KR20100007483A - Water treatment method and equipment for pollution water - Google Patents
Water treatment method and equipment for pollution water Download PDFInfo
- Publication number
- KR20100007483A KR20100007483A KR1020080068130A KR20080068130A KR20100007483A KR 20100007483 A KR20100007483 A KR 20100007483A KR 1020080068130 A KR1020080068130 A KR 1020080068130A KR 20080068130 A KR20080068130 A KR 20080068130A KR 20100007483 A KR20100007483 A KR 20100007483A
- Authority
- KR
- South Korea
- Prior art keywords
- water
- raw water
- supplying
- filter
- floc
- Prior art date
Links
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
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- 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
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- 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
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- 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
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
Abstract
Description
Environmental Water Treatment
Background art of the present invention is to infuse flocculant injected to treat contaminated raw water containing minerals into raw water by injector and line mix and increase the size of mixed flocs by flocculation tank The purified floc flows into the hydrocyclone and is separated by the centrifugal force of the cyclone, and the purified water is filtered by a hydrostatic filter to purify the water more clearly. More specifically, the water flow pressure when supplying the flocculant to the raw water. And the line mixer and floc forming tank to grow the mixed floc with the injector which is rapidly diffused into the injector, and the hydrocyclone to rapidly separate the formed floc, the filtration to filter out the fine solids, and It is a combination of backwashing technology that desorbs the solids attached to the filter by the compressed air.
In the meantime, the raw water is transferred to the coagulation tank, the coagulant is added to the coagulation tank, stirred by the stirrer, and when a floc is formed, the floc-containing water containing the floc is transferred to the sedimentation basin, whereby the solids (frog) are precipitated. After extraction, it is taken out and treated, and the symbolic water of the sedimentation tank is transferred to a filter, filtered, and then discharged or utilized.
Such a method requires a feed pump to inject coagulant, agitators and agitation tanks to mix the coagulant with raw water, and a driving unit or a large area is required to settle flocs. In addition, a sludge collector and a drawer were required to take out the precipitated flocs. In addition, the conventional facilities are installed in series (coagulation tank ⇒ sedimentation tank ⇒ filtration tank) requires a lot of area and power and took a long time to operate.
The problem to be solved by the present invention is to improve the existing methods applied to the flocculant input, floc formation, sedimentation and filtration as described above to combine the respective facilities installed in a small area and significantly reduce the time required The present invention provides a method and apparatus for water treatment that can increase efficiency while significantly reducing energy consumption.
The present invention provides an injector in injecting a coagulant into the raw water to remove contaminants contained in the raw water, a line mix is provided to mix and flocculate the coagulant injected into the raw water, and the floc formed in the raw water can be quickly The hydrocyclone is formed to separate and the filter is formed to remove particulates contained in the supernatant separated by the hydrocyclone. In addition, a backwashing process is provided for desorbing particulates, which are contaminants attached to the surface of the filter, by compressed air so that the filter can be repeatedly used.
According to the present invention, by quickly removing the contaminants contained in the raw water by the above-mentioned solution, the facility can be treated more simply and quickly than the existing water treatment method, so that the contaminated water is treated in a smaller area and shorter time than the existing water treatment method. There is an effect that can significantly reduce the energy and personnel required.
Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
1 is a schematic diagram of an apparatus for treating contaminated water according to the method of the present invention.
Figure 2 is a detailed view of the injector (3) is characterized in that the inlet aperture is gradually reduced to the nozzle neck as shown in the figure, and then gradually expands after passing through the nozzle neck, so that the speed is instantaneously when the fluid passes through the nozzle neck. The nozzle neck portion through which the fluid passes has negative pressure.
The negative pressure generated at this time forms a force capable of sucking another fluid through the suction port of another fluid formed in the nozzle neck.
Referring to the present invention by FIG. 1, when the contaminated water to be treated first is collected in the
When the raw water passes through the nozzle neck of the injector in the above state, a negative pressure is instantaneously generated in the nozzle neck, and the coagulant is sucked into the raw water through the coagulant inlet 3-1 by the above negative pressure. It is characterized by an extended mixing into the raw water instantaneously towards the outlet of this expanding injector.
As described above, the flocculant mixed in the raw water is more finely mixed while passing through the
The floc entering the hydrocyclone is pivoted in the tangential direction of the cylinder, which has a characteristic of giving the floc centrifugal force to separate the floc formed in the raw water. The flocs separated by the above action accumulate under the cyclone and the integrated flocs exit the device through the solids outlet 6-1.
The flocs are discharged out of the cyclone intermittently by the solids outlet control valve 6-3. Meanwhile, the purified water separated by the rotational movement of the cyclone exits out of the cyclone through the purified water outlet 6-2 formed at the upper center of the cyclone, and the purified
Compressed air is generated by the air compressor (8), is supplied to the inside of the purified water filter by the compressed air control valve (8-2) through the compressed air supply pipe (8-1) to remove the particles attached to the outside of the filter Done. At this time, the purified
As described above, the present invention requires a large amount of space by installing the existing flocculation tank, sedimentation tank, filtration tank, etc. by treating the contaminated water by combining the injector, the line mix yarn, the floc forming tank, and the hydrocyclone and the filtration filter. There is an effect that can be treated as a simple facility without complicated facilities.
As described above, the method of the present invention provides a method for a water treatment device having a simple facility, low energy, and good treatment efficiency, and relates to manufacturing the device according to the provided method.
The present invention purifies muddy water generated during large-scale civil engineering works such as pre-treatment facilities, tunnels, etc. in pre-treatment facilities such as simple water supply facilities, wastewater treatment facilities in hospitals, wastewater treatment in hospitals where waterworks are not spread. It is available as facility to say.
1 is a schematic diagram of an apparatus for treating wastewater according to the method of the present invention.
<Description of the symbols for the main parts of the drawings>
1.-raw water tank
2.-Raw water supply pump
2-1. Raw water supply piping
3.-Injector
3-1. -Flocculant inlet
4.-LINE MIX
5.-floc forming tank
6.-Hydro Cyclone
6-1. -Solids outlet
6-2. -Water outlet
6-3. Solid outlet control valve
7.-Water filter
8.-Air compressor
8-1. -Compressed air supply pipe
8-2. -Compressed air control valve
9.-purified water outlet piping
9-1. -Water control valve
10.-Control panel
Figure 2 is a detailed view of the injector
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020080068130A KR20100007483A (en) | 2008-07-14 | 2008-07-14 | Water treatment method and equipment for pollution water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020080068130A KR20100007483A (en) | 2008-07-14 | 2008-07-14 | Water treatment method and equipment for pollution water |
Publications (1)
Publication Number | Publication Date |
---|---|
KR20100007483A true KR20100007483A (en) | 2010-01-22 |
Family
ID=41816457
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020080068130A KR20100007483A (en) | 2008-07-14 | 2008-07-14 | Water treatment method and equipment for pollution water |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR20100007483A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101236004B1 (en) * | 2011-03-09 | 2013-02-21 | 주식회사 동양 | Submerged MBR system comprising U―form inline mixer |
KR101236029B1 (en) * | 2011-03-09 | 2013-02-21 | 주식회사 동양 | Method for controlling submerged MBR system |
-
2008
- 2008-07-14 KR KR1020080068130A patent/KR20100007483A/en not_active Application Discontinuation
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101236004B1 (en) * | 2011-03-09 | 2013-02-21 | 주식회사 동양 | Submerged MBR system comprising U―form inline mixer |
KR101236029B1 (en) * | 2011-03-09 | 2013-02-21 | 주식회사 동양 | Method for controlling submerged MBR system |
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Legal Events
Date | Code | Title | Description |
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A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
E601 | Decision to refuse application |