CN207512019U - A kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device - Google Patents
A kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device Download PDFInfo
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- CN207512019U CN207512019U CN201721198596.6U CN201721198596U CN207512019U CN 207512019 U CN207512019 U CN 207512019U CN 201721198596 U CN201721198596 U CN 201721198596U CN 207512019 U CN207512019 U CN 207512019U
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model provides a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device, including aerating regulation pond, coagulation primary sedimentation tank, hydrolysis acidification pool, aerobic biochemical pool, sedimentation basin, ozone oxidation pond, biological aerated filter, quartz filter, active carbon filter；The utility model uses " hydrolysis acidification and aerobic biochemical " technique, effectively improves the impact resistance of biochemical section.Meanwhile in level-one biochemistry section, the biodegradability of waste water is relatively preferable, and using aerobic biochemical technique, the organic pollution in sewage is preferably removed using the microorganism in activated sludge, meets the design requirement of level-one biochemical process；The utility model is highly practical, convenient for promoting.
Description
Technical field
The utility model is related to a kind of wastewater treatment more particularly to a kind of sanitary sewage, technique waste water, stripper waste water collection
Middle processing unit.
Background technology
Water process is the environment difficulties being commonly encountered in the daily production and living of people, with the acceleration of Urbanization in China,
More and more production and living sewage generate therewith, and traditional water treatment facilities early has been unable to meet the requirement of modern urbanization；
Especially for the synthesis centralized processing system of sanitary sewage, technique waste water and stripper waste water；The wherein temperature of technique waste water
It is high, conductivity is low, containing certain organic matter, there is larger recycling to be worth；And the COD in technique waste water is mainly by gathering
It closes the medicaments such as initiator, dispersant, the terminator added in reaction to cause, it is difficult to remove by coagulation, filtering, and be easy to cause
The dirt of film is blocked up；The features such as treatment of wastewater from stripping has COD high, and biodegradability is low, and water is small, intermittent discharge.It is badly in need of a kind of life at present
Sewage, technique waste water, stripper Wastewater Concentrated device.
Utility model content
For overcome the deficiencies in the prior art, the purpose of this utility model is to provide a kind of sanitary sewage, technique waste water,
Stripper Wastewater Concentrated device using " hydrolysis acidification and aerobic biochemical " technique, effectively improves the shock resistance energy of biochemical section
Power.Meanwhile in level-one biochemistry section, the biodegradability of waste water is relatively preferable, using aerobic biochemical technique, using in activated sludge
Microorganism preferably removes the organic pollution in sewage, meets the design requirement of level-one biochemical process.
The utility model provides a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device, is adjusted including aeration
Save pond, coagulation primary sedimentation tank, hydrolysis acidification pool, aerobic biochemical pool, sedimentation basin, ozone oxidation pond, biological aerated filter, quartz sand mistake
Filter, active carbon filter；Technique waste water accesses aerating regulation pond water inlet end with stripper waste water；The aerating regulation pond
Water outlet is connect with the coagulation primary sedimentation tank water inlet end；The coagulation primary sedimentation tank water outlet, sanitary sewage access the water respectively
Solve acidification pool water inlet end；The hydrolysis acidification pool water outlet is connect with the aerobic biochemical pool water inlet end；The aerobic biochemical pool
Water outlet is connect with the sedimentation basin water inlet end；The sedimentation basin water outlet is connect with ozone oxidation pond water inlet end；It is described
Ozone oxidation pond water outlet is connect with the biological aerated filter water inlet end；The effluent of aeration biological filter is terminated into the stone
Sand filter water inlet end；The quartz filter water outlet is connect with the active carbon filter water inlet end；The activity
Discharge processed waste water in carbon filter water outlet.
Further, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include intermediate pool；It is described
Effluent of aeration biological filter end is connect with the intermediate pool water inlet end；The intermediate pool water outlet is connected to the quartz sand
Filter water inlet end.
Further, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include draining detection cell, institute
It states draining detection cell and is connected to the active carbon filter water outlet；The draining detection cell is equipped with to detect through the activity
The detection device of the waste water index of carbon filter water outlet discharge.
Further, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include cooling tower；The work
Skill waste water is passed through the cooling tower；The cooling tower water outlet is connect with aerating regulation pond water inlet end.
Further, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include sludge concentration tank；Institute
Sludge from sedimentation tank end is stated to connect with the sludge concentration tank feed end respectively with the coagulative precipitation tank spoil disposal end.
Further, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include sludge treatment equipment；
The sludge concentration tank discharge end is connect with the sludge treatment equipment feed end.
Further, the sludge treatment equipment is specially belt type dewaterer；Through the dewatered dirt of the belt type dewaterer
Mud is transported by clearing vehicle.
Further, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include air blower；The drum
Wind turbine respectively with gas circuit pipeline, the biological aerated filter in aerating pipelines in the aerating regulation pond, the aerobic biochemical pool
Interior aerating pipelines connection.
Compared with prior art, the beneficial effects of the utility model are：
The utility model provides a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device, is adjusted including aeration
Save pond, coagulation primary sedimentation tank, hydrolysis acidification pool, aerobic biochemical pool, sedimentation basin, ozone oxidation pond, biological aerated filter, quartz sand mistake
Filter, active carbon filter；Technique waste water and stripper waste water access aerating regulation pond water inlet end；Aerating regulation pond water outlet with
Coagulation primary sedimentation tank water inlet end connects；Coagulation primary sedimentation tank water outlet, sanitary sewage access hydrolysis acidification pool water inlet end respectively；Hydrolysis acid
Hua Chi water outlets are connect with aerobic biochemical pool water inlet end；Aerobic biochemical pool water outlet is connect with sedimentation basin water inlet end；Sedimentation basin goes out
Water end (W.E.) is connect with ozone oxidation pond water inlet end；Ozone oxidation pond water outlet is connect with biological aerated filter water inlet end；Aeration and biological
Quartz filter water inlet end is accessed in filter tank water outlet；Quartz filter water outlet is connect with active carbon filter water inlet end；
Discharge processed waste water in active carbon filter water outlet.The utility model uses " hydrolysis acidification and aerobic biochemical " technique, effectively
Improve the impact resistance of biochemical section.Meanwhile in level-one biochemistry section, the biodegradability of waste water is relatively preferable, using aerobic biochemical
Technique preferably removes the organic pollution in sewage using the microorganism in activated sludge, meets setting for level-one biochemical process
Meter requirement；The utility model is highly practical, convenient for promoting.
The above description is merely an outline of the technical solution of the present invention, in order to better understand the skill of the utility model
Art means, and can be implemented in accordance with the contents of the specification, below on the preferred embodiment of the present invention and the accompanying drawings in detail
It describes in detail bright as after.Specific embodiment of the present utility model is shown in detail by following embodiment and its attached drawing.
Description of the drawings
Attached drawing described herein is used to provide a further understanding of the present invention, and forms the part of the application,
The illustrative embodiments and their description of the utility model are not formed for explaining the utility model to the improper of the utility model
It limits.In the accompanying drawings：
Fig. 1 is a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device the flow signal of the utility model
Figure；
Fig. 2 is a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated the apparatus structure signal of the utility model
Figure.
In figure：Cooling tower 1, aerating regulation pond 2, coagulation primary sedimentation tank 3, hydrolysis acidification pool 4, aerobic biochemical pool 5, sedimentation basin 6,
Ozone oxidation pond 7, biological aerated filter 8, intermediate pool 9, quartz filter 10, active carbon filter 11, draining detection cell
12nd, ozone generator 13, sludge concentration tank 14, sludge treatment equipment 15.
Specific embodiment
In the following, with reference to attached drawing and specific embodiment, the utility model is described further, it should be noted that
Under the premise of not colliding, it can be formed in any combination between various embodiments described below or between each technical characteristic new
Embodiment.
A kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device as Figure 1-Figure 2, are adjusted including aeration
Save pond 2, coagulation primary sedimentation tank 3, hydrolysis acidification pool 4, aerobic biochemical pool 5, sedimentation basin 6, ozone oxidation pond 7, biological aerated filter 8,
Quartz filter 10, active carbon filter 11；Technique waste water and 2 water inlet end of stripper waste water access aerating regulation pond；Aeration
2 water outlet of regulating reservoir is connect with 3 water inlet end of coagulation primary sedimentation tank；Hydrolysis acid is accessed in 3 water outlet of coagulation primary sedimentation tank, sanitary sewage respectively
Change 4 water inlet end of pond；4 water outlet of hydrolysis acidification pool is connect with 5 water inlet end of aerobic biochemical pool；5 water outlet of aerobic biochemical pool and precipitation
Pond 6 water inlet end connection；6 water outlet of sedimentation basin is connect with 7 water inlet end of ozone oxidation pond；It is given birth to aeration 7 water outlet of ozone oxidation pond
The 8 water inlet end connection of object filter tank；10 water inlet end of quartz filter is accessed in 8 water outlet of biological aerated filter；Quartz filter 10
Water outlet is connect with 11 water inlet end of active carbon filter；Discharge processed waste water in 11 water outlet of active carbon filter.
In one embodiment, as shown in Figs. 1-2, sanitary sewage, technique waste water, stripper Wastewater Concentrated device also wrap
Include intermediate pool 9；8 water outlet of biological aerated filter is connect with 9 water inlet end of intermediate pool；9 water outlet of intermediate pool is connected to stone
10 water inlet end of sand filter.Wherein, PAM, PAC water-purifying material are inserted in intermediate pool 8, wherein, PAM, PAC water-purifying material
It is added in water body by compound pump；Suspended particulate in adsorbed water body realizes rapid precipitation；Specifically, sanitary sewage, Waste
Water, stripper Wastewater Concentrated device further include draining detection cell 12, and draining detection cell 12 is connected to active carbon filter 11
Water outlet；Draining detection cell 12 is equipped with the detection dress for detecting the waste water index discharged through 11 water outlet of active carbon filter
It puts.
In one embodiment, as shown in Fig. 2, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include
Cooling tower 1；Technique waste water is passed through cooling tower 1；1 water outlet of cooling tower is connect with 2 water inlet end of aerating regulation pond.By cooling tower 1,
It is quickly cooled down technique waste water.
In one embodiment, as shown in Fig. 2, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include
Sludge concentration tank 14；6 spoil disposal end of sedimentation basin is connect with 3 spoil disposal end of coagulative precipitation tank with 14 feed end of sludge concentration tank respectively.Tool
Body, sludge treatment equipment 15 is specially belt type dewaterer；It is transported through the dewatered sludge of belt type dewaterer by clearing vehicle.
In one embodiment, sanitary sewage, technique waste water, stripper Wastewater Concentrated device further include air blower；Drum
Wind turbine respectively with aerating pipelines in gas circuit pipeline in aerating pipelines in aerating regulation pond 2, aerobic biochemical pool 5, biological aerated filter 8
Connection.Extraneous oxygen is pressed into each pipeline by air blower.
In one embodiment, as shown in Fig. 2, ozone oxidation pond 7 is connect with ozone generator 13, ozone generator 13 generates
Ozone, wherein, ozone O3 is the allotropism gas of oxygen O2, it is to form an ozone molecule by three oxygen atoms, is a kind of
The gas of nascent state, is extremely unstable gas under room temperature, normal pressure, and performance right and wrong are often with active, and instantaneous variation is quickly.
Just there is stronger oxidability when a molecule of ozone is precipitated, making organic matter and inorganic matter progress, quickly oxidation is anti-
New substance should be generated, cuts off molecular link, enhances degradability, improves the biochemical of waste water, utilize the characteristic of above-mentioned ozone O3
And the principle of work and power, by ozone and high molecular weight reactive, so as to reach discoloration, bleaching, deodorization, chain rupture function, it is finally reached height
Purification meets discharge or reuse requirement.It is 5-10mg/ that Ozonation, which is used as merely the ozone concentration that advanced treating adds,
L or so.Ozone in oxidation pond with waste water counter current contacting, 60~120min of time of contact.Pre- place of the ozone as advanced treating
Reason has been obtained for relatively broad application, therefore this engineering pretreating process is used as in the utility model.
Wherein, quartz filter 10 filters out the suspended particle of major part more than 1um and part during intermediate pool 9 is discharged
Colloid protects production water turbidity≤3NTU.Suspended matter during can intermediate pool 9 be discharged is reduced to below 2mg/L.Quartz sand filtration
Device 10 has unique water distribution uniformity mode, and higher flow velocity reduces equipment investment.It simultaneously can be thorough using the backwash of air water joint
Remove retention polluter in bottom；Using filter water distribution, the grading quartz sand of uniform and stable individual layer has good filter effect, and
Be not in the backwash unrest layer phenomenon of more medium filter.
Wherein, active carbon filter 11 is widely used in water treatment technology, such as the deep purifying of drinking water；Process condensate water
Oil removing, the processing except organic matter etc.；The pre-treatment of pure water, high purity water preparation process；The purification of industrial wastewater and sanitary sewage
Processing etc..When equipment is run, processed water inherent filtration device top enters, top-down by activated carbon filtering layer, utilizes activity
The absorption property of charcoal makes the harmful substance in water, such as organic matter, colloid, microorganism, oils, chlorine residue and odor absorption in work
Property carbon surface and be removed, after activated carbon filtering layer " failure ", can be made with the method for backwash its restore adsorption capacity.Activated carbon
The work of filter is completed by charcoal bed.The active carbon particle of composition charcoal bed has very more micropores and huge ratio table
Area has very strong physical absorption ability.Water is effectively adsorbed by charcoal bed, organic pollutants by activated carbon.In addition
There are some oxygen-containing Guan Nengtuan on activated carbon surface non-crystallized part, the organic pollution in the water by charcoal bed is made to be had by activated carbon
The absorption of effect ground.In the present embodiment, save facility from damage using active carbon filter 11 as one kind, avoid activated carbon as consumptive material,
The shortcomings that operating cost is high.
In one embodiment, as shown in Fig. 2, a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device also
Including sludge concentration tank 14；2 spoil disposal end of primary sedimentation tank connects with 7 spoil disposal end of coagulative precipitation tank with 14 feed end of sludge concentration tank respectively
It connects.Preferably, sludge treatment equipment 15 is further included；14 discharge end of sludge concentration tank is connect with 15 feed end of sludge treatment equipment.
14 discharge ends of sludge concentration tank are connected to 2 water inlet end of primary sedimentation tank.Specifically, sludge treatment equipment 15 is specially belt type dewaterer；
It is transported through the dewatered sludge of belt type dewaterer by clearing vehicle.
As shown in Figure 1, a kind of sanitary sewage of the utility model, technique waste water, stripper Wastewater Concentrated device are specific
Technique：
Hydrolysis acidification：The anaerobic degradation process of macromolecule organic is divided into four-stage：Hydrolysis stage, fermentation
(or acidification) stage, production acetic acid stage and methane phase stage.Wherein, hydrolysis may be defined as the polymer quilt of complicated non-solubility
It is converted into the process of simple dissolubility monomer or dimer；Fermentation (or acidification) stage, fermentation may be defined as organic matter chemical combination
Object had both been also the biodegradation process of electron donor as electron acceptor, and dissolved organic matter is converted into wave in the process
End products based on hair property aliphatic acid, therefore this process is also referred to as acidified；Hydrolysis stage is larger molecular organics degradation
Necessary process, macromolecular is organic to be wanted to be utilized by the microorganism, it is necessary to is first hydrolyzed to small organic molecule, could be entered so thin
Bacterium is further degraded into the cell.Souring stage is the speed-raising process of organic matter degradation, because it is organic by the small molecule after hydrolysis
It is further converted to simple compound and is secreted into extracellular.Therefore, in practical Industrial Wastewater Treatment engineering, hydrolysis acid
Change often as the pretreatment unit of biochemical treatment.
Bio-contact oxidation：Based on the biomembrane that is attached on carrier (being commonly called as filler), one kind of purification of organic waste water
Efficient water treatment technology.The biofilm of active sludge feature, the advantages of having activated sludge process and biofilm concurrently.It should
Technique is widely used in each row when having the characteristics that energy-efficient, floor space is small, anti impulsion load, operational management facilitate
The sewage disposal system of each industry.
The basic principle of biological contact oxidation process purification waste water is identical with general biofilm, is exactly useless with biomembrane absorption
Organic matter in water, under conditions of aerobic, organic matter is decomposed by microbiological oxidation, and waste water is purified.Bio-contact oxidation
Biomembrane in pond is made of zoogloea, der Pilz, fungi, protozoan and metazoa.In activated sludge process, der Pilz
Often influence the factor of normal bio catharsis；And in biological contact oxidation pond, der Pilz is between filler gap in vertical
Body structure considerably increases the contact surface of biofacies and waste water, simultaneously as der Pilz to most organic matters have it is stronger
Oxidability has water quality load variations larger adaptability, so being the potent factors for improving detergent power.
In one embodiment, biological aerated filter (biological aerated filter, BAF) belongs to biological treatment
Biofilm scope, be the New Technology about Wastewater Treatment risen in the world in recent years.Have at present in American-European and Japan and other countries
The sewage treatment plant of thousands of different sizes applies this technique.It can be widely applied to treatment of Organic Wastewater, have removal
SS, COD, BOD, nitrification and denitrification, denitrogenation dephosphorizing, the effect for removing AOX, maximum feature are that collection biological oxidation and retention are outstanding
It is floating to be fixed on one.The technique organic matter volumetric loading is high, hydraulic loading is big, hydraulic detention time is short, effluent quality is high, thus
Required floor space is small, capital expenditure is few, energy consumption and operating cost are low.
The characteristics of biological aerated filter：
1) using the parallel upward flow of air water, gas and water is made to be divided equally well, it is therefore prevented that condensation of the bubble in filtering layer,
Coefficient of oxygen utilization is high, and energy consumption is relatively low；
2) with lower to flowing through filter on the contrary, upward flow filtration continues in entire filter tank height to provide positive pressure, Ke Yigeng
Good avoids channel or short stream；
3) upward flow is formd pushes away condition to the attached column that technique is beneficial to, even if using high filtration speed and high load capacity still
It can guarantee the stabilization and reliability of technique；
4) using the parallel upward flow of air water, solid matter can be brought into filter bed depths by air so that filter space can be very well
Be utilized.
The higher technique waste water of temperature is sent into cooling tower 1 through pressure, and water temperature is made to be reduced to 30 DEG C by 40 DEG C, and then gravity flow enters
Aerating regulation pond 2.Stripping process waste water is pumped directly into aerating regulation pond 2.Waste water carries out runoff investigation in aerating regulation pond 2
It is homogenized with water quality, is carried out at the same time pre-exposure gas disposal, can prevent suspended matter from precipitating.Consider hydrochloric acid to be set to add in aerating regulation pond 2
Facility, water can meet an urgent need when being alkaline waste water and add hydrochloric acid and neutralized, waste water is adjusted to neutrality.Then pass through waste water lifting
Pump enters coagulation primary sedimentation tank 3.Suspended matter in 3 coagulation end dosing coagulant of coagulation primary sedimentation tank and flocculation aid make sewage forms wadding
Shape alumen ustum, is precipitated under the effect of gravity, can be removed in waste water largely with pollutant existing for aerosol form, while subtract significantly
The load of light subsequent biochemical section is the critical facility for ensureing that final draining is up to standard.Sewage is entered by flowing automatically after coagulation primary sedimentation tank 3
The level-one biochemical treatment section being made of hydrolysis acidification pool and aerobic biochemical pool.Waste water flows automatically after materialized pretreatment into level-one
Biochemical section, waste water resolve into micromolecular compound after the processing of hydrolysis acidification section, by the compound acidification difficult to degrade of useless water part,
Be conducive to removal of the follow-up aerobe biology to organic matter, while remove a part of COD and BOD, and biochemical unit can be enhanced
Impact resistance.Subsequent waste water enters aerobic biochemical pool, contains a large amount of activated sludge in biochemistry pool, by activated sludge
Under zoogloea and the metabolism of microorganism, a large amount of pollutants removed in sewage.Sewage can be gone in level-one biochemistry section
Except most organic pollution materials, subsequent sewage self-flowing enters sedimentation basin.
Sewage carries out mud-water separation in sedimentation basin 6, and sludge largely flows back into hydrolysis acidification pool supplement sludge quantity, another
Some residual sludge drains into sludge concentration tank 14 and carries out sludge condensation, and supernatant water outlet gravity flow enters ozone oxidation pond 7.Ozone oxygen
Change technology is a kind of oxidation technology improved for the purpose of dystrophy type wastewater biodegradability developed in recent years.Sedimentation basin 6 goes out
Water enters ozone oxidation pond 7.Ozone caused by ozone generator 13 is entered by 7 bottom of ozone oxidation pond, in pond from lower and
It is upper adequately to be contacted with top-down combined sewage, carry out ozone oxidation.Ozone is in the effect come into full contact with waste water
It down can be with the remaining persistent organic pollutants in accelerated decomposition water.
The water outlet gravity flow of ozone oxidation pond 7 enters oxidation-stabilized pond, and the oxidation-stabilized residence time is about 3h, and the residence time is longer
Restricting effect of the residual oxidizing agent to rear biochemical process can more be eliminated.It is built jointly with ozone oxidation pond in oxidation-stabilized pond.It is oxidation-stabilized
Flow-stopping plate in pond is set, makes flow in pulling flow type, sharp-crested weir collect water outlet enter subsequent advanced treating biological aerated filter 8 into
Row is further processed.
Sewage further carries out biochemical treatment in biological aerated filter 8, and high a large amount of volcanoes are filled in biological aerated filter 8
Rock filtrate.Its biodegradability substantially reduces after being handled due to waste water by level-one biochemistry section, and activated sludge is easily lost in, and is aerated
8 easy biofilm of biofilter, effectively prevents the loss of microorganism, improves sludge concentration and treatment effeciency in biochemistry pool.
Organic pollution in waste water is substantially removed.Waste water then flows automatically keeps in into intermediate pool.
The filtered elevator pump of waste water of intermediate pool 9 is lifted into 10 filtration treatment of quartz filter, passes through quartz sand
After filtrate is filtered processing, suspended matter and some of the contaminants in waste water are removed.The water outlet of quartz filter 10 enters activity
Carbon filter 11 further reduces wastewater through organic matter content, and producing water water quality is preferable, it is ensured that standard water discharge is discharged.Sedimentation basin produces
Raw precipitation and biochemical sedimentation basin excess sludge enters sludge concentration tank 14 and is concentrated, then using belt type dewaterer to sludge
Periodically outward transport processing after being carried out dehydrating.
The utility model provides a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device, is adjusted including aeration
Save pond, coagulation primary sedimentation tank, hydrolysis acidification pool, aerobic biochemical pool, sedimentation basin, ozone oxidation pond, biological aerated filter, quartz sand mistake
Filter, active carbon filter；Technique waste water and stripper waste water access aerating regulation pond water inlet end；Aerating regulation pond water outlet with
Coagulation primary sedimentation tank water inlet end connects；Coagulation primary sedimentation tank water outlet, sanitary sewage access hydrolysis acidification pool water inlet end respectively；Hydrolysis acid
Hua Chi water outlets are connect with aerobic biochemical pool water inlet end；Aerobic biochemical pool water outlet is connect with sedimentation basin water inlet end；Sedimentation basin goes out
Water end (W.E.) is connect with ozone oxidation pond water inlet end；Ozone oxidation pond water outlet is connect with biological aerated filter water inlet end；Aeration and biological
Quartz filter water inlet end is accessed in filter tank water outlet；Quartz filter water outlet is connect with active carbon filter water inlet end；
Discharge processed waste water in active carbon filter water outlet.The utility model uses " hydrolysis acidification and aerobic biochemical " technique, effectively
Improve the impact resistance of biochemical section.Meanwhile in level-one biochemistry section, the biodegradability of waste water is relatively preferable, using aerobic biochemical
Technique preferably removes the organic pollution in sewage using the microorganism in activated sludge, meets setting for level-one biochemical process
Meter requirement；The utility model is highly practical, convenient for promoting.
More than, limit in any form is not made the utility model in the only preferred embodiment of the utility model
System；The those of ordinary skill of all industry can swimmingly implement the utility model shown in by specification attached drawing and above；But
It is that all those skilled in the art are not being departed from the range of technical solutions of the utility model, utilizes disclosed above skill
Art content and the equivalent variations of a little variation, modification and evolution made are the equivalent embodiment of the utility model；Meanwhile
Variation, modification and evolution of any equivalent variations that all substantial technologicals according to the utility model make above example etc.,
Still fall within the protection domain of the technical solution of the utility model.
Claims (8)
1. a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device, it is characterised in that：Including aerating regulation pond,
Coagulation primary sedimentation tank, hydrolysis acidification pool, aerobic biochemical pool, sedimentation basin, ozone oxidation pond, biological aerated filter, quartz filter,
Active carbon filter；Technique waste water accesses aerating regulation pond water inlet end with stripper waste water；The aerating regulation pond water outlet
End is connect with the coagulation primary sedimentation tank water inlet end；The hydrolysis acid is accessed in the coagulation primary sedimentation tank water outlet, sanitary sewage respectively
Change pond water inlet end；The hydrolysis acidification pool water outlet is connect with the aerobic biochemical pool water inlet end；The aerobic biochemical pool water outlet
End is connect with the sedimentation basin water inlet end；The sedimentation basin water outlet is connect with ozone oxidation pond water inlet end；The ozone
Oxidation pond water outlet is connect with the biological aerated filter water inlet end；The effluent of aeration biological filter is terminated into the quartz sand
Filter water inlet end；The quartz filter water outlet is connect with the active carbon filter water inlet end；The activated carbon mistake
Discharge processed waste water in filter water outlet.
2. a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device as described in claim 1, feature exist
In：Further include intermediate pool；The effluent of aeration biological filter end is connect with the intermediate pool water inlet end；The intermediate pool
Water outlet is connected to the quartz filter water inlet end.
3. a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device as claimed in claim 2, feature exist
In：Draining detection cell is further included, the draining detection cell is connected to the active carbon filter water outlet；The draining detection cell
Equipped with the detection device of waste water index discharged for detection through the active carbon filter water outlet.
4. a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device as described in claim 1, feature exist
In：Further include cooling tower；The technique waste water is passed through the cooling tower；The cooling tower water outlet and the aerating regulation pond into
Water end (W.E.) connects.
5. such as a kind of sanitary sewage of claim 1-4 any one of them, technique waste water, stripper Wastewater Concentrated device,
It is characterized in that：Further include sludge concentration tank；The sludge from sedimentation tank end and the coagulative precipitation tank spoil disposal end respectively with it is described
Sludge concentration tank feed end connects.
6. a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device as claimed in claim 5, feature exist
In：Further include sludge treatment equipment；The sludge concentration tank discharge end is connect with the sludge treatment equipment feed end.
7. a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device as claimed in claim 6, feature exist
In：The sludge treatment equipment is specially belt type dewaterer；Through the dewatered sludge of the belt type dewaterer by clearing vehicle
It transports.
8. a kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device as claimed in claim 5, feature exist
In：Further include air blower；The air blower respectively with gas circuit in aerating pipelines in the aerating regulation pond, the aerobic biochemical pool
Aerating pipelines connect in pipeline, the biological aerated filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721198596.6U CN207512019U (en) | 2017-09-15 | 2017-09-15 | A kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721198596.6U CN207512019U (en) | 2017-09-15 | 2017-09-15 | A kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207512019U true CN207512019U (en) | 2018-06-19 |
Family
ID=62532703
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721198596.6U Expired - Fee Related CN207512019U (en) | 2017-09-15 | 2017-09-15 | A kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device |
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| Country | Link |
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| CN (1) | CN207512019U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110078318A (en) * | 2019-06-10 | 2019-08-02 | 苏州中色德源环保科技有限公司 | A kind of chemical industry for making chlorine and alkali mother liquor water process and reclaiming system |
| CN113003899A (en) * | 2021-04-28 | 2021-06-22 | 沈阳大学 | Method for treating rhodiola rosea pharmaceutical wastewater |
| CN115626748A (en) * | 2022-11-29 | 2023-01-20 | 深圳永清水务有限责任公司北京分公司 | Sewage treatment system of nitrogen and phosphorus removal |
-
2017
- 2017-09-15 CN CN201721198596.6U patent/CN207512019U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110078318A (en) * | 2019-06-10 | 2019-08-02 | 苏州中色德源环保科技有限公司 | A kind of chemical industry for making chlorine and alkali mother liquor water process and reclaiming system |
| CN113003899A (en) * | 2021-04-28 | 2021-06-22 | 沈阳大学 | Method for treating rhodiola rosea pharmaceutical wastewater |
| CN115626748A (en) * | 2022-11-29 | 2023-01-20 | 深圳永清水务有限责任公司北京分公司 | Sewage treatment system of nitrogen and phosphorus removal |
| CN115626748B (en) * | 2022-11-29 | 2023-08-15 | 深圳永清水务有限责任公司 | Sewage treatment system for denitrification and dephosphorization |
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