CN205347131U - Food and beverage treatment of water regeneration system that gives up - Google Patents
Food and beverage treatment of water regeneration system that gives up Download PDFInfo
- Publication number
- CN205347131U CN205347131U CN201620000355.5U CN201620000355U CN205347131U CN 205347131 U CN205347131 U CN 205347131U CN 201620000355 U CN201620000355 U CN 201620000355U CN 205347131 U CN205347131 U CN 205347131U
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- CN
- China
- Prior art keywords
- ultraviolet disinfection
- flotation tank
- membrane bioreactor
- pond
- food
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- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The utility model relates to a food and beverage treatment of water regeneration system that gives up, including oil removal equalizing basin, air supporting pond, membrane bioreactor and ultraviolet disinfection pond, be equipped with a partition plate group, the 2nd partition plate group, equalizing basin delivery port in the oil removal equalizing basin, the equalizing basin delivery port passes through pipeline, elevator pump and links to each other with the air supporting pond, the upper portion in air supporting pond is equipped with oil and slag scraping machine and ji youqu, and the bottom in air supporting pond is equipped with the mud pipe, the air supporting pond is passed through the pipeline and is linked to each other with membrane bioreactor, be equipped with aerated conduit and hollow fiber membrane subassembly in the membrane bioreactor, the hollow fiber membrane subassembly links to each other with the ultraviolet disinfection pond through filtering outlet pipe, rear pump. The utility model discloses novel structure, technology is advanced, efficient, oily waste treatment is thorough.
Description
Technical field
This utility model relates to Restaurant Wastewater Treatment Technology field, is specifically related to the process regeneration application system of a kind of food and drink waste water.
Background technology
Along with the continuous quickening of urbanization process, hotel, hotel, dining room scale expanding day, quantity is increasing, the food and drink waste water amount produced therewith is also increasing, according to incompletely statistics, the undressed waste water of China's annual catering trade discharge reaches more than one hundred million ton, and has ever-increasing trend.According to another document announcement, food and drink waste water discharge capacity accounts for the 3% of city domestic sewage discharge capacity, but its BOD5And CODcrContent but account for the 1/3 of total load, it is seen that Restaurant Industry Wastewater is high density pollution source, is the contaminated one of the main reasons of peri-urban water body.On the other hand, China is as " poor-water country ", and water resources crisis is increasingly serious; and there is the phenomenon that serious distribution of water resources is uneven; cause the shortage of many urban waters, not only limit the development of urban economy, and the living standard of resident is caused strong influence.Therefore, the process of food and drink waste water, regeneration can not only obtain significant environmental benefit, have more great economic benefit and social benefit.
The complicated component of food and drink waste water, content of organics is high, with Organic substances such as starch based, dietary fiber class, Animal fat classes for main component, has that nutritional labeling height, moisture content be high, oils and fats and a feature such as salt content fermentation high, perishable is smelly.Current domestic commonly used " coalescence ", " biological contact oxidation process " and " electrochemical process " etc. science and engineering skill, also has " stiffener plate film biological treatment ", but still there is problems in that
The process equipment adopting " coalescence ", " electrochemical process " etc. to be main body can only remove some materials such as suspension, insoluble silt particle; the hardly degraded organic substances such as the starch, the Animal fat that are dissolved in the water cannot be removed; such recirculated water arises that water quality blackout fouls in use for some time, it is impossible to ensure the stable operation of system.
" biological contact oxidation process " the process equipment of employing easily occurs that filler blocks, and water distribution and aeration are not easily uniform, and the problems such as dead angle occurs in local.It is complicated that filler arranges the structure making oxidation pond, is unfavorable for that equipment is installed and safeguards, and filler selects improper meeting to have a strong impact on treatment effeciency.
There are the following problems to adopt the process equipment that " biological treatment of stiffener plate film " is main body:
(1) pretreatment is higher to the requirement of equipment and materials, it is necessary to high temperature resistant, high pressure, and corrosion-resistant, and therefore cost of equipment is big, and the one-time investment of system is high；
(2) oxidizing process may produce the intermediate product that toxicity is stronger, be unfavorable for follow-up biochemical treatment；
(3) stiffener plate membrane bioreactor packed density is little, and floor space is big；Flat board diaphragm is easily broken, and after flat board diaphragm breakage, whole film must be changed, and repair and maintenance need to set up large lifting equipment when taking out, and hangs out module, operating difficulties.
(4) recycled water can not meet " urban sewage reutilization urban reclaimed water water quality " (GB/T18920-2002) and flushes the toilet regulation in project: colourity (≤30), turbidity (≤5), total residual chlorine (after contact 30min >=1.0mg/L, pipe network end >=0.2mg/L), total coli group (≤3/L) index request.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, it is provided that a kind of novel structure, technique are advanced, efficiency is high, oily waste treatment food and drink waste water thoroughly processes regeneration application system.
This utility model is achieved by techniques below side:
A kind of process regeneration application system of food and drink waste water, including oil removal regulating reservoir, flotation tank, membrane bioreactor and ultraviolet disinfection pond, the first dividing plate group it is provided with in described oil removal regulating reservoir, second partition group, it is provided with regulating reservoir outlet on the right side of described second partition group, described regulating reservoir outlet passes through pipeline, elevator pump is connected with flotation tank water inlet, the outside of described flotation tank is provided with PAC chemicals dosing plant and pressure air-dissolving tank, described PAC chemicals dosing plant is also connected with flotation tank water inlet each through pipeline with pressure air-dissolving tank, the top of described flotation tank is provided with Oil and slag scraping machine and oil-collecting canal, the bottom of flotation tank is provided with discharge pipeline, the 3rd dividing plate group it is provided with inside described flotation tank, the right side of described 3rd dividing plate group is provided with flotation tank outlet, described flotation tank outlet is connected with membrane bioreactor by pipeline, excess sludge outlet and aerated conduit it is provided with bottom described membrane bioreactor, described aerated conduit is connected with the aerator being arranged on above membrane bioreactor, it is provided with hollow fiber film assembly inside described membrane bioreactor, described hollow fiber film assembly filters out water pipe, rear pump is connected with ultraviolet disinfection pond, described filtering out is additionally provided with pressure transmitter and back purge system on water pipe, it is provided with ultraviolet disinfection module in described ultraviolet disinfection pond, described ultraviolet disinfection module is connected with the control chamber being located at above ultraviolet disinfection pond, described ultraviolet disinfection pond right lower quadrant is provided with reuse outlet.
Further, it is additionally provided with floating ball lever meter in described membrane bioreactor.
Further, it is additionally provided with plug board gate, water lev el control gate and level sensor in described ultraviolet disinfection pond.
The process regeneration application system of a kind of food and drink waste water of this utility model, water quality characteristics and Treated sewage reusing requirement for food and drink waste water, adopt oil removal regulating reservoir, flotation tank, biofilm reactor (inside is provided with hollow fiber film assembly) and ultraviolet disinfection Combined Treatment, sewage is carried out oil removal, breakdown of emulsion, frizing, oil-collecting, membrane filtration, sterilization, and conduct is flushed the toilet, road cleans, fire demand water reuse, it is achieved recycling of water resource.This utility model novel structure, technique are advanced, efficiency is high, oily waste treatment is thorough.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In accompanying drawing: 1 oil removal regulating reservoir, 2 flotation tanks, 3 membrane bioreactors, 4 ultraviolet disinfection ponds, 5 first dividing plate groups, 6 second partition groups, 7 regulating reservoir outlets, 8 elevator pumps, 9 PAC chemicals dosing plants, 10 pressure air-dissolving tanks, 11 the 3rd dividing plate groups, 12 discharge pipelines, 13 Oil and slag scraping machines, 14 oil-collecting canals, 15 flotation tank outlets, 16 hollow fiber film assemblies, 17 rear pumps, 18 aerators, 19 aerated conduits, 20 floating ball lever meters, 21 pressure transmitters, 22 back purge systems, 23 excess sludge outlets, 24 plug board gate, 25 water lev el control gates, 26 level sensors, 27 ultraviolet disinfection modules, 28 control chambers, 29 filter out water pipe, 30 reuse outlets.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As it is shown in figure 1, the process regeneration application system of a kind of food and drink waste water, including oil removal regulating reservoir 1, flotation tank 2, membrane bioreactor 3 and ultraviolet disinfection pond 4.
Being provided with the first dividing plate group 5, second partition group 6 in oil removal regulating reservoir 1, be provided with regulating reservoir outlet 7 on the right side of described second partition group 6, described regulating reservoir outlet 7 is connected with flotation tank 2 water inlet by pipeline, elevator pump 8.
The outside of flotation tank 2 is provided with PAC chemicals dosing plant 9 and pressure air-dissolving tank 10, and described PAC chemicals dosing plant 9 is also connected with flotation tank 2 water inlet each through pipeline with pressure air-dissolving tank 10.The top of flotation tank 2 is provided with Oil and slag scraping machine 13 and oil-collecting canal 14, and sewage is breakdown of emulsion and air supporting in flotation tank 2, and the scum silica frost of generation is collected to oil-collecting canal 14 by Oil and slag scraping machine 13.Flotation tank 2 is internal is provided with the 3rd dividing plate group 11, and the bottom of flotation tank 2 is provided with discharge pipeline 12, and the mud precipitated is discharged by discharge pipeline 12.The right side of the 3rd dividing plate group 11 is provided with flotation tank outlet 15, and described flotation tank outlet 15 is connected with membrane bioreactor 3 by pipeline.
Being provided with excess sludge outlet 23 and aerated conduit 19 bottom membrane bioreactor 3, described aerated conduit 19 is connected with the aerator 18 being arranged on above membrane bioreactor 3.Membrane bioreactor 3 is internal is provided with hollow fiber film assembly 16 and floating ball lever meter 20, and described hollow fiber film assembly 16 filters out water pipe 29, rear pump 17 is connected with ultraviolet disinfection pond 4.Described filtering out is additionally provided with pressure transmitter 21 and back purge system 22 on water pipe 29.
Being provided with ultraviolet disinfection module 27 in ultraviolet disinfection pond 4, described ultraviolet disinfection module 27 is connected with the control chamber 28 being located at above ultraviolet disinfection pond 4.Being additionally provided with plug board gate 24, water lev el control gate 25 and level sensor 26 in ultraviolet disinfection pond 4, ultraviolet disinfection pond 4 right lower quadrant is provided with reuse outlet 30.
Utility model works principle is as follows:
Food and drink waste water collect by gutter is unified after from flowing into oil removal regulating reservoir 1, by the first dividing plate group 5, second partition group 6, remove in water can oil slick and scum silica frost.Sewage after oil removal adjustment processes is flowed out by regulating reservoir outlet 7, first mixed with the PAC demulsifier in PAC chemicals dosing plant 9 by elevator pump 8, then flotation tank 2 is entered again together with the air-water mixture in pressure air-dissolving tank 10, sewage is breakdown of emulsion and air supporting in flotation tank 2, the scum silica frost produced is collected to oil-collecting canal 14 by Oil and slag scraping machine 13, and the mud precipitated is discharged by discharge pipeline 12.Sewage after air supporting, frizing, oil-collecting process is flowed into membrane bioreactor 3 certainly by flotation tank outlet 15, fully after reaction, sewage is entered by doughnut membrane ultrafiltration and filters out water pipe 29, being delivered to ultraviolet disinfection pond 4 by rear pump 17, the aerating system being made up of aerator 18 and aerated conduit 19 simultaneously works as stirring action for biochemical reaction offer oxygen.The service data of reactor monitored by floating ball lever meter 20 and pressure transmitter 21, and when the membrane flux of detection is too low, rear pump 17 is closed down, and opens back purge system 22 and carries out backwash, to recover membrane flux.Excess sludge is by excess sludge outlet 23 discharge.Water after process enters sterilization pool, flows through ultraviolet disinfection module 27 and carries out effluent reuse after disposable sterilization sterilization.Water level in level sensor 26 monitoring pool, and be controlled by plug board gate 24 and water lev el control gate 25.
The above is only preferred implementation of the present utility model, and protection domain of the present utility model is not limited to above-described embodiment, and all technical schemes belonged under this utility model thinking belong to protection domain of the present utility model.It should be pointed out that, for those skilled in the art, without departing from the some improvement under this utility model structure, principle premise and modification, should be regarded as within protection domain of the present utility model.
Claims (3)
1. the process regeneration application system of a food and drink waste water, it is characterized in that: it includes oil removal regulating reservoir, flotation tank, membrane bioreactor and ultraviolet disinfection pond, the first dividing plate group it is provided with in described oil removal regulating reservoir, second partition group, it is provided with regulating reservoir outlet on the right side of described second partition group, described regulating reservoir outlet passes through pipeline, elevator pump is connected with flotation tank water inlet, the outside of described flotation tank is provided with PAC chemicals dosing plant and pressure air-dissolving tank, described PAC chemicals dosing plant is also connected with flotation tank water inlet each through pipeline with pressure air-dissolving tank, the top of described flotation tank is provided with Oil and slag scraping machine and oil-collecting canal, the bottom of flotation tank is provided with discharge pipeline, the 3rd dividing plate group it is provided with inside described flotation tank, the right side of described 3rd dividing plate group is provided with flotation tank outlet, described flotation tank outlet is connected with membrane bioreactor by pipeline, excess sludge outlet and aerated conduit it is provided with bottom described membrane bioreactor, described aerated conduit is connected with the aerator being arranged on above membrane bioreactor, it is provided with hollow fiber film assembly inside described membrane bioreactor, described hollow fiber film assembly filters out water pipe, rear pump is connected with ultraviolet disinfection pond, described filtering out is additionally provided with pressure transmitter and back purge system on water pipe, it is provided with ultraviolet disinfection module in described ultraviolet disinfection pond, described ultraviolet disinfection module is connected with the control chamber being located at above ultraviolet disinfection pond, described ultraviolet disinfection pond right lower quadrant is provided with reuse outlet.
2. the process regeneration application system of a kind of food and drink waste water according to claim 1, it is characterised in that: it is additionally provided with floating ball lever meter in described membrane bioreactor.
3. the process regeneration application system of a kind of food and drink waste water according to claim 1, it is characterised in that: it is additionally provided with plug board gate, water lev el control gate and level sensor in described ultraviolet disinfection pond.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620000355.5U CN205347131U (en) | 2016-01-02 | 2016-01-02 | Food and beverage treatment of water regeneration system that gives up |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620000355.5U CN205347131U (en) | 2016-01-02 | 2016-01-02 | Food and beverage treatment of water regeneration system that gives up |
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| CN205347131U true CN205347131U (en) | 2016-06-29 |
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| CN201620000355.5U Active CN205347131U (en) | 2016-01-02 | 2016-01-02 | Food and beverage treatment of water regeneration system that gives up |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107162349A (en) * | 2017-07-17 | 2017-09-15 | 河海大学 | A kind of duct type highlands sewage treatment unit and processing method |
| CN114149112A (en) * | 2021-12-21 | 2022-03-08 | 西南石油大学 | Laminated double helical optical rotation catalytic purifier suitable for high-concentration wastewater |
| CN115784504A (en) * | 2022-11-28 | 2023-03-14 | 武汉环投千子山环境产业有限公司 | High-efficient deoiling device of meal kitchen waste water |
-
2016
- 2016-01-02 CN CN201620000355.5U patent/CN205347131U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107162349A (en) * | 2017-07-17 | 2017-09-15 | 河海大学 | A kind of duct type highlands sewage treatment unit and processing method |
| CN107162349B (en) * | 2017-07-17 | 2020-07-17 | 河海大学 | Pipeline type plateau area domestic sewage treatment device and treatment method |
| CN114149112A (en) * | 2021-12-21 | 2022-03-08 | 西南石油大学 | Laminated double helical optical rotation catalytic purifier suitable for high-concentration wastewater |
| CN115784504A (en) * | 2022-11-28 | 2023-03-14 | 武汉环投千子山环境产业有限公司 | High-efficient deoiling device of meal kitchen waste water |
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| C14 | Grant of patent or utility model | ||
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