CN106746077A - Advanced treatment of industrial waste water automation equipment system - Google Patents
Advanced treatment of industrial waste water automation equipment system Download PDFInfo
- Publication number
- CN106746077A CN106746077A CN201611152069.1A CN201611152069A CN106746077A CN 106746077 A CN106746077 A CN 106746077A CN 201611152069 A CN201611152069 A CN 201611152069A CN 106746077 A CN106746077 A CN 106746077A
- Authority
- CN
- China
- Prior art keywords
- waste water
- automation equipment
- membrane module
- pump
- equipment system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000010842 industrial wastewater Substances 0.000 title claims abstract description 18
- 239000012528 membrane Substances 0.000 claims abstract description 33
- 239000002351 wastewater Substances 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 238000010926 purge Methods 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 11
- 239000007789 gas Substances 0.000 claims abstract description 10
- 238000001914 filtration Methods 0.000 claims abstract description 9
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000000919 ceramic Substances 0.000 claims abstract description 7
- 239000002253 acid Substances 0.000 claims abstract description 6
- 238000000746 purification Methods 0.000 claims abstract description 5
- 239000002912 waste gas Substances 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 6
- 230000000149 penetrating effect Effects 0.000 claims description 6
- 230000001954 sterilising effect Effects 0.000 claims description 4
- 238000004659 sterilization and disinfection Methods 0.000 claims description 4
- 238000003860 storage Methods 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 125000004122 cyclic group Chemical group 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 108090000862 Ion Channels Proteins 0.000 claims description 2
- 102000004310 Ion Channels Human genes 0.000 claims description 2
- 230000000844 anti-bacterial effect Effects 0.000 claims description 2
- 230000001502 supplementing effect Effects 0.000 claims 2
- 210000004534 cecum Anatomy 0.000 claims 1
- 238000009295 crossflow filtration Methods 0.000 claims 1
- 229910052573 porcelain Inorganic materials 0.000 claims 1
- 238000004140 cleaning Methods 0.000 abstract description 5
- 230000003647 oxidation Effects 0.000 abstract description 5
- 238000007254 oxidation reaction Methods 0.000 abstract description 5
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- 238000005189 flocculation Methods 0.000 abstract 1
- 230000016615 flocculation Effects 0.000 abstract 1
- 238000000108 ultra-filtration Methods 0.000 abstract 1
- 239000012141 concentrate Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- 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
- C02F1/5281—Installations for water purification using chemical agents
-
- 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
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Molecular Biology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The present invention relates to advanced treatment of industrial waste water automation equipment system regions, a kind of combined filtering is specifically disclosed, chemistry, the automation equipment system of oxidation.Including stoste case, agitator, gas purifier, main circulation pump, main membrane module, film water purification mouthful, clear water tanks, draining pump, heater, alkaline purge tank, acid purge tank, auxiliary membrane module, recoil tank, blender, cartridge filter, auxiliary circulating pump, liquid feeding pump.Industrial wastewater removes Wastewater Pollutant by ultrafiltration ceramic membrane by after ozone oxidation and flocculation to the full extent.System can be according to contaminated wastewater extent control cocnentration factor, at utmost the service life of extension cleaning frequency and equipment, while uninterruptedly being filtered when realizing blowdown, is processed waste water process and produces waste gas to be discharged by activated adoption after-purification, secondary pollution is prevented, energy-conserving and environment-protective are realized.
Description
Technical field
It is used for advanced treatment of industrial waste water automation equipment system the present invention relates to one kind, and in particular to one kind was combined
Filter, chemistry, the automation equipment of oxidation bonding.
Technical background
The ceramic membrane equipment for the treatment of industrial wastewater is typically all for semi-automation runs, while concentrate is arranged not at present
Can filter, typically all multiple casings control discharge by switch valve.It is whole equipment to be also reduced while reducing efficiency
Body reliability.
In the research and practice process to the method, the inventors found that：Liquid in traditional membrane filter system
Body control is complicated, stability is low, continuously run low degree.Realized during film works by the liquid dispensing apparatus invented
The effect of automatic distribution concentrate and waste water.
The content of the invention
The present invention is directed to deficiency of the prior art, there is provided a kind of combined filtering, chemistry, the automation equipment of oxidation.
The present invention relates to the liquid dispensing apparatus being used in industrial waste water treatment film filtration system, including：Stoste case 1, stirs
Mix device 1-1, gas purifier 1-2, main circulation pump 2, main membrane module 3, film water purification mouthful 3-1, clear water tanks 4, draining pump 5, heater,
6, alkaline purge tank 7, acid purge tank 8, auxiliary membrane module 9, recoil tank 10, blender 11, cartridge filter 12, auxiliary circulating pump
13, liquid feeding pump 14.
Above-mentioned main membrane module 3 is Multichannel ceramic membrane, and filtering accuracy reaches 50nm, by the frequency conversion control of main circulation pump 2
System, flow velocity reaches 3~5m/s in membrane channels.
Above-mentioned auxiliary membrane module 9 is honeycomb type ceramic film ceramic membrane, and filtering accuracy reaches 50nm, the existing micro- mistake of auxiliary membrane module 9
Flow through filter.
There is function of ultraviolet sterilization in above-mentioned clear water tanks 4, sterilization processing is carried out to the liquid after treatment.
Above-mentioned blender 11 is made up of ejector and blender, and blender mixes pending waste water and ozone, flocculant
Close.
Above-mentioned is mixed pending well mixed by agitator 1-1 in liquid-storing box 1, and mixing speed is 88r/
min。
Above-mentioned liquid-storing box 1 is installed and biological activated carbon, bioactivity is placed in gas purifier 1-2, gas purifier 1-2
Attachment active bio in charcoal hole, realizes absorption and biological treatment synergy.
The above-mentioned mounting temperature sensor of heater 6, control rinse liquid temperature is at 60~75 DEG C.
Recoil tank enters compressed air equipped with pressure-control valve, and it is 0.3 MPa to control kickback pressure.
Dividing plate is provided with above-mentioned liquid-storing box 1, liquid-storing box 1 is divided into two semiclosed regions.
Using the beneficial effect of above-mentioned technical proposal：Industrial wastewater is reacted with flocculant simultaneously by ozone oxidation, ceramics
Film removes Wastewater Pollutant to the full extent.System can at utmost extend according to contaminated wastewater extent control cocnentration factor
Cleaning frequency and the service life of equipment, while uninterruptedly being filtered when realizing blowdown, treatment waste water process produces waste gas by living
Property absorption after-purification discharge, prevent secondary pollution, realize energy-conserving and environment-protective.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present invention.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is all other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Reference picture 1, advanced treatment of industrial waste water automation equipment system, including：Stoste case 1, agitator 1-1, gas is net
Change device 1-2, main circulation pump 2, main membrane module 3, main film produces mouth of a river 3-1, clear water tanks 4, dredge pump 5, heater, 6, alkaline purge tank
7, acid purge tank 8, auxiliary membrane module 9, recoil tank 10, blender 11, cartridge filter 12, auxiliary circulating pump 13, liquid feeding pump 14.Treat
Treatment waste water is entered by liquid feeding pump 14 and enters blender 11 after cartridge filter 12 is filtered, waste water realize in the blender 11 and
Ozone and flocculant mix, and waste water enters stoste case 1 after mixing, and waste water stirs mixing by agitator 1-1, whipping process of intaking
Middle generation waste gas is purified by gas purifier 1-2 discharges.
Scheme one：Waste water flows back in stoste case 1 after entering main membrane module 3 by main circulation pump 2 in stoste case 1, is circulated throughout
Main membrane module 3 produces penetrating fluid to produce mouth of a river 3-1 by main film and enters storage in clear water tanks 4 in journey.Main film produces stoste during water
Pump 14 is simultaneously to supplement waste water in stoste case 1.Waste water when setting multiple is concentrated in stoste case 1 is discharged by dredge pump 5.
Scheme two：Waste water flows back in stoste case 1 after entering auxiliary membrane module 9 by auxiliary circulating pump 13 in stoste case 1, is circulated throughout
The penetrating fluid that auxiliary membrane module 9 is produced in journey enters storage in clear water tanks 4, and raw liquor pump 14 is simultaneously to original during auxiliary membrane module product water
Supplement waste water in liquid case 1.Waste water when setting multiple is concentrated in stoste case 1 is discharged by dredge pump 5.
Can be run simultaneously according to pending waste water quality characteristic scheme one and scheme two or each isolated operation, clear water tanks
4 built with ultraviolet sterilizer, and penetrating fluid is in constantly bactericidal nature in clear water tanks 4.
When main membrane module 3 or the yield of auxiliary membrane module 9 are less than lower limit, recoil the pressurized backwash of tank 10, and pressure is constant
It is 0.3 MPa, when the water time is produced more than higher limit, the alkaline cleaning liquid inside of purge tank 7 is by heater 6, major cycle during alkali cleaning
Pump 2, returns in alkaline purge tank 7 after main membrane module 3, and heater 6 will be stably held in 60~75 DEG C, during pickling in cyclic process
The cleaning liquid inside of acid purge tank 8 is returned in acid purge tank 8 after main membrane module 3, is circulated throughout by heater 6, main circulation pump 2
Heater 6 will be stably held in 60~75 DEG C in journey.
Pre-heating system device of the present invention is described in detail above, specific case used herein is to this
The principle and implementation method of invention are set forth, and the explanation of above example is only intended to help and understands side of the invention
Method and its core concept；Simultaneously for those of ordinary skill in the art, according to thought of the invention, in specific embodiment
And be will change in range of application, in sum, this specification content should not be construed as limiting the invention.
Claims (9)
1. advanced treatment of industrial waste water automation equipment system, including：Stoste case, agitator, gas purifier, main circulation pump,
Main membrane module, film water purification mouthful, clear water tanks, draining pump, heater, alkaline purge tank, acid purge tank, auxiliary membrane module, recoil tank,
Blender, cartridge filter, auxiliary circulating pump, liquid feeding pump, it is characterised in that pending waste water enters security personnel and filters by liquid feeding pump
Enter blender after device filtering, waste water is realized mixing with ozone and flocculant in blender, waste water enters stoste case after mixing,
Waste water by agitator stir mix, water inlet whipping process in produce waste gas by gas purifier purify discharge, can by with
Lower two ways discharge：
A. waste water is flowed back in stoste case after main circulation pump enters main membrane module in stoste case, and main membrane module is produced in cyclic process
Raw penetrating fluid produces the mouth of a river and enters storage in clear water tanks by main film, and raw liquor pump in stoste case simultaneously to supplementing during main film product water
Waste water, the waste water when setting multiple is concentrated in stoste case is discharged by dredge pump;
B. waste water is flowed back in stoste case after auxiliary circulating pump enters auxiliary membrane module in stoste case, and auxiliary membrane module is produced in cyclic process
Raw penetrating fluid enters storage in clear water tanks, auxiliary membrane module produce water during raw liquor pump simultaneously to supplementing waste water in stoste case, when
Waste water when being concentrated to setting multiple in stoste case 1 is discharged by dredge pump 5；
A and b two schemes can run simultaneously or each isolated operation, clear water tanks built with ultraviolet sterilizer, in clear water tanks
Penetrating fluid is in constantly bactericidal nature.
2. advanced treatment of industrial waste water automation equipment system according to claim 1, it is characterised in that main membrane module is
Multichannel ceramic membrane, filtering accuracy reaches 50nm, by the way that to the VFC of main circulation pump 2, flow velocity reaches 3~5m/ in membrane channels
s。
3. advanced treatment of industrial waste water automation equipment system according to claim 1, it is characterised in that auxiliary membrane module is
Honeycomb fashion porcelain film, filtering accuracy reaches 50nm, realizes micro- cross-flow filtration or cecum filtering.
4. advanced treatment of industrial waste water automation equipment system according to claim 1, it is characterised in that tool in clear water tanks
There is function of ultraviolet sterilization, sterilization processing is carried out to the liquid after treatment.
5. advanced treatment of industrial waste water automation equipment system according to claim 1, it is characterised in that pending waste water
Ozone is mixed with flocculant in blender, blender is made up of ejector and blender.
6. advanced treatment of industrial waste water automation equipment system according to claim 1, it is characterised in that after mixing ozone
Waste water it is well mixed by agitator 12 in liquid-storing box, mixing speed is 88r/min.
7. advanced treatment of industrial waste water automation equipment system according to claim 1, it is characterised in that liquid-storing box is installed
Gas purifier, attachment active bio in biological activated carbon, biological activated carbon hole is placed in gas purifier, realize absorption and
Biological treatment synergy.
8. advanced treatment of industrial waste water automation equipment system according to claim 1, it is characterised in that heater is installed
Temperature sensor, control rinse liquid temperature is at 60~75 DEG C.
9. advanced treatment of industrial waste water automation equipment system according to claim 1, it is characterised in that set in liquid-storing box
Dividing plate is equipped with, liquid-storing box 1 is divided into two semiclosed regions.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611152069.1A CN106746077A (en) | 2016-12-14 | 2016-12-14 | Advanced treatment of industrial waste water automation equipment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611152069.1A CN106746077A (en) | 2016-12-14 | 2016-12-14 | Advanced treatment of industrial waste water automation equipment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106746077A true CN106746077A (en) | 2017-05-31 |
Family
ID=58888481
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611152069.1A Pending CN106746077A (en) | 2016-12-14 | 2016-12-14 | Advanced treatment of industrial waste water automation equipment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106746077A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107500442A (en) * | 2017-10-16 | 2017-12-22 | 安徽工业大学 | Integrated treatment method and device for micro-polluted source water |
| CN109453559A (en) * | 2018-11-29 | 2019-03-12 | 合肥科锐特环保工程有限公司 | A kind of ethanol eluate recyclable device |
| CN110902949A (en) * | 2019-11-29 | 2020-03-24 | 江苏久吾高科技股份有限公司 | Sewage treatment process and device capable of achieving surface IV-class water discharge |
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| CN1476923A (en) * | 2002-08-20 | 2004-02-25 | 天津膜天膜工程技术有限公司 | Hollow fibre membrane separation equipment and its operation method |
| CN1785856A (en) * | 2005-10-27 | 2006-06-14 | 韩春来 | Mambrane method of recovery and utilization of refining oil and chemical polluted water and its equipment |
| CN205760657U (en) * | 2016-05-31 | 2016-12-07 | 陕西博源环境工程设备有限公司 | A kind of oiliness sewage treatment ultrafiltration apparatus |
| CN106186393A (en) * | 2015-05-06 | 2016-12-07 | 李少帅 | A kind of industrial waste water disposal device |
-
2016
- 2016-12-14 CN CN201611152069.1A patent/CN106746077A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1476923A (en) * | 2002-08-20 | 2004-02-25 | 天津膜天膜工程技术有限公司 | Hollow fibre membrane separation equipment and its operation method |
| CN1785856A (en) * | 2005-10-27 | 2006-06-14 | 韩春来 | Mambrane method of recovery and utilization of refining oil and chemical polluted water and its equipment |
| CN106186393A (en) * | 2015-05-06 | 2016-12-07 | 李少帅 | A kind of industrial waste water disposal device |
| CN205760657U (en) * | 2016-05-31 | 2016-12-07 | 陕西博源环境工程设备有限公司 | A kind of oiliness sewage treatment ultrafiltration apparatus |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107500442A (en) * | 2017-10-16 | 2017-12-22 | 安徽工业大学 | Integrated treatment method and device for micro-polluted source water |
| CN109453559A (en) * | 2018-11-29 | 2019-03-12 | 合肥科锐特环保工程有限公司 | A kind of ethanol eluate recyclable device |
| CN110902949A (en) * | 2019-11-29 | 2020-03-24 | 江苏久吾高科技股份有限公司 | Sewage treatment process and device capable of achieving surface IV-class water discharge |
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Application publication date: 20170531 |
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