CN107601744A - High-salt wastewater processing system and its method - Google Patents
High-salt wastewater processing system and its method Download PDFInfo
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- CN107601744A CN107601744A CN201711024712.7A CN201711024712A CN107601744A CN 107601744 A CN107601744 A CN 107601744A CN 201711024712 A CN201711024712 A CN 201711024712A CN 107601744 A CN107601744 A CN 107601744A
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- salt wastewater
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- 239000002351 wastewater Substances 0.000 title claims abstract description 63
- 238000000034 method Methods 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 238000000746 purification Methods 0.000 claims abstract description 23
- 238000004062 sedimentation Methods 0.000 claims abstract description 20
- 239000002131 composite material Substances 0.000 claims abstract description 19
- 239000010808 liquid waste Substances 0.000 claims abstract description 16
- 230000008676 import Effects 0.000 claims abstract description 15
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 11
- 238000001704 evaporation Methods 0.000 claims abstract description 8
- 230000008020 evaporation Effects 0.000 claims abstract description 8
- 230000000694 effects Effects 0.000 claims abstract description 7
- 238000011084 recovery Methods 0.000 claims abstract description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 26
- 239000010802 sludge Substances 0.000 claims description 22
- 239000000919 ceramic Substances 0.000 claims description 13
- 239000012528 membrane Substances 0.000 claims description 13
- 238000000108 ultra-filtration Methods 0.000 claims description 12
- 239000004575 stone Substances 0.000 claims description 7
- 239000006004 Quartz sand Substances 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- JYIBXUUINYLWLR-UHFFFAOYSA-N aluminum;calcium;potassium;silicon;sodium;trihydrate Chemical compound O.O.O.[Na].[Al].[Si].[K].[Ca] JYIBXUUINYLWLR-UHFFFAOYSA-N 0.000 claims description 5
- 229910001603 clinoptilolite Inorganic materials 0.000 claims description 5
- 238000005341 cation exchange Methods 0.000 claims description 4
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 4
- 229910052622 kaolinite Inorganic materials 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 239000012266 salt solution Substances 0.000 claims description 3
- 239000006228 supernatant Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 2
- 239000004927 clay Substances 0.000 claims 1
- 238000001764 infiltration Methods 0.000 claims 1
- 238000009832 plasma treatment Methods 0.000 claims 1
- 239000003344 environmental pollutant Substances 0.000 abstract description 8
- 231100000719 pollutant Toxicity 0.000 abstract description 8
- 230000008569 process Effects 0.000 abstract description 7
- 230000000704 physical effect Effects 0.000 abstract description 3
- 238000003672 processing method Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 6
- 239000002734 clay mineral Substances 0.000 description 4
- 230000000712 assembly Effects 0.000 description 3
- 238000000429 assembly Methods 0.000 description 3
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000011033 desalting Methods 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 238000002513 implantation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000012054 meals Nutrition 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000196171 Hydrodictyon reticulatum Species 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
- 230000000903 blocking effect Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000003851 corona treatment Methods 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a kind of high-salt wastewater processing system and its processing method, the system includes purification tank for liquid waste, efficient sedimentation tank, composite electromagnetic water treatment facilities, ultrafilter purifier, reverse-osmosis filtering device and the low-temperature evaporation device being sequentially connected；The composite electromagnetic water treatment facilities is made up of plasma processor, magnetic processor, the import of the plasma processor is connected with the outlet of efficient sedimentation tank, the outlet of the plasma processor is connected with the import of magnetic processor, and the outlet of the magnetic processor is connected with the import of filtering purifying apparatus.The high-salt wastewater processing system of the present invention can effectively reduce Pollutants in Wastewater concentration and improve salinity physical property, reach high-salt wastewater efficient process and the effect of salinity recovery.
Description
Technical field
The present invention relates to the technical field of wastewater treatment, and in particular to a kind of high-salt wastewater processing system and its method.
Background technology
In Chinese society economic development and urbanization process, it is sustainable that water scarcity is increasingly becoming restriction China
One of principal element of development strategy.In recent years, as the plant-scale constantly increase in China, industrial water consumption increase sharply.Meanwhile
Produce wastewater flow rate also to increase rapidly, huge challenge is brought to current wastewater treatment and recovery and utilization technology.Industrial wastewater
As directly discharged, serious pollution will be produced to surrounding soil, water body environment.Waste water through handle it is qualified it is up to standard after, if do not reclaimed
Utilize, then cause water resource waste, aggravate shortage of water resources.
High-salt wastewater refers to containing organic matter and the waste water of the total dissolved solidss thing (TDS) of at least 3.5% (mass concentration).
High-salt wastewater wide material sources, first, in chemical industry, pharmacy, oil, papermaking, dairy produce processing, a variety of industrial productions such as food is canned
During, can discharge a large amount of waste water, not only contain the organic pollution of many high concentrations in water, and with a large amount of calcium, sodium, chlorine,
Sulfate radical plasma；Second, in order to make full use of water resource, many coastal cities directly use sea water as industrial process waters
Or cooling water, although this part of contaminated water does not contain substantial amounts of noxious material, water is big, salt content is high, also more intractable.
It is most of to take the outer row side of dilution due to lacking technology, feasibility and reliability economically for high-salt wastewater
Method.This method not only can not really reduce the total emission volumn of pollutant, and cause the waste of fresh water, and particularly saliferous gives up
The discharge of water, fresh water water resource mineralising and alkalization of soils certainly will be caused.With external high-salt wastewater " zero-emission " or " become zero-emission "
Desalting technology level compare, there is larger gap in China.Therefore, how the effective high-salt wastewater desalting processing technique of exploiting economy
Technology, promote the recycling of high-salt wastewater, and solve the bottleneck problem that water resource recycles.
The content of the invention
It is an object of the invention to overcome the shortcomings of above-mentioned background technology, and it is high to provide a kind of good separating effect, the rate of recovery
High-salt wastewater processing system, additionally provide a kind of method handled using high-salt wastewater processing system.
To achieve the above object, the high-salt wastewater processing system designed by the present invention, it is included at the waste water that is sequentially connected
Manage pond, efficient sedimentation tank, composite electromagnetic water treatment facilities, ultrafilter purifier, reverse-osmosis filtering device and low-temperature evaporation dress
Put；
The composite electromagnetic water treatment facilities is made up of plasma processor, magnetic processor, the plasma processor
Import is connected with the outlet of purification tank for liquid waste, and the outlet of the plasma processor is connected with the import of magnetic processor, the magnetic
The outlet of processor is connected with the import of ultrafilter purifier.
In above-mentioned technical proposal, it also includes sludge treatment equipment, the efficient sedimentation tank, the sludge of ultrafilter purifier
Outlet is connected with the sludge import of sludge treatment equipment respectively.
In above-mentioned technical proposal, net magic square inorganic agent is filled with the purification tank for liquid waste.
In above-mentioned technical proposal, the ultrafilter purifier is made up of several hyperfiltration membrane assemblies, each milipore filter
Component includes center filter pipe, and the outer wall ring of the center filter pipe is covered with ultrafiltration ceramic film, the center filter pipe
Net magic square inorganic agent is filled between outer wall and ultrafiltration ceramic film inwall.
Further, the net magic square inorganic agent is made up of following component in parts by weight：Clinoptilolite, 65-75 parts；It is high
Ridge stone, 10-15 parts；The clay mineral of high-cation exchange capacity, 5-10 parts；Quartz sand, 1-2 parts；Volcanic ash, 6-8 parts；Wheat meal
Stone, 2-3 parts.
Preferably, the net magic square inorganic agent is made up of following component in parts by weight：Clinoptilolite, 70-75 parts；Kaolinite
Stone, 12-15 parts；The clay mineral of high-cation exchange capacity, 6-10 parts；Quartz sand, 1-2 parts；Volcanic ash, 7-8 parts；Wheat meal
Stone, 2-3 parts.
Present invention also offers a kind of method handled using above-mentioned high-salt wastewater processing system, including following step
Suddenly：
1) high-salt wastewater initially enters purification tank for liquid waste, and the net magic square inorganic agent in purification tank for liquid waste is located in advance to waste water
Reason, the waste water by pretreatment enter efficient sedimentation tank and carry out separation of solid and liquid；
2) supernatant after efficient sedimentation tank separates enters composite electromagnetic water treatment facilities, utilizes corona treatment
Device and magnetic processor carry out materializing strategy to waste water；
3) enter ultrafilter purifier from the waste water of composite electromagnetic water treatment facilities discharge, pass through in ultrafilter purifier
The filtering and purification of net magic square inorganic agent and ultrafiltration ceramic film, obtain entering osmosis filtration dress after the only waste water containing salinity
Put；
4) water purification that waste water obtains after the effect of reverse osmosis membrane in reverse-osmosis filtering device is directly outer arranges, caused
Concentration salt solution enters low-temperature evaporation device, and the salinity secondary recovery obtained after treatment utilizes；
5) efficient sedimentation tank, sludge caused by ultrafilter purifier enter after sludge treatment equipment obtains desiccation by processing
Sludge.
Compared with prior art, the invention has the advantages that：
First, the high-salt wastewater Processing System Design of the present invention has purification tank for liquid waste, the efficiency of Water purification can be improved；
Composite electromagnetic water treatment facilities is also devised with, composite electromagnetic water treatment facilities is using plasma processor, magnetic processor series connection group
Into, materializing strategy can be carried out to waste water, it is effective to reduce Pollutants in Wastewater concentration, improve salinity physical property, improve film point
From efficiency.
Second, it is filled with net magic square inorganic agent (BEST in the purification tank for liquid waste of the high-salt wastewater processing system of the present invention
Inorganic agent), the net magic square inorganic agent is made up of following component in parts by weight：Clinoptilolite, 65-75 parts；Kaolinite, 10-15
Part；The clay mineral of high-cation exchange capacity, 5-10 parts；Quartz sand, 1-2 parts；Volcanic ash, 6-8 parts；Medical stone, 2-3 parts.
The inorganic agent is in loose structure and surface charge, by adsorbing, condensing, precipitating and the principles such as biological implantation is degraded are gone in water removal
Pollutant, there is physics and biological nature.Using the loose structure and charge characteristics of net magic square inorganic agent, added in waste water
Net magic square inorganic agent, the electromagnetic action with reference to caused by composite electromagnetic water treatment facilities, efficiently reduces Pollutants in Wastewater concentration, from
And simultaneously simplification of flowsheet can be shortened, reach high-salt wastewater efficient process and the effect of salinity recovery.
Third, the ultrafilter purifier of the present invention is made up of several hyperfiltration membrane assemblies, by special process by net magic square
Inorganic agent is attached to ultrafiltration ceramic film surface, filter layer before forming one layer, can obviously improve the performance of film, avoids ultrafiltration ceramic
Fouling membrane and blocking, significantly extend the service life of ultrafiltration ceramic membrane, improve the effluent quality of super-filtration purifying unit, enhancing separation
Performance.
Brief description of the drawings
Fig. 1 is a kind of structural representation of high-salt wastewater processing system；
Fig. 2 is the partial structural diagram of ultrafilter purifier in Fig. 1；
In figure：1- purification tanks for liquid waste, 2- efficient sedimentation tanks, 3- composite electromagnetics water treatment facilities, 4- ultrafilter purifiers,
4.1- center filters pipe, 4.2- ultrafiltration ceramic film, 5- reverse-osmosis filtering devices, 6- low-temperature evaporations device, 7- Treatment of Sludge dress
Put, 8- plasma processors, 9- magnetic processors.
Embodiment
Describe the performance of the present invention in detail with reference to case study on implementation, but they do not form the limit to the present invention
It is fixed, it is only for example.Simultaneously by illustrating that advantages of the present invention will become clearer and be readily appreciated that.
A kind of high-salt wastewater processing system of the invention as shown in fig. 1, it includes purification tank for liquid waste 1, the height being sequentially connected
Imitate sedimentation basin 2, composite electromagnetic water treatment facilities 3, ultrafilter purifier 4, reverse-osmosis filtering device 5 and low-temperature evaporation device
6；Composite electromagnetic water treatment facilities 3 is made up of plasma processor 8, magnetic processor 9, the import of plasma processor 8 with efficiently
The outlet of sedimentation basin 2 is connected, and the outlet of plasma processor 8 is connected with the import of magnetic processor 9, the outlet of magnetic processor 9 with
The import of ultrafilter purifier 4 is connected.It also includes sludge treatment equipment 7, efficient sedimentation tank 2, the sludge of ultrafilter purifier 4
Outlet is connected with the sludge import of sludge treatment equipment 7 respectively.Net magic square inorganic agent is filled with purification tank for liquid waste 1.Net magic square
Inorganic agent is made up of following component in parts by weight：Clinoptilolite, 65-75 parts；Kaolinite, 10-15 parts；High-cation, which exchanges, to be held
The clay mineral of amount, 5-10 parts；Quartz sand, 1-2 parts；Volcanic ash, 6-8 parts；Medical stone, 2-3 parts.The inorganic agent is in loose structure
And surface charge, by adsorb, condense, precipitate and biological implantation degrade etc. principle go water removal in pollutant, there is physics
And biological nature.Using the loose structure and charge characteristics of net magic square inorganic agent, net magic square inorganic agent is added in waste water, with reference to
Electromagnetic action caused by composite electromagnetic water treatment facilities, Pollutants in Wastewater concentration is efficiently reduced, so as to shorten and simplify
Technological process, reach high-salt wastewater efficient process and the effect of salinity recovery.
As shown in Fig. 2 ultrafilter purifier 4 is made up of several hyperfiltration membrane assemblies, each hyperfiltration membrane assembly includes center
Screen pipe 4.1, the outer wall ring of center filter pipe 4.1 is covered with ultrafiltration ceramic film 4.2, and the outer wall of center filter pipe 4.1 is with surpassing
Net magic square inorganic agent is filled between the filter inwall of ceramic film 4.2.The outer wall of center filter pipe 4.1 has been arranged circumferentially several mistakes
Filter opening.
The method of high-salt wastewater processing system of the present invention：High-salt wastewater initially enters purification tank for liquid waste 1, purification tank for liquid waste 1
The middle net magic square inorganic agent of addition pre-processes to waste water, and the waste water by pretreatment enters efficient sedimentation tank 2 and carries out solid-liquid point
From the supernatant of efficient sedimentation tank 2 enters composite electromagnetic water treatment facilities 3, utilizes plasma processor 8 and magnetic processor 9
Materializing strategy is carried out to waste water, effectively reduces Pollutants in Wastewater concentration, improves salinity physical property, improves UF membrane efficiency.
Enter ultrafilter purifier 4 from the waste water of composite electromagnetic water treatment facilities discharge, pass through net magic square inorganic agent and ultrafiltration ceramic membrane
Filtering and purification obtain only entering reverse-osmosis filtering device 5 after the waste water containing salinity, waste water by reverse osmosis membrane effect
The water purification obtained afterwards is directly outer to be arranged, and caused concentration salt solution enters low-temperature evaporation device 6, and the salt obtained after treatment is in two times
Recycle.Sludge caused by efficient sedimentation tank 2, ultrafilter purifier 4 is done after entering sludge treatment equipment by processing
Change sludge.
It is other unspecified to belong to prior art.
Claims (6)
1. a kind of high-salt wastewater processing system, it is characterised in that it includes purification tank for liquid waste (1), the High-rate sedimentation being sequentially connected
Pond (2), composite electromagnetic water treatment facilities (3), ultrafilter purifier (4), reverse-osmosis filtering device (5) and low-temperature evaporation dress
Put (6)；
The composite electromagnetic water treatment facilities (3) is made up of plasma processor (8), magnetic processor (9), the plasma treatment
The import of device (8) is connected with the outlet of efficient sedimentation tank (2), outlet and the magnetic processor (9) of the plasma processor (8)
Import is connected, and the outlet of the magnetic processor (9) is connected with the import of ultrafilter purifier (4).
2. high-salt wastewater processing system according to claim 1, it is characterised in that it also includes sludge treatment equipment (7),
The efficient sedimentation tank (2), the sludge outlet sludge import phase with sludge treatment equipment (7) respectively of ultrafilter purifier (4)
Even.
3. high-salt wastewater processing system according to claim 2, it is characterised in that filled in the purification tank for liquid waste (1)
There is net magic square inorganic agent.
4. high-salt wastewater processing system according to claim 3, it is characterised in that the ultrafilter purifier (4) if by
Dry hyperfiltration membrane assembly is formed, and each hyperfiltration membrane assembly includes center filter pipe (4.1), the center filter pipe (4.1)
Outer wall ring covered with ultrafiltration ceramic film (4.2), center filter pipe (4.1) outer wall and ultrafiltration ceramic film (4.2)
Net magic square inorganic agent is filled between inwall.
5. the high-salt wastewater processing system according to Claims 2 or 3, it is characterised in that the net magic square inorganic agent is with weight
Amount part meter is made up of following component：Clinoptilolite, 65-75 parts；Kaolinite, 10-15 parts；The clay pit of high-cation exchange capacity
Thing, 5-10 parts；Quartz sand, 1-2 parts；Volcanic ash, 6-8 parts；Medical stone, 2-3 parts.
6. a kind of method that high-salt wastewater processing system using described in any one of Claims 1 to 55 is handled, its feature exist
In comprising the following steps：
1) high-salt wastewater initially enters purification tank for liquid waste (1), and the net magic square inorganic agent in purification tank for liquid waste (1) carries out pre- to waste water
Processing, the waste water by pretreatment enter efficient sedimentation tank (2) and carry out separation of solid and liquid；
2) supernatant after efficient sedimentation tank (2) separation enters composite electromagnetic water treatment facilities (3), at plasma
Manage device (8) and magnetic processor (9) and materializing strategy is carried out to waste water；
3) ultrafilter purifier (4) is entered from the waste water of composite electromagnetic water treatment facilities (3) discharge, in ultrafilter purifier (4)
In by the filtering and purification of net magic square inorganic agent and ultrafiltration ceramic film, obtain entering counter-infiltration after the only waste water containing salinity
Filter (5)；
4) water purification that waste water obtains after the effect of reverse osmosis membrane in reverse-osmosis filtering device (5) is directly outer arranges, caused
Concentration salt solution enters low-temperature evaporation device (6), and the salinity secondary recovery obtained after treatment utilizes；
5) efficient sedimentation tank (2), sludge caused by ultrafilter purifier (4) enter after sludge treatment equipment (7) by handling
To dewatered sludge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711024712.7A CN107601744B (en) | 2017-10-27 | 2017-10-27 | High-salt wastewater treatment system and method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711024712.7A CN107601744B (en) | 2017-10-27 | 2017-10-27 | High-salt wastewater treatment system and method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107601744A true CN107601744A (en) | 2018-01-19 |
| CN107601744B CN107601744B (en) | 2024-02-06 |
Family
ID=61080277
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711024712.7A Active CN107601744B (en) | 2017-10-27 | 2017-10-27 | High-salt wastewater treatment system and method thereof |
Country Status (1)
| Country | Link |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020074806A (en) * | 2001-03-22 | 2002-10-04 | 이센텍(주) | No wasting activated sludge process |
| WO2009157681A2 (en) * | 2008-06-24 | 2009-12-30 | Lumilite Co., Ltd. | Water quality improvement composition containing eco-friendly active natural minerals and method of manufacturing the same |
| CN102583862A (en) * | 2012-02-22 | 2012-07-18 | 北京纬纶华业环保科技股份有限公司 | Method and system for treating saline wastewater to zero discharge and recycling |
| CN104496078A (en) * | 2014-12-23 | 2015-04-08 | 唐山亨通科技有限公司 | Treatment process of high-salinity wastewater |
| DE102014106810A1 (en) * | 2014-05-14 | 2015-11-19 | Aquadetox International Gmbh | Apparatus for the treatment of wastewater |
| CN205953772U (en) * | 2016-08-08 | 2017-02-15 | 广东环院环境工程有限公司 | Waste water recycling processing system of high -efficient desalination |
| CN107285548A (en) * | 2017-07-26 | 2017-10-24 | 广州仁廙环保技术有限公司 | Cold plasma fusion technology sewage disposal system and method |
| CN207671847U (en) * | 2017-10-27 | 2018-07-31 | 长江勘测规划设计研究有限责任公司 | High-salt wastewater processing system |
-
2017
- 2017-10-27 CN CN201711024712.7A patent/CN107601744B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020074806A (en) * | 2001-03-22 | 2002-10-04 | 이센텍(주) | No wasting activated sludge process |
| WO2009157681A2 (en) * | 2008-06-24 | 2009-12-30 | Lumilite Co., Ltd. | Water quality improvement composition containing eco-friendly active natural minerals and method of manufacturing the same |
| CN102583862A (en) * | 2012-02-22 | 2012-07-18 | 北京纬纶华业环保科技股份有限公司 | Method and system for treating saline wastewater to zero discharge and recycling |
| DE102014106810A1 (en) * | 2014-05-14 | 2015-11-19 | Aquadetox International Gmbh | Apparatus for the treatment of wastewater |
| CN104496078A (en) * | 2014-12-23 | 2015-04-08 | 唐山亨通科技有限公司 | Treatment process of high-salinity wastewater |
| CN205953772U (en) * | 2016-08-08 | 2017-02-15 | 广东环院环境工程有限公司 | Waste water recycling processing system of high -efficient desalination |
| CN107285548A (en) * | 2017-07-26 | 2017-10-24 | 广州仁廙环保技术有限公司 | Cold plasma fusion technology sewage disposal system and method |
| CN207671847U (en) * | 2017-10-27 | 2018-07-31 | 长江勘测规划设计研究有限责任公司 | High-salt wastewater processing system |
Non-Patent Citations (1)
| Title |
|---|
| 商平等: "《环境矿物材料》", 化学工业出版社, pages: 87 * |
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| CN107601744B (en) | 2024-02-06 |
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