CN206395887U - A kind of Novel iron-carbon micro-electrolysis reactor - Google Patents
A kind of Novel iron-carbon micro-electrolysis reactor Download PDFInfo
- Publication number
- CN206395887U CN206395887U CN201720046533.2U CN201720046533U CN206395887U CN 206395887 U CN206395887 U CN 206395887U CN 201720046533 U CN201720046533 U CN 201720046533U CN 206395887 U CN206395887 U CN 206395887U
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- CN
- China
- Prior art keywords
- guide shell
- reactor
- iron
- shell
- filler
- 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.)
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- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 23
- 239000000945 filler Substances 0.000 claims abstract description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000005276 aerator Methods 0.000 claims abstract description 9
- 238000011049 filling Methods 0.000 claims abstract description 5
- 229910000831 Steel Inorganic materials 0.000 claims description 4
- 238000011068 loading method Methods 0.000 claims description 4
- 239000010959 steel Substances 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 abstract description 20
- 238000006243 chemical reaction Methods 0.000 abstract description 9
- 239000010842 industrial wastewater Substances 0.000 abstract description 2
- -1 reaction is complete Substances 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 238000005273 aeration Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 238000004148 unit process Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000002161 passivation Methods 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
A kind of Novel iron-carbon micro-electrolysis reactor, including reactor shell, water intake and wastewater effluent mouthful are set in reactor shell, it is provided with reactor enclosure body in the multiple reative cells being sequentially connected in series, each reative cell and is provided with guide shell, filling iron carbon filler in guide shell, guide shell bottom is provided with jet aerator, the guide shell left and right sides, which is respectively arranged with the top of deflection plate and overflow weir, guide shell, to be provided with every empty baffling cover plate, and baffling cover plate is fixed in reactor shell.During using iron-carbon micro-electrolysis reactor for treatment industrial wastewater of the present utility model, waste water can be promoted to be contacted repeatedly with iron carbon filler, reaction is complete, and filler be difficult it is hardened.
Description
Technical field
The utility model belongs to environmental project technical field of waste water processing, specifically a kind of iron-carbon micro-electrolysis reactor
Improvement.
Background technology
Iron-carbon micro-electrolysis technology is acted on according to metal erosion, and iron carbon filler is immersed in electrolyte solution into (waste water),
Countless micro- galvanic cells are formed, by electric field action, by some in waste water are inorganic, organic impurities passes through galvanic interaction, oxygen
Change reduction, flocculation adsorption and precipitation to remove, so that a kind of pretreatment mode that waste water is purified.
Iron-carbon micro-electrolysis technology has cost low in terms of waste water is handled, the advantages of efficiency high, but in actual motion mistake
With the extension in reaction time in journey, iron filings surface can form passivating film, cause iron dissolution rate to decline, so that processing effect
Fruit declines, simultaneously because packed tower is higher, iron carbon filler pressure knot causes filler hardened, reduces treatment effect.
Utility model content
The purpose of this utility model is that there is provided one kind is new in order to overcome above-mentioned of the prior art some or some defect
Iron-carbon micro-electrolysis reactor.
According to Novel iron-carbon micro-electrolysis reactor of the present utility model, including reactor shell, set in reactor shell
It is provided with the multiple reative cells being sequentially connected in series, each reative cell and sets in water intake and wastewater effluent mouthful, reactor enclosure body
Filling iron carbon filler in guide shell, guide shell is equipped with, guide shell bottom is provided with jet aerator, guide shell left and right sides difference
It is provided with the top of deflection plate and overflow weir, guide shell and is provided with every empty baffling cover plate, baffling cover plate is fixed on reactor enclosure
On body.
In a preferred embodiment, filler frame is provided with guide shell, for loading iron carbon filler, filler frame top is provided with
Hanger, is lifted on baffling cover plate, and the bottom of filler frame is covered with the filter plate of stainless steel, and the aperture of filter plate is straight less than iron carbon filler
Footpath.In this case, guide shell upper and lower opening, bottom is provided with bell-mouthed guide shell bottom cover.
In another preferred embodiment, guide shell is glass steel material, and guide shell is fixed by support with reactor shell.
The utility model is relative to prior art, with advantages below：
(1) iron-carbon micro-electrolysis reactor provided by the utility model, several unit process rooms are divided into by reaction tank,
Guiding device is set in each unit process room, and the mentality of designing of this reaction member can promote waste water, filler, exposure
Gas is fully contacted, and water flow is circulated in unit process indoor and outdoor, it is ensured that waste water is contacted with iron carbon filler repeatedly, reduces reaction
Dead angle in device.
(2) deflection plate, the use of overflow weir in iron-carbon micro-electrolysis reactor provided by the utility model, can be more preferable
Constraint, guiding current, air-flow, be avoided as much as the generation of short flow phenomenon.
(3) iron-carbon micro-electrolysis reactor provided by the utility model, only sets immediately below guiding device and concentrates aeration
Device.Aeration export volume is reduced in the case where total aeration quantity is constant, the aeration quantity of a single point can be effectively increased；Expose simultaneously
Gas device is jet aerator, can strengthen mixing wastewater with air effect, and to the souring of iron carbon filler, delay iron carbon filler
Passivation.
(4) iron-carbon micro-electrolysis reactor provided by the utility model, filler filling mode is set to only in guiding device
Filler framework in fill a small amount of iron carbon filler, and when passivation phenomenon occurs in filler, filler frame is lifted out using overhead traveling crane
The water surface, rinses filler surface with giant and backfills again, can effectively prevent the hardened of filler, and improve the utilization of iron filings
Rate.
Brief description of the drawings：
Fig. 1 is the overall structure diagram of Novel iron-carbon micro-electrolysis reactor of the present utility model；
Fig. 2 is the schematic side view of Novel iron-carbon micro-electrolysis reactor of the present utility model；
Label declaration：1. the wastewater effluent mouthful of 4. overflow weir of reactor shell 2. water intake, 3. deflection plate 5. 6.
Cover the base of 10. jet aerator, 11. mud discharging mouth 12. in the guide shell bottom of 7. guide shell of baffling cover plate, 8. filler 9..
Embodiment
To describe the utility model technology contents, construction feature, the objects and the effects in detail, below in conjunction with embodiment party
Formula simultaneously coordinates accompanying drawing to be explained in detail.
Referring to Fig. 1 and Fig. 2, mainly included according to Novel iron-carbon micro-electrolysis reactor of the present utility model reactor shell 1,
Deflection plate 3, overflow weir 4, guide shell 7 and jet aerator 10.
Reactor shell 1 is in set to set on water intake 2, right side wall on cuboid, the left side wall of reactor shell 1
Put wastewater effluent mouthful 5.Be provided with reactor shell 1 be provided with four reative cells of series connection, each reative cell side by side two
Individual guide shell 7.Filling iron carbon filler 8 in guide shell 7.Iron carbon filler 8 is mainly made up of cast-iron scrap and carbon dust.Reactor shell 1
Bottom is provided with mud discharging mouth 11, inspection and maintenance during emptying for equipment.The bottom of reactor shell 1 is provided with support W-response
The stainless steel base 12 of device.
The left and right sides of guide shell 7 is respectively arranged with deflection plate 3 and overflow weir 4, and wherein deflection plate 3 guides current from water conservancy diversion
7 bottoms of cylinder enter carries out micro-electrolysis reaction with iron carbon filler 8 in guide shell 7, the overfall of overflow weir 4 is higher than guide shell 7, made
Fully reacted waste water automatic overflow is to next reative cell or discharges.The top of guide shell 7 is provided with every empty folding
Cover plate 6 is flowed, baffling cover plate 6 is fixed in reactor shell 1.Baffling cover plate 6 can make reacted waste water turn back again to leading
The bottom of flow cartridge 7, is recycled into guide shell 7 and is reacted with iron carbon filler 8.In addition, baffling cover plate 6 can also make the bubble that reaction is produced
Foam is fallen back in guide shell 7 after vanishing.
Guide shell 7 is preferred to use glass steel material, thus it is corrosion-resistant, it can be used for a long time.Guide shell 7 passes through support and reaction
Device housing 1 is fixed.When guide shell 7 itself is used for loading iron carbon filler, the bottom of guide shell 7 is provided with Porous Base, many bottom holes
Jet aerator 10 is set below plate.But filler is changed for convenience, in a preferred embodiment, filler is provided with guide shell 7
Frame (not shown), for loading iron carbon filler, filler frame top is provided with hanger, is lifted on baffling cover plate 7, filler frame
Bottom is covered with the filter plate of stainless steel, and the aperture of filter plate is less than iron carbon filler diameter.In this case, the upper and lower opening of guide shell 7,
Bottom is provided with into bell-mouthed guide shell bottom cover 9, and jet aerator 10 is set below guide shell bottom cover 9.
When being used for Industrial Wastewater Treatment using Novel iron-carbon micro-electrolysis reactor of the present utility model, pH waste water will be mixed up
Flowed into through pump from water intake 2, by the use of deflection plate 3 and bottom jet aerator 10, waste water can be guided to enter
With the abundant haptoreaction of iron carbon filler 8 in guide shell 7, and by baffling cover plate 6 waste water is reacted with the multiple-contact of filler 8.
Waste water flows into next reaction process from wastewater effluent mouthful 5 after completion of the reaction.
Embodiment of the present utility model is the foregoing is only, the scope of the claims of the present utility model is not thereby limited, it is every
The equivalent structure or equivalent flow conversion made using specification of the present utility model and accompanying drawing content, or directly or indirectly use
In other related technical fields, similarly it is included in the utility model protection domain.
Claims (5)
1. water intake is set in a kind of Novel iron-carbon micro-electrolysis reactor, including reactor shell, reactor shell and useless
Water delivery port, it is characterised in that be provided with the multiple reative cells being sequentially connected in series, each reative cell and be provided with reactor enclosure body
Filling iron carbon filler in guide shell, guide shell, guide shell bottom is provided with jet aerator, and the guide shell left and right sides is set respectively
Have and be provided with the top of deflection plate and overflow weir, guide shell every empty baffling cover plate, baffling cover plate is fixed in reactor shell.
2. Novel iron-carbon micro-electrolysis reactor according to claim 1, it is characterised in that filler is provided with guide shell
Frame, for loading iron carbon filler, filler frame top is provided with hanger, is lifted on baffling cover plate, and the bottom of filler frame is covered with stainless
The filter plate of steel, the aperture of filter plate is less than iron carbon filler diameter.
3. Novel iron-carbon micro-electrolysis reactor according to claim 2, it is characterised in that guide shell upper and lower opening, bottom
It is provided with bell-mouthed guide shell bottom cover.
4. Novel iron-carbon micro-electrolysis reactor according to claim 1, it is characterised in that guide shell is glass steel material,
Guide shell is fixed by support with reactor shell.
5. Novel iron-carbon micro-electrolysis reactor according to claim 1, it is characterised in that reactor shell bottom wall is provided with
Mud discharging mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720046533.2U CN206395887U (en) | 2017-01-16 | 2017-01-16 | A kind of Novel iron-carbon micro-electrolysis reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720046533.2U CN206395887U (en) | 2017-01-16 | 2017-01-16 | A kind of Novel iron-carbon micro-electrolysis reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206395887U true CN206395887U (en) | 2017-08-11 |
Family
ID=59518003
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720046533.2U Active CN206395887U (en) | 2017-01-16 | 2017-01-16 | A kind of Novel iron-carbon micro-electrolysis reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206395887U (en) |
-
2017
- 2017-01-16 CN CN201720046533.2U patent/CN206395887U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 061000 Floor 5, R&D Building, No. 9, Guofeng Avenue, High tech Zone, Cangzhou City, Hebei Province Patentee after: Hebei Fengyuan Environmental Protection Technology Group Co.,Ltd. Address before: 061000 south of No.1 Road, Zhongjie Industrial Park, Cangzhou City, Hebei Province Patentee before: HEBEI FENGYUAN GREEN TECHNOLOGY Inc. |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 010000 West Wanda Sales Center, Genghis Khan West Street, Huimin District, Hohhot City, Inner Mongolia Autonomous Region Patentee after: Antai Fengyuan Environmental Protection Technology (Inner Mongolia) Group Co.,Ltd. Country or region after: China Address before: 061000 Floor 5, R&D Building, No. 9, Guofeng Avenue, High tech Zone, Cangzhou City, Hebei Province Patentee before: Hebei Fengyuan Environmental Protection Technology Group Co.,Ltd. Country or region before: China |
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| CP03 | Change of name, title or address |