CN102826638A - Multiphase flow assembly type closed coagulation settling device - Google Patents
Multiphase flow assembly type closed coagulation settling device Download PDFInfo
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- CN102826638A CN102826638A CN2012100497960A CN201210049796A CN102826638A CN 102826638 A CN102826638 A CN 102826638A CN 2012100497960 A CN2012100497960 A CN 2012100497960A CN 201210049796 A CN201210049796 A CN 201210049796A CN 102826638 A CN102826638 A CN 102826638A
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Abstract
A multiphase flow assembly type closed coagulation settling device comprises a tank, a water inlet segment A, a flocculation mixed reaction segment B, a coalescence separation segment C, a coalescence separation segment C, a steady flow segment E and a water outlet segment F, wherein the tank is designed in a closed manner, and the water inlet segment A, the flocculation mixed reaction segment B, the coalescence separation segment C, the coalescence separation segment D, the steady flow segment E and the water outlet segment F are arranged in a left-to-right order; the water segment is communicated with the flocculation mixed reaction segment through a water inlet chamber, and grid flocculation is added in a flocculation cylinder, so medicine mixing and reacting effects are improved through utilizing the grid flocculation reaction; and sewage treated by the flocculation mixed reaction segment sequentially goes through the above two coalescence separation segments, oil comes up, mud sinks, and the treated sewage goes through the steady flow segment, enters the water outlet segment and is discharged by a water outlet tube. The device has the advantages of no oxygen exposure points because of tight pressure in the whole course, good separation effect because of the high treatment efficiency, corrosion resistant filler, stable separation effect, adjustable inclined plate interval, convenient dismounting and recondition because of the assembly type structure, occupied land saving because of the high integrated level, convenient operation because of the high automation degree, and convenient construction and short period because of the prefabricated whole skid.
Description
Technical field
The present invention relates to the conventional coagulant precipitation jar water outlet of oilfield sewage station expose to the sun oxygen, receive problem such as oil is difficult, sludge discharge effects is poor, the big occupation of land of tank body is many, polymer-contained sewage efficient difference and the airtight coagulant precipitation device of a kind of polyphasic flow assembled researched and developed; Purpose is further to improve the processing efficiency of conventional sewage and low polymer-bearing waste-water; Improve treatment effect, reduce the operational management difficulty.
Background technology
The sewage works coagulant precipitation device in present domestic oil field mostly adopts vertical coagulant precipitation jar; But this kind device tank body is big, occupation of land is many, device separates polymer-bearing waste-water efficient is low; Hydraulic detention time is longer, and along with the carrying out of production run, conventional coagulant precipitation jar demonstrate water outlet expose to the sun oxygen, receive problems such as oil difficulty, sludge discharge effects difference; Influence sewage treating efficiency to a certain extent, increased the difficulty of sewage plant operational management.
Summary of the invention
The purpose of this invention is to provide the airtight coagulant precipitation device of a kind of polyphasic flow assembled, this device utilizes little grid reaction, improves medicament and mixes and reaction effect; Utilize shallow pool principle, improve processing efficiency, reduce the device volume; The multistage setting of filler segmentation increases separated space, promotes separating effect; Select high gradient lateral flow 316L Stainless Steel Helices, anti-aging, smooth surface, separating effect is stable, and the swash plate spacing can be according to coming water variation water quality situation to adjust, and the whole prefabricated structure of swash plate group is convenient to field-strip; Employing is dashed automatically, the sludge drainage system design, improves sludge discharge effects, the assurance effluent quality; Tank body top receiving port adopts the design of polyphasic flow open type, can realize synchronous exhaust when receiving oil, improves comprehensive treatment capability.
Technical scheme of the present invention realizes in the following manner: the present invention includes tank body, intelligent control cabinet, inlet segment A, flocculation hybrid reaction section B, coarse separation section C, D, steady flow segment E and water exit end F and form; It is characterized in that the airtight design of tank body, be made as inlet segment, flocculation hybrid reaction section, coarse separation section, steady flow segment and water exit end by preface from left to right from tank body; Inlet segment is connected with flocculation hybrid reaction section through intake antrum, is provided with the flocculation tube in the flocculation hybrid reaction section, is provided with grid in the tube that flocculates, and utilizes the grid flocculation reaction, improves the effect that medicament mixes and reacts, and guarantees whole flocculating effect; Through be provided with two section coarse separation sections of side direction ripple swash plate group, by receiving port discharged successively by the oil come-up of coalescence for sewage side direction after flocculation hybrid reaction section is handled, and sewage gets into steady flow segment, and mud sinks, and is discharged by mud discharging mouth, improves separating effect; Sewage after the processing gets into water exit end through the overflow plate of steady flow segment, and the sewage that gets into water exit end is discharged by rising pipe;
Sewage gets into intake antrum by water inlet pipe, gets into flocculation hybrid reaction section through inlet segment through eddy current flocculator water-in behind the water distribution uniformity.Flocculation hybrid reaction section is made up of the eddy current flocculation reactor through optimization design, sets up grid flocculation in the flocculation reactor, utilizes little grid reaction, improves medicament and mixes and reaction effect.The coarse separation section is made up of two sections high gradient lateral flow 316L Stainless Steel Helices; The swash plate angle of inclination is increased to 60 °; Be convenient to the oil droplet come-up, mud glides, and supports between swash plate and also adopts corrosion-resistant material 316L stainless steel; Coarse separation section tank body top is provided with receiving port, and the bottom is provided with rinse mouth, mud flushing tube and mud discharging mouth.Steady flow segment comprises overflow plate and water storage cavity, the current diffusion, and not short stream, steady flow segment tank body top is provided with receiving port, and the bottom is provided with rinse mouth, mud flushing tube and mud discharging mouth.Water exit end is made up of water chamber, header, rising pipe.
Advantage compared with prior art of the present invention is:
1, install omnidistance pressure-tight, do not have the oxygen point of exposing to the sun: the omnidistance pressure-tight of apparatus of the present invention, convenient oil and the spoil disposal received, thus do not slow down the sewage disposal device corrosion owing to there is the oxygen point of exposing to the sun, it is high to reclaim former oil quality.
2, processing efficiency is high, and good separating effect: the present invention utilizes little grid reaction, improves medicament and mixes and reaction effect; Utilize shallow pool principle, improve processing efficiency; Integrate coagulating, settlement separate, receiving port adopts the design of polyphasic flow open type, can realize synchronous exhaust when receiving oil, improves comprehensive treatment capability, reduces the device volume; The multistage setting of filler segmentation increases separated space, promotes separating effect.
3, corrosion-resistant, separating effect is stable: the present invention selects high gradient lateral flow 316L Stainless Steel Helices, corrosion-resistant, anti-aging, smooth surface, and separating effect is stable; Changing the inclined tube sedimentation is lateral flow ripple swash plate, makes the water side direction, the oil come-up, and mud sinks; Two sections layouts can in time be got rid of big oil droplet, and separating effect is stable, and according to coming the water variation of water; The swash plate spacing is adjustable, and the whole prefabricated structure of swash plate group is convenient to field-strip.
4, floor space is little: integrated level height of the present invention, compact construction, occupation of land economize.
5, level of automation is high, and is easy to operate: level of automation of the present invention is high, carries the PLC system, receives oil, can realize robotization towards mud, spoil disposal, reduces the operation element amount, and spoil disposal is even.
6, construction is convenient, the cycle short: the whole sledge of the present invention is adorned prefabricated, convenient, the cycle weak point of constructing, and convenient operation and management, safe and reliable, with high content of technology.
Description of drawings
Accompanying drawing 1 is the airtight coagulant precipitation device of a polyphasic flow assembled two dimensional structure synoptic diagram.
A is an inlet segment among the figure, and B is flocculation hybrid reaction section, and C is one section of a coarse separation, and D is two sections of coarse separation, and E is a steady flow segment, and F is a water exit end.
1-water inlet pipe 2-intake antrum 3-eddy current flocculator water-in 4-eddy current flocculation reactor 5-receiving port 6-eddy current flocculator water outlet 7-ripple swash plate group 8-overflow plate 9-rising pipe 10-manhole 11-header 12-mud discharging mouth 13-rinse mouth 14-mud flushing tube 15-saddle
Embodiment:
As shown in Figure 1, the present invention includes tank body, inlet segment A, flocculation hybrid reaction section B, coarse separation section C, D, steady flow segment E and water exit end F, water inlet pipe 1, intake antrum 2, eddy current flocculator water-in 3, eddy current flocculation reactor 4, receiving port 5, eddy current flocculator water outlet 6, ripple swash plate group 7, overflow plate 8, rising pipe 9, manhole 10, header 11, mud discharging mouth 12, rinse mouth 13, mud flushing tube 14, saddle 15.Sewage gets into intake antrum 2 by water inlet pipe 1; Pass through inlet segment A gets into flocculation hybrid reaction section B through eddy current flocculator water-in 3 eddy current flocculation reactor 4 behind the water distribution uniformity; Flocculation tube leading portion size can guarantee the outer venturi effect of tube through optimization design, sets up grid flocculation in the flocculation tube; Utilize little grid reaction, can improve the effect that medicament mixes and reacts.Flowed out by eddy current flocculator water outlet 6 through the sewage after the abundant flocculation reaction, at first get into coarse separation section C, lateral flow is through the adjustable 316L stainless steel ripple swash plate group filler 7 of spacing; Utilize shallow pool principle, in time get rid of big oil droplet, improve the coalescence effect; Get into coarse separation section D afterwards; Further realize oily water separation and sludge settling through ripple swash plate filler 7, the oil come-up, mud sinks.Device carries the PLC housing, can realize receiving automatically oil, automatic mud removing, and receiving port 5 reclaims the come-up sump oil through tank body top, and receiving port adopts the design of polyphasic flow open type, can realize synchronous exhaust when receiving oil; Sinking mud is discharged through tank base mud discharging mouth 12 after being compiled by the flushing of the current of the rinse mouth 13 of flowing through, mud flushing tube 14.Effluent stream behind oil removing, the mud gets into steady flow segment water storage cavity E through overflow plate 8 overflows, is discharged by rising pipe 9 through header 11.
Claims (4)
1. airtight coagulant precipitation device of polyphasic flow assembled; Comprise that tank body, intelligent control cabinet, inlet segment A, flocculation hybrid reaction section B, coarse separation section C, D, steady flow segment E and water exit end F form; It is characterized in that the airtight design of tank body, be made as inlet segment, flocculation hybrid reaction section, coarse separation section, steady flow segment and water exit end by preface from left to right from tank body; Inlet segment is connected with flocculation hybrid reaction section through intake antrum, is provided with the flocculation tube in the flocculation hybrid reaction section, is provided with grid flocculation in the tube that flocculates, and utilizes the grid flocculation reaction, improves the effect that medicament mixes and reacts, and guarantees whole flocculating effect; Through be provided with two section coarse separation sections of side direction ripple swash plate group, by receiving port discharged successively by the oil come-up of coalescence for sewage side direction after flocculation hybrid reaction section is handled, and sewage gets into steady flow segment, and mud sinks, and is discharged by mud discharging mouth, improves separating effect; Sewage after the processing gets into water exit end through the overflow plate of steady flow segment, and the sewage that gets into water exit end is discharged by rising pipe, and draining, receipts oil and spoil disposal are realized draining, receipts oil and spoil disposal automatic management through the control of the PLC programmable control system in the intelligent control cabinet.
2. the airtight coagulant precipitation device of a kind of polyphasic flow assembled according to claim 1 is characterized in that ripple swash plate group is made up of the 316L Stainless Steel Helices, and the swash plate angle of inclination is 60 °; The swash plate spacing can be according to coming water variation water quality situation to adjust; Support between swash plate and also adopt corrosion-resistant material 316L stainless steel, the whole prefabricated structure of swash plate group is convenient to field-strip; Coarse separation section tank body top is provided with receiving port, and the bottom is provided with rinse mouth, mud flushing tube and mud discharging mouth.
3. the airtight coagulant precipitation device of a kind of polyphasic flow assembled according to claim 1; It is characterized in that steady flow segment comprises overflow plate and water storage cavity, current diffusion, not short stream; Steady flow segment tank body top is provided with receiving port, and the bottom is provided with rinse mouth, mud flushing tube and mud discharging mouth.
4. the airtight coagulant precipitation device of a kind of polyphasic flow assembled according to claim 1 is characterized in that water exit end is made up of water chamber, header, rising pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210049796.0A CN102826638B (en) | 2012-02-21 | 2012-02-21 | Multiphase flow assembly type closed coagulation settling device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210049796.0A CN102826638B (en) | 2012-02-21 | 2012-02-21 | Multiphase flow assembly type closed coagulation settling device |
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| Publication Number | Publication Date |
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| CN102826638A true CN102826638A (en) | 2012-12-19 |
| CN102826638B CN102826638B (en) | 2014-10-29 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201210049796.0A Active CN102826638B (en) | 2012-02-21 | 2012-02-21 | Multiphase flow assembly type closed coagulation settling device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336221A (en) * | 2018-12-04 | 2019-02-15 | 宁夏北控睿源再生资源有限公司 | A kind of high efficiency oil-water neutral section |
| 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 |
| CN110894085A (en) * | 2019-11-25 | 2020-03-20 | 中海油能源发展股份有限公司 | Inclined plate oil remover for oily sewage |
| CN111620499A (en) * | 2020-05-06 | 2020-09-04 | 江苏超惠环保科技有限公司 | Integrated treatment equipment for waste gas and waste water |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2442988Y (en) * | 2000-08-30 | 2001-08-15 | 胜利石油管理局孤东采油厂 | Coagulating setting tank for treating sewage |
| CN2442987Y (en) * | 2000-08-30 | 2001-08-15 | 胜利石油管理局孤东采油厂 | Pot for removing oil and sand from sewage |
| CN2477617Y (en) * | 2000-10-27 | 2002-02-20 | 胜利石油管理局勘察设计研究院 | Pressure oil removing settling pot |
| CN202671276U (en) * | 2012-02-21 | 2013-01-16 | 胜利油田胜利勘察设计研究院有限公司 | Multiphase flow assembled type sealing coagulating sedimentation device |
-
2012
- 2012-02-21 CN CN201210049796.0A patent/CN102826638B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2442988Y (en) * | 2000-08-30 | 2001-08-15 | 胜利石油管理局孤东采油厂 | Coagulating setting tank for treating sewage |
| CN2442987Y (en) * | 2000-08-30 | 2001-08-15 | 胜利石油管理局孤东采油厂 | Pot for removing oil and sand from sewage |
| CN2477617Y (en) * | 2000-10-27 | 2002-02-20 | 胜利石油管理局勘察设计研究院 | Pressure oil removing settling pot |
| CN202671276U (en) * | 2012-02-21 | 2013-01-16 | 胜利油田胜利勘察设计研究院有限公司 | Multiphase flow assembled type sealing coagulating sedimentation device |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336221A (en) * | 2018-12-04 | 2019-02-15 | 宁夏北控睿源再生资源有限公司 | A kind of high efficiency oil-water neutral section |
| 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 |
| CN110894085A (en) * | 2019-11-25 | 2020-03-20 | 中海油能源发展股份有限公司 | Inclined plate oil remover for oily sewage |
| CN111620499A (en) * | 2020-05-06 | 2020-09-04 | 江苏超惠环保科技有限公司 | Integrated treatment equipment for waste gas and waste water |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102826638B (en) | 2014-10-29 |
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| C14 | Grant of patent or utility model | ||
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Addressee: SINOPEC OILFIELD SERVICE CORPORATION Document name: Notification that Application Deemed not to be Proposed |
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| TR01 | Transfer of patent right |
Effective date of registration: 20190522 Address after: 257026 No. 49 Jinan Road, Dongying District, Dongying City, Shandong Province Patentee after: SINOPEC PETROLEUM ENGINEERING DESIGN CO., LTD. Address before: 257000 No. 49 Jinan Road, Dongying City, Shandong Province Co-patentee before: Shandong Sairui Petroleum Science & Technology Development Co., Ltd. Patentee before: Shengli Oilfield Shengli Engineering & Consulting Co., Ltd. |
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| TR01 | Transfer of patent right |