CN107324537A - A kind of method and system of plasma ozone chlorination drinking water - Google Patents
A kind of method and system of plasma ozone chlorination drinking water Download PDFInfo
- Publication number
- CN107324537A CN107324537A CN201710598837.4A CN201710598837A CN107324537A CN 107324537 A CN107324537 A CN 107324537A CN 201710598837 A CN201710598837 A CN 201710598837A CN 107324537 A CN107324537 A CN 107324537A
- Authority
- CN
- China
- Prior art keywords
- drinking water
- ozone
- chlorination
- processing
- advanced oxidation
- 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.)
- Pending
Links
- 239000003651 drinking water Substances 0.000 title claims abstract description 64
- 235000020188 drinking water Nutrition 0.000 title claims abstract description 63
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 238000005660 chlorination reaction Methods 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 29
- 230000003647 oxidation Effects 0.000 claims abstract description 33
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 33
- 238000012545 processing Methods 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000005189 flocculation Methods 0.000 claims abstract description 19
- 230000016615 flocculation Effects 0.000 claims abstract description 19
- 230000015556 catabolic process Effects 0.000 claims abstract description 9
- 238000006731 degradation reaction Methods 0.000 claims abstract description 9
- 238000001914 filtration Methods 0.000 claims abstract description 7
- 238000010521 absorption reaction Methods 0.000 claims abstract description 4
- 239000003610 charcoal Substances 0.000 claims abstract description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 12
- 239000000575 pesticide Substances 0.000 claims description 12
- 238000004062 sedimentation Methods 0.000 claims description 12
- 239000005416 organic matter Substances 0.000 claims description 9
- 229910001385 heavy metal Inorganic materials 0.000 claims description 8
- -1 hydroxyl radical free radical Chemical class 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000003814 drug Substances 0.000 claims description 3
- 238000001179 sorption measurement Methods 0.000 claims description 3
- 239000007800 oxidant agent Substances 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims 1
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 26
- 230000001954 sterilising effect Effects 0.000 abstract description 15
- 230000008569 process Effects 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 7
- 230000004927 fusion Effects 0.000 abstract description 3
- 230000009182 swimming Effects 0.000 abstract description 3
- 241000894006 Bacteria Species 0.000 description 5
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 3
- 241000700605 Viruses Species 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical group O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000004155 Chlorine dioxide Substances 0.000 description 2
- 210000000170 cell membrane Anatomy 0.000 description 2
- 235000019398 chlorine dioxide Nutrition 0.000 description 2
- 230000009849 deactivation Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 241000726221 Gemma Species 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 102000004895 Lipoproteins Human genes 0.000 description 1
- 108090001030 Lipoproteins Proteins 0.000 description 1
- 235000012206 bottled water Nutrition 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 231100000315 carcinogenic Toxicity 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
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000002158 endotoxin Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 229920006008 lipopolysaccharide Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000725 suspension Substances 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- 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
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/78—Details relating to ozone treatment devices
- C02F2201/782—Ozone generators
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/02—Specific form of oxidant
- C02F2305/023—Reactive oxygen species, singlet oxygen, OH radical
Abstract
The invention discloses a kind of method and system of plasma ozone chlorination drinking water, this method includes：Dosing is flocculated；Advanced oxidation is pre-processed；Flocculation treatment；Filtering；Advanced oxidation processing；Charcoal absorption；Chlorination processing.Technical solution of the present invention realizes the high accuracy fusion of one body swimming processing equipment, realize system-wide integrated and Automated condtrol, efficient effect and sterilization of the oxidisability of plasma advanced oxidation gas to the macromolecular in degradation water are given full play to, a kind of safe and reliable, thorough and noresidue sterilization process is provided for drinking water disinfection.
Description
Technical field
The present invention relates to ozone application field, the method for more particularly to a kind of plasma ozone chlorination drinking water and it is
System.
Background technology
With the continuous improvement and the continuous enhancing of environmental consciousness of people's living standard, quality and dirt to drinking water quality
Water process and the standard of reuse require also more and more higher.
The combination type sterilizing that disinfection by chlorine dioxide, disinfection by ultraviolet light and several sterilization process are constituted in recent years, from technology
Technique has obtained quick development, has been also accumulated from rich experience and service data into the practical application of various regions.But each work
Skill has obvious shortcomings and deficiencies.
Disinfection way of the tradition based on liquid chlorine, its shortcoming includes：
1）, liquid chlorine disinfection be also easy to produce DBPs, cause the generally worry of people.
2）, liquid chlorine disinfection storage link have the shortcomings that security is poor, easily leak.
3）, since the 1970s, because it is found that chlorine can form the production of carcinogenic or pathogenic change with many kinds of substance in water
Thing, causes the technique to start to be restricted in application.
4）, cost it is high.Because disinfection by chlorine dioxide exists unstable and greatly must with volatile shortcoming, thus in consumption
Palpus making in site, adds use cost.Although having enough precaution measures in system design and operation, but still it should be noted equipment
Performance and safety operation.
The major defect of disinfection by ultraviolet light includes：
1）, Disinfection Effect it is big by the influence of water quality, especially suspension, turbidity, design major parameter is referred to as ultraviolet penetrance.
2）, cost it is high.Because sewage water outlet penetrance differs greatly, when penetrance is reduced to 50% from 60%, it is necessary to
Ultraviolet dosage to double, the configuration of same equipment and operating cost also increase with times；On the other hand, disinfection by ultraviolet light
Need import equipment one-time investment higher.
In summary, though current Disinfection Processes in Drinking Water Treatment is widely used, and technical maturity is not high, do not have also
A kind of perfect drinking water disinfection technology occurs.So in order to improve drinking water quality conscientiously, livelihood issues are effectively solved,
The drawbacks of needing effectively to solve present in existing sterilization process, improves drinking water quality.
The content of the invention
The present invention provides a kind of method and system of plasma ozone chlorination drinking water, realizes one body swimming processing
The high accuracy fusion of equipment, realizes system-wide integrated and Automated condtrol, plasma advanced oxidation is disappeared
Malicious process integration chlorination technique is commonly applied in drinking water treatment, gives full play to the oxidation of plasma advanced oxidation gas
Property efficient effect to the macromolecular in degradation water and sterilization, provide a kind of safe and reliable, thorough for drinking water disinfection
Bottom and the sterilization process of noresidue.
Technical scheme provides a kind of method of plasma ozone chlorination drinking water, including following step
Suddenly：
Dosing is flocculated；
Advanced oxidation is pre-processed；
Flocculation treatment；
Filtering；
Advanced oxidation processing；
Charcoal absorption；
Chlorination processing.
Further, the bulky grain that the dosing flocculation is produced, enters subsequent processing after all sedimentations are completed.
Further, the advanced oxidation pretreatment is to be mixed advanced oxidation gas with drinking water, and removal is drunk
Organic matter, heavy metal, residues of pesticides and colourity in water.
Further, advanced oxidation processing be by primary oxidizers of hydroxyl radical free radical and drinking water in organic matter
Reacted, remove small organic molecule, residues of pesticides and the heavy metal of difficult degradation in water removal.
Technical scheme additionally provides a kind of system of plasma ozone chlorination drinking water, including dosing wadding
It is solidifying pond, plasma ozone generator, pre- ozone contact tank, flocculation sedimentation tank, screen pack, ozone contact tank, activated carbon filter, clear
Pond, Plasma contact pond and chlorination processing pond, wherein：
Dosing flocculation basin is used to add medicine in water, produces sedimentation；
Plasma ozone generator is used to produce ozone；
Pre- ozone contact tank is used to be mixed advanced oxidation gas with drinking water, removes organic matter, a huge sum of money in drinking water
Category, residues of pesticides and colourity；
Flocculation sedimentation tank is used to precipitate the drinking water of the pre- ozone contact tank；
The debris that screen pack is used in filtering drinking water；
Chlorination processing pond is used to carry out chlorination to drinking water, and purified treatment is carried out to drinking water；
Clear water reserviors are used for the drinking water for storing the chlorination pond processing；
Ozone contact tank is used to carry out advanced treating to drinking water, by primary oxidizers of hydroxyl radical free radical with having in drinking water
Machine thing is reacted, and removes small organic molecule, residues of pesticides and the heavy metal of difficult degradation in water removal；
Activated carbon filter is used to carry out adsorption cleaning processing to drinking water.
Further, the ozone produced by the plasma ozone generator supply the pre- ozone contact tank simultaneously, it is clear
Pond and ozone contact tank.
Plasma advanced oxidation generation sterilization process joint chlorination technique is commonly applied to by technical solution of the present invention
In drinking water treatment, efficient effect of the oxidisability to the macromolecular in degradation water of plasma advanced oxidation gas is given full play to
And sterilization, realize one body swimming processing equipment high accuracy fusion, realize it is system-wide integrated and from
Dynamicization is controlled, and a kind of safe and reliable, thorough and noresidue sterilization process is provided for drinking water disinfection.
Other features and advantages of the present invention will be illustrated in the following description, also, partly becomes from specification
Obtain it is clear that or being understood by implementing the present invention.The purpose of the present invention and other advantages can be by the explanations write
Specifically noted structure is realized and obtained in book, claims and accompanying drawing.
Below by drawings and examples, technical scheme is described in further detail.
Brief description of the drawings
Accompanying drawing is used for providing a further understanding of the present invention, and constitutes a part for specification, the reality with the present invention
Applying example is used to explain the present invention together, is not construed as limiting the invention.In the accompanying drawings：
Fig. 1 is the method flow diagram of plasma ozone chlorination drinking water in the embodiment of the present invention one；
Fig. 2 is the system construction drawing of plasma ozone chlorination drinking water in the embodiment of the present invention one；Fig. 3 is implemented for the present invention
The physical structure of plasma ozone chlorination potable water system in example one.
Embodiment
The preferred embodiments of the present invention are illustrated below in conjunction with accompanying drawing, it will be appreciated that preferred reality described herein
Apply example to be merely to illustrate and explain the present invention, be not intended to limit the present invention.
Fig. 1 is the method flow diagram of plasma ozone chlorination drinking water in the embodiment of the present invention one, the stream of this method
Journey comprises the following steps：
Step 101, dosing flocculation.
The bulky grain that dosing flocculation is produced in water, enters step 102 after all sedimentations are completed.
Step 102, advanced oxidation pretreatment.
Advanced oxidation pretreatment be to be mixed advanced oxidation gas with drinking water, removal drinking water in organic matter,
Heavy metal, residues of pesticides and colourity.
Step 103, flocculation treatment.
Step 104, filtering.
Step 105, advanced oxidation processing.
Advanced oxidation processing is to be reacted by primary oxidizers of hydroxyl radical free radical with the organic matter in drinking water, removal
The small organic molecule of difficult degradation, residues of pesticides and heavy metal in water.
Step 106, charcoal absorption.
Step 107, chlorination processing.
In order to realize the flow of above-mentioned plasma ozone chlorination drinking water, the present embodiment additionally provides a kind of plasma
The system of ozone chlorination drinking water, Fig. 2 is the system of plasma ozone chlorination drinking water in the embodiment of the present invention one
Structure chart.As shown in Fig. 2 the system include dosing flocculation basin 201, plasma ozone generator 202, pre- ozone contact tank 203,
Flocculation sedimentation tank 204, screen pack 205, ozone contact tank 206, activated carbon filter 207, clear water reserviors 208, Plasma contact pond
209 and chlorination processing pond 210, wherein：
Dosing flocculation basin is used to add medicine in water, produces sedimentation；
Plasma ozone generator is used to produce ozone；
Pre- ozone contact tank is used to be mixed advanced oxidation gas with drinking water, removes organic matter, a huge sum of money in drinking water
Category, residues of pesticides and colourity；
Flocculation sedimentation tank is used to precipitate the drinking water of pre- ozone contact tank；
The debris that screen pack is used in filtering drinking water；
Chlorination processing pond is used to carry out chlorination to drinking water, and purified treatment is carried out to drinking water；
Clear water reserviors are used for the drinking water for storing the processing of chlorination pond；
Ozone contact tank is used to carry out advanced treating to drinking water, by primary oxidizers of hydroxyl radical free radical with having in drinking water
Machine thing is reacted, and removes small organic molecule, residues of pesticides and the heavy metal of difficult degradation in water removal；
Activated carbon filter is used to carry out adsorption cleaning processing to drinking water.
Wherein, the ozone produced by plasma ozone generator is supplied pre- ozone contact tank, clear water reserviors and ozone simultaneously and connect
Touch pond.
The advantage of the combined treatment process of the present invention is：
1st, unharmful substance is generated after handling.
As a kind of strong oxidizer, it has efficient non-secondary pollution, can oxidation of organic compounds, and can sterilize except color, it is smelly,
The features such as taste.Ozonization is not by NH in sewage.One N and pH influence, its final product is carbon dioxide and water.
2nd, sterilizing is more thorough.Advanced oxidation sterilization process belongs to physics, chemistry and biological respinse, advanced oxidation sterilizing
There are following three kinds of effects：
(1) enzyme necessary to advanced oxidation gas energy oxidation Decomposition bacterium internal oxidation glucose, makes bacteria inactivation dead.
(2) directly with bacterium, virus function, destroy their cell membrane, DNA and RNA, cause death.
(3) lipoprotein and internal lipopolysaccharides that outer membrane is acted in after birth tissue, intrusion cell membrane are permeated, bacterium is sent out
Raw permeability distortion, dissolving is dead.Therefore, ozone can also can except algae sterilization, the microorganism stronger to vitality such as virus, gemma
Play good deactivation.
3rd, broad spectrum activity is good and sustainable sterilization.Advanced oxidation gas has deactivation to various bacteria and virus, sterilizes
Broad spectrum activity is high.
Obviously, those skilled in the art can carry out the essence of various changes and modification without departing from the present invention to the present invention
God and scope.So, if these modifications and variations of the present invention belong to the scope of the claims in the present invention and its equivalent technologies
Within, then the present invention is also intended to comprising including these changes and modification.
Claims (6)
1. a kind of method of plasma ozone chlorination drinking water, it is characterised in that comprise the following steps：
Dosing is flocculated；
Advanced oxidation is pre-processed；
Flocculation treatment；
Filtering；
Advanced oxidation processing；
Charcoal absorption；
Chlorination processing.
2. according to the method described in claim 1, it is characterised in that the bulky grain that the dosing flocculation is produced, complete all
Enter subsequent processing after sedimentation.
3. according to the method described in claim 1, it is characterised in that the advanced oxidation pretreatment be by advanced oxidation gas with
Drinking water is mixed, and removes organic matter, heavy metal, residues of pesticides and colourity in drinking water.
4. according to the method described in claim 1, it is characterised in that it using hydroxyl radical free radical is main that the advanced oxidation processing, which is,
Oxidant is reacted with the organic matter in drinking water, removes small organic molecule, residues of pesticides and the huge sum of money of difficult degradation in water removal
Category.
5. a kind of system of plasma ozone chlorination drinking water, it is characterised in that including dosing flocculation basin, plasma ozone
Generator, pre- ozone contact tank, flocculation sedimentation tank, screen pack, ozone contact tank, activated carbon filter, clear water reserviors, plasma connect
Pond and chlorination processing pond are touched, wherein：
Dosing flocculation basin is used to add medicine in water, produces sedimentation；
Plasma ozone generator is used to produce ozone；
Pre- ozone contact tank is used to be mixed advanced oxidation gas with drinking water, removes organic matter, a huge sum of money in drinking water
Category, residues of pesticides and colourity；
Flocculation sedimentation tank is used to precipitate the drinking water of the pre- ozone contact tank；
The debris that screen pack is used in filtering drinking water；
Chlorination processing pond is used to carry out chlorination to drinking water, and purified treatment is carried out to drinking water；
Clear water reserviors are used for the drinking water for storing the chlorination pond processing；
Ozone contact tank is used to carry out advanced treating to drinking water, by primary oxidizers of hydroxyl radical free radical with having in drinking water
Machine thing is reacted, and removes small organic molecule, residues of pesticides and the heavy metal of difficult degradation in water removal；
Activated carbon filter is used to carry out adsorption cleaning processing to drinking water.
6. system according to claim 5, it is characterised in that the ozone produced by the plasma ozone generator is simultaneously
Supply the pre- ozone contact tank, clear water reserviors and ozone contact tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710598837.4A CN107324537A (en) | 2017-07-21 | 2017-07-21 | A kind of method and system of plasma ozone chlorination drinking water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710598837.4A CN107324537A (en) | 2017-07-21 | 2017-07-21 | A kind of method and system of plasma ozone chlorination drinking water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107324537A true CN107324537A (en) | 2017-11-07 |
Family
ID=60200547
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710598837.4A Pending CN107324537A (en) | 2017-07-21 | 2017-07-21 | A kind of method and system of plasma ozone chlorination drinking water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107324537A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020189998A1 (en) * | 2000-04-03 | 2002-12-19 | Haase Richard A. | Processes and apparatus for potable water purification that include bio-filtration, and treated water from such processes and apparatus |
| CN102633409A (en) * | 2012-04-26 | 2012-08-15 | 复旦大学 | Technological method for controlling disinfection by-product and pathogenic microorganism risk of drinking water |
| CN205087985U (en) * | 2015-09-21 | 2016-03-16 | 河南迪诺环保科技股份有限公司 | Industry sewage plasma pretreatment systems |
-
2017
- 2017-07-21 CN CN201710598837.4A patent/CN107324537A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020189998A1 (en) * | 2000-04-03 | 2002-12-19 | Haase Richard A. | Processes and apparatus for potable water purification that include bio-filtration, and treated water from such processes and apparatus |
| CN102633409A (en) * | 2012-04-26 | 2012-08-15 | 复旦大学 | Technological method for controlling disinfection by-product and pathogenic microorganism risk of drinking water |
| CN205087985U (en) * | 2015-09-21 | 2016-03-16 | 河南迪诺环保科技股份有限公司 | Industry sewage plasma pretreatment systems |
Non-Patent Citations (1)
| Title |
|---|
| 梁天成: "《矿井水处理技术及标准规范使用手册》", 当代中国音像出版社, pages: 426 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| PT1519900E (en) | Effluent treatment combining solid/liquid separation and pulsed electric fields | |
| CN107117765B (en) | A kind of drinking water purification device and purifying treatment method | |
| CN104230118A (en) | Method of removing AOC (Assimilable Organic Carbon) from drinking water | |
| Cao et al. | Comparison of peracetic acid and sodium hypochlorite enhanced Fe (Ⅱ) coagulation on algae-laden water treatment | |
| CN104086036B (en) | A kind of method for treating water | |
| CN104150660A (en) | Micro cluster mineral water and preparation method thereof | |
| Belibagli et al. | An integrated process for wet scrubber wastewater treatment using electrooxidation and pressure-driven membrane filtration | |
| CN1810684B (en) | Three-in-one drinking water treating process and apparatus | |
| CN201395538Y (en) | Emergency drinking water treatment equipment | |
| CN202849202U (en) | Water purification apparatus for preparing domestic water | |
| CN104556509B (en) | A kind of running water sterilization system based on membrane technology | |
| CN107324537A (en) | A kind of method and system of plasma ozone chlorination drinking water | |
| CN103951141B (en) | A kind of garbage leachate treatment process and treatment unit | |
| Lu et al. | Efficient removal of Escherichia coli from ballast water using a combined high-gradient magnetic separation-ultraviolet photocatalysis (HGMS-UV/TiO 2) system | |
| CN207031142U (en) | A kind of device of plasma ozone chlorination drinking water | |
| CN106746035A (en) | A kind of drinking water algae-removing technology | |
| CN109970251A (en) | A kind of multistage water treatment system of catalytic ozonation | |
| CN210915728U (en) | Domestic sewage treatment equipment | |
| CN106335965A (en) | Movable water purification equipment with efficient disinfection effect | |
| CN107804946B (en) | The technique for handling nitrosamines disinfection by-products in drinking water | |
| CN206298473U (en) | Natural drink water bromate processing system | |
| CN206266303U (en) | Urban sewage reutilization pathogenic microorganism control device | |
| CN205367994U (en) | Medical treatment sewage treatment device | |
| CN204973514U (en) | Organic waste gas high energy oxidation unit | |
| CN212609932U (en) | Device for improving quality of organic sewage reuse water |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20220704 Address after: 101300 4th floor, building 3, No. 22, Tengren Road, Niulanshan Town, Shunyi District, Beijing Applicant after: BEIJING JINDA WANXIANG ENVIRONMENTAL SCIENCE AND TECHNOLOGY CO.,LTD. Address before: 100000 4th floor, building 3, No. 22, Tengren Road, Niulanshan Town, Shunyi District, Beijing Applicant before: BEIJING JINDA WANXIANG ENVIRONMENTAL SCIENCE AND TECHNOLOGY CO.,LTD. Applicant before: BEIJING YISHUI-NET ENVIRONMENTAL PROTECTION Co.,Ltd. |
|
| TA01 | Transfer of patent application right | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20171107 |
|
| RJ01 | Rejection of invention patent application after publication |