CN104817138A - Electric flocculation device with inclined plate electrodes - Google Patents
Electric flocculation device with inclined plate electrodes Download PDFInfo
- Publication number
- CN104817138A CN104817138A CN201510243071.9A CN201510243071A CN104817138A CN 104817138 A CN104817138 A CN 104817138A CN 201510243071 A CN201510243071 A CN 201510243071A CN 104817138 A CN104817138 A CN 104817138A
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- swash plate
- plate electrode
- electric flocculation
- water
- slot
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Abstract
The invention discloses an electric flocculation device with inclined plate electrodes. The electric flocculation device comprises a shell, wherein an air-floatation sediment scraper is arranged outside the top of the shell, a water inlet pipe and a water outlet pipe are arranged at the left side and the right side of the outer part of the shell respectively, a water distribution groove used for changing the water flow direction is formed in one side, which is provided with the water inlet pipe, in the shell, the inclined plate electrodes used for electrolyzing and precipitating impurities are arranged inside the shell, and a perforated sludge discharging pipe is arranged below the inclined plate electrodes inside the shell. According to the electric flocculation device, an inclined plate precipitating process and an electric flocculation air floatation process are combined together in one device, so that the problem that the device occupies a large space as the two processes are implemented by two difference devices in the prior art can be effectively solved.
Description
Technical field
The invention belongs to technical field of water treatment equipment, be specifically related to a kind of electric flocculation apparatus with swash plate electrode.
Background technology
In oil production in earlier stage, in order to improve crude production rate, the water mixed liquid adding the chemical substance such as a certain amount of coagulant aids, guanidine glue is injected into down-hole, the crude oil in extruding subterranean strata, to improve output.Under this working condition, not only containing the general impurity such as large water gaging, silt in the crude oil produced, the complicated chemical compositions such as the guanidine glue be added to the water before being also mingled with injection, isolate crude oil and pressure break water after treatment.Crude oil fracturing water constituent is complicated, leachable etc. in mixture containing number of chemical materials such as crude oil, silt, guanidine glue, coagulant aidss, soil and rock, the water quality requirement of reinjected water just need can be reached through process, i.e. suspended particle < 1 μm, suspension content < 1mg/L, oleaginousness < 1mg/L.
Pressure break water produces and the place of seasoning is followed the change in exploitation place and changes, and therefore requires that corresponding pressure break water treating equipment are also wanted to move along with the former aquatic products dried rhizome of rehmannia.Needs are met the requirements of for meeting conveniently moving, effluent quality and processing power, taking up room and own wt of equipment should be reduced as far as possible, also need to consider the factors such as operation of equipment, maintenance, maintenance space, require higher to technical process, technical process can not be oversize, to reduce equipment occupation space; Also need to consider cost, operation cost, serviceability etc. simultaneously.In current treatment facility, each operation is independently skid form, needs dismounting time mobile, needs to re-assembly after arriving point of destination, and whole moving process labor capacity is large, length consuming time, and can affect the stability of whole plant operation.
Pre-processing device in crude oil fracturing water treatment process is cantboard clarifier and electric flocculation-air floating treatment unit normally, because swash plate clarification in current existing treatment facility and electricity flocculation are two equipment separately, therefore takes up room larger.The process of tradition pressure break water mainly adopts electric flocculation-air floating device, and electric flocculation-air floating technique has following advantage: do not need in electric flocculation process to add any chemical agent, the sludge quantity of generation is few, and the water ratio of mud is low, is easy to process; Simple to operate, only need the impressed voltage changing electric field with regard to the change of energy controlling run condition, be easy to realize Automated condtrol.But the pole plate common level of existing electric flocculation-air floating device or vertically install, pre-treatment then adopts inclined-plate clarifying basin, and the treatment facility of these two kinds of operations takes up room all larger.
Summary of the invention
The object of this invention is to provide a kind of electric flocculation apparatus with swash plate electrode, integrate sloping plate deposition technique and electric flocculation-air floating technique, solve this two kinds of techniques in prior art by two different equipment separately process, the problem that therefore equipment occupation space is larger.
The technical solution adopted in the present invention is: a kind of electric flocculation apparatus with swash plate electrode, comprise housing, the top outer of housing is provided with air supporting slag scraper, the outside left and right sides of housing is separately installed with water inlet pipe and rising pipe, the side being installed into water pipe in housing is provided with the water distribution cloth tank for changing the direction of a stream of water, enclosure interior is provided with the swash plate electrode for electrolysis and precipitated impurities, and the below that enclosure interior is positioned at swash plate electrode is provided with perforated sludge discharge pipe.
Feature of the present invention is also:
Swash plate electrode is that two or more are arranged on the battery lead plate before and after enclosure interior on two side, is parallel to each other and is the angle of 55 °-60 ° with horizontal direction between battery lead plate.
Swash plate electrode is fixed by the electrode permanent seat a be arranged on before and after enclosure interior on two side and electrode permanent seat b, is connected on the two side, front and back of enclosure interior on the two side, front and back that electrode permanent seat a and electrode permanent seat b is welded on enclosure interior respectively or by bolt.
Electrode permanent seat a is arranged with two or more slot a in parallel, slot a and horizontal direction are the angle of 55 °-60 °, on electrode permanent seat b, the position corresponding with slot a is provided with slot b, the vergence direction of slot b and angle of inclination and slot a match, and are fastened by bolts in the slot b that swash plate electrode is inserted into slot a and correspondence.
Swash plate electrode is the one in iron plate, stainless steel plate, graphite cake or aluminium sheet.
Swash plate electrode adopts high frequency pulse power supply to power.
Water inlet pipe is serpentine tube.
Water distribution cloth tank is the groove that steel plate surrounds, and this steel plate is vertically welded in the mouth of pipe opposite side place that housing inner top surface is positioned at water inlet pipe.
The top that enclosure interior is positioned at swash plate electrode is provided with water leg near case top place, perforated sludge discharge pipe is arranged perpendicular to the front-rear side walls of housing, the below of perforated sludge discharge pipe is provided with the V-type groove for collecting precipitation thing, and the top of rising pipe is provided with oil slick accumulator tank.
Oil slick accumulator tank is metal sheet welding groove.
The invention has the beneficial effects as follows: a kind of electric flocculation apparatus with swash plate electrode of the present invention, in a table apparatus, sloping plate deposition technique and electric flocculation-air floating technique are combined as a whole, efficiently solve this two kinds of techniques in prior art by two different equipment separately process, the problem that therefore equipment occupation space is larger.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation with the electric flocculation apparatus of swash plate electrode of the present invention;
Fig. 2 is a kind of part left view with the electric flocculation apparatus of swash plate electrode of the present invention;
Fig. 3 is a kind of top partial view diagram with the electric flocculation apparatus of swash plate electrode of the present invention;
Fig. 4 is that the A-A of Fig. 2 is to sectional view;
Fig. 5 is that the B-B of Fig. 2 is to sectional view.
In figure, 1. water inlet pipe, 2. swash plate electrode, 3. electrode permanent seat a, 4. water distribution cloth tank, 5. air supporting slag scraper, 6. oil slick accumulator tank, 7. perforated sludge discharge pipe, 8. rising pipe, 9. water leg, 10.V type groove, 11. electrode permanent seat b, 12. slot a, 13. slot b.
Embodiment
Below in conjunction with accompanying drawing and embodiment, the present invention is described in further detail:
A kind of electric flocculation apparatus with swash plate electrode of the present invention, as shown in Figure 1, comprise housing, the top outer of housing is provided with air supporting slag scraper 5, the outside left and right sides of housing is separately installed with water inlet pipe 1 and rising pipe 8, water inlet pipe 1 is serpentine tube, the top of rising pipe 8 is provided with oil slick accumulator tank 6, oil slick accumulator tank 6 is metal sheet welding grooves, air supporting slag scraper 5 scrapes oil slick in this groove, the bottom opening of oil slick accumulator tank 6, tapping welds a pipeline, and oil slick is flow in collection container by pipeline.The side being installed into water pipe 1 in housing is provided with water distribution cloth tank 4.Enclosure interior is provided with swash plate electrode 2, and swash plate electrode 2 is arranged on the battery lead plate before and after described enclosure interior on two side for two or more, is parallel to each other and is the angle of 55 °-60 ° with horizontal direction between battery lead plate.Swash plate electrode 2 is fixed by electrode permanent seat a3 and electrode permanent seat b11, swash plate electrode 2 is 55 °-60 ° with the angle of horizontal direction, swash plate electrode 2 selects iron plate, stainless steel plate, graphite cake or aluminium sheet according to raw water quality, and swash plate electrode 2 adopts high frequency pulse power supply to power.Swash plate electrode 2 and electrode permanent seat a3, the concrete mounting means of electrode permanent seat b11 is: as Fig. 2, shown in Fig. 3, electrode permanent seat a3 and electrode permanent seat b11 welds respectively or is connected to before in housing with bolt, on rear two side, as shown in Figure 4, electrode permanent seat a3 is arranged with several slots a12 in parallel, slot a12 and horizontal direction are the angle of 55 °-60 °, as shown in Figure 5, on electrode permanent seat b11, the position corresponding with slot a12 is provided with slot b13 simultaneously, the vergence direction of slot b13 and angle of inclination and slot a12 match, be fastened by bolts in the slot b13 that each swash plate electrode 2 is inserted into slot a12 and correspondence.Swash plate electrode 2 is the one in iron plate, stainless steel plate, graphite cake or aluminium sheet, and every block swash plate electrode 2 has terminal stud, and compartment of terrain is connected with power positive cathode, that is the polarity of two often adjacent swash plate electrodes 2 is contrary.
Get back to Fig. 1, the top that enclosure interior is positioned at swash plate electrode 2 is provided with water leg 9 near case top place, the below that enclosure interior is positioned at swash plate electrode 2 is provided with perforated sludge discharge pipe 7, and perforated sludge discharge pipe 7 is arranged perpendicular to the front-rear side walls of housing, and the below of perforated sludge discharge pipe 7 is provided with V-type groove 10.Enclosure interior is divided into settling region and clear water zone, and the space of swash plate electrode 2 bottom is settling region, and the space on swash plate electrode 2 top is clear water zone.
Working process of the present invention is specific as follows: according to raw water quality condition and processing requirement, before Yuan Shui enters treatment facility, the medicaments such as filling coagulant aids, flocculation agent, emulsion splitter, make former water reach the inflow requirement for the treatment of facility, inject device of the present invention through water pump.
Former water passes through water circulating pump, through water inlet pipe 1, after entering water distribution cloth tank 4, during water outlet, current become the space that horizontal direction enters swash plate electrode 2 bottom, water distribution cloth tank 4 is grooves that the steel plate being vertically welded in housing inner top surface on the mouth of pipe opposite of water inlet pipe 1 surrounds, and the water (flow) direction that level can be made to enter this electric flocculation apparatus changes 90 degree, becomes downward direction, and then flowing to swash plate electrode 2 from housing bottom, break-in like this can effectively reduce impact when current directly enter.Current can be reduced to the sedimentary impact in settling region, the homogenizing of the medicament that simultaneously contributes to annotating in water through water distribution cloth tank 4 twice break-in.After settling region water is full, current can pass swash plate electrode 2, and after swash plate electrode 2 process, throw out is deposited to after settling region collects V-type groove 10, is discharged in mud recovery system through perforated sludge discharge pipe 7 by residual sea water pump; Suspended substance floats to surface, clear water zone, is recovered in oil slick accumulator tank 6 through air supporting slag scraper 5.The clear water zone that swash plate electricity level 2 top has about 600mm high, clear water flow to subsequent processing device after water leg 9.
Former water after swash plate electrode 2, electrolysis produce Ca
2+, Mg
2+plasma and OH
-, CO
3 2-in conjunction with generation throw out, throw out and silt etc. sink to settling region.The electrolysis of swash plate electricity level 2 produces small H
2deng micro-bubble, the suspended substance that promoting flocculates produces and oil stain etc. float to the clear water zone water surface, collect in oil slick accumulator tank 6 through air supporting slag scraper 5.Swash plate electrode 2 combines the advantage of electricity flocculation and sloping plate deposition two kinds of techniques, the Fe that the electrolysis of electricity flocculation cathode plate produces
2+the OH of electrolysis in iron ion final sum water
-ionic bond becomes to be insoluble in the Fe (OH) of water
3, increase precipitate density in water, can strengthen the sedimentation effect of swash plate electrode 2, the microbubble that electrolysis produces contributes to the flocculate suspended substance of generation and the ascent rate of greasy dirt, improves processing efficiency.
The present invention in conjunction with two kinds of equipment, substantially reduces treatment facility and takes up room simultaneously, transportation cost when saving equipment manufacturing cost and move.The micro-bubble that electrolytic process produces and the throw out that metal ion is formed can improve sloping plate deposition efficiency simultaneously.The pole plate group of battery lead plate will ensure when connecing electricity that negative electrode is in upside, is convenient to catholyte like this and produces H
2upwards overflow Deng micro-bubble, the Fe of anode electrolysis generation simultaneously
2+settling tank is flowed to along positive plate etc. flocculate precipitate.For ease of replacing and the maintenance of pole plate, pole plate group is made modular form, select unlike material, size, thickness and spacing according to raw water quality, pole plate group is made modular form, easy access and replacing.
Claims (10)
1. one kind has the electric flocculation apparatus of swash plate electrode, it is characterized in that, comprise housing, the top outer of housing is provided with air supporting slag scraper (5), the outside left and right sides of housing is separately installed with water inlet pipe (1) and rising pipe (8), the side being installed into water pipe (1) in housing is provided with the water distribution cloth tank (4) for changing the direction of a stream of water, enclosure interior is provided with the swash plate electrode (2) for electrolysis and precipitated impurities, and the below that enclosure interior is positioned at swash plate electrode (2) is provided with perforated sludge discharge pipe (7).
2. a kind of electric flocculation apparatus with swash plate electrode according to claim 1, it is characterized in that, described swash plate electrode (2) is arranged on the battery lead plate before and after described enclosure interior on two side for two or more, is parallel to each other and is the angle of 55 °-60 ° with horizontal direction between described battery lead plate.
3. a kind of electric flocculation apparatus with swash plate electrode according to claim 1, it is characterized in that, described swash plate electrode (2) is fixed by the electrode permanent seat a (3) be arranged on before and after enclosure interior on two side and electrode permanent seat b (11), is connected on the two side, front and back of enclosure interior on the two side, front and back that described electrode permanent seat a (3) and electrode permanent seat b (11) are welded on enclosure interior respectively or by bolt.
4. a kind of electric flocculation apparatus with swash plate electrode according to claim 3, it is characterized in that, described electrode permanent seat a (3) is arranged with two or more slot a (12) in parallel, slot a (12) and horizontal direction are the angle of 55 °-60 °, the upper position corresponding with slot a (12) of electrode permanent seat b (11) is provided with slot b (13), the vergence direction of slot b (13) and angle of inclination and slot a (12) match, be fastened by bolts in the slot b (13) that described swash plate electrode (2) is inserted into slot a (12) and correspondence.
5. a kind of electric flocculation apparatus with swash plate electrode according to claim 1, is characterized in that, described swash plate electrode (2) is iron plate, one in stainless steel plate, graphite cake or aluminium sheet.
6. a kind of electric flocculation apparatus with swash plate electrode according to claim 1, is characterized in that, described swash plate electrode (2) adopts high frequency pulse power supply to power.
7. a kind of electric flocculation apparatus with swash plate electrode according to claim 1, it is characterized in that, described water inlet pipe (1) is serpentine tube.
8. a kind of electric flocculation apparatus with swash plate electrode according to claim 1, it is characterized in that, the groove that described water distribution cloth tank (4) surrounds for steel plate, described steel plate is vertically welded in the mouth of pipe opposite side place that housing inner top surface is positioned at water inlet pipe (1).
9. a kind of electric flocculation apparatus with swash plate electrode according to claim 1, it is characterized in that, the top that described enclosure interior is positioned at swash plate electrode (2) is provided with water leg (9) near case top place, described perforated sludge discharge pipe (7) is arranged perpendicular to the front-rear side walls of housing, the below of described perforated sludge discharge pipe (7) is provided with the V-type groove (10) for collecting precipitation thing, and the top of described rising pipe (8) is provided with oil slick accumulator tank (6).
10. a kind of electric flocculation apparatus with swash plate electrode according to claim 9, is characterized in that, described oil slick accumulator tank (6) is metal sheet welding groove.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510243071.9A CN104817138A (en) | 2015-05-13 | 2015-05-13 | Electric flocculation device with inclined plate electrodes |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510243071.9A CN104817138A (en) | 2015-05-13 | 2015-05-13 | Electric flocculation device with inclined plate electrodes |
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| Publication Number | Publication Date |
|---|---|
| CN104817138A true CN104817138A (en) | 2015-08-05 |
Family
ID=53727650
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510243071.9A Pending CN104817138A (en) | 2015-05-13 | 2015-05-13 | Electric flocculation device with inclined plate electrodes |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105967285A (en) * | 2016-05-27 | 2016-09-28 | 扬州大学 | Treatment method of high-concentration benzoate industrial wastewater |
| CN105967428A (en) * | 2016-06-17 | 2016-09-28 | 中海油天津化工研究设计院有限公司 | Electromagnetic coupling inclined plate electric flocculation reactor |
| CN108911047A (en) * | 2018-07-19 | 2018-11-30 | 方达 | A kind of processing unit and method of organic high strength wastewater |
| CN109553241A (en) * | 2017-09-27 | 2019-04-02 | 中国石油化工股份有限公司 | A kind of oil-contained waste water treatment device and method |
| CN113044935A (en) * | 2021-05-17 | 2021-06-29 | 北京华舜伟业环保科技有限公司 | Electric flocculation purifier |
| CN113173628A (en) * | 2020-02-12 | 2021-07-27 | 大唐环境产业集团股份有限公司 | Desulfurization wastewater clarification system and desulfurization wastewater treatment method |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105967285A (en) * | 2016-05-27 | 2016-09-28 | 扬州大学 | Treatment method of high-concentration benzoate industrial wastewater |
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| CN109553241A (en) * | 2017-09-27 | 2019-04-02 | 中国石油化工股份有限公司 | A kind of oil-contained waste water treatment device and method |
| CN109553241B (en) * | 2017-09-27 | 2021-10-29 | 中国石油化工股份有限公司 | Oily sewage treatment device and method |
| CN108911047A (en) * | 2018-07-19 | 2018-11-30 | 方达 | A kind of processing unit and method of organic high strength wastewater |
| CN113173628A (en) * | 2020-02-12 | 2021-07-27 | 大唐环境产业集团股份有限公司 | Desulfurization wastewater clarification system and desulfurization wastewater treatment method |
| CN113044935A (en) * | 2021-05-17 | 2021-06-29 | 北京华舜伟业环保科技有限公司 | Electric flocculation purifier |
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Application publication date: 20150805 |
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