CN2477617Y - Pressure oil removing settling pot - Google Patents
Pressure oil removing settling pot Download PDFInfo
- Publication number
- CN2477617Y CN2477617Y CN 00260870 CN00260870U CN2477617Y CN 2477617 Y CN2477617 Y CN 2477617Y CN 00260870 CN00260870 CN 00260870 CN 00260870 U CN00260870 U CN 00260870U CN 2477617 Y CN2477617 Y CN 2477617Y
- Authority
- CN
- China
- Prior art keywords
- water
- tank body
- oil removing
- plate
- chamber
- 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 - Fee Related
Links
Images
Landscapes
- Removal Of Floating Material (AREA)
Abstract
The utility model discloses a pressure oil separating and sedimentation tank used in the handling technique of water pumped from an oil filed. The tank comprises a tank body, a liquid entering pipe, an oil receiving opening and a water exiting pipe. The position from the internal part at the left end of the tank body to the middle part of the tank body is orderly provided with the liquid entering pipe, an agglutination cavity, an oil separating cavity and a central water receiving cavity. The position from the internal part at the right end of the tank body to the middle part of the tank body is orderly provided with a reacting cavity, a sedimentation cavity and a final water receiving cavity. The wasted water entering the liquid entering pipe are orderly agglutinated and precipitated as well as separated so as to enable the released wasted water content contained in the oil field to reduce from 500mg per liter below 20mg per liter with floating articles removing efficiency of above 90 percent. The pressing oil separating and sedimentation tank manufactured as per the technical scheme enables a new built wasted water handling station with daily handling amount of 4 by 10 <4>m<3> to reduce the fundamental building investment by 4 million 500 thousand RMB, furthermore, the economic benefit is substantial.
Description
The utility model relates to a kind of pressure oil removing slurry tank that is used for oil field produced water treatment.
Consult the pressure oil removing slurry tank that still finds no dependency structure by retrieval.
Oil field extracted water is not only polluted by crude oil, and it has dissolved various salts and the gas in the stratum in high temperature, highly compressed oil reservoir; In oil recovery process, in oil reservoir, carry many suspended solidss; All kinds of chemical agents in the oil-gas gathering and transportation process, have been mixed into; Contain large amount of organic in the recovered water again, suitable microorganism survival environment is arranged, encouraged the breeding of bacterium.In a word, recovered water is the waste water that contains plurality of impurities.Oil field produced water technology is started in the fifties in China, the research of going through 40 years is used and development, now formed comparatively supporting technical system, but raising along with oil recovery technique, variation has taken place in the character of recovered water, particularly in recent years, adopt " three adopt engineering " for improving oil recovery factor, injected a large amount of oil-displacing agents to underground, the also corresponding oil-displacing agent composition (average polymer content reaches more than the 50mg/L in the recovered water at present) that contains in the extraction liquid, and the water quality requirement after handling has also been had large increase, this goes out water treatment just for oil field Bian and has brought new problem, new difficult point.
The present situation of each oil recovery factory's oily water treatment, problem and countermeasure and each sewage plant hay tank working condition were done investigation and analysis under Prospecting Design Inst., Shengli Petroleum Administration began Shengli Petroleum Administration Bureau in 1998, discovery as liquid-liquid, liquid-solid heterogeneous isolating extracted water deoiling, remove the most economical way of suspended substance and remain gravity method, promptly utilize the density variation of water, oil, suspended substance, make dispersed oil droplets in the water, the sedimentation of suspended substance buoyance lift and the three is separated.Liquid-the liquid of different densities difference, the separation efficiency of liquid-solid system are by " shallow pond " principle, only relevant with the buoyance lift settling area with the terminal velocity of oil droplet, solid particulate, and it is irrelevant with the buoyance lift settling height, this inclined tube swash plate treatment technology just occurred, plate distance or honeycomb diameter are more little, under identical treatment capacity, can get rid of more little oil droplet of particle diameter and solid particulate, increase the oil removing settling efficiency; Or under the condition of same treatment efficient, improve the processing power of equipment.But minification is given on the spoil disposal oil removing structure treatment again and has been brought difficulty, has limited size between further shortening plate, has just limited further raising processing efficiency.By " shallow pond " theory, another approach of strengthening the profit gravity separation is the particle diameter that increases oil droplet, has so just developed coalescence technology, is about to tiny oil droplet and adheres to coalescent peeling off on the solid matter of surperficial oleophilic drainage, formation larger oil droplet and accelerate its sepn process.
The purpose of this utility model combines coalescence technology and " shallow pond " principle exactly, has designed and developed and has gathered knot small echo plate lateral flow oil removing and eddy flow grid reaction small echo plate flocculating settling in the pressure oil removing slurry tank of one.
The technical solution of the utility model realizes in the following manner:
This utility model is the pressure oil removing slurry tank of using in the treatment Technology for Petroleum Water Flooding, comprise tank body, liquid-inlet pipe, coalescent bead, the high lateral flow ripple plate that intersects of the small echo that has drain hole, mixing device, eddy flow graticule mesh reaction tube, not with the corrugated-crossed plate of the many crests of little wave height of drain hole, receiving port, mud discharging mouth, receive water pipe, it is characterized in that intersegmental part only is provided with admission chamber A by preface in play tank body left end inside, coalescent chamber B, oil removing disengagement chamber C and receipts water cavity D, intersegmental part only is provided with reaction chamber E by preface again in play tank body right-hand member inside, settlement separate chamber F and receipts water cavity G, tank body is provided with mixing tank outward.The water outlet of the water of one section processing through receiving water cavity D enters the import of two sections processing and carry out two sections processing, and be defeated outside the outlet of the water after the processing through receiving water cavity G;
Longitudinal section is provided with dividing plate in the tank body middle part, and the dividing plate left side is established and received water cavity D, and the right is established and received water cavity G, vertically is provided with the mountain font in the D and receives water pipe, and middle pipe water outlet pass-out tank body water-ins outer and two sections processing join.In G, vertically be provided with mountain font rising pipe, middle water outlet, the outer and external transport pipeline of pass-out tank body joins;
Two ends are provided with the filler barrier in the coalescent chamber, and the right-hand member barrier is provided with baffle plate in two ends up and down, and the top of packing cavity is provided with receiving port/feeding port, and the bottom is provided with sewage draining exit/discharge gate.The sewage draining exit place is provided with dividing plate with holes;
Be furnished with the high lateral flow ripple plate that intersects of the small echo that has drain hole in the oil removing disengagement chamber, the plate group is made up of less than the waved plate that has drain hole of 25mm by 45 °-60 ° bonding wave height of intersection a series of, every group tiltedly is put in oil removing disengagement chamber on jar intravital filler support by 45 °-60 °, the oil removing disengagement chamber is provided with a receiving port, the side is provided with feeding port, oil removing disengagement chamber bottom is provided with sewage draining exit, is provided with the sand clean out pipe of band nozzle on the sewage draining exit both sides;
Be furnished with the corrugated-crossed plate of the many crests of little wave height of not being with drain hole in the settlement separate chamber, the plate group is made up of less than the waved plate that does not have drain hole of 25mm by 45 °-60 ° bonding wave height of intersection a series of, every group tiltedly is put in settlement separate chamber on jar intravital filler support by 45 °-60 °, settlement separate chamber is provided with a receiving port, a feeding port, bottom, settlement separate chamber is provided with sewage draining exit, is provided with the sand clean out pipe of band nozzle on the sewage draining exit both sides;
Be provided with eddy flow grid reaction tube at the tank body right-hand member, its top is provided with a receiving port, and the bottom is provided with a sewage draining exit;
On the connection pipe of the water outlet of receiving water cavity D and eddy flow grid reaction tube water-in, mixing equipment is housed.
The utility model is compared with used sewage treatment pot, the sewage by suspended thing content≤10mg/L after the processing, oil-containing≤20mg/L.And sewage load is big, and the residence time is short, and is effective, not only can be used for the sewage disposal of tertiary oil recovery, also is suitable for the sewage disposal of secondary oil recovery, is a kind of sewage disposal oil removing slurry tank with application prospect.Pressure oil removing slurry tank according to the technique scheme manufacturing can make the newly-built treatment capacity 4 * 10 of saying
4m
3Sewage works is saved 4,500,000 yuan of initial costs, and economic benefit is considerable.
For the clear the technical program of expressing, be further elaborated by embodiment below in conjunction with Figure of description.
Fig. 1 is the utility model one-piece construction sectional view
Fig. 2 is that the I-I view is vertical waved plate support synoptic diagram among Fig. 1
Fig. 3 is that the II-II view is coalescent bead support figure among Fig. 1
Fig. 4 is that the III-III view is the middle water pipe/water outlet synoptic diagram of receiving among Fig. 1
Fig. 5 is that the IV-IV view is oil removing section and settling section pipe connecting synoptic diagram among Fig. 1
Fig. 6 is that the V-V view is the final water pipe/water outlet synoptic diagram of receiving among Fig. 1
Fig. 7 is that the X-X view is the grid synoptic diagram among Fig. 1
Fig. 8 is that the IX-IX view is the graticule mesh synoptic diagram among Fig. 1
Fig. 9 is that the VIII-VIII view is the graticule mesh synoptic diagram among Fig. 1
Figure 10 is that the VII-VII view is the graticule mesh synoptic diagram among Fig. 1
Figure 11 is that the VI-VI view is the graticule mesh synoptic diagram among Fig. 1
Among Fig. 1, the 1st, liquid-inlet pipe, the 2nd, hand-hole, the 3rd, sewage draining exit, the 4th, saddle support, 5 mud discharging mouths/hand-hole, the 6th, sand clean out pipe, the 7th, middle water-in, the 8th, receiving port, the 9th, receiving port/inlet, the 10th, feeding port/receiving port, the 11st, vertical intersection ripple plate, the 12nd, the coalescent bead of SH type, the 13rd, the high lateral flow ripple plate that intersects of small echo, the 14th, eddy flow graticule mesh reactive moieties, the 15th, the middle water section/middle water outlet of receiving, the 16th, finally receive water section/final outflow water mouth, the 17th, mixing device, the 18th, cylindrical shell, the 19th, the corrugated-crossed plate of the many crests of little wave height.
The technological principle flow process of this device is:
Oil field extracted water enters admission chamber A by liquid-inlet pipe 1; spray to the spherical cap of tank body 18 by fluid inlet; entering coarse part 12 by 11 water distributions of vertical intersection ripple plate behind the reduction kinetic energy flocculates coalescent; then enter the high lateral flow ripple plate 13 that intersects of small echo that leading portion has drain hole and carry out oily water separation; separate back sewage and enter receipts water cavity D; receive water pipe/middle water outlet 15 by the centre and enter eddy flow graticule mesh reactive moieties 14; then carry out the suspended substance flocculation sediment, handle back water and pass through final water pipe/final water shoot 16 outer the failing of receiving by the corrugated-crossed plate 19 of the many crests of the little wave height of back segment.Sewage is in flow process, and the little oil droplet in the sewage has high coalescent, the coarse separation of peeling off, float of lateral flow ripple plate 13 surface adsorption of intersecting of small echo of drain hole by waved plate group 11, Ball-type packing 12, leading portion, makes crude oil float over tank inner chamber top.Remove and to enter eddy flow graticule mesh reactive moieties 14 after the dosing then of japanned sewage is mixed by mixing tank 17 and flocculate, suspended substance is settlement separate by the corrugated-crossed plate of the many crests of little wave height 19.The final back sewage of handling is collected outer defeated by final receipts water section/final outflow water mouth 16.With crude oil recovery, the mud that falls to the bottom is effluxed by sewage draining exit 3,5 by sand clean out pipe 6 flushings the sump oil of come-up by receiving port 8,9 in the pressure oil removing slurry tank.
Claims (7)
1, the pressure oil removing slurry tank of using in a kind of treatment Technology for Petroleum Water Flooding, comprise tank body, liquid-inlet pipe, coalescent bead, the high lateral flow ripple plate that intersects of the small echo that has drain hole, mixing device, eddy flow graticule mesh reaction tube, not with the corrugated-crossed plate of the many crests of little wave height of drain hole, receiving port, mud discharging mouth, receive water pipe, it is characterized in that intersegmental part only is provided with admission chamber A by preface in play tank body left end inside, coalescent chamber B, oil removing disengagement chamber C and receipts water cavity D, intersegmental part only is provided with reaction chamber E by preface again in play tank body right-hand member inside, settlement separate chamber F and receipts water cavity G, tank body is provided with mixing tank outward.
2, oil field produced water pressure oil removing slurry tank according to claim 1, it is characterized in that longitudinal section is provided with dividing plate in the tank body middle part, the dividing plate left side is established and is received water cavity D, the right is established and is received water cavity G, vertically be provided with the mountain font in the D and receive water pipe, middle pipe water outlet pass-out tank body water-ins outer and two sections processing join, and vertically are provided with mountain font rising pipe in G, middle water outlet, the outer and external transport pipeline of pass-out tank body joins.
3, oil removing slurry tank according to claim 1 is characterized in that two ends are provided with the filler barrier in the coalescent chamber, and the right-hand member barrier is provided with baffle plate in two ends up and down, and the top of packing cavity is provided with receiving port/feeding port, and the bottom is provided with sewage draining exit/discharge gate.The sewage draining exit place is provided with dividing plate with holes.
4, pressure oil removing slurry tank according to claim 1, it is characterized in that being furnished with in the oil removing disengagement chamber the high lateral flow ripple plate that intersects of the small echo that has drain hole, the plate group is made up of less than the waved plate that has drain hole of 25mm by 45 °-60 ° bonding wave height of intersection a series of, every group tiltedly is put in oil removing disengagement chamber on jar intravital filler support by 45 °-60 °, the oil removing disengagement chamber is provided with a receiving port, the side is provided with feeding port, oil removing disengagement chamber bottom is provided with sewage draining exit, is provided with the sand clean out pipe of band nozzle on the sewage draining exit both sides.
5, pressure oil removing slurry tank according to claim 1, it is characterized in that being furnished with in the settlement separate chamber the corrugated-crossed plate of the many crests of little wave height of not being with drain hole, the plate group is made up of less than the waved plate that does not have drain hole of 25mm by 45 °-60 ° bonding wave height of intersection a series of, every group tiltedly is put in settlement separate chamber on jar intravital filler support by 45 °-60 °, settlement separate chamber is provided with a receiving port, a feeding port, bottom, settlement separate chamber is provided with sewage draining exit, is provided with the sand clean out pipe of band nozzle on the sewage draining exit both sides.
6, pressure oil removing slurry tank according to claim 1 is characterized in that being provided with eddy flow grid reaction tube at the tank body right-hand member, and its top is provided with a receiving port, and the bottom is provided with a sewage draining exit.
7, sewage degrease slurry tank according to claim 1 is characterized in that on the connection pipe of the water outlet of receiving water cavity D and eddy flow grid reaction tube water-in mixing equipment being housed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00260870 CN2477617Y (en) | 2000-10-27 | 2000-10-27 | Pressure oil removing settling pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00260870 CN2477617Y (en) | 2000-10-27 | 2000-10-27 | Pressure oil removing settling pot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2477617Y true CN2477617Y (en) | 2002-02-20 |
Family
ID=33616576
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00260870 Expired - Fee Related CN2477617Y (en) | 2000-10-27 | 2000-10-27 | Pressure oil removing settling pot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2477617Y (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102266680A (en) * | 2011-06-23 | 2011-12-07 | 江苏中源电力设备有限公司 | Oil-water separator |
| CN102397712A (en) * | 2010-09-15 | 2012-04-04 | 张步芳 | Mobile oil-water separation device with floating oil absorber |
| CN102745771A (en) * | 2012-02-21 | 2012-10-24 | 胜利油田胜利勘察设计研究院有限公司 | Multi-phase flow assembly type sealing coalescence oil removing apparatus |
| CN102826638A (en) * | 2012-02-21 | 2012-12-19 | 胜利油田胜利勘察设计研究院有限公司 | Multiphase flow assembly type closed coagulation settling device |
| CN101880072B (en) * | 2009-05-04 | 2013-11-06 | 上海巴安水务股份有限公司 | Flocculent settling degreaser |
| CN104593046A (en) * | 2014-12-26 | 2015-05-06 | 上海安赐机械设备有限公司 | Crude oil dehydration device and process |
| CN104707363A (en) * | 2013-12-16 | 2015-06-17 | 乔治·克劳德方法的研究开发空气股份有限公司 | Apparatus for mechanical separation of oil and tar from gas condensate |
| CN110040876A (en) * | 2019-05-04 | 2019-07-23 | 陕西宇阳石油科技工程有限公司 | A kind of pressure oil removing settling pot for gas field produced water treatment |
-
2000
- 2000-10-27 CN CN 00260870 patent/CN2477617Y/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101880072B (en) * | 2009-05-04 | 2013-11-06 | 上海巴安水务股份有限公司 | Flocculent settling degreaser |
| CN102397712A (en) * | 2010-09-15 | 2012-04-04 | 张步芳 | Mobile oil-water separation device with floating oil absorber |
| CN102397712B (en) * | 2010-09-15 | 2014-04-23 | 张步芳 | Mobile oil-water separation device with floating oil absorber |
| CN102266680A (en) * | 2011-06-23 | 2011-12-07 | 江苏中源电力设备有限公司 | Oil-water separator |
| CN102266680B (en) * | 2011-06-23 | 2013-08-14 | 江苏中源电力设备有限公司 | Oil-water separator |
| CN102826638A (en) * | 2012-02-21 | 2012-12-19 | 胜利油田胜利勘察设计研究院有限公司 | Multiphase flow assembly type closed coagulation settling device |
| CN102745771A (en) * | 2012-02-21 | 2012-10-24 | 胜利油田胜利勘察设计研究院有限公司 | Multi-phase flow assembly type sealing coalescence oil removing apparatus |
| CN102826638B (en) * | 2012-02-21 | 2014-10-29 | 胜利油田胜利勘察设计研究院有限公司 | Multiphase flow assembly type closed coagulation settling device |
| CN102745771B (en) * | 2012-02-21 | 2015-03-04 | 胜利油田胜利勘察设计研究院有限公司 | Multi-phase flow assembly type sealing coalescence oil removing apparatus |
| CN104707363A (en) * | 2013-12-16 | 2015-06-17 | 乔治·克劳德方法的研究开发空气股份有限公司 | Apparatus for mechanical separation of oil and tar from gas condensate |
| CN104593046A (en) * | 2014-12-26 | 2015-05-06 | 上海安赐机械设备有限公司 | Crude oil dehydration device and process |
| CN104593046B (en) * | 2014-12-26 | 2017-04-05 | 上海安赐环保科技股份有限公司 | A kind of crude oil water trap and technique |
| CN110040876A (en) * | 2019-05-04 | 2019-07-23 | 陕西宇阳石油科技工程有限公司 | A kind of pressure oil removing settling pot for gas field produced water treatment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102745771B (en) | Multi-phase flow assembly type sealing coalescence oil removing apparatus | |
| CN2477617Y (en) | Pressure oil removing settling pot | |
| CN201395548Y (en) | Device for treating suspended sludge of compound alkali-surfactant-polymer oil extraction sewage | |
| CN101391824A (en) | Aggregation sinking and emerging treatment device for oilfield produced waste water | |
| CN110527554A (en) | A kind of oilfield sump oil recycling equipment | |
| CN105000704B (en) | Pipe type oil moisture trap and separation method | |
| CN105540893B (en) | Laterally stream coalescence cavitation air flotation reactor and ternary recovered water laterally flow agglomerated air floatation A/O bioremediations | |
| CN212610043U (en) | High-water-content oilfield hauling and exploiting synergistic device | |
| CN207259251U (en) | A kind of equipment for water-oil separating | |
| CN113023914A (en) | Oil-water separation treatment system and treatment method for oil field chemical flooding oil displacement produced water | |
| CN207016587U (en) | A kind of oil field output water pretreatment sedimenting system | |
| CN201729725U (en) | Oilfield-produced sewage aggregation and floating-sinking processing device | |
| CN2442987Y (en) | Pot for removing oil and sand from sewage | |
| CN113323645A (en) | Separation method and separation device for oil, gas and water at well mouth and application of separation device | |
| CN211546178U (en) | Multistage circulation flotation column and treatment system for oil-field chemical flooding oil-displacement produced water | |
| CN2647850Y (en) | Apparatus for dirty sand containing oil separating washing and dirty oil recovering | |
| CN207227070U (en) | Device for water-oil separating | |
| CN207227068U (en) | Equipment for water-oil separating | |
| CN2442730Y (en) | Oil containing waste water cross flow combined sedimentation separator | |
| CN207227069U (en) | A kind of oily-water seperating equipment | |
| CN208648945U (en) | Compound oil partiting precipitation pool | |
| CN206680323U (en) | Oil-containing sewage treatment system | |
| CN2532066Y (en) | Two-purpose settle pound for sewage treatment | |
| CN207483483U (en) | Integrated high efficiency mud-water separation purifier | |
| CN205999234U (en) | Sludge in sewage effectively can be carried out the sewage disposal system of precipitation and separation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20020220 Termination date: 20091127 |