CN206204101U - A kind of integrated waste-water treater of efficient energy-saving - Google Patents
A kind of integrated waste-water treater of efficient energy-saving Download PDFInfo
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- CN206204101U CN206204101U CN201620870460.4U CN201620870460U CN206204101U CN 206204101 U CN206204101 U CN 206204101U CN 201620870460 U CN201620870460 U CN 201620870460U CN 206204101 U CN206204101 U CN 206204101U
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Abstract
The utility model discloses a kind of integrated waste-water treater of efficient energy-saving, including deflector type medicine feeding mixing tank and advanced oxidation reactor；Baffling passage is provided with deflector type medicine feeding mixing tank, one end of baffling passage is connected on inlet water lifting pumps, the other end is connected on advanced oxidation reactor by pipeline, multiple folded plates are evenly distributed with baffling passage, separation folded plate is provided with the top of advanced oxidation reactor, separate folded plate and advanced oxidation reactor is separated into IIth area of Ith area of reaction and reaction, react and be provided with water inlet at the top of Ith area, react and be provided with delivery port at the top of IIth area, the bottom for reacting IIth area of Ith area and reaction is equipped with annular perforations aeration tube, the bottom for reacting Ith area is provided with band mesh baffle plate, with being provided with packing area above mesh baffle plate, granular filler is filled with packing area；Apparatus structure of the present utility model is compact, and floor space is small, and treatment effeciency is high, waste water is decolourized using advanced oxidation processes, drops COD treatment, it is ensured that the waste water after treatment reaches the requirement of country-level A standards.
Description
Technical field
The utility model is related to technical field of waste water processing, more particularly to a kind of integrated wastewater treatment of efficient energy-saving to fill
Put.
Background technology
Over nearly 20 years, with quickly propelling for the high speed development of China's economic, especially urbanization, artificial synthesized is organic
Species are growing day by day with quantity, cause the organic pollution of large amount of complex difficult degradation to enter water body, enter easily by food chain
Row biological concentration, a series of harm such as carcinogenic, teratogenesis, mutagenesis are produced to organism.Therefore, the promulgation of new environmental law and " water
Ten " appearance, also increasingly stricter to the requirement of the discharge standard of pollutant, sensitizing range water outlet should reach《At town sewage
Reason factory pollutant emission standard》（GB18918-2002）The requirement of one-level A standards, some are even up to《Surface water environment quality
Standard》（GB3838-2002）The requirement of IV class standards, thus must be had using persistent organic pollutants in treatment waste water at present
The method of effect has micro-electrolysis method, advanced oxidation processes.
Micro-electrolysis method is that a kind of utilization Principles of Metal Erosion form the technology that galvanic cell processes waste water, with process is simple,
Pretreating effect is good, can effectively improve the biodegradability of waste water, if it is widely studied and be applied to printing and dyeing, the difficult drop such as oil field
The treatment of industrial wastewater is solved, but it is during pretreated waste water, it is impossible to will such as nitrobenzene compounds difficult degradation pollution
Thing is thoroughly degraded to inorganic molecules material.
Current representational advanced oxidation processes have Ozonation, Fenton or class Fenton oxidation method, using oxidant, catalysis
Agent produces the stronger oxidizing substance such as OH of a large amount of oxidisability, triggers a series of radical chain reactions, so that Quick Oxidation point
Solution persistent organic pollutants.But Ozonation has wastewater treatment, and the time is long, power consumption is big, relatively costly, ozone is sharp
With the low defect of rate, for Fenton or class Fenton process, lack that to have that reagent consumption amount is big, medicament reacts insufficient, utilization rate low, residual
Remaining oxidant is more, operating cost is high, sludge yield is big, there is a problem of secondary pollution containing more sulfate radical and iron in water.
Because there is certain defect in above-mentioned technology, typically all can be by certain design, by all kinds of technologies
Combination application, to improve that degradation of organic waste water treatment effeciency.Such as Chinese patent（Publication number CN102180558A）Disclose one
Compound advanced oxidation processing technique is planted, its electrochemical reaction area is mainly micro-electrolysis reaction, Fe2+Directly given birth to ozone reactor
OH is produced, reaction rate is well below Fenton's reaction system；Chinese patent（Publication number CN101955280A）Disclose a kind of multiple
Electrochemical treatments technique is closed, H is produced in its electro-catalysis2O2Reaction and light electrolysis produce Fe2+Reaction is respectively in different reactors, and electricity is fragrant
The reaction synergy that pauses is not good；Chinese patent（Publication number CN201510160332）Disclose a kind of for that degradation of organic waste water
The advanced oxidation coupling device and technique for the treatment of, have coupled electrocatalytic oxidation, ozone oxidation, Fenton oxidation and microelectrolysis processing
Four kinds of technologies, apparatus structure is complicated, and manufacture craft is cumbersome, with high costs.
Above-mentioned advanced oxidation combination unit, although the treatment to organic wastewater with difficult degradation thereby can be lifted to a certain extent
Efficiency, but still also there is effect and be not added with, lack flexibility the problems such as, limit commercial introduction application.
The content of the invention
For the defect of prior art Trends of Advanced Oxidation Process Methods, the utility model purpose is a kind of efficient energy-saving for providing
Advanced oxidation integration waste water decoloring, drop COD device, with ensure treatment after waste water reach country-level A standards will
Ask.
In order to achieve the above object, the technical solution adopted in the utility model is as follows：A kind of integration of efficient energy-saving is given up
Water treatment facilities, described wastewater treatment dress includes deflector type medicine feeding mixing tank and advanced oxidation reactor；
Be provided with baffling passage in deflector type medicine feeding mixing tank described in the utility model, one end of baffling passage be connected into
On water elevator pump, the other end is connected on advanced oxidation reactor by pipeline, and multiple folded plates are evenly distributed with baffling passage,
It is sequentially provided with alkali dosing mouth, composite oxidant dosing mouth in described baffling passage in water (flow) direction, it is the alkali dosing mouth, multiple
Oxidant dosing mouth is closed to be connected with alkali dosing measuring pump, composite oxidant dosing measuring pump respectively；
As a kind of improvement of the present utility model, separation folded plate is provided with the top of the advanced oxidation reactor, separates folding
Advanced oxidation reactor is separated into IIth area of Ith area of reaction and reaction by plate, and the bottom for reacting Ith area is connected with IIth area of reaction, reaction I
Water inlet is provided with the top of area, delivery port is provided with the top of IIth area of reaction, the bottom in IIth area of Ith area of reaction and reaction is equipped with annular
Boring aeration pipe, the bottom in the described area of reaction I is provided with band mesh baffle plate, with being provided with packing area, filler above mesh baffle plate
Granular filler is filled with area, the volume of packing area is 0.5 ~ 1 times that reacts I area's volume.
As it is of the present utility model it is a kind of improve, include successively in water (flow) direction in described baffling passage leading portion, in
The folded plate installed in section and back segment, leading portion baffling passage is same setback plate, and the folded plate installed in the baffling passage of stage casing is different setback
The folded plate installed in plate, back segment baffling passage is flat board, and 5~10 folded plates, 2~4 foldings of leading portion are typically used in baffling passage
Plate is used with setback plate, and 2~4, stage casing folded plate uses different setback plate, 1~2 folded plate of back segment to use flat board；Different setback plate and same
Wave angle on setback plate is 120 °, and this kind combination and folded structure are conducive to processed waste water fully to be mixed with medicine
Close.
Used as a kind of improvement of the present utility model, the back segment of the baffling passage is provided with pH on-line computing models, and pH is supervised online
Instrument is surveyed to be linked with alkali dosing measuring pump by self-control cabinet.
As it is of the present utility model it is a kind of improve, described granular filler is activated carbon, iron powder and copper powder mixed sintering and
Into spherical particle, the particle diameter of spherical particle is 3 ~ 5mm；This kind of spherical particle has that catalysis activity is high, bulk density is low, consumption
Amount less, it is stable the characteristics of.
As it is of the present utility model it is a kind of improve, described band mesh baffle plate as made by engineering plastics or polypropylene, band
Mesh aperture on mesh baffle plate is 1 ~ 2mm.
Used as a kind of improvement of the present utility model, the reaction is provided with pH on-line computing models and acid-adding port in the middle part of IIth area,
PH on-line computing models are linked by self-control cabinet with acid adding measuring pump.
As it is of the present utility model it is a kind of improve, the delivery port in the described area of reaction II be provided with ORP on-line computing models,
COD on-line computing models, both are linked by self-control cabinet with composite oxidant dosing measuring pump.
Used as a kind of improvement of the present utility model, the bottom of described advanced oxidation reactor is inclined housing, is inclined
Angle [alpha] is 15 °~30 °, and the bottom for inclining housing is provided with sediment outlet,
Used as a kind of improvement of the present utility model, the bottom of the advanced oxidation reactor is provided with air pump, described sky
Air pump is connected with annular perforations aeration tube.
Operating method of the present utility model is as follows：
1）Pending waste water pumps into deflector type mixing dosing tank through inlet water lifting pumps, is carried out with alkali, composite oxidant successively
Hydraulic mixing mix, incorporation time be 5 ~ 15min, by robot control system(RCS) control deflector type mixing dosing tank end pH be 10 with
On；Then advanced oxidation reactor is entered with the well-mixed waste water gravity flow of medicine.
2）Waste water is introduced into advanced oxidation and reacts Ith area, starts air pump and is aerated, the activated carbon catalysis ball in the region
On the one hand to colourity, refractory organic compounds carry out Adsorption to shape particle, while activated carbon catalysis ball catalysis composite oxidant
Produce the Strong oxdiative hydroxyl radical free radical of high concentration（·OH）Generation advanced oxidation reacts, and decomposes through the difficulty of activated carbon ball adsorption and enrichment
Degradation of organic substances.
3）Waste water continues advanced oxidation reaction by band mesh baffle plate, and due to the presence of folded plate, waste water is obtained fully
Mixing, reaction is thorough, and the whole advanced oxidation reaction time is 30 ~ 120min.Acid adding in the middle part of IIth area, control are reacted in advanced oxidation
PH6.0 ~ 8.0, final waste water is discharged by the delivery port of reactor upper right quarter, obtains the water outlet for decolourizing to drop COD.
4）The housing for reacting the gradient that the deposit for producing passes through advanced oxidation reactor bottom is collected, Ran Houcong
Bottom sediment outlet is discharged.
The utility model has the advantage of：
1）This advanced oxidation integrated reactor apparatus structure is compact, and floor space is small；
2）The present apparatus is used with compositions such as activated carbon, iron powder, copper powders and sinters the spherical particle to be formed as filler, with catalysis
It is active high, bulk density is low, consumption is few, it is stable the characteristics of.One side adsorption and enrichment hardly degraded organic substance, while having
The effect of composite oxidant is catalyzed, small with required pharmaceutical quantities, sludge output is low, the few advantage of Residuals
3）Advanced oxidation reactor in the present apparatus separates into two reaction zones by folded plate, it is ensured that reaction mixed effect,
So that reaction is more thorough；
4）The present apparatus uses deflector type mixing dosing tank, and without being aerated or stirring, apparatus structure is simple, save energy consumption；
5）The composite oxidant that this reactor assembly is used is a kind of based on the formation of the key components such as enzyme, peroxide
A kind of high-performance compound environmental purification function material, product non-secondary pollution, added amount of chemical are few, reaction condition control letter
It is single；
6）This energy-efficient advanced oxidation integrated waste-water treater, is capable of achieving auto-controll operation, it is ensured that water outlet is steady
Surely treatment necessary requirement is reached；
7）This energy-efficient advanced oxidation integrated waste-water treater, is widely portable to（Chemical industry, medicine and other fields）
Indegradable industrial effluent treatment need badly carry mark transformation existing enterprise not up to standard or require that stable water outlet is up to standard or technique reuse
Newly-built enterprise, is also applied for the pretreatment of above-mentioned field high concentration hard-degraded organic waste water.
Brief description of the drawings
Fig. 1 is apparatus structure sketch of the present utility model；
Fig. 2 is the top view of baffling mixing channel in the utility model device.
Wherein, 1 deflector type medicine feeding mixing tank；2 advanced oxidation reactors；3 separate folded plate；4 packing areas；5 band mesh
Baffle plate；6 annular perforations aeration tubes；7 air pumps；8 Ith area of reaction；9 sediment outlets；10 delivery ports；11 water inlet liftings
Pump；12 add alkali measuring pump；13 composite oxidant dosing measuring pumps；14 acid adding measuring pumps；15 IIth area of reaction；16 online pH
Meter；17 ORP on-line computing models；18 COD on-line computing models.
Specific embodiment
Explanation and specific embodiment are described in further detail to the utility model below in conjunction with the accompanying drawings.
Embodiment 1：A kind of integrated waste-water treater of efficient energy-saving as illustrated in fig. 1 and 2, described wastewater treatment
Dress includes deflector type medicine feeding mixing tank 1 and advanced oxidation reactor 2；
Baffling passage is provided with deflector type medicine feeding mixing tank 1, one end of baffling passage is connected on inlet water lifting pumps 11, separately
One end is connected on advanced oxidation reactor 2 by pipeline, and multiple folded plates are evenly distributed with baffling passage, and described baffling leads to
Alkali dosing mouth, composite oxidant dosing mouth, the alkali dosing mouth, composite oxidant dosing are sequentially provided with road in water (flow) direction
Mouth is connected with alkali dosing measuring pump 12, composite oxidant dosing measuring pump 13 respectively；
The top of advanced oxidation reactor 2 is provided with separation folded plate 3, separates folded plate 3 and is separated into anti-advanced oxidation reactor
II area 15 of I area 8 and reaction is answered, the bottom for reacting I area 8 is connected with II area 15 of reaction, and the top for reacting I area 8 is provided with water inlet,
The top for reacting II area 15 is provided with delivery port 10, and the bottom in II area 15 of the area 8 of reaction I and reaction is equipped with annular perforations aeration tube 6,
The bottom in the described area 8 of reaction I is provided with band mesh baffle plate 5, and the top with mesh baffle plate 5 is provided with packing area 4, packing area 4 and fills out
Filled with granular filler, the volume of packing area 4 is 0.5 ~ 1 times that reacts the volume of Ith area 8.
Embodiment 2：As illustrated in fig. 1 and 2, leading portion, stage casing and back segment are included in baffling passage successively in water (flow) direction, it is preceding
The folded plate installed in Duan Zheliu passages is same setback plate, and the folded plate installed in the baffling passage of stage casing is different setback plate, back segment baffling
The folded plate installed in passage is flat board, typically uses 5~10 folded plates, 2~4 folded plates of leading portion to use same setback in baffling passage
Plate, 2~4, stage casing folded plate uses different setback plate, 1~2 folded plate of back segment to use flat board；Different setback plate and with the ripple on setback plate
Unrestrained angle β is 120 °, and this kind combination and folded structure are conducive to processed waste water to be sufficiently mixed with medicine.
Embodiment 3：As illustrated in fig. 1 and 2, the back segment of the utility model baffling passage is provided with pH on-line computing models 16, and pH exists
Line monitor 16 is linked by self-control cabinet with alkali dosing measuring pump 12；The middle part in II area 15 of reaction described in the utility model is provided with pH
On-line computing model 16 and acid-adding port, pH on-line computing models 16 are linked by self-control cabinet with acid adding measuring pump 14；The utility model institute
The delivery port 10 in the area of reaction II for stating is provided with ORP on-line computing models 17, COD on-line computing models 18, both by self-control cabinet with
Composite oxidant dosing measuring pump 13 links.
Embodiment 4：As illustrated in fig. 1 and 2, granular filler of the present utility model is various materials such as activated carbon, iron powder and copper powder
Expect the spherical particle of mixed sintering, the particle diameter of spherical particle is 3 ~ 5mm；This kind of spherical particle has that catalysis activity is high, heap
Product density it is low, consumption is few, it is stable the characteristics of.
Embodiment 5：As illustrated in fig. 1 and 2, it is of the present utility model band mesh baffle plate 5 as made by engineering plastics or polypropylene,
It is 1 ~ 2mm with the mesh aperture on mesh baffle plate 5.
Embodiment 6：As illustrated in fig. 1 and 2, the bottom of advanced oxidation reactor 2 of the present utility model is inclined housing, is inclined
Rake angle α is 15 °~30 °, and the bottom for inclining housing is provided with sediment outlet 9,
Embodiment 7：As illustrated in fig. 1 and 2, the bottom of advanced oxidation reactor 2 of the present utility model is provided with air pump 7, institute
The air pump 7 stated is connected with annular perforations aeration tube 6.
Embodiment 8：As illustrated in fig. 1 and 2, operating method of the present utility model is as follows：
1）Pending waste water pumps into deflector type mixing dosing tank 1 through inlet water lifting pumps 11, enters with alkali, composite oxidant successively
Row hydraulic mixing mixes, and incorporation time is 5 ~ 15min, and the pH for controlling the end of deflector type mixing dosing tank 1 by robot control system(RCS) is
More than 10；Then advanced oxidation reactor 2 is entered with the well-mixed waste water gravity flow of medicine.
2）Waste water is introduced into I area 8 of reaction, starts air pump 7 and is aerated, the activated carbon catalysis spherical particle in the region
On the one hand to colourity, refractory organic compounds carry out Adsorption, while activated carbon catalysis ball catalysis composite oxidant produces height
The Strong oxdiative hydroxyl radical free radical of concentration（·OH）Generation advanced oxidation reacts, and decomposition has through the difficult degradation of activated carbon ball adsorption and enrichment
Machine thing.
3）Waste water continues advanced oxidation reaction by band mesh baffle plate 5, and due to separating the presence of folded plate 3, waste water is obtained
To being sufficiently mixed, reaction is thorough, and the whole advanced oxidation reaction time is 30 ~ 120min.In the reaction middle part acid adding of IIth area 15, control
PH is 6.0 ~ 8.0, and final waste water is discharged by reacting the delivery port 10 on the top of IIth area 15, obtains the water outlet for decolourizing to drop COD.
4）The deposit for producing is reacted to be collected by the housing of the gradient of the bottom of advanced oxidation reactor 2,
Then discharged from bottom sediment outlet 9.
Embodiment 9：Liaoning Panjin chemical plant organic wastewater with difficult degradation thereby, water-quality constituents is complicated, and pollutant load is high.Through oil
Water separation+air supporting+hydrolysis acidification+contact oxidation technology, water outlet 200 ~ 300mg/L of COD, 300 ~ 400 times of colourity, it is difficult to meet
《Town sewage pump treatment plant pollutant emission standard》（GB18918-2002）One-level A standards, it is energy-efficient using this for this
Advanced oxidation integrated apparatus are processed its water outlet.
The boosted pump pump of processed water is thoroughly mixed, incorporation time to deflector type mixing dosing tank through hydraulic action
It is 6min, pH of mixed is 10；Then waste water enters Ith area of advanced oxidation reaction, and the activated carbon that the advanced oxidation reacts Ith area is urged
Change granular filler and account for 1/2,3 ~ 5mm of grain diameter, absorption and advanced oxidation reaction, control advanced oxidation reaction occur in the region
Time 75min, reacts in advanced oxidation and adds acid for adjusting pH to 7.5 in the middle part of IIth area.Waste water is discharged from its upper right quarter after reaction, now
Water outlet COD averagely about 38.7mg/L, effluent color dilution almost below 8 times, meets《Town sewage pump treatment plant pollutant emission mark
It is accurate》（GB18918-2002）One-level A standards.
Embodiment 10：Taihu Lake basin Jiangsu Province chemical enterprise is by after hydrolysis acidification+contact oxidation technology, processing water outlet
（COD about 148mg/L, about 95 times of colourity）Can not《Urban wastewater treatment firm》The requirement of GB18918-2002 one-level A standards, in order to
Reach emission request, take Fenton process to carry out advanced treating to it, reaction pH is adjusted to 2.5, add 4.5g/L ferrous sulfate and
The hydrogen peroxide of 1.5ml30%, carries out Fenton's reaction 2.5h, plus alkali regulation pH to 7.0, water outlet COD about 48.9mg/ after flocculation sediment
L, about 15 times of colourity, about 1.8kg/ tons of water of sludge yield.
The water outlet not up to standard is carried out using the energy-efficient advanced oxidation integration waste plant of the utility model simultaneously
Advanced treating.Waste water pump is promoted in deflector type medicine feeding mixing tank, is mixed with alkali, 45mg/L composite oxidants successively
Close.Waterpower mixes 5min, adjusts pH to 11, and then mixed liquor gravity flow enters Ith area of advanced oxidation reaction, controls activated carbon catalysis
Particulate filler accounts for the 1/3 of volume, aeration, carries out absorption and advanced oxidation reaction；IIth area is reacted in advanced oxidation again to continue to react, it is whole
The individual reaction time is 60min.Then again in the middle part of higher order reaction area plus acid for adjusting pH is 6.5, supernatant is from reactor upper right quarter
Discharge, water outlet COD averagely about 32.6mg/L, effluent color dilution is almost below 4 times.Reactor bottom tilt angle alpha is 20 °, is produced
Raw precipitating sludge enters sediment outlet from inclined slope, is computed about 0.19kg/ tons of water of sludge yield, relatively conventional sweet smell
Pause method mud decrement about 90%, greatlys save sludge treatment expense.
Embodiment 11：Using this energy-efficient advanced oxidation integration waste plant to Wuxi printing and dyeing enterprise difficult degradation
Waste water（Raw water COD18200mg/L, pH12, B/C0.11）Processed.Waste water pump to deflector type is added using inlet water lifting pumps
Medicine mixing channel, is mixed with composite oxidant, incorporation time 15min, pH of mixed 11.5 after mixing.Mixed liquor gravity flow enters
Advanced oxidation reacts Ith area, and activated carbon catalysis granular filler accounts for volume 1/2 in control reaction zone, and granular filler 3 ~ 5mm of particle diameter exposes
Gas, the reaction time is 120min, is then reacted in the middle part of IIth area plus alkali regulation pH to 8.0 in advanced oxidation, and supernatant is from reactor
Upper right quarter is discharged, water outlet COD4540mg/L, clearance 75%, and B/C ratios are 0.39.Subsequent technique is used based on basalt fibre
Bioreactor is processed, and reaches the requirement of the discharge standard of dyeing waste water.
It should be noted that above-mentioned is only preferred embodiment of the present utility model, not for limiting the utility model
Protection domain, any combination or equivalents made on the basis of above-described embodiment belong to guarantor of the present utility model
Shield scope.
Claims (10)
1. a kind of integrated waste-water treater of efficient energy-saving, it is characterised in that described wastewater treatment equipment includes folding
Streaming medicine feeding mixing tank and advanced oxidation reactor；
Baffling passage is provided with described deflector type medicine feeding mixing tank, one end of baffling passage is connected on inlet water lifting pumps, separately
One end is connected on advanced oxidation reactor by pipeline, and multiple folded plates are evenly distributed with baffling passage, and described baffling leads to
Alkali dosing mouth, composite oxidant dosing mouth, the alkali dosing mouth, composite oxidant dosing are sequentially provided with road in water (flow) direction
Mouth is connected with alkali dosing measuring pump, composite oxidant dosing measuring pump respectively；
Separation folded plate is provided with the top of the advanced oxidation reactor, is separated folded plate and advanced oxidation reactor is separated into reaction I
IIth area of area and reaction, the bottom for reacting Ith area is connected with IIth area of reaction, and water inlet is provided with the top of Ith area of reaction, IIth area of reaction
Top is provided with delivery port, and the bottom in IIth area of Ith area of reaction and reaction is equipped with annular perforations aeration tube, the bottom in the described area of reaction I
Portion is provided with band mesh baffle plate, with packing area is provided with above mesh baffle plate, granular filler, the body of packing area is filled with packing area
Product is 0.5 ~ 1 times of I area's volume of reaction.
2. the integrated waste-water treater of efficient energy-saving according to claim 1, it is characterised in that described baffling leads to
Include that the folded plate installed in leading portion, stage casing and back segment, leading portion baffling passage is same setback plate successively in water (flow) direction in road, in
The folded plate installed in Duan Zheliu passages is that the folded plate installed in different setback plate, back segment baffling passage is flat board.
3. the integrated waste-water treater of efficient energy-saving according to claim 2, it is characterised in that described different setback
Plate and it is 120 ° with the wave angle on setback plate.
4. the integrated waste-water treater of efficient energy-saving according to claim 2, it is characterised in that the baffling passage
Back segment be provided with pH on-line computing models, pH on-line computing models are linked by self-control cabinet with alkali dosing measuring pump.
5. the integrated waste-water treater of efficient energy-saving according to claim 1, it is characterised in that described particle is filled out
Expect to be the spherical particle of activated carbon, iron powder and copper powder mixed sintering, the particle diameter of spherical particle is 3 ~ 5mm.
6. the integrated waste-water treater of efficient energy-saving according to claim 1, it is characterised in that described band mesh
Baffle plate is 1 ~ 2mm with the mesh aperture on mesh baffle plate as made by engineering plastics or polypropylene.
7. the integrated waste-water treater of efficient energy-saving according to claim 1, it is characterised in that the area of the reaction II
Middle part be provided with pH on-line computing models and acid-adding port, pH on-line computing models are linked by self-control cabinet with acid adding measuring pump.
8. the integrated waste-water treater of efficient energy-saving according to claim 1, it is characterised in that described reaction II
The delivery port in area is provided with ORP on-line computing models, COD on-line computing models, and both are by self-control cabinet and composite oxidant dosing meter
Amount pump linkage.
9. the integrated waste-water treater of efficient energy-saving according to claim 1, it is characterised in that described senior oxygen
The bottom for changing reactor is inclined housing, and angle of inclination is 15 ° ~ 30 °, and the bottom for inclining housing is provided with sediment outlet.
10. the integrated waste-water treater of efficient energy-saving according to claim 1, it is characterised in that the senior oxygen
The bottom for changing reactor is provided with air pump, and described air pump is connected with annular perforations aeration tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620870460.4U CN206204101U (en) | 2016-08-12 | 2016-08-12 | A kind of integrated waste-water treater of efficient energy-saving |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620870460.4U CN206204101U (en) | 2016-08-12 | 2016-08-12 | A kind of integrated waste-water treater of efficient energy-saving |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206204101U true CN206204101U (en) | 2017-05-31 |
Family
ID=58755469
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620870460.4U Expired - Fee Related CN206204101U (en) | 2016-08-12 | 2016-08-12 | A kind of integrated waste-water treater of efficient energy-saving |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082559A (en) * | 2016-08-12 | 2016-11-09 | 江苏艾特克环境工程设计研究院有限公司 | A kind of integrated waste-water treater of efficient energy-saving |
| CN113998827A (en) * | 2021-11-30 | 2022-02-01 | 四川兴澳环境技术服务有限公司 | Advanced oxidation treatment device and treatment method for desulfurization wastewater of oil and gas field |
-
2016
- 2016-08-12 CN CN201620870460.4U patent/CN206204101U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082559A (en) * | 2016-08-12 | 2016-11-09 | 江苏艾特克环境工程设计研究院有限公司 | A kind of integrated waste-water treater of efficient energy-saving |
| CN113998827A (en) * | 2021-11-30 | 2022-02-01 | 四川兴澳环境技术服务有限公司 | Advanced oxidation treatment device and treatment method for desulfurization wastewater of oil and gas field |
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