CN205473235U - Handle cowherd's water distribution and wash modular sewage treatment device of waste water - Google Patents
Handle cowherd's water distribution and wash modular sewage treatment device of waste water Download PDFInfo
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- CN205473235U CN205473235U CN201620096804.0U CN201620096804U CN205473235U CN 205473235 U CN205473235 U CN 205473235U CN 201620096804 U CN201620096804 U CN 201620096804U CN 205473235 U CN205473235 U CN 205473235U
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- pond
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- sludge
- water
- chemicals dosing
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 239000010865 sewage Substances 0.000 title claims abstract description 36
- 239000002351 wastewater Substances 0.000 title claims abstract description 31
- 238000004062 sedimentation Methods 0.000 claims abstract description 26
- 239000010802 sludge Substances 0.000 claims abstract description 17
- 239000004576 sand Substances 0.000 claims abstract description 12
- 239000000126 substance Substances 0.000 claims description 33
- 230000001105 regulatory Effects 0.000 claims description 27
- 238000000034 method Methods 0.000 claims description 26
- 238000005406 washing Methods 0.000 claims description 23
- 238000005188 flotation Methods 0.000 claims description 16
- 239000003814 drug Substances 0.000 claims description 12
- 238000009298 carbon filtering Methods 0.000 claims description 10
- 238000005273 aeration Methods 0.000 claims description 9
- 238000005189 flocculation Methods 0.000 claims description 8
- 230000016615 flocculation Effects 0.000 claims description 8
- 238000005276 aerator Methods 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 6
- 238000006460 hydrolysis reaction Methods 0.000 claims description 5
- 239000002244 precipitate Substances 0.000 claims description 5
- 206010042602 Supraventricular extrasystoles Diseases 0.000 claims description 4
- 230000033228 biological regulation Effects 0.000 claims description 4
- 230000020477 pH reduction Effects 0.000 claims description 4
- 229920002401 polyacrylamide Polymers 0.000 claims description 4
- 238000001556 precipitation Methods 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
- 238000007790 scraping Methods 0.000 claims description 4
- 239000002893 slag Substances 0.000 claims description 4
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 3
- 230000000844 anti-bacterial Effects 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 231100000719 pollutant Toxicity 0.000 claims description 3
- 238000010276 construction Methods 0.000 abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 6
- 239000010813 municipal solid waste Substances 0.000 abstract description 6
- 230000001131 transforming Effects 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract 2
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 229910000831 Steel Inorganic materials 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 206010002660 Anoxia Diseases 0.000 description 2
- 241000976983 Anoxia Species 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000005446 dissolved organic matter Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000000102 heterotrophic Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Abstract
The utility model relates to a handle cowherd's water distribution and wash modular sewage treatment device of waste water, a serial communication port, including the pump, the catch basin, the equalizing basin is being connected to the catch basin, a charge device is equipped with on the equalizing basin, the air supporting unit is being connected to the equalizing basin, the air supporting unit is equipped with the 2nd charge device and the 3rd charge device, first pond in the air supporting unit connection, blower connection the equalizing basin, first pond and second pond, the second pond is connected in first pond, the sedimentation tank is being connected in the second pond, the third pond is being connected to the sedimentation tank, the carbon filtration pond is being connected in the third pond, carbon filtration is connecting the sand filter in the pond, the clean water basin is being connected to the sand filter, the sludge impoundment is still being connected to the sedimentation tank, and filter press is being connected to the sludge impoundment. Each module can remove in a flexible way, and to place strong adaptability, area is little, but the equipment module workshop independently makes, on -site Assembly, and engineering construction period is short, but equipment unit module reutilization reduces the transformation and upgrading investment, the production that also reduces trash.
Description
Technical field
This utility model relates to a kind of technical field of sewage, more particularly, it relates to a kind of module type sewage processing equipment processing Cowboy Cloth Water Washing Wastewater.
Background technology
The treatment technology comparative maturity of Cowboy Cloth Water Washing Wastewater, but the intensive and plant area soil produced in the face of enterprise efficiently utilize development for, existing treatment technology has a following shortcoming: cesspool cell body, pipeline many employings xoncrete structure, construction work amount is big, floor space width, long construction period；Systematization is built, and globality is strong, and unit transformation and process modification are big by entire effect, it is difficult to individually upgrade；Between concrete basin, pipeline upgrading construction work amount is bigger；Pre-buried parts increase quantities, and later stage difficulty is transformed；After Fei Qi, difficulty is restored in place, produces concrete rubbish.
Therefore, prior art urgently has greatly improved.
Utility model content
The technical problems to be solved in the utility model is, above-mentioned defect for prior art, a kind of module type sewage processing equipment processing Cowboy Cloth Water Washing Wastewater is provided, it is characterized in that, including pump, equipped with artificial grid on collecting-tank, collecting-tank is connected to regulating reservoir, equipped with the first chemicals dosing plant on regulating reservoir, regulating reservoir is connected to air flotation cell, air flotation cell is provided with the second chemicals dosing plant and the 3rd chemicals dosing plant, air flotation cell is connected to the first pond, aerator is connected to regulating reservoir, first pond and the second pond, the second pond is connected below first pond, second pond is connected to sedimentation tank, sedimentation tank is connected to the 3rd pond, 3rd pond is connected to carbon filtering pool, carbon filtering pool is connected to sand filter, sand filter is connected to clear water reserviors；Sedimentation tank is also connected with sludge-tank, and sludge-tank is connected to filter press.
Wherein, described first chemicals dosing plant is provided with the alkali liquor that adding medicine is concentration 30%, is used for regulating pH value；Second chemicals dosing plant is provided with the PAC that adding medicine is concentration 5%, and the 3rd chemicals dosing plant is provided with the PAM that adding medicine is concentration 2 ‰, and waste water enters collecting-tank through artificial grid stream, rises to regulating reservoir through pump；Regulating reservoir utilizes pH meter and the first chemicals dosing plant regulation pH value, is mentioned air flotation cell by pump after uniform water quality；Air flotation cell front end adds flocculation medicament and flocculation aid, and by air-water mixing pump mixing water and gas-pressurized, flco is climbed up on top of the water by dissolved air water, and upper strata offscum is struck off through Slag Scraping Device, and lower layer of water gravity flow enters the first pond, precipitate and offscum and enters sludge-tank；First pond sewage enters the second pond after hydrolysis acidification, aerator aeration aerating is utilized in second pond, biochemical action through antibacterial removes pollutant, water outlet gravity flow enters precipitation suspended sludge in sedimentation tank, sedimentation tank, and partial sludge utilizes sludge reflux pump to be back to the first pond, unnecessary mud rises to sludge-tank by sludge pump, sedimentation tank water outlet flows automatically to the 3rd pond, then is promoted by pump, flows into clear water reserviors through carbon filtering pool and sand filter.
In the module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater described in the utility model, described regulating reservoir, the 3rd pond farther include: liquidometer.
In the module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater described in the utility model, described first chemicals dosing plant is provided with blender.
In the module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater described in the utility model, described second chemicals dosing plant is provided with blender.
In the module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater described in the utility model, described 3rd chemicals dosing plant is provided with blender.
In the module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater described in the utility model, described second pond aeration mode is disc type aeration.
In the module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater described in the utility model, filling inclined tube filler, strengthen suspended substance removal effect in described sedimentation tank, bottom sets sludge hopper.
In the module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater described in the utility model, described clear water reserviors are that carbon steel material makes.
Implementing the module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater of the present utility model, have the advantages that each module can move flexibly, to place strong adaptability, floor space is little；EM equipment module can independently make in workshop, Assembling, and the engineering construction cycle is short；Can be by increasing, reduce, change module, changing the mode such as module process position and upgrade flexibly the sewage treatment capacity of this equipment and process technique；Unit module can utilize by secondary, reduces transformation and upgrade investment, also reduces the generation of rubbish；The each module of equipment uses steel construction, and after equipment is completely discarded, steel are recyclable, will not produce garbage environment pollution, and engineering ground recovery operation is simple；Wastewater purifying efficiency is good, and equipment effluent quality meets national standard, can be back to use plant area, saves plant area's water cost.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is described in further detail, in accompanying drawing: Fig. 1 is the module diagram that this utility model processes the first embodiment of the module type sewage processing equipment of Cowboy Cloth Water Washing Wastewater.
Detailed description of the invention
Refer to Fig. 1, process the module diagram of the first embodiment of the module type sewage processing equipment of Cowboy Cloth Water Washing Wastewater for this utility model.As shown in Figure 1, in the module type sewage processing equipment processing Cowboy Cloth Water Washing Wastewater that this utility model first embodiment provides, at least include, pump, equipped with artificial grid on collecting-tank, collecting-tank is connected to regulating reservoir, equipped with the first chemicals dosing plant on regulating reservoir, regulating reservoir is connected to air flotation cell, air flotation cell is provided with the second chemicals dosing plant and the 3rd chemicals dosing plant, air flotation cell is connected to the first pond, aerator is connected to regulating reservoir, first pond and the second pond, first pond connects the second pond, second pond is connected to sedimentation tank, sedimentation tank is connected to the 3rd pond, 3rd pond is connected to carbon filtering pool, carbon filtering pool is connected to sand filter, sand filter is connected to clear water reserviors；Sedimentation tank is also connected with sludge-tank, and sludge-tank is connected to filter press.
Wherein, described first chemicals dosing plant is provided with the alkali liquor that adding medicine is concentration 30%, is used for regulating pH value；Second chemicals dosing plant is provided with the PAC that adding medicine is concentration 5%, and the 3rd chemicals dosing plant is provided with the PAM that adding medicine is concentration 2 ‰, and waste water enters collecting-tank through artificial grid stream, rises to regulating reservoir through pump；Regulating reservoir utilizes pH meter and the first chemicals dosing plant regulation pH value, is mentioned air flotation cell by pump after uniform water quality；Air flotation cell front end adds flocculation medicament and flocculation aid, and by air-water mixing pump mixing water and gas-pressurized, flco is climbed up on top of the water by dissolved air water, and upper strata offscum is struck off through Slag Scraping Device, and lower layer of water gravity flow enters the first pond, precipitate and offscum and enters sludge-tank；First pond sewage enters the second pond after hydrolysis acidification, aerator aeration aerating is utilized in second pond, biochemical action through antibacterial removes pollutant, water outlet gravity flow enters precipitation suspended sludge in sedimentation tank, sedimentation tank, and partial sludge utilizes sludge reflux pump to be back to the first pond, unnecessary mud rises to sludge-tank by sludge pump, sedimentation tank water outlet flows automatically to the 3rd pond, then is promoted by pump, flows into clear water reserviors through carbon filtering pool and sand filter.
Preferably, described regulating reservoir, the 3rd pond farther include: liquidometer.
Preferably, described first chemicals dosing plant is provided with blender.
Preferably, described second chemicals dosing plant is provided with blender.
Preferably, described 3rd chemicals dosing plant is provided with blender.
Preferably, described second pond aeration mode is disc type aeration.
Preferably, filling inclined tube filler, strengthen suspended substance removal effect in described sedimentation tank, bottom sets sludge hopper.
Preferably, described clear water reserviors are that carbon steel material makes.
Comprehensive wastewater gravity flow after bigger float removed by artificial grid enters collecting-tank, then rises to regulating reservoir with pump, carries out water quantity and quality regulation, adds lye pH adjustment to 7～8, uniformly after control water pump lifting to air supporting by liquidometer.
Air supporting front end adds flocculant PAC and flocculation aid PAM, produces flocculation with the small granular suspended matters in waste water, and gradually forms bigger floccule body, floats into offscum, scrapes sludge-tank with Slag Scraping Device, and sewage enters hydrolysis acidification pool, the i.e. first pond and the second pond.
Anoxia section and the oxygen consumption section of biochemical treatment are cascaded by the first pond and the second pond, anoxia section heterotrophic bacteria, the suspended contaminant such as the starch in sewage, fiber, carbohydrate and dissolved organic matter are hydrolyzed to organic acid, larger molecular organics is made to be decomposed into small organic molecule, insoluble Organic substance changes into dissolved organic matter, improve the biodegradability of sewage, when these carry out Aerobic Process for Treatment through the product entrance Aerobic Pond of anaerobic hydrolysis, the removal efficiency of aerobic section organic pollution can be improved.Aerobic section passes through aerator oxygen supply, utilizes aerobic bacteria to absorb decomposing organic matter, and removable major part can biochemical organic pollution.
Second pond water outlet enters sedimentation tank, carries out precipitation process, precipitates float, precipitate partial reflux to the first front end, pond, and remainder enters sludge-tank, and sewage enters the 3rd pond.
Utilizing liquidometer to control water pump in 3rd pond, lifting sewage enters activated carbon filter+quartz sand filter tank, further decolouring and filtration float, and water outlet flows into clear water reserviors.Activated carbon filter and quartz sand filter tank are according to water outlet situation, variable interval backwash.
Clear water reserviors water quality reaches emission request, and water outlet is directly discharged or plant area's reuse.
In Waste Water Treatment, produced mud fills through filter press processed, the outward transport of dry mud or is uniformly processed, and filter pressing water is from flowing back into regulating reservoir.
This utility model design by first embodiment above, can accomplish that each module can move flexibly, and to place strong adaptability, floor space is little；EM equipment module can independently make in workshop, Assembling, and the engineering construction cycle is short；Can be by increasing, reduce, change module, changing the mode such as module process position and upgrade flexibly the sewage treatment capacity of this equipment and process technique；Unit module can utilize by secondary, reduces transformation and upgrade investment, also reduces the generation of rubbish；The each module of equipment uses steel construction, and after equipment is completely discarded, steel are recyclable, will not produce garbage environment pollution, and engineering ground recovery operation is simple；
Efficiency of Sewage Treatment is good, and equipment effluent quality meets national standard, can be back to use plant area, saves plant area's water cost.
This utility model is described according to specific embodiment, but those skilled in the art is when without departing from this utility model scope, can carry out various change and equivalent.Additionally, be the specific occasion adapting to this utility model technology, this utility model can be carried out many amendments without deviating from its protection domain.Therefore, this utility model is not limited to specific embodiment disclosed herein, and includes all embodiments dropping into claims.
Claims (8)
1. the module type sewage processing equipment processing Cowboy Cloth Water Washing Wastewater, it is characterized in that, including pump, collecting-tank, collecting-tank is connected to regulating reservoir, equipped with the first chemicals dosing plant on regulating reservoir, regulating reservoir is connected to air flotation cell, air flotation cell is provided with the second chemicals dosing plant and the 3rd chemicals dosing plant, air flotation cell is connected to the first pond, aerator is connected to regulating reservoir, first pond and the second pond, first pond connects the second pond, second pond is connected to sedimentation tank, sedimentation tank is connected to the 3rd pond, 3rd pond is connected to carbon filtering pool, carbon filtering pool is connected to sand filter, sand filter is connected to clear water reserviors；Sedimentation tank is also connected with sludge-tank, and sludge-tank is connected to filter press,
Wherein, described first chemicals dosing plant is provided with the alkali liquor that adding medicine is concentration 30%, is used for regulating pH value；Second chemicals dosing plant is provided with the PAC that adding medicine is concentration 5%, and the 3rd chemicals dosing plant is provided with the PAM that adding medicine is concentration 2 ‰, and waste water enters collecting-tank through artificial grid stream, rises to regulating reservoir through pump；Regulating reservoir utilizes pH meter and the first chemicals dosing plant regulation pH value, is mentioned air flotation cell by pump after uniform water quality；Air flotation cell front end adds flocculation medicament and flocculation aid, and by air-water mixing pump mixing water and gas-pressurized, flco is climbed up on top of the water by dissolved air water, and upper strata offscum is struck off through Slag Scraping Device, and lower layer of water gravity flow enters the first pond, precipitate and offscum and enters sludge-tank；First pond sewage enters the second pond after hydrolysis acidification, aerator aeration aerating is utilized in second pond, biochemical action through antibacterial removes pollutant, water outlet gravity flow enters precipitation suspended sludge in sedimentation tank, sedimentation tank, and partial sludge utilizes sludge reflux pump to be back to the first pond, unnecessary mud rises to sludge-tank by sludge pump, sedimentation tank water outlet flows automatically to the 3rd pond, then is promoted by pump, flows into clear water reserviors through carbon filtering pool and sand filter.
The module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater the most according to claim 1, it is characterised in that described regulating reservoir, the 3rd pond farther include: liquidometer.
The module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater the most according to claim 1, it is characterised in that described first chemicals dosing plant is provided with blender.
The module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater the most according to claim 1, it is characterised in that described second chemicals dosing plant is provided with blender.
The module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater the most according to claim 1, it is characterised in that described 3rd chemicals dosing plant is provided with blender.
The module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater the most according to claim 1, it is characterised in that described second pond aeration mode is disc type aeration.
The module type sewage processing equipment of process Cowboy Cloth Water Washing Wastewater the most according to claim 1, it is characterised in that filling inclined tube filler in described sedimentation tank, bottom sets sludge hopper.
8. according to the module type sewage processing equipment processing Cowboy Cloth Water Washing Wastewater described in claim 1 to 7 any one claim, it is characterized in that, described regulating reservoir, air flotation cell, the first pond, the second pond, sludge-tank, sedimentation tank, the 3rd pond, carbon filtering pool, sand filter, clear water reserviors are carbon steel material and make.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620096804.0U CN205473235U (en) | 2016-01-29 | 2016-01-29 | Handle cowherd's water distribution and wash modular sewage treatment device of waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620096804.0U CN205473235U (en) | 2016-01-29 | 2016-01-29 | Handle cowherd's water distribution and wash modular sewage treatment device of waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205473235U true CN205473235U (en) | 2016-08-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620096804.0U Active CN205473235U (en) | 2016-01-29 | 2016-01-29 | Handle cowherd's water distribution and wash modular sewage treatment device of waste water |
Country Status (1)
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| CN (1) | CN205473235U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109534608A (en) * | 2018-12-21 | 2019-03-29 | 泽州县和美环保科技有限公司 | A kind of domestic sewage processing system and processing method |
-
2016
- 2016-01-29 CN CN201620096804.0U patent/CN205473235U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109534608A (en) * | 2018-12-21 | 2019-03-29 | 泽州县和美环保科技有限公司 | A kind of domestic sewage processing system and processing method |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211022 Address after: 277000 southeast of Yicheng bridge vegetable wholesale market, Zaozhuang City, Shandong Province Patentee after: Zaozhuang Yixin Environmental Technology Co.,Ltd. Address before: 250101 rooms 1-2317, building 1, No.88, West Convention and Exhibition Road, high tech Zone, Jinan City, Shandong Province Patentee before: JINAN MEIYADA ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
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| TR01 | Transfer of patent right |