CN117023895A - Integrated water treatment device - Google Patents
Integrated water treatment device Download PDFInfo
- Publication number
- CN117023895A CN117023895A CN202311133895.1A CN202311133895A CN117023895A CN 117023895 A CN117023895 A CN 117023895A CN 202311133895 A CN202311133895 A CN 202311133895A CN 117023895 A CN117023895 A CN 117023895A
- Authority
- CN
- China
- Prior art keywords
- tank
- water treatment
- treatment device
- water
- ultrafiltration membrane
- 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.)
- Withdrawn
Links
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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
- C02F1/62—Heavy metal compounds
- C02F1/64—Heavy metal compounds of iron or manganese
-
- 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- 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
- C02F2101/203—Iron or iron compound
-
- 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
- C02F2101/206—Manganese or manganese 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
- 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
- C02F2303/00—Specific treatment goals
- C02F2303/02—Odour removal or prevention of malodour
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The application relates to an integrated water treatment device, the pretreatment can be divided into a coagulation sedimentation process and a micro flocculation air floatation process, the ultrafiltration membrane process position can be divided into a manganese sand filter process for removing iron and manganese before or after an ozone activated carbon process, the integrated water treatment device is an integrated water treatment device taking air floatation as pretreatment or an integrated water treatment device taking sedimentation as pretreatment, and both the integrated water treatment devices comprise an ultrafiltration membrane pool. The integrated device is formed by combining the preozonation, air flotation (or precipitation), post-ozonation, active carbon, ultrafiltration membrane, iron and manganese removal manganese sand filter tank and other processes commonly used in drinking water treatment according to different requirements, can reasonably select different raw water quality, ensure the standard reaching, and provide high-quality water.
Description
Technical Field
The application relates to the technical field of water treatment equipment, in particular to an integrated water treatment device.
Background
In the prior art, the conditions of village and town drinking water sources are various, the water quantity and the water quality are greatly changed, and the adopted water treatment process and the water treatment process are mainly in the form of single process single device or multiple process devices in series, so that the occupied area is large, the pipeline length and the equipment length and width are not uniform, and the elevation is not consistent, so that the raw water quality cannot be reasonably selected. With the formal execution of new drinking water sanitation standards, the village and town drinking water treatment process also needs targeted and adaptive measures.
Disclosure of Invention
Aiming at the defects existing in the prior art, the application aims to provide an integrated water treatment device which combines the common pre-ozone and air floatation (or sedimentation), post-ozone, activated carbon, ultrafiltration membrane, manganese sand filter for iron and manganese removal and other processes in the drinking water treatment into an integrated device according to different requirements, can reasonably select and use different raw water quality, ensures the standard and provides high-quality water.
The above object of the present application is achieved by the following technical solutions:
the integrated water treatment device is an integrated water treatment device taking air floatation as pretreatment or an integrated water treatment device taking precipitation as pretreatment, and both the integrated water treatment devices comprise ultrafiltration membrane tanks.
The present application may be further configured in a preferred example to: the integrated water treatment device with the air floatation as pretreatment comprises a pre-ozone tank, a mixing stirring tank, a flocculation tank, an air floatation sand filter tank, an upflow activated carbon filter tank and an ultrafiltration membrane tank which are sequentially connected, wherein equipment rooms are arranged below the pre-ozone tank and the flocculation tank, a water collecting tank on the upper part of the upflow activated carbon filter tank collects water and is used for water inflow from the upper part of the ultrafiltration membrane tank, and the integrated water treatment device with the air floatation as pretreatment adopts ultrafiltration membrane water production to perform downflow water inflow and forward flushing.
The present application may be further configured in a preferred example to: the integrated water treatment device with the air floatation as pretreatment comprises a pre-ozone tank, a mixing stirring tank, a flocculation tank, an air floatation activated carbon filter tank and an ultrafiltration membrane tank which are sequentially connected, wherein equipment rooms are arranged below the pre-ozone tank and the flocculation tank.
The present application may be further configured in a preferred example to: the integrated water treatment device with the air floatation as pretreatment comprises a pre-ozone tank, a mixing stirring tank, a flocculation tank, an air floatation ultrafiltration membrane tank, a middle water tank, a rear ozone tank and an activated carbon filter tank which are sequentially connected, wherein a water outlet pipe at the middle position of the air floatation ultrafiltration membrane tank is connected with the bottom of the middle water tank through a pipeline, a lifting pump is arranged on the pipeline, and a wastewater tank communicated with the bottom of the activated carbon filter tank is arranged at the bottom of the activated carbon filter tank.
The present application may be further configured in a preferred example to: the integrated water treatment device with sedimentation as pretreatment comprises a pre-ozone tank, a mixing stirring tank, a flocculation tank, an inclined tube sedimentation tank, a manganese sand filter tank, a middle water tank, an upflow type active carbon filter tank and an ultrafiltration membrane tank which are sequentially connected, wherein a water outlet pipe at the bottom of the manganese sand filter tank is connected with the bottom of the middle water tank through a pipeline, a lifting pump is arranged on the pipeline, a wastewater tank communicated with the bottom of the ultrafiltration membrane tank is arranged at the bottom of the ultrafiltration membrane tank, and equipment rooms are arranged below the middle water tank and the upflow type active carbon filter tank.
The present application may be further configured in a preferred example to: the integrated water treatment device with sediment is pretreatment comprises a pre-ozone tank, a mixing stirring tank, a flocculation tank, an inclined tube sedimentation tank, an ultrafiltration membrane tank, a middle water tank, an ozone tank and an activated carbon filter tank which are sequentially connected, wherein the middle position of the ultrafiltration membrane tank is connected with the bottom of the middle water tank through a pipeline, a lifting pump is arranged on the pipeline, the middle water tank and the lower part of the ozone tank are provided with equipment rooms, and the integrated water treatment device with sediment is pretreatment adopts the forward flow process treatment water to carry out down water forward flushing.
The present application may be further configured in a preferred example to: the water flow direction width of each treatment unit is consistent, the front water treatment tank and the rear water treatment tank are attached and are co-walled, and water is uniformly fed and produced.
The present application may be further configured in a preferred example to: the various connecting pipes, the mud discharging pipes and the air inlet pipes outside the tank body are all arranged on one side, and the two groups of integrated device pipelines form a double-device parallel arrangement mode of the middle pipe gallery.
The present application may be further configured in a preferred example to: the foundation slab where the integrated water treatment device is positioned is flush, and the middle water tank is arranged at the position where middle lifting is required in the process, so that the water level is improved, water distribution is carried out on the subsequent process, and flushing water is provided for a filtering tank in front of the middle water tank.
In summary, the present application includes at least one of the following beneficial technical effects:
1. the application discloses an integrated water treatment device which is an integrated water treatment device taking air floatation as pretreatment or an integrated water treatment device taking precipitation as pretreatment. The integrated device is formed by combining the preozonation, air flotation (or precipitation), the post-ozonation, active carbon, an ultrafiltration membrane, a manganese sand filter for removing iron and manganese and the like which are commonly used in the drinking water treatment according to different requirements, can reasonably select different raw water quality, ensures the standard reaching, and provides high-quality water.
2. The basic configuration of the integrated water treatment device comprises: the pretreatment, the ozone activated carbon and the ultrafiltration membrane can be optionally configured as a ferric manganese filter, and the pre-ozone and the post-ozone can be simultaneously configured or selected. And multiple processes are combined, the pool body is reasonable in utilization of the same width, the front and rear common walls and the elevation, the arrangement is compact and the occupied area is small, and the pool body can be flexibly arranged into double groups of middle pipe galleries or a plurality of double groups of adjacent arrangement.
3. The ultrafiltration membrane pool in the integrated water treatment device adopts a lower water inlet gas-water forward flushing and upper water discharging mode, so that suspended particles are taken away upwards as much as possible, the number of times of downward emptying is reduced, water used in forward flushing makes use of water discharged in the previous process as much as possible, the consumption of product water can be reduced by forward flushing of process water, and the defects caused by restarting the previous process after stopping running can be avoided.
Drawings
Fig. 1 is a cross-sectional view of the second embodiment.
Fig. 2 is a plan view of the second embodiment.
Fig. 3 is a cross-sectional view of the third embodiment.
Fig. 4 is a cross-sectional view of the fourth embodiment.
Fig. 5 is a cross-sectional view of the fifth embodiment.
Fig. 6 is a cross-sectional view of the sixth embodiment.
Reference numerals:
fig. 1 and 2 show: 1. pre-ozone pool; 2. mixing and stirring pool; 3. a flocculation tank; 4. an air-float sand filter tank; 5. an upflow activated carbon filter; 6. an ultrafiltration membrane pool; 7. the equipment room;
shown in fig. 3: 1. pre-ozone pool; 2. mixing and stirring pool; 3. a flocculation tank; 4. an air-floating activated carbon filter tank; 5. an ultrafiltration membrane pool; 6. the equipment room;
shown in fig. 4: 1. pre-ozone pool; 2. mixing and stirring pool; 3. a flocculation tank; 4. an air floatation ultrafiltration membrane pool; 5. a lift pump; 6. an intermediate water tank; 7. a rear ozone pool; 8. an activated carbon filter tank; 9. a wastewater tank; 10. the equipment room;
shown in fig. 5: 1. pre-ozone pool; 2. mixing and stirring pool; 3. a flocculation tank; 4. a pipe chute sedimentation tank; 5. a manganese sand filter tank; 6. a lift pump; 7. an intermediate water tank; 8. upflow active carbon filtration; 9. an ultrafiltration membrane pool; 10. a wastewater tank; 11. the equipment room;
shown in fig. 6: 1. pre-ozone pool; 2. mixing and stirring pool; 3. a flocculation tank; 4. a pipe chute sedimentation tank; 5. an ultrafiltration membrane pool; 6. a lift pump; 7. an intermediate water tank; 8. an ozone pool; 9. an activated carbon filter tank; 10. the equipment room;
Detailed Description
The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present application; it is apparent that the described embodiments are only some embodiments of the present application, not all embodiments, and that all other embodiments obtained by persons of ordinary skill in the art without making creative efforts based on the embodiments in the present application are within the protection scope of the present application.
In the description of the present application, it should be noted that the positional or positional relationship indicated by the terms such as "upper", "lower", "inner", "outer", "top/bottom", etc. are based on the positional or positional relationship shown in the drawings, are merely for convenience of describing the present application and simplifying the description, and do not indicate or imply that the apparatus or elements referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus should not be construed as limiting the present application. Furthermore, the terms "first," "second," and the like, are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present application, it should be noted that, unless explicitly specified and limited otherwise, the terms "mounted," "configured to," "engaged with," "connected to," and the like are to be construed broadly, and may be either fixedly connected, detachably connected, or integrally connected, for example; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present application will be understood in specific cases by those of ordinary skill in the art.
Embodiment one:
the application discloses an integrated water treatment device, the pretreatment can be divided into a coagulation sedimentation process and a micro flocculation air floatation process, the ultrafiltration membrane process position can be divided into a manganese sand filter process for removing iron and manganese before or after an ozone active carbon process, the integrated water treatment device is an integrated water treatment device taking air floatation as pretreatment or an integrated water treatment device taking sedimentation as pretreatment, and in the embodiment, both integrated water treatment devices comprise an ultrafiltration membrane pool.
Embodiment two:
referring to fig. 1-2, the integrated water treatment device using air floatation as pretreatment comprises a pre-ozone tank 1, a mixing stirring tank 2, a flocculation tank 3, an air floatation (manganese sand) sand filter tank 4, an upflow activated carbon filter tank 5 and an ultrafiltration membrane tank 6 which are sequentially connected, wherein an equipment room 7 is arranged below the pre-ozone tank 1 and the flocculation tank 3, water is collected in a water collecting tank at the upper part of the upflow activated carbon filter tank 5 and is fed from the upper part of the ultrafiltration membrane tank 6, the integrated water treatment device using air floatation as pretreatment adopts ultrafiltration membrane water production to carry out downward water inflow forward flushing, and the integrated water treatment device using air floatation as pretreatment adopts water collection at the upper part of the upflow activated carbon tank 5 and enters the ultrafiltration membrane tank 6 from the upper part.
Embodiment III:
referring to fig. 3, the integrated water treatment device using air floatation as pretreatment comprises a pre-ozone tank 1, a mixing and stirring tank 2, a flocculation tank 3, an air floatation activated carbon filter tank 4 and an ultrafiltration membrane tank 5 which are sequentially connected, wherein an equipment room 6 is arranged below the pre-ozone tank 1 and the flocculation tank 3.
Embodiment four:
referring to fig. 4, the integrated water treatment device using air floatation as pretreatment comprises a pre-ozone tank 1, a mixing stirring tank 2, a flocculation tank 3, an air floatation ultrafiltration membrane tank 4, a middle water tank 6, a rear ozone tank 7 and an activated carbon filter tank 8 which are sequentially connected, wherein a water outlet pipe at the middle position of the air floatation ultrafiltration membrane tank 4 is connected with the bottom of the middle water tank 6 through a pipeline, a lifting pump 5 is arranged on the pipeline, and a wastewater tank 9 communicated with the bottom of the activated carbon filter tank 8 is arranged at the bottom of the activated carbon filter tank.
Fifth embodiment:
referring to fig. 5, the integrated water treatment device using precipitation as pretreatment comprises a pre-ozone tank 1, a mixing stirring tank 2, a flocculation tank 3, an inclined tube (inclined plate) sedimentation tank 4, a manganese sand filter tank 5, an intermediate water tank 7, an upflow activated carbon filter 8 tank and an ultrafiltration membrane tank 9 which are sequentially connected, wherein a water outlet pipe at the bottom of the manganese sand filter tank 5 is connected with the bottom of the intermediate water tank 7 through a pipeline, a lifting pump 6 is mounted on the pipeline, a wastewater tank 10 communicated with the wastewater tank is mounted at the bottom of the ultrafiltration membrane tank 9, and an equipment room 11 is arranged below the intermediate water tank 7 and the upflow activated carbon filter 8 tank.
Example six:
referring to fig. 6, the integrated water treatment device using the sedimentation as the pretreatment comprises a pre-ozone tank 81, a mixing stirring tank 2, a flocculation tank 3, an inclined tube (inclined plate) sedimentation tank 4, an ultrafiltration membrane tank 5, an intermediate water tank 7, an ozone tank 8 and an activated carbon filter tank 9 which are sequentially connected, wherein the intermediate position of the ultrafiltration membrane tank 5 is connected with the bottom of the intermediate water tank 7 through a pipeline, a lifting pump 6 is arranged on the pipeline, an equipment room 10 is arranged below the intermediate water tank 7 and the ozone tank 8, and the integrated water treatment device using the sedimentation as the pretreatment adopts the prior follow current process to treat water for forward flushing.
The implementation principle of the application is as follows: the application discloses an integrated water treatment device which is an integrated water treatment device taking air floatation as pretreatment or an integrated water treatment device taking precipitation as pretreatment. The integrated device is formed by combining the preozonation, air flotation (or precipitation), the post-ozonation, active carbon, an ultrafiltration membrane, a manganese sand filter for removing iron and manganese and the like which are commonly used in the drinking water treatment according to different requirements, can reasonably select different raw water quality, ensures the standard reaching, and provides high-quality water.
The water flow direction width of each treatment unit is consistent, the front water treatment tank and the rear water treatment tank are attached and are co-walled, and water is uniformly fed and produced. The various connecting pipes, the mud discharging pipes and the air inlet pipes outside the tank body are all arranged on one side, and the two groups of integrated device pipelines form a double-device parallel arrangement mode of the middle pipe gallery.
The foundation slab where the integrated water treatment device is positioned is flush, and the middle water tank is arranged at the position where the middle lifting is required in the process, so that the water level is improved, the water distribution of the back process is realized, and flushing water is provided for the filtering ponds in front of the middle water tank. The ultrafiltration membrane tanks in the integrated water treatment device all adopt a flushing drainage mode that air water which is discharged from the lower water inlet and the upper water outlet is flushed along the upper water outlet.
The integrated water treatment device of each process combination has different requirements of removing turbidity, algae, organic matters, smell, iron and manganese and the like, can be used selectively according to different raw water conditions, ensures the safety of drinking water in rural areas and villages and towns, improves the quality of water supply, and has the advantages of high combined pool type intensive land saving, small overall body quantity, low investment and wide application prospect.
The embodiments of the present application are all preferred embodiments of the present application, and are not intended to limit the scope of the present application in this way, therefore: all equivalent changes in structure, shape and principle of the application should be covered in the scope of protection of the application.
Claims (9)
1. The integrated water treatment device is characterized by comprising an ultrafiltration membrane pool.
2. The integrated water treatment device according to claim 1, wherein the integrated water treatment device using air floatation as pretreatment comprises a pre-ozone tank (1), a mixing stirring tank (2), a flocculation tank (3), an air floatation sand filter tank (4), an upflow activated carbon filter tank (5) and an ultrafiltration membrane tank (6) which are sequentially connected, an equipment room (7) is arranged below the pre-ozone tank (1) and the flocculation tank (3), water is collected in a water collecting tank at the upper part of the upflow activated carbon filter tank (5) and is fed from the upper part of the ultrafiltration membrane tank (6), and the integrated water treatment device using air floatation as pretreatment adopts ultrafiltration membrane water production to perform downflow forward flushing.
3. The integrated water treatment device according to claim 1, wherein the integrated water treatment device using air floatation as pretreatment comprises a pre-ozone tank (1), a mixing stirring tank (2), a flocculation tank (3), an air floatation activated carbon filter tank (4) and an ultrafiltration membrane tank (5) which are sequentially connected, wherein an equipment room (6) is arranged below the pre-ozone tank (1) and the flocculation tank (3).
4. The integrated water treatment device according to claim 1, wherein the integrated water treatment device using air floatation as pretreatment comprises a pre-ozone tank (1), a mixing stirring tank (2), a flocculation tank (3), an air floatation ultrafiltration membrane tank (4), an intermediate water tank (6), a rear ozone tank (7) and an activated carbon filter tank (8) which are sequentially connected, a water outlet pipe at the intermediate position of the air floatation ultrafiltration membrane tank (4) is connected with the bottom of the intermediate water tank (6) through a pipeline, a lifting pump (5) is mounted on the pipeline, and a wastewater tank (9) communicated with the activated carbon filter tank (8) is mounted at the bottom of the activated carbon filter tank.
5. The integrated water treatment device according to claim 1, wherein the integrated water treatment device using precipitation as pretreatment comprises a pre-ozone tank (1), a mixing stirring tank (2), a flocculation tank (3), an inclined tube sedimentation tank (4), a manganese sand filter tank (5), an intermediate water tank (7), an upflow activated carbon filter (8) tank and an ultrafiltration membrane tank (9) which are sequentially connected, a water outlet pipe at the bottom of the manganese sand filter tank (5) is connected with the bottom of the intermediate water tank (7) through a pipeline, a lifting pump (6) is mounted on the pipeline, a wastewater tank (10) communicated with the bottom of the ultrafiltration membrane tank (9) is mounted, and an equipment room (11) is arranged below the intermediate water tank (7) and the upflow activated carbon filter (8) tank.
6. The integrated water treatment device according to claim 1, wherein the integrated water treatment device using precipitation as pretreatment comprises a pre-ozone tank (8) (1), a mixing stirring tank (2), a flocculation tank (3), an inclined tube sedimentation tank (4), an ultrafiltration membrane tank (5), an intermediate water tank (7), an ozone tank (8) and an activated carbon filter tank (9) which are sequentially connected, the intermediate position of the ultrafiltration membrane tank (5) is connected with the bottom of the intermediate water tank (7) through a pipeline, a lifting pump (6) is mounted on the pipeline, an equipment room (10) is arranged below the intermediate water tank (7) and the ozone tank (8), and the integrated water treatment device using precipitation as pretreatment uses the pre-flow process treated water to perform downwash.
7. The integrated water treatment device according to any one of claims 1 to 6, wherein the water flow direction width of each treatment unit is consistent, the front water treatment tank and the rear water treatment tank are attached and co-wall, and water is uniformly fed and produced.
8. The integrated water treatment device according to any one of claims 1 to 6, wherein various connecting pipes, sludge discharge pipes and air inlet pipes outside the tank body are arranged on one side, and two groups of integrated device pipelines form a double-device parallel arrangement mode of a middle pipe gallery.
9. The integrated water treatment device of any one of claims 1-6, wherein the foundation slab on which the integrated water treatment device is located is flush, and wherein intermediate tanks are provided at positions in the process where intermediate lifting is required to raise the water level to distribute water to the subsequent process and to provide rinse water to the filter tank preceding the intermediate tanks.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311133895.1A CN117023895A (en) | 2023-09-05 | 2023-09-05 | Integrated water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311133895.1A CN117023895A (en) | 2023-09-05 | 2023-09-05 | Integrated water treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN117023895A true CN117023895A (en) | 2023-11-10 |
Family
ID=88628267
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202311133895.1A Withdrawn CN117023895A (en) | 2023-09-05 | 2023-09-05 | Integrated water treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN117023895A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2025175366A1 (en) * | 2024-02-20 | 2025-08-28 | Sartori Mario Sergio | System and method for continuous flow treatment of sewage/effluent |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103253787A (en) * | 2012-02-17 | 2013-08-21 | 上海市政工程设计研究总院（集团）有限公司 | Season metal polluted low-turbidity high-alga raw water strengthening treatment apparatus and technology thereof |
| CN203247164U (en) * | 2013-03-15 | 2013-10-23 | 佛山市水业集团有限公司 | Raw water treatment device |
| CN103523967A (en) * | 2013-11-05 | 2014-01-22 | 哈尔滨工业大学 | Method for treating short-flow water with sedimentation and air-floating coupling as core |
| CN104118957A (en) * | 2014-07-09 | 2014-10-29 | 上海交通大学 | Traditional water purification process based land saving reconstruction upgrade method |
| CN204643997U (en) * | 2015-02-04 | 2015-09-16 | 芜湖市晨曦新型建材科技有限公司 | A kind of novel ultrafiltration ozone water purifier |
| CN115849640A (en) * | 2023-02-13 | 2023-03-28 | 浙江钱江水利供水有限公司 | Pressure flowing water ozone ultrafiltration membrane water purification treatment method |
-
2023
- 2023-09-05 CN CN202311133895.1A patent/CN117023895A/en not_active Withdrawn
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103253787A (en) * | 2012-02-17 | 2013-08-21 | 上海市政工程设计研究总院（集团）有限公司 | Season metal polluted low-turbidity high-alga raw water strengthening treatment apparatus and technology thereof |
| CN203247164U (en) * | 2013-03-15 | 2013-10-23 | 佛山市水业集团有限公司 | Raw water treatment device |
| CN103523967A (en) * | 2013-11-05 | 2014-01-22 | 哈尔滨工业大学 | Method for treating short-flow water with sedimentation and air-floating coupling as core |
| CN104118957A (en) * | 2014-07-09 | 2014-10-29 | 上海交通大学 | Traditional water purification process based land saving reconstruction upgrade method |
| CN204643997U (en) * | 2015-02-04 | 2015-09-16 | 芜湖市晨曦新型建材科技有限公司 | A kind of novel ultrafiltration ozone water purifier |
| CN115849640A (en) * | 2023-02-13 | 2023-03-28 | 浙江钱江水利供水有限公司 | Pressure flowing water ozone ultrafiltration membrane water purification treatment method |
Non-Patent Citations (6)
| Title |
|---|
| 刘前军;周胜昔;: "超滤膜组合工艺在大型净水厂扩建工程中的应用", 中国给水排水, no. 08, 17 April 2017 (2017-04-17) * |
| 刘杰: "生活用水和工业废水处理理论和技术研究", 31 December 2018, 北京工业大学出版社, pages: 73 - 75 * |
| 常春: "东丽PVDF中空纤维超滤膜在污染地表水处理中的应用研究", 中国建设信息（水工业市场）, no. 03, 31 March 2009 (2009-03-31), pages 99 * |
| 常春;杨瑜芳;董秉直;高乃云;: "东丽PVDF中空纤维超滤膜在污染地表水处理中的应用研究", 中国建设信息(水工业市场), no. 03, 31 March 2009 (2009-03-31), pages 99 * |
| 广州市市政工程设计研究总院有限公司: "臭氧预氧化-絮凝-气浮-砂滤-臭氧活性炭耦合生活饮用水处理工艺生产性试验研究", Retrieved from the Internet <URL:http://zfcxjst.gd.gov.cn/zwzt/kjhdz/kjcg/content/post_4186771.html> * |
| 郑钊等: "微污染水库水超滤膜处理工艺的试验研究", 水资源保护, vol. 32, no. 3, 31 May 2016 (2016-05-31) * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2025175366A1 (en) * | 2024-02-20 | 2025-08-28 | Sartori Mario Sergio | System and method for continuous flow treatment of sewage/effluent |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103922527B (en) | Integrated sewage water advanced treatment apparatus and technique thereof | |
| CN201292263Y (en) | Vertical flow type aerobic gas float filter chamber | |
| CN102179073A (en) | Pump suction type sludge residue external reflux high-efficiency clarification tank | |
| CN203613071U (en) | Sewage treatment device | |
| CN110590080A (en) | A biofilm sewage treatment equipment | |
| CN101530681A (en) | Seawater clarifier turbulence construction and clarifier thereof | |
| CN201056512Y (en) | Film component integrated oxidation ditch | |
| CN117023895A (en) | Integrated water treatment device | |
| CN103539280A (en) | Integrated water purification device | |
| CN101870534A (en) | Combined water purification structure | |
| CN115770419A (en) | A Vertical Inclined Tube Precipitation Structure and Its Application | |
| CN201999778U (en) | Single-layer pressure integration oil eliminator | |
| CN201890787U (en) | Double-layered pressure type integrated deoiler | |
| CN212504433U (en) | Black and odorous river water body treatment system based on ultramicro separation and aerobic biochemical treatment | |
| CN108164038A (en) | A kind of Water feeding treatment device and processing method | |
| CN107935273A (en) | Gravity installation intelligent control backwashing sewage water processing system | |
| CN202139152U (en) | Integrated three-phase separation purifier | |
| CN201952305U (en) | A kind of sewage treatment equipment | |
| CN201033744Y (en) | Air-float filter chamber | |
| CN213141681U (en) | Sedimentation tank for siphon sludge discharge | |
| CN206396000U (en) | Aquaculture wastewater processing system | |
| CN203890153U (en) | Complete set of water quality purification treatment all-in-one equipment | |
| CN201370981Y (en) | Seawater clarification pool with turbulent flow structure | |
| CN108083507A (en) | A kind of integrated form Water feeding treatment device and processing method | |
| CN211620172U (en) | High-density air flotation sedimentation tank |
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 | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20231110 |