CN203754535U - Efficient micro-electrolysis multiphase flow air flotation reactor - Google Patents
Efficient micro-electrolysis multiphase flow air flotation reactor Download PDFInfo
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- CN203754535U CN203754535U CN201420172828.0U CN201420172828U CN203754535U CN 203754535 U CN203754535 U CN 203754535U CN 201420172828 U CN201420172828 U CN 201420172828U CN 203754535 U CN203754535 U CN 203754535U
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Abstract
The utility model aims to provide an efficient micro-electrolysis multiphase flow air flotation reactor for pretreating wastewater in chemical, pharmaceutical and other industries. The efficient micro-electrolysis multiphase flow air flotation reactor comprises a multiphase flow dissolved air intake pump, a reactor main body which comprises a water distribution zone, a micro-electrolysis filler zone, an air flotation separation zone and a clean water zone, a water distribution device arranged in the water distribution zone, a pipeline for connecting the multiphase flow dissolved air intake pump with the water distribution device, a perforated partition plate arranged between the water distribution device and the micro-electrolysis filler zone, a micro-electrolysis filler arranged in the micro-electrolysis filler zone, a partition screen arranged between the micro-electrolysis filler zone and the air flotation separation zone, a slag discharge tank arranged at the upper part of the air flotation separation zone, an effluent pipe arranged at the lower part of the clean water zone and an effluent control valve connected with the effluent pipe.
Description
Technical field
The utility model belongs to field of waste water treatment, particularly a kind of efficient micro-electrolysis polyphasic flow air supporting reactor for poor Wastewater Pretreatment of biodegradability such as chemical industry, pharmaceutical industries.
Background technology
Chemical industry, it is high that the waste water such as pharmacy have pollutant concentration conventionally, complicated component, waste water has certain toxicity, contain the features such as component that multiple-microorganism is difficult to degraded, therefore, adopt not only difficulty up to standard of single treatment process, and investment and running cost can be very high, waste water just must be carried out to the shunting of removing contamination according to concentration, collect respectively and select physicochemical techniques targetedly to carry out pre-treatment to high-concentration waste water, reduce its toxicity and concentration and improve its biodegradability, then mix with low concentration wastewater and carry out biochemical treatment, after biochemical treatment, water outlet can reach takes over or emission standard.For high density, the waste water that poisonous, biochemical is poor, conventionally adopt chemical method to carry out pre-treatment.The effect of electroplating effluent recycling and using is the organic concentration that reduces the waste water that enters biochemical system; Decompose the hardly-biodegradable materials such as macromole aromatic hydrocarbon, improve biodegradability; Decomposition, modification hazardous and noxious substances, reduce its concentration to the biochemical scope allowing.Waste water method of chemical treatment is compared with biological treatment, can more rapidly, effectively remove more pollutent, can be used as the pre-treatment measure before biological treatment, also can be used as the tertiary treatment measure after biological treatment.This method also has equipment and easily operates, easily realizes and automatically detect and control, be convenient to the advantages such as recycling.Method of chemical treatment can be removed multiple severe toxicity and high malicious pollutent in waste water effectively.Chemical method is to utilize the work of chemical reaction in order to remove organism, the inorganics impurity in water.Mainly contain chemical coagulation process, chemical oxidization method, electrochemical oxidation process etc.Chemical coagulation process effective object is mainly small suspended substance and colloidalmaterial in water, and the cohesion and the throwing out that by adding chemical agent, produce make elimination of colloid stability form precipitation or scum silica frost and remove.Coagulation Method not only can be removed the tiny suspended particle that the particle diameter in waste water is 1O～10mm, and can also remove colourity, microorganism and organism etc., the method is subject to the variable effects such as pH value, water temperature, water quality, the water yield large, and the organic and inorganic material clearance good to some solubility is low; Chemical oxidization method normally carries out the method for oxidation removal to the organic pollutant in wastewater from chemical industry with oxygenant.Waste water, through chemistry redox, can make organic and inorganic toxic substance contained in waste water be transformed into material nontoxic or that toxicity is less, thereby reach the object of purification of waste water.Conventional have atmospheric oxidation, oxychlorination, ozonization method, micro-electrolysis method and a Fenton oxidation method.Atmospheric oxidation because of its oxidation capacity a little less than, be mainly used in the wastewater treatment containing the stronger material of reductibility, Cl is the oxygenant of common use, is mainly used in containing in phenol, processing containing organic waste waters such as cyanogen, uses ozonize waste water, oxidation capacity is strong, non-secondary pollution.Ozonation, oxychlorination method, its water treatment is effective, but energy consumption is large, and cost is high, is not suitable for processing wastewater of chemical industry with high concentration.
Micro electrolysis tech is a kind of ideal technology of processing at present high concentrated organic wastewater, claims again internal electrolysis.It is in cold situation, utilizes the iron carbon filler self being filled in waste water to produce 1.2V potential difference waste water is carried out to electrolysis treatment, to reach the object of degradable organic pollutant.
The reaction of iron carbon galvanic cell:
Anode: Fe-2e → Fe
2+e(Fe/Fe
2+)=0.44V
Negative electrode: 2H
++ 2e → H
2e(H
+/ H
2)=0.00V
When aerobic exists, cathodic reaction is as follows:
O
2+ 4H
++ 4e → 2H
2O E (O
2)=1.23V
O
2+ 2H
2O + 4e → 4OH
-E（O
2/OH
-）=0.41V
After system water flowing, in equipment, can form countless microbattery systems, at its action space, form an electric field.The nascent state producing in treating processes [H], Fe
2+deng can with waste water in many component generation redox reactions, such as can damaged colored chromophoric group or the auxochrome group of coloring matter in waste water, even chain rupture, reaches the effect of degradation and decolorization; The Fe generating
2+further be oxidized to Fe
3+, their hydrate has stronger absorption-flocculation activity, the molecule, metallics and the organic macromolecule that in planar water, disperse in a large number.The acting in conjunction of its principle of work based on electrochemistry, oxidation-reduction, physical adsorption and flocculation sediment processed waste water.That this method has is applied widely, treatment effect good, with low cost, convenient operating maintenance, do not need the advantages such as power consumption resource.This technique can reduce COD and colourity significantly for the pre-treatment of hard-degrading high concentrated waste water, improves the biodegradability of waste water, can have good effect to removing of ammonia nitrogen simultaneously.
The micro-electrolysis process of tradition is in the process of using, reaction product forms sealing coat can not proceed and ineffective micro-electrolysis, iron carbon filler is easy to passivation and hardens, form short circuit and channel, cause treatment effect to decline, effluent quality worsens, and for maintaining treatment effect, must change continually micro-electrolysis material, and not only working cost is high but also bring very big inconvenience to operational management.In addition, existing micro-electrolysis reactor can only be realized single micro-electrolysis reaction conventionally, cannot synchronously remove the suspended substance generating in reaction, can only remove the suspended substance in water outlet by the settler or the air-floating apparatus that arrange in addition, increased water treatment system overall cost of ownership, this has all had a strong impact on utilization and the popularization of micro-electrolysis process.
Summary of the invention
This practical new object is to provide a kind of for chemical industry, pretreated efficient micro-electrolysis polyphasic flow air supporting reactor of waste water of pharmaceutical industry, this reactor has carried out organic ingenious combination by micro-electrolysis and polyphasic flow air flotation technology principle, by adopting multiphase flow pump to carry out after high pressure solution gas former water, former water after molten gas is sent into reactor bottom cloth pool, in cloth pool, the air that high pressure is dissolved in former water obtains explosive decompression release, form the micro-bubble of 30 μ m ~ 50 μ m, microbubble and the former water reactor filler district that flows through from bottom to top, former water carries out micro-electrolysis reaction in packing area, reacted resultant flco continues to rise under the effect of water and microbubble, water overflow is afterwards crossed reactor internal layer dividing plate and is entered clean water chamber and flow downward, and finally by clean water chamber bottom water outlet, discharge reactor, and the scum silica frost that micro-electrolysis reaction resultant flco forms forms scum layer under microbubble adhesion and buoyancy on reactor top, scum silica frost is regularly discharged reactor by ash pit.High pressure solution air lift high the oxygen level in water, be conducive to promote the efficient performance of micro-electrolytic action, micro-bubble can provide larger specific surface area, be conducive to adsorb more resultant of reaction flco, make air supporting removal efficiency higher, the buoyancy that mobile water and countless microbubble produce that makes progress makes iron carbon filler be fluidized, increased the abundant contact reacts chance of water and filler, improved micro-electrolysis reaction efficiency, in addition, the timely removal of resultant of reaction and the fluidized of filler all can effectively be avoided the filler passivation phenomenon that hardens.Efficient micro-electrolysis polyphasic flow air supporting reactor of the present utility model, has overcome existing micro-electrolysis reactor technical finesse waste water efficiency low, and the filler shortcomings such as passivation that easily harden have saved micro-electrolysis aerating apparatus and follow-up coagulating sedimentation or air supporting facility simultaneously.Compare prior art, this reactor, for Wastewater Pretreatment such as chemical industry, pharmacy, has effect remarkable, reduces investment outlay and takes up an area, can operation steady in a long-term etc. advantage, also can be widely used in high density, difficult degradation, the virose Wastewater Pretreatment of other industry.
Efficient micro-electrolysis polyphasic flow air supporting reactor of the present utility model, comprise the molten gas intake pump of polyphasic flow, by cloth pool, micro-electrolysis stuffing district, flotation separation zone, the reactor body that clear water zone forms, be arranged on the water-distributing device in cloth pool, the pipeline that connects the molten gas intake pump of polyphasic flow and water-distributing device, be arranged on the Perforated clapboard between cloth pool and micro-electrolysis stuffing district, be arranged on the micro-electrolysis stuffing in micro-electrolysis stuffing district, be arranged on the filter between micro-electrolysis stuffing district and flotation separation zone, be arranged on the ash pit on top, flotation separation zone, be arranged on the rising pipe of bottom, clear water zone, the outlet water control valve being connected with rising pipe.It is characterized in that described water distribution district is positioned at the bottom of reactor body, described micro-electrolysis stuffing district is positioned at the middle part of reactor body, described flotation separation zone is positioned at the top of reactor body, described clear water zone is positioned at the outside of reactor body, described cloth pool, micro-electrolysis stuffing district cut off by dividing plate and clear water zone, described micro-electrolysis stuffing is regular shape iron carbon sintered compact, and proportion is 1.0 ~ 1.1g/cm
3, the molten gas intake pump of described polyphasic flow is ripe commercially available prod, as the multiphase flow gas-dissolving pump of German EDUR company, and the multiphase flow gas-dissolving pump of Japanese Ni Keni company.
Efficient micro-electrolysis polyphasic flow air supporting reactor of the present utility model, compared with prior art, it has following beneficial effect: overcome existing micro-electrolysis reactor technical finesse waste water efficiency low, the filler shortcomings such as passivation that easily harden, micro-electrolysis aerating apparatus and follow-up coagulating sedimentation or air supporting facility have been saved simultaneously, there is effect remarkable, reduce investment outlay and take up an area, the advantages such as energy operation steady in a long-term.
Accompanying drawing explanation: Fig. 1 is structural representation of the present utility model.
Embodiment: the utility model is described in further detail below in conjunction with the specific embodiment of accompanying drawing, structure shown in Fig. 1 is one of them preferred structure of the utility model, it is efficient micro-electrolysis polyphasic flow air supporting reactor, mainly comprise the molten gas intake pump 1 of polyphasic flow, by cloth pool 2, micro-electrolysis stuffing district 3, flotation separation zone 4, the reactor body that clear water zone 5 forms, be arranged on the water-distributing device 6 in cloth pool 2, the pipeline 7 that connects the molten gas intake pump 1 of polyphasic flow and water-distributing device 6, be arranged on the Perforated clapboard 8 between cloth pool 2 and micro-electrolysis stuffing district 3, be arranged on the micro-electrolysis stuffing 9 in micro-electrolysis stuffing district 3, be arranged on the filter 10 between micro-electrolysis stuffing district 3 and flotation separation zone 4, be arranged on the ash pit 11 on 4 tops, flotation separation zone, be arranged on the rising pipe 12 of 5 bottoms, clear water zone, the outlet water control valve 13 being connected with rising pipe 12.Cloth pool 2 is positioned at the bottom of reactor body, micro-electrolysis stuffing district 3 is positioned at the middle part of reactor body, flotation separation zone 4 is positioned at the top of reactor body, and clear water zone 5 is positioned at the outside of reactor body, and cloth pool 2, micro-electrolysis stuffing district 3 cut off by dividing plate 14 and clear water zone 5.
Claims (2)
1. efficient micro-electrolysis polyphasic flow air supporting reactor, it is characterized in that comprising the molten gas intake pump of polyphasic flow, by cloth pool, micro-electrolysis stuffing district, flotation separation zone, the reactor body that clear water zone forms, be arranged on the water-distributing device in cloth pool, the pipeline that connects the molten gas intake pump of polyphasic flow and water-distributing device, be arranged on the Perforated clapboard between cloth pool and micro-electrolysis stuffing district, be arranged on the micro-electrolysis stuffing in micro-electrolysis stuffing district, be arranged on the filter between micro-electrolysis stuffing district and flotation separation zone, be arranged on the ash pit on top, flotation separation zone, be arranged on the rising pipe of bottom, clear water zone, the outlet water control valve being connected with rising pipe.
2. efficient micro-electrolysis polyphasic flow air supporting reactor according to claim 1, it is characterized in that described water distribution district is positioned at the bottom of reactor body, described micro-electrolysis stuffing district is positioned at the middle part of reactor body, described flotation separation zone is positioned at the top of reactor body, described clear water zone is positioned at the outside of reactor body, and described cloth pool, micro-electrolysis stuffing district cut off by dividing plate and clear water zone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420172828.0U CN203754535U (en) | 2014-04-11 | 2014-04-11 | Efficient micro-electrolysis multiphase flow air flotation reactor |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420172828.0U CN203754535U (en) | 2014-04-11 | 2014-04-11 | Efficient micro-electrolysis multiphase flow air flotation reactor |
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| CN203754535U true CN203754535U (en) | 2014-08-06 |
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|---|---|---|---|
| CN201420172828.0U Expired - Fee Related CN203754535U (en) | 2014-04-11 | 2014-04-11 | Efficient micro-electrolysis multiphase flow air flotation reactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103936208A (en) * | 2014-04-11 | 2014-07-23 | 无锡博美环境工程有限公司 | Efficient micro-electrolysis multiphase flow air flotation reactor |
| CN105217709A (en) * | 2014-06-14 | 2016-01-06 | 周春江 | A kind of heterogeneous catalytic oxidation air-floating apparatus |
-
2014
- 2014-04-11 CN CN201420172828.0U patent/CN203754535U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103936208A (en) * | 2014-04-11 | 2014-07-23 | 无锡博美环境工程有限公司 | Efficient micro-electrolysis multiphase flow air flotation reactor |
| CN105217709A (en) * | 2014-06-14 | 2016-01-06 | 周春江 | A kind of heterogeneous catalytic oxidation air-floating apparatus |
| CN105217709B (en) * | 2014-06-14 | 2018-01-30 | 周春江 | A kind of heterogeneous catalytic oxidation air-floating apparatus |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 214204 Xieqiao Kechuang B4 Building, Xinjie Street, Yixing City, Wuxi City, Jiangsu Province Patentee after: Wuxi Bomei Environmental Technology Co., Ltd. Address before: 214214 No. 77 Far East Avenue, Gaoyong Town, Yixing City, Jiangsu Province Patentee before: Wuxi Bo Mei Genie et Environnement |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140806 Termination date: 20200411 |