CN207845440U - Production waste water mixes purification system with sanitary wastewater - Google Patents
Production waste water mixes purification system with sanitary wastewater Download PDFInfo
- Publication number
- CN207845440U CN207845440U CN201721849055.5U CN201721849055U CN207845440U CN 207845440 U CN207845440 U CN 207845440U CN 201721849055 U CN201721849055 U CN 201721849055U CN 207845440 U CN207845440 U CN 207845440U
- Authority
- CN
- China
- Prior art keywords
- pipe
- pond
- waste water
- septic tank
- purification system
- 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.)
- Active
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 78
- 238000000746 purification Methods 0.000 title claims abstract description 28
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 23
- 239000010865 sewage Substances 0.000 claims abstract description 47
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000009826 distribution Methods 0.000 claims abstract description 17
- 238000004062 sedimentation Methods 0.000 claims abstract description 16
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 10
- 230000001105 regulatory effect Effects 0.000 claims abstract description 10
- 230000015271 coagulation Effects 0.000 claims abstract description 9
- 238000005345 coagulation Methods 0.000 claims abstract description 9
- 239000002699 waste material Substances 0.000 claims abstract description 4
- 239000010802 sludge Substances 0.000 claims description 29
- 238000005507 spraying Methods 0.000 claims description 16
- 239000004744 fabric Substances 0.000 claims description 12
- 238000001035 drying Methods 0.000 claims description 9
- 238000005189 flocculation Methods 0.000 claims description 8
- 230000016615 flocculation Effects 0.000 claims description 8
- 239000000645 desinfectant Substances 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 210000003608 fece Anatomy 0.000 claims description 2
- 238000007667 floating Methods 0.000 claims description 2
- 238000001727 in vivo Methods 0.000 claims description 2
- 239000010871 livestock manure Substances 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 9
- 239000002245 particle Substances 0.000 description 8
- 230000008569 process Effects 0.000 description 7
- 238000004140 cleaning Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000009300 dissolved air flotation Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000003550 marker Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a kind of production waste water to mix purification system with sanitary wastewater comprising combined sewage pond, grid pond, regulating reservoir, coagulation floatation, anaerobic pond, contact-oxidation pool, sedimentation basin and the discharge canal being sequentially communicated；Dining room sewage pipe is connected to the water inlet pipe of oil separator, the outlet pipe connection combined sewage pond of oil separator；Life office sewage pipe is connected to the feed pipe of septic tank, the discharge nozzle connection combined sewage pond of septic tank；Produce waste pipe connection combined sewage pond；The septic tank includes：Septic tank ontology, distribution device, cone bucket, eddy flow paddle, first gas collecting pipe and second gas collecting pipe.The utility model production waste water mixes purification system with sanitary wastewater and is pre-processed to the waste water of separate sources, reduces the purification difficulty in subsequent purification process.
Description
Technical field
The utility model belongs to pharmaceutical factory Comprehensive Treatment For Waste Water technical field, useless with life more particularly to a kind of production waste water
Water mixes purification system.
Background technology
The sewage of pharmaceutical manufacturing factory is life office waste water, dining room waste water and production waste water according to source different demarcation.
Sanitary sewage includes staff canteen, office, employee's life and bath water, and biodegradability is good, and sanitary sewage is through oil separator, change excrement
Stain disease treating stations are accessed after the pretreating process of pond converges further advanced treating with production waste water.
It includes production cleaning waste water, boiler soft brush treatment system acidic and alkaline waste water and water making station waste water to produce waste water.Cleaning is useless
Water is that the corresponding process procedure of preparation workshop carries out medicine bottle and facility cleaning, and a variety of materials and operating table surface, equipment etc. are clear
The cleaning waste water of clean generation, the waste water are intermittent discharge, mainly contain a small amount of drug and residue COD about 150mg/L, SS about 70mg/
L.Boiler water treatment room soft brush treatment system, ion-exchanger has in positive and negative flushing to be discharged containing acid, alkali waste water interruption on a small quantity,
About 2.5 m3/d of water, pH values are 3 ~ 12.The part acidic and alkaline waste water water is smaller, therefore mixing is discharged into Sewage Disposal, for
Sewage disposal system influences little.Pure water machine equipment by the way that municipal water supply is prepared pure water using two steps ro technique, due to
Medicament compartment is higher to the index request of pure water, and the water that the index requests such as conductivity are not achieved cannot act as pure water, the system of pure water
Yield only about 70%.Contain a small amount of TDS in remaining water, is free of other harmful substances, water nonpollution.
Since the major pollutants contained by the waste water of separate sources are different, existing sewage disposal device fails according to useless
The source of water individually pre-processes waste water, causes the processing cost of later stage process and intractability larger.
Utility model content
The purpose of this utility model is to provide a kind of production waste water and mixes purification system with sanitary wastewater.
The technical solution that the utility model solves above-mentioned technical problem is as follows：A kind of production waste water mixes only with sanitary wastewater
Change system comprising the combined sewage pond that is sequentially communicated, grid pond, regulating reservoir, coagulation floatation, anaerobic pond, contact-oxidation pool,
Sedimentation basin and discharge canal；Dining room sewage pipe is connected to the water inlet pipe of oil separator, the outlet pipe connection combined sewage pond of oil separator；It is raw
The feed pipe of office sewage pipe connection septic tank living, the discharge nozzle connection combined sewage pond of septic tank；It is mixed to produce waste pipe connection
Close cesspool；The septic tank includes：Septic tank ontology, distribution device, cone bucket, eddy flow paddle, first gas collecting pipe and second
Gas-collecting pipe；The cone bucket is mounted in septic tank ontology, and cone bucket is opening up；The distribution device is mounted on septic tank sheet
In vivo, it is located at the top of cone bucket, distribution device is connected to feed pipe；The eddy flow paddle is mounted on the lower section of cone bucket outlet；It is described
Discharge nozzle connects pulp pump, and pulp pump is mounted below cone bucket；First gas collecting pipe is mounted on the top of septic tank ontology, the second gas
Body collecting pipe is mounted in the air collecting chamber that cone bucket is formed with septic tank ontology.
The utility model produces waste water and mixes purification system with sanitary wastewater as described above, further, the cloth of septic tank
Expect that device includes cloth ring and stuff-spraying pipe, stuff-spraying pipe is connected on the cloth ring.
The utility model produces waste water and mixes purification system with sanitary wastewater as described above, further, in cloth ring institute
In the horizontal plane, stuff-spraying pipe all tilts in the direction of the clock or stuff-spraying pipe all tilts counterclockwise；In vertical plane
On, stuff-spraying pipe tilts down.
The utility model produces waste water and mixes purification system with sanitary wastewater as described above, further, the coagulation gas
Floating pond includes interconnected the first flocculation basin and the second flocculation basin.
The utility model produces waste water and mixes purification system with sanitary wastewater as described above, further, the sedimentation basin
For inclined-tube sedimentation tank, sludge hopper is set in the bottom of inclined-tube sedimentation tank.
The utility model produces waste water and mixes purification system with sanitary wastewater as described above, further includes sludge further
Mummifying pool, sludge pump is respectively provided in regulating reservoir, anaerobic pond, contact-oxidation pool and sedimentation basin, and the discharge nozzle of sludge pump is connected to sludge
Mummifying pool；The sludge drying pond connects disinfectant adding set.
The utility model has the beneficial effects that：
The utility model production waste water mixes purification system with sanitary wastewater and is pre-processed to the waste water of separate sources, drops
Purification difficulty in low subsequent purification process.
Description of the drawings
By being described in detail made by conjunction with the following drawings, the above-mentioned and/or otherwise advantage of the utility model will
It becoming more apparent upon and is easier to understand, these attached drawings are only schematical, are not intended to limit the utility model, wherein：
Fig. 1 is that a kind of production waste water of embodiment mixes purification system schematic diagram with sanitary wastewater；
Fig. 2 is a kind of septic tank vertical cross section schematic diagram of embodiment of the utility model；
Fig. 3 is a kind of horizontal profile schematic diagram of embodiment of the utility model.
In attached drawing, parts list represented by the reference numerals are as follows：
1, septic tank ontology, 2, feed pipe, 3, cloth ring, 4, stuff-spraying pipe, 5, cone bucket, 6, eddy flow paddle, 7, pulp pump, 8, discharging
Pipe, 9, second gas collecting pipe, 10, first gas collecting pipe, 11, Anaerobic Treatment chamber, 12, distribution cavity.
Specific implementation mode
Hereinafter, the production waste water for describing the utility model with reference to the accompanying drawings mixes the reality of purification system with sanitary wastewater
Apply example.
The embodiment recorded herein is the specific specific implementation mode of the utility model, for illustrating the utility model
Design, is explanatory and illustrative, should not be construed as the limit to the utility model embodiment and the scope of the utility model
System.In addition to the embodiment recorded herein, those skilled in the art can also be based on the application claims and specification institute is public
For the content opened using obvious other technical solutions, these technical solutions include doing using the embodiment to recording herein
Go out the technical solution of any obvious substitutions and modifications.
The attached drawing of this specification is schematic diagram, aids in illustrating the design of the utility model, it is schematically indicated each section
Shape and its correlation.It note that the structure of each component for the ease of clearly showing the utility model embodiment, respectively
It is not drawn according to identical ratio between attached drawing.Identical reference marker is for indicating identical part.
Fig. 1 shows that a kind of production waste water of embodiment of the utility model mixes purification system with sanitary wastewater comprising according to
Combined sewage pond, grid pond, regulating reservoir, coagulation floatation, anaerobic pond, contact-oxidation pool, sedimentation basin and the discharge canal of secondary connection；
Dining room sewage pipe is connected to the water inlet pipe of oil separator, the outlet pipe connection combined sewage pond of oil separator；Life office sewage pipe connects
The discharge nozzle 8 of the feed pipe 2 of Tonghua manure pit, septic tank is connected to combined sewage pond；Produce waste pipe connection combined sewage pond；
Dining room sewage and daily sewage in sanitary sewage are introduced through individual sewage conduct creates oil separator, septic tank
It handles respectively, improves biodegradability, reduce later stage Sewage Disposal load；After pretreated, mixing is discharged into later stage combined sewage
Pond.
As shown in Figures 2 and 3, septic tank includes：Septic tank ontology 1, distribution device, cone bucket 5, eddy flow paddle 6, first gas
Collecting pipe 10 and second gas collecting pipe 9；Cone bucket 5 is mounted in septic tank ontology 1, and cone bucket 5 is opening up；Distribution device is installed
In septic tank ontology 1, it is located at the top of cone bucket 5, distribution device is connected to feed pipe 2；Eddy flow paddle 6 is exported mounted on cone bucket 5
Lower section；Discharge nozzle 8 connects pulp pump 7, and pulp pump 7 is mounted on 5 lower section of cone bucket；First gas collecting pipe 10 is mounted on septic tank ontology
1 top, second gas collecting pipe 9 are mounted in the air collecting chamber that cone bucket 5 is formed with septic tank ontology 1.
Above cone bucket and space that septic tank ontology is formed is distribution cavity 12, below distribution cavity cone bucket with septic tank ontology
The space of formation is Anaerobic Treatment chamber 11.When above-mentioned septic tank operation, waste water enters distribution device by feed pipe, and then realizes
The cloth of waste water；Smaller impurities sink down speed in waste water faster, is exported by cone bucket and falls and utilize the active set of eddy flow paddle
In to the bottom of Anaerobic Treatment chamber center, liquid carries out the anaerobic fermentation of microorganism in Anaerobic Treatment chamber, and the gas of generation is logical
It crosses first gas collecting pipe and second gas collecting pipe is exported and collected.
In the utility model above-described embodiment：
Oil separator can remove the greasy dirt in the waste water of dining room, and later stage sewage disposal system pipeline and equipment is avoided to be blocked；
Biochemical sewage is improved, later stage Sewage Disposal load is reduced.
Septic tank removes suspension organic matter in sanitary sewage using the principle of precipitation and anaerobic fermentation.Septic tank has
The function of bulky grain sundries and suspended matter is retained, and there is certain anaerobism effect.
Waste water can retain the small granular suspended matters in sewage, further decrease dirt by the fine fack in grid pond
Contaminate object factor concentration.
Since the water of sewage, water quality are all continually changing at any time, there are peak flow and ebb flow, also there is height
Cmax and ebb concentration.Flow and the uneven of concentration often bring many difficulties to processing equipment, or make it that can not protect
It holds and is run under optimal process conditions, or can not work in short-term, or even destroyed.In order to improve sewage disposal system
Water and water quality need to be adjusted in operating condition, and the major way of adjusting is exactly that sewage regulating reservoir is arranged.Regulating reservoir is intended to
Sewerage amount of inlet water is controlled, to realize even load, the stable operation of sewage disposal system.Regulating reservoir sewage is through submersible sewage pump
It is promoted to subsequent processing facility.
Coagulation floatation includes interconnected the first flocculation basin and the second flocculation basin.First flocculation basin is firstly added hydrogen-oxygen
Change sodium and PH is adjusted to 8.5-9, adds aluminium polychloride（PAC）, PAC can be with colloid small in water, suspended matter very after adding
It mutually collides and bonds to larger molecular organics, eliminate the electrostatic repulsion between colloidal solid so that colloidal particles become unstable
Determine state, and make particle coalesce to form larger particles, to achieve the purpose that precipitation.Compared with similar other products, particle shape of wadding a quilt with cotton
It is weighed greatly at very fast and particle, it is less to add rear original water basicity reduction.PAM is added in second flocculation basin, and PAM is a kind of organic high score
Sub- coagulant after being dissolved in water, will produce poly-condensation and hydrolysis and form the high polymer of linear structure, this structure makes line
Colloidal solid is respectively adsorbed at both ends, plays cohesive bridging action between two particles apart from each other, so that particle is gradually become larger, shape
At the floccule body of bulky grain（Alumen ustum）, neutralized colloidal particles is helped further to agglomerate.Waste water flows automatically through coagulation reactor
Into air supporting consersion unit, this air supporting unit is pressurized dissolved air flotation, and airfloat equipment is pumped by pressure air-dissolving and generates micro-bubble
So that the sludge that coagulation reactor generates is bubbled through the water column, scraped top sludge by scum board, into sludge drying pond, sludge warp
Outward transport is handled after desiccation, and clear water is flowed out by lower part, has the function that purified water.
Anaerobic waste water biological treatment refers to passing through anaerobic organism under condition of free-dioxygen（Including simultaneous oxygen biology）Effect,
Various complicated organic molecules in waste water are converted to the process of the substances such as methane, carbon dioxide, also referred to as anaerobic digestion.Detest
Hydraulic detention time is counted for 24 hours in oxygen pond, built-in elastic filler.Water inlet realizes effective waterpower using bottom of pond portion perforation pipe pressure water distribution
Residence time；And to prevent sludge settling, anaerobic sludge is made to be in suspended state.Need to control the water temperature of anaerobic pond, pH value is answered
Between 6.5-7.8, dissolved oxygen concentration is preferably in 0.5mg/L.
Contact-oxidation pool is to build aerobic environment, is conducive to support microorganism growth.Water reuse aerobic activated sludge is inhaled
Attached, degradation of organic substances is nitrified by organophosphor oxidation processes, while by ammonia nitrogen, and nitrification liquid flows back into anaerobic pond.Operation principle
For：Filler is set in aeration tank, as the carrier of biomembrane.Pending waste water is flowed through after oxygenation with certain flow rate
Filler, with biofilm contact, the activated sludge collective effect of biomembrane and suspension has the function that purify waste water.
Sewage after catalytic oxidation by being discharged into sedimentation basin, by way of gravitational settling, by the fine suspension in water
It is gathered in bottom of pond, to further decrease the concentration of suspension in water.Sludge reflux pump, extra sludge reflux to water is arranged in bottom of pond
Solution acidification pool is discharged into sludge drying pond.
It is mixed in purification system with sanitary wastewater in a kind of production waste water of preferred embodiment, the distribution device packet of septic tank
Cloth ring 3 and stuff-spraying pipe 4 are included, stuff-spraying pipe 4 is connected on cloth ring 3；The institute of cloth ring 3 in the horizontal plane, stuff-spraying pipe 4 is all pressed
It tilts clockwise or stuff-spraying pipe 4 all tilts counterclockwise；In vertical plane, stuff-spraying pipe 4 tilts down.Profit
With the distribution device of above structure, the waste water of circinate movement can be formed, contamination precipitation speed in waste water is conducive to.
It is mixed in purification system with sanitary wastewater in a kind of production waste water of preferred embodiment, sedimentation basin is tube settling
Sludge hopper is arranged in the bottom of inclined-tube sedimentation tank in pond.
It is mixed in purification system with sanitary wastewater in a kind of production waste water of preferred embodiment, further includes sludge drying pond,
Sludge pump is respectively provided in regulating reservoir, anaerobic pond, contact-oxidation pool and sedimentation basin, the discharge nozzle 8 of sludge pump is connected to sludge drying pond；
Sludge drying pond connects disinfectant adding set.
Each technical characteristic of above-mentioned disclosure is not limited to disclosed and other feature combination, and those skilled in the art are also
Other combinations between each technical characteristic can be carried out according to the purpose of invention, be subject to the purpose for realizing the utility model.
Claims (6)
1. a kind of production waste water mixes purification system with sanitary wastewater, which is characterized in that including be sequentially communicated combined sewage pond,
Grid pond, regulating reservoir, coagulation floatation, anaerobic pond, contact-oxidation pool, sedimentation basin and discharge canal；Dining room sewage pipe be connected to every
The water inlet pipe of oil sump, the outlet pipe connection combined sewage pond of oil separator；Life office sewage pipe is connected to the feed pipe of septic tank, changes
The discharge nozzle connection combined sewage pond of manure pit；Produce waste pipe connection combined sewage pond；The septic tank includes：Septic tank sheet
Body, distribution device, cone bucket, eddy flow paddle, first gas collecting pipe and second gas collecting pipe；The cone bucket is mounted on septic tank sheet
In vivo, cone bucket is opening up；The distribution device be mounted on septic tank ontology in, be located at cone bucket top, distribution device with into
Expects pipe is connected to；The eddy flow paddle is mounted on the lower section of cone bucket outlet；The discharge nozzle connects pulp pump, and pulp pump is mounted under cone bucket
Side；First gas collecting pipe is mounted on the top of septic tank ontology, and second gas collecting pipe is mounted on cone bucket and septic tank ontology
In the air collecting chamber of formation.
2. production waste water according to claim 1 mixes purification system with sanitary wastewater, which is characterized in that the cloth of septic tank
Expect that device includes cloth ring and stuff-spraying pipe, stuff-spraying pipe is connected on the cloth ring.
3. production waste water according to claim 2 mixes purification system with sanitary wastewater, which is characterized in that in cloth ring institute
In the horizontal plane, stuff-spraying pipe all tilts in the direction of the clock or stuff-spraying pipe all tilts counterclockwise；In vertical plane
On, stuff-spraying pipe tilts down.
4. production waste water according to claim 1 mixes purification system with sanitary wastewater, which is characterized in that the coagulation gas
Floating pond includes interconnected the first flocculation basin and the second flocculation basin.
5. production waste water according to claim 1 mixes purification system with sanitary wastewater, which is characterized in that the sedimentation basin
For inclined-tube sedimentation tank, sludge hopper is set in the bottom of inclined-tube sedimentation tank.
6. produce waste water according to claim 1-5 any one of them mixes purification system with sanitary wastewater, which is characterized in that also
Including sludge drying pond, sludge pump, the discharge nozzle of sludge pump are respectively provided in regulating reservoir, anaerobic pond, contact-oxidation pool and sedimentation basin
It is connected to sludge drying pond；The sludge drying pond connects disinfectant adding set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721849055.5U CN207845440U (en) | 2017-12-26 | 2017-12-26 | Production waste water mixes purification system with sanitary wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721849055.5U CN207845440U (en) | 2017-12-26 | 2017-12-26 | Production waste water mixes purification system with sanitary wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207845440U true CN207845440U (en) | 2018-09-11 |
Family
ID=63418698
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721849055.5U Active CN207845440U (en) | 2017-12-26 | 2017-12-26 | Production waste water mixes purification system with sanitary wastewater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207845440U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109502923A (en) * | 2018-12-29 | 2019-03-22 | 苏州泥宝环境科技有限公司 | A kind of sludge anhydration burning waste water treatment process |
| CN110092545A (en) * | 2019-05-21 | 2019-08-06 | 江苏尚裕润环保工程有限公司 | A kind of nitrogenous processing exhaust system of coating wastewater |
-
2017
- 2017-12-26 CN CN201721849055.5U patent/CN207845440U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109502923A (en) * | 2018-12-29 | 2019-03-22 | 苏州泥宝环境科技有限公司 | A kind of sludge anhydration burning waste water treatment process |
| CN110092545A (en) * | 2019-05-21 | 2019-08-06 | 江苏尚裕润环保工程有限公司 | A kind of nitrogenous processing exhaust system of coating wastewater |
| CN110092545B (en) * | 2019-05-21 | 2022-07-12 | 江苏尚裕润环保工程有限公司 | Coating wastewater nitrogen-containing treatment and discharge system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109179910A (en) | A kind of domestic sewage treatment process | |
| CN106565017B (en) | A kind of bicirculating denitrogenation dephosphorizing waste water treatment system and its method | |
| CN101434437B (en) | Processing method for wastewater from cephalosporin synthesis pharmaceutical production | |
| CN106242190A (en) | A kind of modularity sewage disposal system | |
| CN101468863A (en) | Hospital waste water purification system | |
| CN107311405A (en) | Urban sewage treatment system and technique | |
| CN106977059A (en) | A kind of new and effective sewage disposal system and method | |
| CN105967435A (en) | Double-circulation nitrogen and phosphorus removal wastewater treatment system and process | |
| CN105884154A (en) | Novel combined process for treating chemical wastewater | |
| CN104591473A (en) | Advanced nitrogen and phosphorus removal technology | |
| CN109970194A (en) | It is a kind of integrate Ao Baoer, biological multiplication, MBBR, MBR diversification technique sewage treatment pot | |
| CN204509049U (en) | Integration Combined sewage treatment system | |
| CN108975632A (en) | A kind of integration distributing high-efficiency wastewater treatment system | |
| CN209292178U (en) | A kind of Sewage Disposal suitable for biological industry garden the dirty water decontamination handles | |
| CN105668946B (en) | A kind of Cattle Wastewater processing system and processing method | |
| CN214060278U (en) | Mariculture tail water discharging device | |
| CN207845440U (en) | Production waste water mixes purification system with sanitary wastewater | |
| CN108467154A (en) | A kind of SBR waste water treatment process of soybean lecithin production | |
| CN202543002U (en) | Sewage treatment system | |
| CN109824212A (en) | An aquaculture wastewater treatment system | |
| CN213327183U (en) | A public toilet sewage integrated treatment system | |
| CN105884151B (en) | Method for treating industrial wastewater by combined process | |
| CN105948411B (en) | A kind of technique for treating industrial wastewater | |
| CN103819062A (en) | MBR (membrane biological reactor) sewage treatment equipment for integrated fluidizing pool | |
| CN208933187U (en) | A kind of integration distributing high-efficiency wastewater treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |