CN105585218B - Wastewater from mechanical industry treatment process - Google Patents
Wastewater from mechanical industry treatment process Download PDFInfo
- Publication number
- CN105585218B CN105585218B CN201610018843.3A CN201610018843A CN105585218B CN 105585218 B CN105585218 B CN 105585218B CN 201610018843 A CN201610018843 A CN 201610018843A CN 105585218 B CN105585218 B CN 105585218B
- Authority
- CN
- China
- Prior art keywords
- waste water
- pond
- wastewater
- water
- sedimentation basin
- 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 79
- 238000011282 treatment Methods 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims abstract description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 238000004062 sedimentation Methods 0.000 claims abstract description 23
- 238000001914 filtration Methods 0.000 claims abstract description 9
- 238000006243 chemical reaction Methods 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 238000009300 dissolved air flotation Methods 0.000 claims abstract description 6
- 239000013618 particulate matter Substances 0.000 claims abstract description 6
- 238000000926 separation method Methods 0.000 claims abstract description 6
- 239000010802 sludge Substances 0.000 claims description 24
- 239000000126 substance Substances 0.000 claims description 14
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- 241001148470 aerobic bacillus Species 0.000 claims description 9
- 239000000945 filler Substances 0.000 claims description 6
- 239000012535 impurity Substances 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 238000012856 packing Methods 0.000 claims description 5
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 238000004659 sterilization and disinfection Methods 0.000 claims description 5
- 239000000725 suspension Substances 0.000 claims description 5
- 238000011068 loading method Methods 0.000 claims description 4
- 229920002521 macromolecule Polymers 0.000 claims description 4
- 230000001954 sterilising effect Effects 0.000 claims description 4
- 238000005273 aeration Methods 0.000 claims description 3
- 238000000247 postprecipitation Methods 0.000 claims description 3
- 230000002708 enhancing effect Effects 0.000 claims description 2
- 230000003311 flocculating effect Effects 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims description 2
- 230000006641 stabilisation Effects 0.000 abstract description 2
- 238000011105 stabilization Methods 0.000 abstract description 2
- 239000010865 sewage Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000004060 metabolic process Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Physical Water Treatments (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The present invention provides a kind of wastewater from mechanical industry treatment process, after waste water retains large particulate matter by grid pond, demulsification reaction dephosphorization is carried out into demulsification pond, dissolved air flotation is carried out subsequently into air floatation machine, anaerobic pond, anoxic pond, aerobic tank are sequentially entered again carries out biochemical treatment, be separated by solid-liquid separation subsequently into sedimentation basin, finally through filtering, sterilize it is up to standard after discharge.The processing technological flow of wastewater from mechanical industry of the present invention is simple, operating cost is low, safe and reliable to operation, water stabilization is up to standard.
Description
Technical field
The present invention relates to sewage treatment field, especially a kind of wastewater from mechanical industry treatment process.
Background technology
Mechanical processing sewage main source is that metallic wastewaters, the waste water such as workshop manufacture cleaning iron content waste water include mainly：It washes
It washs outside the waste water oil removals such as waste water, cleaning waste water, cleaning ground waste water, emulsifying liquid waste water, also containing there are many grease, pH value
In acidity, COD high, biodegradability is poor.Water quality is more complex, is unable to direct emission.It is huge to be machined water consumption, how to utilize useless
It is engineering difficult point that water, which carries out recovery processing,.
Invention content
That the purpose of the present invention is to provide a kind of flows is simple, operating cost is low, safe and reliable to operation, water stabilization is up to standard
Wastewater from mechanical industry treatment process.
To achieve the above object, wastewater from mechanical industry treatment process of the invention, waste water retain bulky grain by grid pond
After substance, demulsification reaction dephosphorization is carried out into demulsification pond, carries out dissolved air flotation subsequently into air floatation machine, then sequentially enter anaerobism
Pond, anoxic pond, aerobic tank carry out biochemical treatment, are separated by solid-liquid separation subsequently into sedimentation basin, finally up to standard by filtering, sterilizing
After discharge.
Further, specific process step is as follows：
（1）Pretreatment：Waste water enters grid pond and retains large particulate matter by grid, then from regulating reservoir is flowed into equilibrium water
Matter water, makes waste water even into subsequent processing units；
（2）Demulsification reaction dephosphorization：Waste water enters demulsification pond, and CaCl is put into demulsification pond2, add PAC and flocculate
Sedimentation；
（3）Dissolved air flotation：Waste water enters air floatation machine, and the suspension flco in waste water is adhered to the microbubble of air floatation machine generation
On, it climbs up on top of the water with bubble, forms dross and scrape removing dross；
（4）AAO technique biochemical treatments：Waste water sequentially enters anaerobic pond, anoxic pond, aerobic tank, and by the mixing of aerobic tank
Liquid and the sludge in post precipitation pond flow back into anoxic pond, the wherein built-in flexible biologic packing material of anaerobic pond, anoxic pond simultaneously, will give up
Deliquescent macromolecule, hard-degraded substance are decomposed into low molecule, degradable substance in water, improve the ratio of BOD/COD, enhancing
Biodegradability；Then waste water carries out Aerobic Process for Treatment from aerobic tank is flowed into, and the elastic biological filler installed in aerobic tank is attached with
Oxygen bacterium is handled the organic substance in waste water by aerobic bacteria and the extraneous oxygen provided；
（5）It is separated by solid-liquid separation：From flowing into sedimentation basin, solid impurity caused by biochemical treatment can flow out waste water with waste water, sink
Shallow lake pond carries out settlement treatment to solid impurity；Meanwhile the activated sludge that biochemical treatment generates is sunk in sedimentation basin with waste water
It forms sediment and detaches, most of activated sludge flows back into anoxic pond, and excess sludge is discharged to sludge concentration tank and carries out concentration；
（6）Filtering：Waste water is sent to pressure filter by water pump and is filtered from intermediate pool is flowed by waste water；
（7）Sterilize water storage：Waste water by filtering carries out disinfection in sterilization pool, final qualified discharge water storage.
The anaerobic pond, anoxic pond effective stay time are 10~12 hours.
The space network of elastic biological filler for the benefit of aerobic bacteria attachment in the aerobic tank.
The oxygen provided needed for the aerobic tank makes in such a way that air blower carries out aeration aerating to waste water in aerobic tank
Dissolved oxygen be maintained at 2.0mg/L.
The sedimentation basin is vertical-flow inclined-tube sedimentation tank, and sedimentation basin surface loading is 1.0m3/m2.h, hydraulic detention time is
4.5h。
The substantive distinguishing features of the present invention and progress are：
The application wastewater from mechanical industry treatment process has the beneficial effect that：
（1）First using demulsification reaction dephosphorization, air floatation machine is then taken to remove the suspended matter in waste water, effective purified water
Matter.
（2）Using AAO technique biochemical treatments, 1. so that flow is simple, structures are few, and capital cost is greatly saved, and
Operating cost is low, and floor space is small；2. using in raw wastewater carbonaceous organic material and endogenous metabolism product as carbon source, save and add
The expense of outer carbon source, and the C/N ratios of raising are obtained, to ensure the abundant progress of denitrification；3. anoxic pond aerobic tank it
Before, since denitrification consumes a part of organic matter in waste water, the organic loading of aerobic tank had not only been alleviated in this way, but also can improve
The settling property of activated sludge is in favor of controlling sludge bulking, and the basicity that denitrification process generates can compensate nitrifying process
Consumption to basicity.
（3）High degree of automation, effluent characteristics are stablized.
Description of the drawings
Fig. 1 is the process flow diagram of the present invention.
Specific implementation mode
Below in conjunction with drawings and examples, the present invention is described further.
The wastewater from mechanical industry treatment process of the present invention, specific process step are as follows：
（1）Pretreatment：Waste water enters grid pond and retains large particulate matter by grid, and large particulate matter is avoided to enter sewage
Processing system results in blockage.Make waste water even into subsequent processing units with Balance Water Quality water from regulating reservoir is flowed into again.
It is arranged by regulating reservoir, energy fully Balance Water Quality, water enable sewage is relatively uniform to enter subsequent processing units,
The shock resistance for improving whole system reduces the design scale of processing unit.Advantageously reduce operating cost and variation water quality band
The influence come.In view of wastewater from mechanical industry coefficient of variation is bigger, regulating reservoir designs hydraulic detention time 24 hours.
（2）Demulsification reaction dephosphorization：Waste water enters demulsification pond, and CaCl is put into demulsification pond2, add PAC and flocculate
Sedimentation.
Because of mechanic factory workers, there are many cathode active agent on surface, has a large amount of phosphorus reagent, waste water that must first be broken
Breast reaction.CaCl2Generation calcium phosphate is carried out, water is not readily dissolved in, is added after PAC carries out biochemical flocculating setting and goes dephosphorization.
（3）Dissolved air flotation：Waste water enters air floatation machine, and the suspension flco in waste water is adhered to the microbubble of air floatation machine generation
On, it climbs up on top of the water with bubble, forms dross and scrape removing dross.
Air floatation machine be using air and water under-fixed pressure condition, so that gas is greatly dissolved in water, make every effort to
In saturation state, is then discharged the molten carbonated drink of pressure is formed by by depressurizing, a large amount of micro air bubble is generated, and in waste water
Suspension flco come into full contact with, so that suspension flco is adhered on micro air bubble, climb up on top of the water with bubble, formed dross, scrape
Removing dross can reach purpose of purifying the water quality.
（4）AAO technique biochemical treatments：Waste water sequentially enters anaerobic pond, anoxic pond, aerobic tank, and by the mixing of aerobic tank
Liquid and the sludge in post precipitation pond flow back into anoxic pond, the wherein built-in flexible biologic packing material of anaerobic pond, anoxic pond simultaneously, will give up
Deliquescent macromolecule, hard-degraded substance are decomposed into low molecule, degradable substance in water, improve the ratio of BOD/COD, increase
Strong biodegradability；Then waste water carries out Aerobic Process for Treatment from aerobic tank is flowed into, the elastic biological filler attachment installed in aerobic tank
There is aerobic bacteria, the organic substance in waste water is handled by aerobic bacteria and the extraneous oxygen provided.
AAO techniques are a kind of front establishment methods, belong to single-stage sludge denitrification technique, i.e., only there are one sludge recirculation systems
It is alternately under aerobic and anoxia condition with the microorganism species of mixed-liquor return system, mixed liquor, in organic concentration height
Or its different effect will be played when low respectively.Its technological process is the advanced anoxic pond of waste water, then into aerobic tank, and by aerobic tank
Mixed liquor and sedimentation basin sludge simultaneously flow back into anoxic pond.
The built-in flexible biologic packing material of anaerobic pond, anoxic pond, it acts as by deliquescent macromolecule in waste water, difficult to degrade
Substance decomposition is low molecule, degradable substance enhances biodegradability to improve the ratio of BOD/COD, is subsequent
Aerobic Process for Treatment provides condition, and anaerobic pond, anoxic pond effective stay time are 10~12 hours, COD removal rates about 30~60%.It is useless
Water carries out Aerobic Process for Treatment from aerobic tank is flowed into.The built-in flexible biologic packing material of aerobic tank, the elastic biological filler are for the benefit of aerobic
The space network of bacterium attachment, has good gas distribution distribution performance, the treatment effect of aerobic tank, netted knot is greatly improved
Structure can make aerobic bacteria be easy to adhere to, and be handled the organic substance in water by aerobic bacteria after biofilm, and the external world to be provided
Substance be oxygen, the present invention using air blower to waste water carry out aeration aerating, so that contact-oxidation pool dissolved oxygen is maintained at
The level of 2.0mg/L.COD and BOD is able to 80% or more removal.
（5）It is separated by solid-liquid separation：From flowing into sedimentation basin, solid impurity caused by biochemical treatment can flow out waste water with waste water, sink
Shallow lake pond carries out settlement treatment to solid impurity；Meanwhile the activated sludge that biochemical treatment generates is sunk in sedimentation basin with waste water
It forms sediment and detaches, most of activated sludge flows back into anoxic pond, and excess sludge is discharged to sludge concentration tank and carries out concentration.
It is 1.0m that sedimentation basin, which uses vertical-flow inclined-tube sedimentation tank, sedimentation basin surface loading,3/m2.h, hydraulic detention time is
4.5h.Also there are one the process of metabolism, the biomembrane of aging death can fall off and be drifted out with water the microorganism of aerobic tank, sink
Shallow lake pond carries out settlement treatment to the biomembrane to fall off.Meanwhile sedimentation basin makes activated sludge and waste water carry out precipitation to detach, wherein greatly
To anoxic pond, excess sludge is discharged to sludge concentration tank and carries out concentration amount of activated sludge reflux.
（6）Filtering：Waste water is sent to pressure filter by water pump and is filtered from intermediate pool is flowed by waste water.
（7）Sterilize water storage：Waste water by filtering carries out disinfection in sterilizing tank, final qualified discharge water storage.
Claims (5)
1. a kind of wastewater from mechanical industry treatment process, which is characterized in that after waste water retains large particulate matter by grid pond, enter
Demulsification pond carries out demulsification reaction dephosphorization, and dissolved air flotation is carried out subsequently into air floatation machine, then sequentially enters anaerobic pond, anoxic pond, good
Oxygen pond carry out biochemical treatment, be separated by solid-liquid separation subsequently into sedimentation basin, finally through filtering, sterilize it is up to standard after discharge；
Specific process step is as follows：
（1）Pretreatment：Waste water enters grid pond and retains large particulate matter by grid, then from regulating reservoir is flowed into Balance Water Quality water
Amount, makes waste water even into subsequent processing units；
（2）Demulsification reaction dephosphorization：Waste water enters demulsification pond, and CaCl is put into demulsification pond2, add PAC and carry out flocculating setting；
（3）Dissolved air flotation：Waste water enters air floatation machine, and the suspension flco in waste water is adhered on the microbubble of air floatation machine generation, with
Bubble climbs up on top of the water together, forms dross and scrapes removing dross；
（4）AAO technique biochemical treatments：Waste water sequentially enters anaerobic pond, anoxic pond, aerobic tank, and by the mixed liquor of aerobic tank and
The sludge in post precipitation pond flows back into anoxic pond, the wherein built-in flexible biologic packing material of anaerobic pond, anoxic pond simultaneously, will be in waste water
Deliquescent macromolecule, hard-degraded substance are decomposed into low molecule, degradable substance, improve the ratio of BOD/COD, and enhancing can give birth to
The property changed；Then waste water carries out Aerobic Process for Treatment from aerobic tank is flowed into, and the elastic biological filler installed in aerobic tank is attached with aerobic bacteria,
The organic substance in waste water is handled by aerobic bacteria and the extraneous oxygen provided；
（5）It is separated by solid-liquid separation：Waste water is from flowing into sedimentation basin, and solid impurity caused by biochemical treatment can be flowed out with waste water, sedimentation basin
Settlement treatment is carried out to solid impurity；Meanwhile the activated sludge that biochemical treatment generates carries out precipitation point in sedimentation basin with waste water
From most of activated sludge flows back into anoxic pond, and excess sludge is discharged to sludge concentration tank and carries out concentration；
（6）Filtering：Waste water is sent to pressure filter by water pump and is filtered from intermediate pool is flowed by waste water；
（7）Sterilize water storage：Waste water by filtering carries out disinfection in sterilization pool, final qualified discharge water storage.
2. wastewater from mechanical industry treatment process according to claim 1, it is characterised in that：The anaerobic pond, anoxic pond have
It is 10~12 hours to imitate the residence time.
3. wastewater from mechanical industry treatment process according to claim 1, it is characterised in that：Elasticity in the aerobic tank is raw
The space network of object filler for the benefit of aerobic bacteria attachment.
4. wastewater from mechanical industry treatment process according to claim 1, it is characterised in that：It is provided needed for the aerobic tank
Oxygen makes the dissolved oxygen in aerobic tank be maintained at 2.0mg/L in such a way that air blower carries out aeration aerating to waste water.
5. wastewater from mechanical industry treatment process according to claim 1, it is characterised in that：The sedimentation basin is vertical-flow oblique
Pipe sedimentation basin, sedimentation basin surface loading are 1.0m3/m2H, hydraulic detention time 4.5h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610018843.3A CN105585218B (en) | 2016-01-13 | 2016-01-13 | Wastewater from mechanical industry treatment process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610018843.3A CN105585218B (en) | 2016-01-13 | 2016-01-13 | Wastewater from mechanical industry treatment process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105585218A CN105585218A (en) | 2016-05-18 |
| CN105585218B true CN105585218B (en) | 2018-11-02 |
Family
ID=55925165
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610018843.3A Active CN105585218B (en) | 2016-01-13 | 2016-01-13 | Wastewater from mechanical industry treatment process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105585218B (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106007208A (en) * | 2016-07-04 | 2016-10-12 | 衢州市晟煜化工有限公司 | Chemical wastewater purification treatment method |
| CN106186580A (en) * | 2016-08-31 | 2016-12-07 | 武汉东川自来水科技开发有限公司 | A kind of emulsion sewage disposal system and processing method |
| CN106587497A (en) * | 2016-12-07 | 2017-04-26 | 河池市技术开发中心 | Machining wastewater treatment system |
| CN107032564A (en) * | 2017-06-21 | 2017-08-11 | 孙东光 | A kind of fecal treatment equipment and method |
| CN107585972A (en) * | 2017-10-27 | 2018-01-16 | 山东三星玉米产业科技有限公司 | Grease processing waste water handling process and device |
| RU187325U1 (en) * | 2018-06-19 | 2019-03-01 | Общество с ограниченной ответственностью "ИНФРАЭКОПРОЕКТ" | SEWAGE TREATMENT DEVICE |
| CN109437494A (en) * | 2018-12-26 | 2019-03-08 | 苏州苏沃特环境科技有限公司 | A kind of processing unit and method of water-jet loom sewage |
| CN110759584A (en) * | 2019-10-10 | 2020-02-07 | 天津中冀源环保科技有限公司 | Emulsion wastewater treatment process |
| CN111559827B (en) * | 2020-04-23 | 2021-06-15 | 南京禹智智能科技有限公司 | Biological treatment method of desulfurization and denitrification tail liquid |
| CN112607975A (en) * | 2020-12-25 | 2021-04-06 | 苏州市环境保护有限公司 | Comprehensive treatment method of cutting fluid wastewater |
| CN113788584A (en) * | 2021-09-24 | 2021-12-14 | 惠州市吉邦精密技术有限公司 | Machining wastewater treatment method and industrial wastewater purification method |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1931749A (en) * | 2006-09-27 | 2007-03-21 | 山东贵和显星纸业股份有限公司 | Paper-making effluent purifying treatment process |
| CN101327996A (en) * | 2007-06-22 | 2008-12-24 | 宝山钢铁股份有限公司 | Treating process of dilute emulsified oily watewater |
| CN102557341A (en) * | 2011-12-26 | 2012-07-11 | 上海集惠环保科技发展有限公司 | Treatment method of high-concentration emulsion waste water |
| CN102942285A (en) * | 2012-11-06 | 2013-02-27 | 中国石油集团工程设计有限责任公司 | Sewage treatment system and method for natural gas purifying factory in H2S-containing gas field |
| CN103395931A (en) * | 2013-08-02 | 2013-11-20 | 江苏和顺环保股份有限公司 | Processing technology for waste emulsified liquid and machining wastewater |
| CN103864266A (en) * | 2014-03-24 | 2014-06-18 | 江苏省环境科学研究院 | Waste-paper papermaking wastewater and sludge recycling method |
| CN104370418A (en) * | 2014-11-10 | 2015-02-25 | 辽宁省石油化工规划设计院有限公司 | Treatment method of chemical sewage |
| CN104803548A (en) * | 2015-04-01 | 2015-07-29 | 浙江碧源环保科技有限公司 | Treating and recycling zero-emission technology and equipment for coking phenol-cyanogen wastewater |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103068748A (en) * | 2010-08-18 | 2013-04-24 | 西门子工业公司 | Contact-stabilization/prime-float hybrid |
-
2016
- 2016-01-13 CN CN201610018843.3A patent/CN105585218B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1931749A (en) * | 2006-09-27 | 2007-03-21 | 山东贵和显星纸业股份有限公司 | Paper-making effluent purifying treatment process |
| CN101327996A (en) * | 2007-06-22 | 2008-12-24 | 宝山钢铁股份有限公司 | Treating process of dilute emulsified oily watewater |
| CN102557341A (en) * | 2011-12-26 | 2012-07-11 | 上海集惠环保科技发展有限公司 | Treatment method of high-concentration emulsion waste water |
| CN102942285A (en) * | 2012-11-06 | 2013-02-27 | 中国石油集团工程设计有限责任公司 | Sewage treatment system and method for natural gas purifying factory in H2S-containing gas field |
| CN103395931A (en) * | 2013-08-02 | 2013-11-20 | 江苏和顺环保股份有限公司 | Processing technology for waste emulsified liquid and machining wastewater |
| CN103864266A (en) * | 2014-03-24 | 2014-06-18 | 江苏省环境科学研究院 | Waste-paper papermaking wastewater and sludge recycling method |
| CN104370418A (en) * | 2014-11-10 | 2015-02-25 | 辽宁省石油化工规划设计院有限公司 | Treatment method of chemical sewage |
| CN104803548A (en) * | 2015-04-01 | 2015-07-29 | 浙江碧源环保科技有限公司 | Treating and recycling zero-emission technology and equipment for coking phenol-cyanogen wastewater |
Non-Patent Citations (1)
| Title |
|---|
| 气浮+A/O组合工艺处理汽车机械加工废水;倪宁 蒋岸;《环境科技》;20101231;第23卷(第6期);第41页左栏第一段至第42页左栏最后一段 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105585218A (en) | 2016-05-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105585218B (en) | Wastewater from mechanical industry treatment process | |
| US4178239A (en) | Biological intermediate sewage treatment with ozone pretreatment | |
| CN202898159U (en) | Sewage treatment device | |
| CN105693014B (en) | A kind of sewage disposal system and sewage water treatment method | |
| CN207933226U (en) | A kind of industrial wastewater treatment system | |
| CN106430845A (en) | Kitchen garbage wastewater treatment apparatus | |
| CN105481174A (en) | Wastewater treatment system in rubber and synthetic plastic industry | |
| JP2021107082A (en) | Reduction of substances in contaminated fluid using naturally occurring biological growth media | |
| JPH1190483A (en) | Method and apparatus for treating waste water | |
| CN106242191B (en) | A kind for the treatment of process of Pb-Zn deposits beneficiation wastewater | |
| CN209759222U (en) | Novel food processing waste water treatment equipment | |
| CN106698852A (en) | Brassica juncea pickling waste water treatment device and method | |
| CN202156978U (en) | High salinity waste water purification device | |
| CN107973488B (en) | Method for denitrification treatment of ammonia nitrogen wastewater | |
| CN206736017U (en) | Antibiotic waste water processing unit | |
| CN203461924U (en) | Grain and oil production sewage treatment system | |
| CN208071544U (en) | A kind of railway communication system production wastewater treatment system | |
| CN111892257A (en) | Aluminum product production wastewater treatment system and treatment process thereof | |
| CN111995193A (en) | Integrated intelligent device and method for advanced treatment of medical wastewater | |
| CN205528260U (en) | Sewage treatment system | |
| RU2439001C1 (en) | Method of treating waste water | |
| CN105254123B (en) | Coking advanced waste treatment system and its reuse technology | |
| JPH06292900A (en) | Waste water treating device using ultrafilter membrane | |
| CN103803757A (en) | Bean product waste water treatment method | |
| CN104386880A (en) | Soybean protein sewage treatment method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240419 Address after: 530022, 29th Floor, Building A, Nanhu Mingdu Plaza, No. 30 Shuangyong Road, Qingxiu District, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: HUAHONG WATER GROUP CO.,LTD. Country or region after: China Address before: 543000 Lanshichong, Enyi Village, Longwei Town, Longwei District, Wuzhou City, Guangxi Zhuang Autonomous Region Patentee before: WUZHOU HUAHONG SEWAGE TREATMENT Co.,Ltd. Country or region before: China |
|
| TR01 | Transfer of patent right |