CN201330215Y - Vehicle mobile integral device - Google Patents
Vehicle mobile integral device Download PDFInfo
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- CN201330215Y CN201330215Y CNU2009201054272U CN200920105427U CN201330215Y CN 201330215 Y CN201330215 Y CN 201330215Y CN U2009201054272 U CNU2009201054272 U CN U2009201054272U CN 200920105427 U CN200920105427 U CN 200920105427U CN 201330215 Y CN201330215 Y CN 201330215Y
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- coagulation
- catalyzed oxidation
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Abstract
The utility model discloses a vehicle mobile integral device, comprising: a coagulation-sedimentation device, an advanced catalytic oxidation device, an MBR reactor and a lifting pump. The coagulation-sedimentation device is connected with the lifting pump and the advanced catalytic oxidation device through a communicating pipe; the advanced catalytic oxidation device is also connected with the MBR reactor through a communicating pipe. The device is suitable for the fracturing outlet liquid with characteristics of little discharge amount, dispersion, high concentration of organic matter, and large chroma and viscosity, does not need outside energy just by storing the vehicle mobile integral device to a storage tank of fracturing liquid; besides other devices are not needed in site, thereby ensuring simple operation, high automation level and low operational cost.
Description
Technical field
The utility model relates to sewage disposal device, relates in particular to the integrated equipment for wastewater treatment that a kind of oil field compression fracture returns discharge opeing.
Background technology
Along with China's sustained and rapid development of economy, the predatoriness of water resources is developed and is used, and seriously restricts and affect the industrial and agricultural development of China's most laboratories, and the pollution of water body is also more and more serious simultaneously.Water pollution problems not only is related to common people's health, quality and the safety of farm crop, also has influence on the development of industrial economy, also can cause the shortage of water resources simultaneously.What allow more the people worries is that water pollutes the important factor that has become the restriction Economic development, has had a strong impact on economic sustainable development.Therefore the improvement and the water saving of water pollution, the protection of water resources and reasonable development have become China governments at all levels problem anxious to be solved.
Fracturing technology is an integral part in the oil-gas field development, and the purpose of pressure break mainly is to improve hydrocarbon zone penetrating power and de-plugging etc., new well formation testing, the old liberated area oil well is taped the latent power and the individual well volume increase in occupy irreplaceable position.Therefore use commonplacely, but the backflow waste liquid that produces in the frac job process is the source of pollution that can not be ignored in oil field.At present, because of there not being effective treatment process, almost each oil field is all taked to dig the pond mound in the side area, oil field and is left concentratedly.
The characteristic of wellfracturing operation backflow waste liquid and pollution level and fracturing liquid system and construction operation technology have substantial connection, therefore, different oil-gas fields, different well depths, the character of the backflow waste liquid that produces in the frac job process is different.
Wellfracturing operation backflow waste liquid is a kind of heterogeneous dispersion system of complexity, and existing clay particle and the landwaste of taking out of from the depths, stratum also contains the pollution substances such as organic and inorganic additives in crude oil and the fracturing liquid, forms very complicated.Organic additive mostly is benzene series derivative and polycyclic aromatic hydrocarbon compounds, is difficult to degraded with biochemical degradation method and ordinary chemical method.Main additive is an anionic polyacrylamide, and main chain is the carbon carbochain, and side chain is the carboxyl after amide group or the hydrolysis, and according to the organic chemistry theory, main chain is the compound stability height of carbon carbochain, and difficult degraded must be carried out strong oxidative degradation.Bring a lot of difficulties to work of treatment.The unstable of fracturing outlet liquid water quality, to constitute fluctuation range very complicated and that every mouthful of well in operation returns lifting rate bigger, and the layout of giving treatment process and member being set is brought bigger difficulty.
In summary, oil field compression fracture returns discharge opeing and has that organic concentration height, complicated component, biodegradability are poor, concentration height, viscosity and colourity is big, wastewater flow rate is little and the dispersive characteristics, the treatment process that adopts both at home and abroad only rests on the materilization freatment method at present, and the water quality after the processing also is higher than the comprehensive first discharge standard of country far away.Along with the fast development of national economy and continuing to increase of national environmental protection law enforcement dynamics, processing to wellfracturing operation backflow waste liquid, be subjected to the attention of national environmental protection department day by day, therefore exploitation is advanced, efficient, stable, the fracturing outlet liquid treatment facility is very important cheaply, also is instant.
Summary of the invention
For solving effective processing of oil field compression fracture being returned discharge opeing, the utility model provides a kind of vehicle-mounted removable integration apparatus.
The utility model is achieved through the following technical solutions:
A kind of vehicle-mounted removable integration apparatus that the utility model is related comprises:
Coagulation-sedimentation equipment, senior catalyzed oxidation equipment, MBR reactor, lift pump, wherein, coagulation-sedimentation equipment was connected with lift pump and senior catalyzed oxidation equipment by communicating pipe, and described senior catalyzed oxidation equipment also is connected with the MBR reactor by communicating pipe.
Vehicle-mounted removable integration apparatus according to claim 1 is characterized in that described coagulation-sedimentation equipment comprises chemicals dosing plant, agitator and soil discharging facility.Described senior catalyzed oxidation equipment also comprises chemicals dosing plant, agitator, soil discharging facility and PH on-line testing equipment.Described MBR reactor is an integral type film biological reactor, and this reactor comprises gas blower and vacuum primingpump.Described equipment also comprises a Controlling System, and this Controlling System is connected respectively with between coagulation-sedimentation equipment, senior catalyzed oxidation equipment, the MBR reactor.
The beneficial effect of the technical scheme that the utility model provides is:
1, this equipment is movably, be fit to very much water displacement little, than the dispersive fracturing outlet liquid.
2, adopted the coagulating sedimentation technology in this equipment, effectively reduced the suspended substance and the viscosity of fracturing outlet liquid, for follow-up core processing technology has been created favourable condition of water quality.
3, adopted senior catalyzed oxidation technology in this equipment, utilize strong oxidizer to destroy the long-chain organic polymer and the organic look group of difficult degradation, effectively reduce the organic concentration and the colourity of fracturing outlet liquid, improved the biodegradability of fracturing outlet liquid, for follow-up biochemical technology provides assurance.
4, adopted the integral type film biological reactor of my company's independent development in this equipment, the hardly degraded organic substance in the waste water of effectively having degraded has guaranteed to reach after fracturing outlet liquid is handled " integrated wastewater discharge standard " (GB8978-1996) middle primary standard.
5, this automation degree of equipment height is simple to operate, need not professional's execute-in-place.
Description of drawings
Fig. 1 is a vehicular integration apparatus cut-away view;
Fig. 2 is a vehicle-mounted removable integration apparatus outside view.
Embodiment
For making the purpose of this utility model, technical scheme and advantage clearer, the utility model embodiment is described in further detail below in conjunction with accompanying drawing:
As shown in Figure 1, showed the vehicular integration apparatus, this equipment comprises: coagulation-sedimentation equipment 11, senior catalyzed oxidation equipment 12, MBR reactor 13, lift pump 14 and Controlling System, wherein, coagulation-sedimentation equipment 11 was connected with lift pump 14 and senior catalyzed oxidation equipment 12 by communicating pipe, and described senior catalyzed oxidation equipment 12 also is connected with MBR reactor 13 by communicating pipe.
Coagulation-sedimentation equipment comprises chemicals dosing plant 15, agitator 16 and soil discharging facility 17, and catalyzed oxidation equipment 12 also comprises chemicals dosing plant 15, agitator 16, soil discharging facility 17 and PH on-line testing equipment 18.MBR reactor 13 is an integral type film biological reactor, and this reactor 13 comprises gas blower 20 and vacuum primingpump 19.Fracturing outlet liquid promotes through lift pump 14 and enters coagulative precipitation tank, under the effect of coagulating agent and coagulant aids, reduces suspended substance, colourity and viscosity in the waste water; The coagulative precipitation tank water outlet is from flowing to senior catalyzed oxidation pond, under the catalyzed oxidation of strong oxidizer, big chain difficult degradation organic polymer in the degrading waste water and organic look group, reduce the biodegradability of organism, colourity and raising waste water in the waste water, for follow-up aerobic process has been created good condition of water quality; The water outlet gravity flow of catalyzed oxidation pond enters the MBR reactor, the MBR reactor adopts the integral type film biological reactor of my company's independent development, further the organism in the degrading waste water is handled water up to standard and is squeezed into discharging pond 21 through vacuum primingpump 19, and the water in the discharging pond 21 enters near water body.
As shown in Figure 2, only there are water inlet pipe 1 and delivery pipe 2 in vehicle-mounted removable integration apparatus outside, only need this device is parked near fracturing liquid storage hole, water inlet pipe is put into the hole, utilize the electromechanical equipment of integration apparatus inside normally to move, fracturing liquid in the hole can be opened after disposing to another pressing filtering liquid that need handle store the place, hole, be fit to very much handle the little and dispersive fracturing outlet liquid of quantity discharged.
The above; it only is the preferable embodiment of the utility model; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; the variation that can expect easily or replacement all should be encompassed within the protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of claim.
Claims (5)
1, vehicle-mounted removable integration apparatus, it is characterized in that, described equipment comprises: coagulation-sedimentation equipment, senior catalyzed oxidation equipment, MBR reactor, lift pump, wherein, coagulation-sedimentation equipment was connected with lift pump and senior catalyzed oxidation equipment by communicating pipe, and described senior catalyzed oxidation equipment also is connected with the MBR reactor by communicating pipe.
2, vehicle-mounted removable integration apparatus according to claim 1 is characterized in that, described coagulation-sedimentation equipment comprises chemicals dosing plant, agitator and soil discharging facility.
3, vehicle-mounted removable integration apparatus according to claim 1 is characterized in that, described senior catalyzed oxidation equipment also comprises chemicals dosing plant, agitator, soil discharging facility and PH on-line testing equipment.
4, vehicle-mounted removable integration apparatus according to claim 1 is characterized in that, described MBR reactor is an integral type film biological reactor, and this reactor comprises gas blower and vacuum primingpump.
5, according to claim 1 year mobile integrated equipment is characterized in that, described equipment also comprises a Controlling System, and this Controlling System is connected respectively with between coagulation-sedimentation equipment, senior catalyzed oxidation equipment, the MBR reactor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009201054272U CN201330215Y (en) | 2009-01-23 | 2009-01-23 | Vehicle mobile integral device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009201054272U CN201330215Y (en) | 2009-01-23 | 2009-01-23 | Vehicle mobile integral device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201330215Y true CN201330215Y (en) | 2009-10-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2009201054272U Expired - Fee Related CN201330215Y (en) | 2009-01-23 | 2009-01-23 | Vehicle mobile integral device |
Country Status (1)
| Country | Link |
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| CN (1) | CN201330215Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103159351A (en) * | 2013-03-29 | 2013-06-19 | 北京矿冶研究总院 | Component adjusting device and method for liquid preparation after fracturing flow-back fluid treatment |
| CN103288308A (en) * | 2013-07-01 | 2013-09-11 | 大唐国际化工技术研究院有限公司 | Slack coal pressure gasification wastewater recycling treatment method and treatment system as well as application |
| CN103288310A (en) * | 2013-07-01 | 2013-09-11 | 大唐国际化工技术研究院有限公司 | Slack coal pressure gasification wastewater treatment method and treatment system as well as application |
| CN103359867A (en) * | 2013-08-06 | 2013-10-23 | 华油惠博普科技股份有限公司 | Method and device for fracturing flowback fluid treatment |
| CN104710082A (en) * | 2015-03-19 | 2015-06-17 | 韩山师范学院 | Movable restaurant waste water treatment system |
| CN106219897A (en) * | 2016-09-10 | 2016-12-14 | 安徽蓝鼎环保能源科技有限公司 | A kind of package plant |
| CN106277626A (en) * | 2016-08-31 | 2017-01-04 | 四川省威尔敦化工有限公司 | Fracturing outlet liquid processes dosing fracturing technique again |
-
2009
- 2009-01-23 CN CNU2009201054272U patent/CN201330215Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103159351A (en) * | 2013-03-29 | 2013-06-19 | 北京矿冶研究总院 | Component adjusting device and method for liquid preparation after fracturing flow-back fluid treatment |
| CN103288308A (en) * | 2013-07-01 | 2013-09-11 | 大唐国际化工技术研究院有限公司 | Slack coal pressure gasification wastewater recycling treatment method and treatment system as well as application |
| CN103288310A (en) * | 2013-07-01 | 2013-09-11 | 大唐国际化工技术研究院有限公司 | Slack coal pressure gasification wastewater treatment method and treatment system as well as application |
| CN103288308B (en) * | 2013-07-01 | 2014-09-03 | 大唐国际化工技术研究院有限公司 | Slack coal pressure gasification wastewater recycling treatment method and treatment system as well as application |
| CN103288310B (en) * | 2013-07-01 | 2015-04-15 | 大唐国际化工技术研究院有限公司 | Slack coal pressure gasification wastewater treatment method and treatment system as well as application |
| CN103359867A (en) * | 2013-08-06 | 2013-10-23 | 华油惠博普科技股份有限公司 | Method and device for fracturing flowback fluid treatment |
| CN104710082A (en) * | 2015-03-19 | 2015-06-17 | 韩山师范学院 | Movable restaurant waste water treatment system |
| CN106277626A (en) * | 2016-08-31 | 2017-01-04 | 四川省威尔敦化工有限公司 | Fracturing outlet liquid processes dosing fracturing technique again |
| CN106219897A (en) * | 2016-09-10 | 2016-12-14 | 安徽蓝鼎环保能源科技有限公司 | A kind of package plant |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHANG YAJUN Free format text: FORMER OWNER: BEIJING JIYATE ENVIRONMENTAL ENGINEERING CO., LTD. Effective date: 20130628 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 101400 HUAIROU, BEIJING TO: 100085 HAIDIAN, BEIJING |
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| TR01 | Transfer of patent right |
Effective date of registration: 20130628 Address after: 100085 Beijing city Haidian District East Road No. 1, block E 401-A a power surplus Patentee after: Zhang Yajun Address before: Seven in 101400 districts in Beijing District of Huairou Yanqi Industrial Development Zone No. 36 Patentee before: Beijing Jiyate Environmental Engineering Co., LTD. |
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| ASS | Succession or assignment of patent right |
Owner name: BEIJING JIYATE ENVIRONMENTAL ENGINEERING CO., LTD. Free format text: FORMER OWNER: ZHANG YAJUN Effective date: 20130924 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 100085 HAIDIAN, BEIJING TO: 101400 HUAIROU, BEIJING |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130924 Address after: Seven in 101400 districts in Beijing District of Huairou Yanqi Industrial Development Zone No. 36 Patentee after: Beijing Jiyate Environmental Engineering Co., LTD. Address before: 100085 Beijing city Haidian District East Road No. 1, block E 401-A a power surplus Patentee before: Zhang Yajun |
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| C56 | Change in the name or address of the patentee |
Owner name: BEIJING G + T ENVIRONMENTAL PROTECTION TECHNOLOGY Free format text: FORMER NAME: BEIJING JIYATE ENVIRONMENTAL ENGINEERING CO., LTD. |
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| CP01 | Change in the name or title of a patent holder |
Address after: Seven in 101400 districts in Beijing District of Huairou Yanqi Industrial Development Zone No. 36 Patentee after: BEIJING G&T ENVIRONMENTAL PROTECTION SCIENCE AND TECHNOLOGY CO., LTD. Address before: Seven in 101400 districts in Beijing District of Huairou Yanqi Industrial Development Zone No. 36 Patentee before: Beijing Jiyate Environmental Engineering Co., LTD. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20091021 Termination date: 20170123 |
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| CF01 | Termination of patent right due to non-payment of annual fee |