CN203095769U - Miniature multifunctional continuous water treatment device - Google Patents
Miniature multifunctional continuous water treatment device Download PDFInfo
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- CN203095769U CN203095769U CN 201220704731 CN201220704731U CN203095769U CN 203095769 U CN203095769 U CN 203095769U CN 201220704731 CN201220704731 CN 201220704731 CN 201220704731 U CN201220704731 U CN 201220704731U CN 203095769 U CN203095769 U CN 203095769U
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Abstract
The utility model discloses a miniature multifunctional continuous water treatment device. The device comprises an agitating tank, at least one pharmaceutical preparation slot, a cyclone reactor, an electrochemical viscosity breaker, a sloping panel oil eliminator, a sewage buffer slot and at least one dual-filter-material filter, wherein the agitating tank and the pharmaceutical preparation slot are both communicated with the cyclone reactor; the top of the cyclone reactor is communicated with the electrochemical viscosity breaker; an oleic phase outlet and an impurity outlet of the electrochemical viscosity breaker are both communicated with a dirt discharge groove, and an aqueous phase outlet is communicated with the sloping panel oil eliminator; the oleic phase outlet and impurity outlet of the sloping panel oil eliminator are both communicated with the dirt discharge groove, and an aqueous phase outlet is communicated with the sewage buffer slot; and the sewage buffer slot is communicated with the dual-filter-material filter, and the dual-filter-material filter is communicated with a post-filtration water tank. The miniature multifunctional continuous water treatment device disclosed by the utility model carries out all-sided correct efficiency evaluation on processes and devices in polymer-containing and oil-containing sewage treatment systems, and provides a scientific reference for the reconstruction of sewage treatment systems and the reconstruction of process flows.
Description
Technical field
The utility model relates to the continuous water treatment device of a kind of miniature multi-function, belongs to the oil-contaminated water of oil field process field.
Background technology
In the oil field mining liquid treating processes, particularly in the oil-containing sewage treatment technique after the oily water separation, because sink drainage oil-containing or contain poly-, as to contain suspended substance complicacy, cause oily(waste)water viscosity to raise, oil-water emulsion is serious, form thermodynamic stable system, oil, water and suspended substance separation difficulty.Because the variation of recovered water character, existing water treatment device and technical process more and more are difficult to adapt to the complicated day by day poly-oily(waste)water characteristic that contains, can not satisfy the processing requirement of existing water treatment.For these reasons, the continuous water treatment device of miniature multi-function is come out, utilize this device that oil-containing polymer-bearing waste-water characteristic, sewage disposal medicament drug effect, relevant treatment unit equipment process structure and operating parameters etc. are carried out continuous dynamic testing and dynamic evaluation, in time find the defective workmanship that Sewage treatment systems exists, for disposing polluted water in oil system process and equipment technology reconstruction provide experimental study means and technical support.
The utility model content
The purpose of this utility model provides the continuous water treatment device of a kind of miniature multi-function, the static state of using continuous water treatment device of the present utility model can become the discontinuous of routine is evaluated as the dynamic evaluation pattern of present continous way, this pattern more can truly reflect the effect of water treatment agent, more can accurately expose the defective that water treating equipment exist, more can in time find the problem of water technology, handle the technical director that science is provided for oil-contaminated water of oil field.
The continuous water treatment device of a kind of miniature multi-function provided by the utility model comprises steel basin, at least 1 medicament Preparation tank, Cyclonic reactor, electrochemistry viscosity reduction machine, swash plate oil eliminator, sewage dashpot and at least 1 double filtering strainer;
Described steel basin and described medicament Preparation tank all are connected with described Cyclonic reactor; The top of described Cyclonic reactor is connected with described electrochemistry viscosity reduction machine; The oil phase outlet and the impurity outlet of described electrochemistry viscosity reduction machine all are connected with dirt discharge groove, and the water outlet is connected with described swash plate oil eliminator; The oil phase outlet and the impurity outlet of described swash plate oil eliminator all are connected with described dirt discharge groove, and the water outlet is connected with described sewage dashpot;
Described sewage dashpot is connected with described double filtering strainer, and described double filtering strainer is connected with filter back tank.
Above-mentioned continuous water treatment device, described device comprises 2 described medicament Preparation tanks, described medicament Preparation tank all is connected with described Cyclonic reactor by dosing pump, the medicament that needs needs ready for use in described medicament Preparation tank in advance, be pumped to then in the described Cyclonic reactor and react with sewage, reaction product flows out from the top of described Cyclonic reactor and enters the described electrochemistry viscosity reduction machine then, in described electrochemistry viscosity reduction machine, carry out viscosity reduction, cohesion, air supporting, electrostatic coalescence, finish oily water separation.
Above-mentioned continuous water treatment device, described steel basin is connected with described Cyclonic reactor by sewage pump.
Above-mentioned continuous water treatment device, described device comprise 2 described double filtering strainers.
Above-mentioned continuous water treatment device, 2 described double filtering strainers are for being connected in parallel or being connected in series.
Above-mentioned continuous water treatment device, the filtrate of described double filtering strainer are selected from quartz sand filter media, ANTHRACITE FILTER MEDIA, shell filtrate (as nut-shell, Exocarpium cocois (Cocos nucifera L)), carbon leaching material, manganese sand filtering material, medical stone filtrate, deoxygenation sponge iron filtering material, magnetite filtrate, zeolite filler, volcanics biofilter material, cobble bed course, garnet filtrate, ceramic grain filter, rare earth porcelain sand filtering material, foam filter pearl filtrate, coke filtrate, baton round and glass fibre.
Above-mentioned continuous water treatment device, also be connected between described filter back tank and the described double filtering strainer by backwash pump, adopt described back flushing to carry out the cleaning of filtrate, filtration in the utility model and backwash step can adopt programme controlled full-automatic operation pattern.
Above-mentioned continuous water treatment device, be equipped with sampling spot between described electrochemistry viscosity reduction machine and the described swash plate oil eliminator, between described swash plate oil eliminator and the described sewage dashpot and between described double filtering strainer and the described filter back tank, the water quality sampling analysis that is used for treating processes is by effect, the optimizing of processing condition and the separation efficiency of unit for treating water equipment of Analysis Results of Water Quality evaluation sewage disposal medicament.
The utlity model has following beneficial effect:
(1) correctly implements the dynamic screening and the dynamic evaluation of oily water treatment medicament, the efficient processing medicament that is fit to sewage characteristic is provided for the scene;
(2) utilize synergies such as electrochemistry viscosity reduction, flocculation-air floating and electrostatic coalescence to solve and contain the oily water separation problem of gathering in the oily(waste)water, for the scene provides the optimised process combined method;
(3) research different load amount instructs the design and the operation of swash plate (pipe) oil eliminator oil to the influence of swash plate (pipe) oil eliminator oily water separation efficient;
(4) research unlike material, different grain size, different gradation than the filtration medium of, different geometries to suspended substance in the sewage (SS) catch with hold back efficient and different filtering velocity under filter effect, instruct the grating mode of filter design and filtrate.
To sum up, the utility model is made correct efficiency rating comprehensively to existing technology and the equipment that contains in the poly-oil-containing sewage treatment system, for the scrap build and the transformation process of Sewage treatment systems provides scientific basis.
Description of drawings
The structural representation of the continuous water treatment device that Fig. 1 provides for the utility model.
Each mark is as follows among the figure: 1 steel basin, 21,22 medicament Preparation tanks, 3 Cyclonic reactors, 4 electrochemistry viscosity reduction machines, 5 swash plate oil eliminators, 6 sewage dashpots, 71,72 double filtering strainers, 8 sewage pumps, 9 dirt discharge grooves, 10 filter lift pump, 101,102,103,104 sampling spots, 11 filter back tanks, 12 backwashing pumps.
Embodiment
Below in conjunction with accompanying drawing the utility model is described further, but the utility model is not limited to following examples.
The continuous water treatment device of the miniature multi-function that the utility model provides comprises steel basin 1, medicament Preparation tank 21 and 22, Cyclonic reactor 3, electrochemistry viscosity reduction machine 4, swash plate oil eliminator 5, sewage dashpot 6 and double filtering strainer 71 and 72; Wherein steel basin 1 is used to deposit the pending poly-oily(waste)water that contains, and can carry out heat tracing to it and stir; This steel basin 1 is connected with Cyclonic reactor 3, and the pipeline of connection is provided with sewage pump 8, is used for the certain density compound pump for preparing is transported to Cyclonic reactor 3 and contained poly-oily(waste)water and react; The top of Cyclonic reactor 3 is connected with electrochemistry viscosity reduction machine 4, and the reaction product of coming out from Cyclonic reactor 3 enters carries out electrolysis viscosity reduction, air supporting flocculation and electrostatic coalescence in the electrochemistry viscosity reduction machine 4, finishes oily water separation for the first time.The oil phase outlet and the impurity outlet of electrochemistry viscosity reduction machine 4 all are connected with dirt discharge groove 9, and the water outlet is connected with swash plate oil eliminator 5, and should connection place be provided with sampling spot 101, is used for the water quality sampling analysis for the treatment of processes; The oil phase outlet and the sludge outlet of swash plate oil eliminator 5 all are connected with dirt discharge groove 9, and the water outlet is connected with sewage dashpot 6, and should connection place be provided with sampling spot 102, is used for the water quality sampling analysis for the treatment of processes; Sewage dashpot 6 is connected with 2 double filtering strainers 71 and 72, and strainer carries out filter operation by lift pump 10, can carry out parallel connection or serial operation as required.Its stopping composition is selected from quartz sand filter media, ANTHRACITE FILTER MEDIA, shell filtrate (as nut-shell, Exocarpium cocois (Cocos nucifera L)), carbon leaching material, manganese sand filtering material, medical stone filtrate, deoxygenation sponge iron filtering material, magnetite filtrate, zeolite filler, volcanics biofilter material, cobble bed course, garnet filtrate, ceramic grain filter, rare earth porcelain sand filtering material, foam filter pearl filtrate, coke filtrate, baton round and glass fibre etc.; 2 double filtering strainers 71 and 72 all are connected with filter back tank 11, are used to receive the water after handling after filtration, double filtering strainer 71 and 72 with filter after the place of connection of tank 11 be provided with sampling spot 103 and 104 respectively, be used for the water quality sampling analysis for the treatment of processes; Filter back tank 11 also is connected with 2 double filtering strainers 71 and 72 by backwashing pump 12, is used for the filling material of double filtering strainer 71 and 72 is carried out the back flushing of filtrate.
The use of above-mentioned continuous water treatment device is as follows: the oil-containing polymer-bearing waste-water is introduced steel basin 1, unlatching is stirred and is heated up, set suitable mixing speed, liquid level and a temperature according to sewage characteristic, after steel basin 1 build-in test parameter reaches set(ting)value, enter automatic control state.After the sewage temperature rise reaches requirement in the steel basin 1, open sewage pump 8 to Cyclonic reactor 3 feed flows, adjust the flow of sewage pump 8, and according to the flow of the flow set dosing pump of sewage pump 8, open dosing pump simultaneously and import certain density medicament, make medicament and sewage in Cyclonic reactor 3, finish reaction.Reacted sewage enters electrochemistry viscosity reduction machine 4 from the top of Cyclonic reactor 3, carries out electrolysis viscosity reduction, air supporting flocculation and electrostatic coalescence in electrochemistry viscosity reduction machine 4, finishes oily water separation for the first time.Float over the greasy dirt on electrochemistry viscosity reduction machine 4 tops, introduce dirt discharge groove 9 by upper pipeline; Be deposited on the mud of electrochemistry viscosity reduction machine 4 bottoms, introduce dirt discharge groove 9 by electrochemistry viscosity reduction machine 4 bottom line; Water after electrochemistry viscosity reduction machine 4 separates is then introduced swash plate oil eliminator 5 by the pipeline on right side, stable after, contain the wet goods water-quality guideline in the valve sampling analysis water by sampling spot 101 places.The sewage that comes out from electrochemistry viscosity reduction machine 4 or bypass line enters swash plate oil eliminator 5, carry out at the swash plate group inner chamber of swash plate oil eliminator 5 coalescent settlement separate, thereby reach the isolating purpose of profit mud; The greasy dirt on swash plate oil eliminator 5 tops, introduce dirt discharge groove 9 by upper pipeline, be deposited on the mud of swash plate oil eliminator 5 bottoms, enter dirt discharge groove 9 by swash plate oil eliminator 5 bottom line, water after swash plate oil eliminator 5 separates is then introduced sewage dashpot 6 by the pipeline on right side, after stable, by oil-containing and suspension content in the valve sampling analysis water at sampling spot 102 places.Water in the sewage dashpot 6 is input into by lift pump 10 and carries out filtering under pressure in double filtering strainer 71 and 72, two strainers can be set to parallel connection or serial operation to filter type as required, can carry out water quality analysis by sampling spot 103 and 104 in this process.
Claims (8)
1. continuous water treatment device of miniature multi-function, it is characterized in that: described device comprises steel basin, at least 1 medicament Preparation tank, Cyclonic reactor, electrochemistry viscosity reduction machine, swash plate oil eliminator, sewage dashpot and at least 1 double filtering strainer;
Described steel basin and described medicament Preparation tank all are connected with described Cyclonic reactor; The top of described Cyclonic reactor is connected with described electrochemistry viscosity reduction machine; The oil phase outlet and the impurity outlet of described electrochemistry viscosity reduction machine all are connected with dirt discharge groove, and the water outlet is connected with described swash plate oil eliminator; The oil phase outlet and the impurity outlet of described swash plate oil eliminator all are connected with described dirt discharge groove, and the water outlet is connected with described sewage dashpot;
Described sewage dashpot is connected with described double filtering strainer, and described double filtering strainer is connected with filter back tank.
2. water treatment device according to claim 1 is characterized in that: described device comprises 2 described medicament Preparation tanks, and described medicament Preparation tank all is connected with described Cyclonic reactor by dosing pump.
3. water treatment device according to claim 1 and 2 is characterized in that: described steel basin is connected with described Cyclonic reactor by sewage pump.
4. water treatment device according to claim 1 and 2 is characterized in that: described device comprises 2 described double filtering strainers.
5. water treatment device according to claim 4 is characterized in that: 2 described double filtering strainers are for being connected in parallel or being connected in series.
6. water treatment device according to claim 1 and 2 is characterized in that: the filtrate of described double filtering strainer is selected from quartz sand filter media, ANTHRACITE FILTER MEDIA, shell filtrate, carbon leaching material, manganese sand filtering material, medical stone filtrate, deoxygenation sponge iron filtering material, magnetite filtrate, zeolite filler, volcanics biofilter material, cobble bed course, garnet filtrate, ceramic grain filter, rare earth porcelain sand filtering material, foam filter pearl filtrate, coke filtrate, baton round and glass fibre.
7. water treatment device according to claim 1 and 2 is characterized in that: also be connected by backwash pump between described filter back tank and the described double filtering strainer.
8. water treatment device according to claim 1 and 2 is characterized in that: be equipped with sampling spot between described electrochemistry viscosity reduction machine and the described swash plate oil eliminator, between described swash plate oil eliminator and the described sewage dashpot and between described double filtering strainer and the described filter back tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220704731 CN203095769U (en) | 2012-12-19 | 2012-12-19 | Miniature multifunctional continuous water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220704731 CN203095769U (en) | 2012-12-19 | 2012-12-19 | Miniature multifunctional continuous water treatment device |
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| CN203095769U true CN203095769U (en) | 2013-07-31 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201220704731 Expired - Lifetime CN203095769U (en) | 2012-12-19 | 2012-12-19 | Miniature multifunctional continuous water treatment device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103588333A (en) * | 2013-10-29 | 2014-02-19 | 中国地质大学（北京） | Oilfield fracturing wastewater treatment equipment |
| CN109794100A (en) * | 2017-11-16 | 2019-05-24 | 柳州市皇盛环保科技有限公司 | A kind of sewage treatment filtrate |
-
2012
- 2012-12-19 CN CN 201220704731 patent/CN203095769U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103588333A (en) * | 2013-10-29 | 2014-02-19 | 中国地质大学（北京） | Oilfield fracturing wastewater treatment equipment |
| CN103588333B (en) * | 2013-10-29 | 2014-12-10 | 中国地质大学（北京） | Oilfield fracturing wastewater treatment equipment |
| CN109794100A (en) * | 2017-11-16 | 2019-05-24 | 柳州市皇盛环保科技有限公司 | A kind of sewage treatment filtrate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 100010 Beijing, Chaoyangmen, North Street, No. 25, No. Co-patentee after: CNOOC RESEARCH INSTITUTE Co.,Ltd. Patentee after: CHINA NATIONAL OFFSHORE OIL Corp. Co-patentee after: Yangtze University Address before: 100010 Beijing, Chaoyangmen, North Street, No. 25, No. Co-patentee before: CNOOC Research Institute Patentee before: CHINA NATIONAL OFFSHORE OIL Corp. Co-patentee before: Yangtze University |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130731 |