering electric field operation not steady.
Summary of the invention
Technical problem to be solved in the utility model is to overcome the problem that the dewatering system operation existing in background technology is not steady and deviate from poor water mass, and provide a kind of refiltered oil deposition dehydrating device, this refiltered oil deposition dehydrating device, can improve the running stability of dewatering system, effectively improve and deviate from quality.
The invention for solving the technical problem can reach by following technical solution: this refiltered oil deposition dehydrating device, comprise tank body, described center, tank body one end has fluid inlet, fluid inlet connects horizontal feed liquor pipeline, described feed liquor pipeline connects the cloth liquid case in the relative side tank body of fluid inlet, in tank body, by the first coalescent pack section and the second coalescent pack section, inner chamber is divided into San Ge district from left to right, be respectively feed liquor district, the first disengaging zone, the second disengaging zone, described cloth liquid case is in feed liquor district, the second disengaging zone tank body right-hand member is respectively arranged with grease chamber up and down, hydroecium, described grease chamber, hydroecium have oil outlet, water outlet.
The utility model is compared and can be had following beneficial effect with above-mentioned background technology: this refiltered oil deposition dehydrating device, owing to adopting said structure, improves the running stability of dewatering system, has effectively improved and has deviate from quality.Apply this device processes refiltered oil, adding emulsion splitter 100mg/L, 70 ℃ of left and right for the treatment of temp, under the condition of residence time 6h, can reach de-rear oily water ratio below 0.5%.
accompanying drawing explanation:
Accompanying drawing 1 is structural representation of the present utility model.
In figure: 1-cloth liquid case, 2-tank body, 3-the first coalescent pack section, 4-light hole A, 5-the second coalescent pack section, 6-light hole B, 7-detector for oil-water interface table mouth, 8-venting port, 9-oil outlet, 10-fluid inlet, 11-water outlet, 12-grease chamber, 13-hydroecium, 14-sewage draining exit A, 15-feed liquor pipeline, 16-sewage draining exit B.
embodiment:
Below in conjunction with accompanying drawing, the utility model is described in further detail:
As shown in Figure 1, this refiltered oil deposition dehydrating device comprises tank body 2, described tank body 2 centers, one end have fluid inlet 10, fluid inlet 10 connects horizontal feed liquor pipeline 15, the cloth liquid case 1 that feed liquor pipeline 15 connects in the relative side tank body of fluid inlet, in tank body 2, by the first coalescent pack section 3 and the second coalescent pack section 5, inner chamber is divided into San Ge district from left to right, be respectively feed liquor district, the first disengaging zone, the second disengaging zone, described cloth liquid case 1 is in feed liquor district, the second disengaging zone tank body right-hand member is respectively arranged with grease chamber 12 up and down, hydroecium 13, on the first described disengaging zone tank body, have light hole A4, sewage draining exit A14, on the second disengaging zone tank body, have light hole B 6, sewage draining exit B16, detector for oil-water interface table mouth 7, venting port 8, described grease chamber 12, hydroecium 13 have oil outlet 9, water outlet 11.
This refiltered oil deposition dehydrating device, refiltered oil enters from one end of device through feed liquor pipeline 15 by fluid inlet 10, the end of feed liquor pipeline arranges Novel cloth liquid case 1, box type cloth liquid case not only has good current stabilization rectification characteristic, simultaneously liquid at this through water washing process, be conducive to breakdown of emulsion, there is certain pre-separation effect.Liquid, through 3 rectifications of the first packing section and coalescence effect, comes liquid flow velocity trend after rectification even, and the kinestate of liquid stream is adjusted, liquid stream is evenly distributed, constant speed is advanced, and is conducive to liquid layered, has reduced due to the inhomogeneous impact causing on oil-water separation of liquid stream.Second segment knot filler poly-5 coalescence effects, the effectively dewatering efficiency of ageing oil settling separation device.For the ease of the cleaning of coalescent pack, the top every section of coalescent pack, is provided with breather hole, plays the effect of ventilation and printing opacity during maintenance.Produced Liquid after layering, oil reservoir enters grease chamber 12, through oil outlet 9, flows out, and low oily(waste)water enters hydroecium 13, through water outlet 11, flows out.
Apply this device processes refiltered oil, add emulsion splitter 100mg/L in feed liquor pipeline, 70 ℃ of left and right for the treatment of temp, under the condition of residence time 6h, can reach de-rear oily water ratio below 0.5%, reach the moisture index request of outer oil transportation.
This refiltered oil deposition dehydrating device, fluid inlet arranges box type sparger, and box type not only has good current stabilization rectification characteristic, liquid, at this through water washing process, is conducive to breakdown of emulsion simultaneously, has certain pre-separation effect, simple in structure, be easy to install, be suitable for applying in engineering.Consider that refiltered oil content of impurities is high, easily make conventional coalescent pack stop up, settling section is arranged two sections of renewable ceramic packings of being convenient to cleaning, utilizes the water-wet behavior of ceramic packing, and what be conducive to that W/O drips is coalescent.First paragraph filler plays rectifying action, comes liquid flow velocity trend after rectification even, and the kinestate of liquid stream is adjusted, and liquid stream is evenly distributed, and constant speed is advanced, and is conducive to liquid layered, has reduced due to the inhomogeneous impact causing on oil-water separation of liquid stream.Second segment filler plays coalescence effect, effectively the dewatering efficiency of ageing oil settling separation device.In oil, water chamber structure, oil export baffle plate adopts ramp type, and the destruction of sloping baffle stream field stable uniformity is less.Adopt less grease chamber, increase water settling volume, and then improve the processing power of equipment.Before water outlet, set up sand control baffle plate, be convenient to sand removal sand control simultaneously.
Claims (3)
1. a refiltered oil deposition dehydrating device, comprise tank body (2), described tank body (2) center, one end has fluid inlet (10), fluid inlet (10) connects horizontal feed liquor pipeline (15), it is characterized in that: described feed liquor pipeline (15) connects the cloth liquid case (1) in the relative side tank body of fluid inlet, in tank body (2), by the first coalescent pack section (3) and the second coalescent pack section (5), inner chamber is divided into San Ge district from left to right, be respectively feed liquor district, the first disengaging zone, the second disengaging zone, described cloth liquid case (1) is in feed liquor district, the second disengaging zone tank body right-hand member is respectively arranged with grease chamber (12) up and down, hydroecium (13), described grease chamber (12), hydroecium (13) have oil outlet (9), water outlet (11).
2. refiltered oil deposition dehydrating device according to claim 1, it is characterized in that: on the first described disengaging zone tank body, have light hole A(4), sewage draining exit A(14), on the second disengaging zone tank body, have light hole B(6), sewage draining exit B(16), detector for oil-water interface table mouth (7), venting port (8).
3. refiltered oil deposition dehydrating device according to claim 1, is characterized in that: in the first described coalescent pack section (3) and the second coalescent pack section (5), the filler of filling is renewable ceramic packing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320658321.1U CN203513592U (en) | 2013-10-24 | 2013-10-24 | Recovered oil sedimentation and dehydration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320658321.1U CN203513592U (en) | 2013-10-24 | 2013-10-24 | Recovered oil sedimentation and dehydration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203513592U true CN203513592U (en) | 2014-04-02 |
Family
ID=50372549
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320658321.1U Expired - Lifetime CN203513592U (en) | 2013-10-24 | 2013-10-24 | Recovered oil sedimentation and dehydration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203513592U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115161069A (en) * | 2021-04-06 | 2022-10-11 | 中国石油天然气集团有限公司 | Distributor, oil product dehydration device, oil product dehydration system and method |
-
2013
- 2013-10-24 CN CN201320658321.1U patent/CN203513592U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115161069A (en) * | 2021-04-06 | 2022-10-11 | 中国石油天然气集团有限公司 | Distributor, oil product dehydration device, oil product dehydration system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140402 |