CN207294435U - Advanced oxidation bi-membrane method wastewater reusing device - Google Patents
Advanced oxidation bi-membrane method wastewater reusing device Download PDFInfo
- Publication number
- CN207294435U CN207294435U CN201721132298.7U CN201721132298U CN207294435U CN 207294435 U CN207294435 U CN 207294435U CN 201721132298 U CN201721132298 U CN 201721132298U CN 207294435 U CN207294435 U CN 207294435U
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- China
- Prior art keywords
- tank
- pipeline
- pump
- dosing
- ozone oxidation
- Prior art date
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- 230000003647 oxidation Effects 0.000 title claims abstract description 38
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 15
- 239000012528 membrane Substances 0.000 title claims abstract description 14
- 239000002351 wastewater Substances 0.000 title claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 52
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 40
- 229910052571 earthenware Inorganic materials 0.000 claims abstract description 22
- 238000011001 backwashing Methods 0.000 claims abstract description 14
- 238000001764 infiltration Methods 0.000 claims abstract description 11
- 238000004519 manufacturing process Methods 0.000 claims abstract description 10
- 238000005273 aeration Methods 0.000 claims abstract description 6
- 238000009434 installation Methods 0.000 claims abstract description 3
- 238000010276 construction Methods 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 3
- 239000010865 sewage Substances 0.000 description 11
- 230000008569 process Effects 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000003026 anti-oxygenic effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000149 chemical water pollutant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model is specifically related to a kind of advanced oxidation bi-membrane method wastewater reusing device, it is characterized by comprising ozone oxidation tank, earthenware slab film, dosing tank, intermediate water tank and counter-infiltration system, ozone oxidation tank sets water inlet and ozone air inlet pipe, ozone air inlet bottom of the tube extends to the bottom of ozone oxidation tank, inside installation earthenware slab film, earthenware slab film passes through the backwashing pump outside pipeline and ozone oxidation tank respectively, Aeration fan, produce water pump connection, backwashing pump, production water pump is connected by pipeline with intermediate water tank respectively, intermediate water tank is connected by pipeline with counter-infiltration system, above-mentioned pipeline is equipped with high-pressure pump, dosing tank is additionally provided with outside ozone oxidation tank, dosing tank is connected by pipeline with dosing pump, dosing pump is connected by the pipeline between pipeline and backwashing pump and ozone oxidation tank.The advantages of the utility model is grown with service life, and water treatment efficiency is good, construction cost and low operating cost.
Description
Technical field
The utility model belongs to field of sewage treatment, and in particular to a kind of advanced oxidation bi-membrane method reusing sewage dress
Put.
Background technology
With the continuous improvement of national environmental protection sewage drainage standard, the requirement to sewage-treatment plant is also higher and higher, passes
The sewage-treatment plant of system cannot meet the requirement of sewage discharge, in traditional sewage-treatment plant, ozone-oxidizing device
Be provided separately with ultrafiltration apparatus, construction cost is high, its reason in environment of traditional organic film in oxidation service life it is big
Amplitude declines, even if being provided separately, remaining oxidisability also can cause strong influence to the service life of organic film in water, make
The replacement frequency of film increases, and causes operating cost very high, although can be adjusted by dosing, operating cost is still very high.
Utility model content
The purpose of this utility model solve traditional wastewater processing unit there are it is of high cost the defects of, there is provided a kind of advanced oxygen
Change bi-membrane method wastewater reusing device, it is by together with ozone-oxidizing device and earthenware slab film combination, service life length, water process
Effect is good, and construction cost and operating cost are low.
The utility model is achieved by the following technical solution：
I.e. a kind of advanced oxidation bi-membrane method wastewater reusing device, it is characterised in that including ozone oxidation tank, earthenware slab film,
Dosing tank, intermediate water tank and counter-infiltration system, ozone oxidation tank set water inlet and ozone air inlet pipe, ozone air inlet bottom of the tube to prolong
Reach the bottom of ozone oxidation tank, inside installation earthenware slab film, earthenware slab film respectively by pipeline and ozone oxidation tank outside
The backwashing pump in portion, Aeration fan, production water pump connection, backwashing pump, production water pump are connected by pipeline with intermediate water tank respectively, middle water
Case is connected by pipeline with counter-infiltration system, and above-mentioned pipeline is equipped with high-pressure pump, is additionally provided with dosing tank outside ozone oxidation tank, adds
Medicine-chest is connected by pipeline with dosing pump, and dosing pump is connected by the pipeline between pipeline and backwashing pump and ozone oxidation tank.
The earthenware slab film of the utility model makes current be filtered by film by producing water pump suction, is supervised by vacuum table
Survey, when the negative pressure of suction reaches predeterminable level, illustrate film surface generate it is dirty block up, automatically begin to backwash process, use backwashing pump
Backwash will be carried out to diaphragm after water pressurization in intermediate water tank, while be added to the cleaning liquid in dosing tank by dosing pump
In backwash water, filter process is transferred to after backwash again.
For the ozone oxidation tank of the utility model by deepening water level height, the residence time increase of increase microbubble in water is smelly
The dissolved efficiency of oxygen.
The earthenware slab film antioxygenic property of the utility model is strong, can be used for a long time in Strong oxdiative environment.
The earthenware slab film (Ceramic Plate Membrane) of the utility model is with Al2O3Passed through for main material
Porous membrane prepared by 1300-1600 DEG C of high temperature, the product developed mainly for current organic film shortcoming, it possesses machinery
Intensity is high, and chemical stability is good, and resistance to oxidation, antipollution, easy cleaning, long lifespan, even aperture distribution is indeformable, UF membrane efficiency
Height, good hydrophilic property, the advantage such as energy saving, particularly suitable for the highly difficult waste water of the industry such as chemical industry, pharmacy, printing and dyeing, landfill leachate
Processing.
The counter-infiltration system of the utility model uses counter-infiltration system known in the art.
The utility model is realized using the technique of ozone high grade oxidation+bi-membrane method (earthenware slab film+reverse osmosis membrane) combination
The technology of reusing sewage.Ozone is a kind of excellent strong oxidizer, in wastewater disinfection, except color, deodorization, organics removal and COD
Aspect has good effect.Ozone oxidation degradation of organic substances speed is fast, and mild condition, does not produce secondary pollution." bi-membrane method " water
Treatment process, is the brand-new water treatment technology proposed around advanced film science and technology, can be returned most trade effluent
With it organically combines different membrane process, and certain water standard is reached after rational advanced treating, returns
With to boiler feed water system and circulating cooling make-up water, it is changed into " reusing sewage " by " sewage disposal " of traditional sense, is realized
The reusing sewage of real meaning.
The utility model greatly reduces earthenware slab film by together with ozone-oxidizing device and earthenware slab film combination
Replacement cycle, is greatly reduced the operating cost of whole device, have service life length, water treatment efficiency is good, construction cost and
The advantages of operating cost is low.
Brief description of the drawings
Fig. 1 is the structure diagram of the utility model；
As shown in FIG.：1. water inlet；2. ozone oxidation tank；3. earthenware slab film；4. dosing tank；5. dosing pump；6. production
Water pump；7. backwashing pump；8. Aeration fan；9. intermediate water tank；10. high-pressure pump；11. counter-infiltration system；12. ozone air inlet pipe.
Embodiment
As shown in Figure 1：2 one end of ozone oxidation tank is equipped with water inlet 1, and ozone air inlet pipe 12 is inserted into ozone oxidation tank 2, its bottom
End extends to the bottom of ozone oxidation tank 2, and ozone oxidation tank 2 is internally provided with earthenware slab film 3, and earthenware slab film 3 passes through pipe
Road is connected with the Aeration fan 8 outside ozone oxidation tank 2, backwashing pump 7, production water pump 6 respectively, and backwashing pump 7, production water pump 6 lead to respectively
Cross pipeline intermediate water tank 9 to connect, intermediate water tank 9 is connected by high-pressure pump 10 with counter-infiltration system 11, and dosing tank 4 passes through dosing pump
Pipeline between backwashing pump 7 and earthenware slab film 3 is connected, and the cleaning liquid of backwash is equipped with dosing tank.
When the utility model is used, waste water enters ozone oxidation tank 2 by water inlet 1, and ozone passes through ozone air inlet pipe 12
The oxidisable impurity such as COD in water removal is removed into ozone oxidation tank 2, is then filtered by earthenware slab film 3, removes SS in water removal
Deng suspended impurity, the water after oxidation and filtering is delivered to intermediate water tank 9 by production water pump 6, is collected and is adjusted in intermediate water tank 9
Store, then pressurizeed by high-pressure pump 10, carry out desalination into counter-infiltration system 11, production water can reach the water inlet of low-pressure boiler water
Standard, can also carry out advanced treating again, to adapt to different requirements.When needing backwash, pass through Aeration fan 8 and backwash
Pump 7 carries out backwash, and after system long-play, water yield reduces by more than 10%, or pressure difference increase by more than 10%, by adding
Teat pipette 5, to 3 dosing of earthenware slab film, carries out recovering flux chemical cleaning out of dosing tank 4.
Claims (1)
1. a kind of advanced oxidation bi-membrane method wastewater reusing device, it is characterised in that including ozone oxidation tank, earthenware slab film, dosing
Case, intermediate water tank and counter-infiltration system, ozone oxidation tank set water inlet and ozone air inlet pipe, ozone air inlet bottom of the tube to extend to
The bottom of ozone oxidation tank, inside installation earthenware slab film, earthenware slab film is respectively by outside pipeline and ozone oxidation tank
Backwashing pump, Aeration fan, production water pump connection, backwashing pump, production water pump are connected by pipeline with intermediate water tank respectively, and intermediate water tank leads to
Cross pipeline to be connected with counter-infiltration system, above-mentioned pipeline is equipped with high-pressure pump, and dosing tank, dosing tank are additionally provided with outside ozone oxidation tank
It is connected by pipeline with dosing pump, dosing pump is connected by the pipeline between pipeline and backwashing pump and ozone oxidation tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721132298.7U CN207294435U (en) | 2017-09-05 | 2017-09-05 | Advanced oxidation bi-membrane method wastewater reusing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721132298.7U CN207294435U (en) | 2017-09-05 | 2017-09-05 | Advanced oxidation bi-membrane method wastewater reusing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207294435U true CN207294435U (en) | 2018-05-01 |
Family
ID=62445943
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721132298.7U Active CN207294435U (en) | 2017-09-05 | 2017-09-05 | Advanced oxidation bi-membrane method wastewater reusing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207294435U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114105346A (en) * | 2020-08-31 | 2022-03-01 | 中国石油化工股份有限公司 | PVC mother liquor recycling treatment device and process |
-
2017
- 2017-09-05 CN CN201721132298.7U patent/CN207294435U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114105346A (en) * | 2020-08-31 | 2022-03-01 | 中国石油化工股份有限公司 | PVC mother liquor recycling treatment device and process |
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