KR20130043461A - The coagulantion method and using floc coagulantion device - Google Patents
The coagulantion method and using floc coagulantion device Download PDFInfo
- Publication number
- KR20130043461A KR20130043461A KR1020110107606A KR20110107606A KR20130043461A KR 20130043461 A KR20130043461 A KR 20130043461A KR 1020110107606 A KR1020110107606 A KR 1020110107606A KR 20110107606 A KR20110107606 A KR 20110107606A KR 20130043461 A KR20130043461 A KR 20130043461A
- Authority
- KR
- South Korea
- Prior art keywords
- flocculation
- water
- rotating
- rotation
- shaft
- Prior art date
Links
Images
Classifications
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
- C02F1/481—Treatment of water, waste water, or sewage with magnetic or electric fields using permanent magnets
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
- C02F1/488—Treatment of water, waste water, or sewage with magnetic or electric fields for separation of magnetic materials, e.g. magnetic flocculation
-
- 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
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells
Abstract
Description
The present invention relates to an apparatus for agglomeration of flocs in a flocculation process for water treatment and a flocculation method using the same, and more particularly, a rotation shaft having a predetermined length is vertically installed on the first to third flocculation tanks. A plurality of impellers are installed at the lower part of the upper part, and a plurality of magnets are installed at the upper part in a radial shape, and a magnetic body is installed at a position proximate to the rotating body, and the magnetic body is left / right by an electric cylinder. A flocculation device and flocculation device using the same to move the rotating body, the rotating shaft and the impeller at a constant speed by magnetic force so that the flocs can be easily flocculated from the fresh water contained in the first to third flocculation tanks. It is about a method.
As is well known in order to use rainwater or river water (hereinafter referred to as raw water) to the drinking water must go through a water treatment process, the water treatment process is a water purification process through a flocculation process, a precipitation process and a filtration process is completed.
In the flocculation process, the raw water supplied through the raw water pipe in the intake station is mixed with the chemicals by the chemical injector and the chemical mixer in the chemical chamber and the mixed paper, and then mixed and mixed with the chemicals, so that fine flocs are formed and grown in the flocculant to be precipitated in the sedimentation basin. Is a very important process.
That is, in the water purification plant, chemicals are introduced into the introduced raw water, and the raw water and chemicals are mixed by stirring the raw water treatment, and then the raw water and the chemicals are mixed uniformly. Through the process of settling, the raw water introduced into the water purification plant is purified.
The first to the third agglomeration tank of the conventional flocculation device as described above, respectively, the structure of the motor and the reducer is installed on the top of the agglomeration tank, a plurality of impellers in the lower portion of the rotating shaft driven by the drive of the motor Installed to rotate constantly at each input RPM (RPM) is to flocculate the flocks.
However, these flocculators are driven by the motor continuously from the point of operation of the water purification plant to the point of closure, which increases the cost of electricity due to the high electricity consumption. There was a high possibility of contamination, and the rotational speed of each of the motors installed in the first to the third agglomeration tank continues to rotate with the first input state. However, the change of the rotational speed of the motor according to the conventional flocculation device does not have accurate data value according to the temperature change and rotates at the first rotational speed, which makes the flocculation of the floc easy. This caused a problem that the reliability of the purified water was lowered.
Therefore, in order to solve the above problems, the present invention includes a plurality of impellers installed at the lower portion of the rotating shaft, and a rotating body installed so that a plurality of permanent magnets are embedded at the outer circumference of the rotating shaft, and the rotating body is rotated. It is possible to provide a flocculation device comprising a cylinder provided in front of the permanent magnet, a charging unit and a control unit for supplying power to the cylinder, and at the same time a plurality of flocculation devices are respectively installed on the first to third flocculation tanks. By operating the flocculators respectively, it is possible to set the rotational speed of the rotational shaft when the flocculation of the flocks contained in the raw water flowing into the first to third flocculation tanks is the best, respectively, thereby semi-permanently Can be operated to maximize energy efficiency, and the rotation axis It is possible to increase efficiency in water purification plant operation as it does not generate noise by rotating it, and it is possible to prevent water pollution by not needing oil of motor or reducer during flocculation of flocks, and to make data of the viscosity difference of raw water according to seasonal changes. It is an object of the present invention to provide a flocculation apparatus and a flocculation method using the same to control the rotational speed of the flocculation device to greatly improve the flocculation of the floc to increase the reliability of the purified water.
In order to achieve the above object, the present invention is applied to a water purification plant capable of supplying purified water through a water treatment process for river water or rainwater, and rotated respectively installed in the first to third flocculation tanks during the water treatment process. In a flocculation apparatus for generating and growing a floc by rotating in a number, the flocculator is vertically rotatably installed by a plurality of bearings installed on upper surfaces of the first to third flocculation tanks, and a lower portion of the rotation shaft includes a plurality of impellers integrally formed therein. ; A axial hole penetrating the rotating shaft and a permanent magnet embedded in an outer circumference thereof; A magnetic body in which a permanent magnet for rotating the rotating body by magnetic force is inserted into and installed in the housing; An electric cylinder which adjusts a distance from the rotating body by the movement of the magnetic body; A storage battery for supplying power to the electric cylinder is connected to a plurality of heat collecting plates for collecting solar heat, and includes an inverter for converting electric power charged in the storage battery, and operates the electric cylinder to control the rotation speed of the rotating shaft. And a control unit.
In addition, the present invention is applied to a water purification plant that can supply the purified water through the water treatment process of the river water or rainwater, the flocculation method using a flocculation device to agglomerate floc through the first to third flocculation tank in the water treatment process In the first to third agglomeration tank, respectively, the flocculating device is installed on each of the first step, the drug and raw water is uniformly mixed and introduced into the flocculation paper; The rotational speed of the rotational shaft of the coagulation apparatus installed in the first flocculation tank is 50 to 75 RPM, the rotational speed of the rotational shaft of the coagulation apparatus installed in the second flocculation tank is 25 to 50 RPM, A second step of agglomerating the flocks each with a rotational speed of 15 to 25 RPM of the rotation shaft; The rotation axis of the flocculator is rotated within a range of revolutions for a predetermined time to measure the turbidity of the fresh water contained in the first to third flocculation tanks, and at the same time measure the particle coefficient of the floc to control the data of the flocculator. Inputting a third step; If the turbidity of the raw water or the particle count of the flocks is less than the reference value by analyzing the data input to the control unit of the flocculating apparatus, the rotation axis of the flocculating apparatus is rotated within the respective rotation speed ranges to refill the flocks of the first to third flocculating tanks. A fourth step of agglomeration; A fifth step of measuring turbidity and particle count of fresh water freshly stored in the first to third flocculation tanks and storing the temperature and the rotational speed data of the rotating shaft in the controller if the reference value is satisfied; If a viscosity difference occurs due to a change in the water temperature of the fresh water inside the first to third flocculation tanks using the data stored in the fifth step, the controller controls the rotation axis of the flocculator to the number of rotations based on the stored data. And a sixth step of agglomerating the flocks of the first to third flocculation tanks by rotating.
As described above, the rotary shaft can be operated semi-permanently even without the electric supply of the present invention, thereby maximizing energy efficiency, and rotating the rotary shaft by magnetic force so that no noise is generated, thereby improving efficiency in water purification plant operation. Water can be prevented because oil is not needed during operation, and the rotational speed of the flocculator can be controlled by recording the viscosity difference of raw water according to the seasonal change, which greatly improves the cohesiveness of the floc and improves the reliability of water purification. It is a useful invention that can be increased.
1 is a front view illustrating a flocculation device according to the present invention.
Figure 2 is an exemplary view showing an operating state of the flocculation apparatus according to the present invention.
Figure 3 is an exemplary plan view showing an installation state of the flocculation apparatus according to the present invention.
Figure 4 is a process diagram showing a flocculation method according to the present invention.
Figure 5 is a schematic diagram showing a flocculation method according to the present invention.
Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
As shown, the flocculation apparatus of the present invention is used in the flocculation process of the water purification process of the water purification plant, and a plurality of flocculation tanks D1 to D3 in order to efficiently flocculate the flocs. Are respectively installed, the configuration is largely composed of a rotating
The
The rotating
The
In this case, a
The
The
The action of the coagulation apparatus of the present invention having a plurality of configurations as described above is the first to third agglomeration tank (D1) to (D3) the water is uniformly mixed with chemicals and raw water is introduced, the
The method of efficiently flocculating the floc by using the flocculation apparatus of the present invention as described above, first, in the first step (S10), the first to third flocculation of water uniformly mixed with the raw water, such as rainwater or river water and the chemicals. What is necessary is to flow into tank D1-D3 sequentially.
The second step (S20) is a rotation of the
The third step (S30) is to rotate the rotating
The fourth step (S40) is to analyze the data input to the
At this time, the particle coefficient of the floc does not have a specific value, and the reference value is when the floc particles formed in the first to third flocculation tanks D1 to D3 are the largest and the smallest floc is the smallest. Is preferably.
The fifth step (S50) measures the turbidity and particle count of the fresh water in the first to third coagulation tank (D1) ~ (D3) to enter the reference value, the water temperature and the rotational speed data of the
The sixth step (S60) is a difference in viscosity according to the change in the water temperature of the fresh water in the first to third agglomeration tank (D1) (D3) using the data stored in the fifth step (S50) Is generated, the
Thus, when the flocculation device of the floc according to the present invention is applied in the flocculation process of the water treatment process, it is possible to minimize the occurrence of noise, thereby eliminating the space limitation due to the operation of the equipment, and greatly improving energy efficiency without using electricity. In addition, by applying the flocculation method using the flocculator, the rotation speed of the rotating
On the other hand, the present invention is not limited to the above embodiments, various modifications can be presented in the art without departing from the scope of the claims.
10: axis of rotation 12: impeller
20: rotating body 22: shaft hole
24: permanent magnet 30: magnetic material
32: permanent magnet 34: housing
36: rail groove 38: stopper
40: electric cylinder 42: rod
50
54: heat collecting plate 56: inverter
B: bearings D1 to D3: first to third flocculation tanks
Claims (6)
It is installed vertically rotatable by a plurality of bearings (B) provided on the upper surface of the first to third aggregation tanks (D1) to (D3), the lower portion of the rotary shaft 10 is formed integrally with a plurality of impeller 12 )and;
A shaft hole 22 penetrates the rotary shaft 10 and a rotor 20 having a permanent magnet 24 embedded in an outer circumference thereof;
A magnetic body 30 into which the permanent magnet 32 which rotates the rotating body 20 magnetically by the rotating body 20 is inserted into and installed in the housing 34;
An electric cylinder 40 for adjusting a distance from the rotating body 20 by the movement of the magnetic body 30;
The storage battery 52 for supplying power to the electric cylinder 40 is connected to a plurality of heat collecting plate 54 for collecting solar heat, and includes an inverter 56 for converting the power charged in the storage battery 52 And a control unit (50) for operating the electric cylinder (40) to control the rotation speed of the rotating shaft (10).
A first step (S10) in which a flocculating device is installed on each of the first to third agglomeration tanks D1 to D3, respectively, and raw water mixed with the chemicals flows in uniformly;
The rotation speed of the rotation shaft 10 of the flocculation apparatus installed in the first flocculation tank D1 is 50 to 75 RPM, and the rotation speed of the rotation shaft 10 of the flocculation apparatus installed in the second flocculation tank D2 is 25 A second step (S20) of agglomeration of the flocks each at a rotational speed of the rotation shaft 10 of the agglomeration apparatus installed at the third agglomeration tank (D3) at 15 to 50 RPM, respectively;
Rotating the rotating shaft 10 of the flocculation device within the respective rotation speed range for a predetermined time to measure the turbidity of the fresh water in the first to third flocculation tank (D1) to (D3) at the same time, the particle count of the floc A third step (S30) of measuring data and inputting data to the controller 50 of the coagulation apparatus;
If the turbidity of the raw water or the particle coefficient of the floc is less than the reference value by analyzing the data input to the control unit 50 of the flocculating apparatus, the rotation shaft 10 of the flocculating apparatus is rotated within each rotational speed range, and then the first to the second A fourth step S40 of reaggregating the flocks of the three flocculation tanks D1 to D3;
By measuring the turbidity and particle count of the fresh water contained in the first to third agglomeration tank (D1) to (D3) and storing the water temperature and the rotational speed data of the rotary shaft 10 in the control unit 50 at a reference value A fifth step (S50) to be performed;
The controller 50 when the viscosity difference according to the change in the water temperature of the fresh water in the first to third agglomeration tank (D1) to (D3) using the data stored in the fifth step (S50) occurs. And a sixth step (S60) of agglomerating the flocks of the first to third flocculation tanks (D1) to (D3) by rotating the rotation shaft 10 of the flocculator at a rotation speed based on the stored data. Agglomeration method using a flocculation device characterized in that.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020110107606A KR20130043461A (en) | 2011-10-20 | 2011-10-20 | The coagulantion method and using floc coagulantion device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020110107606A KR20130043461A (en) | 2011-10-20 | 2011-10-20 | The coagulantion method and using floc coagulantion device |
Publications (1)
Publication Number | Publication Date |
---|---|
KR20130043461A true KR20130043461A (en) | 2013-04-30 |
Family
ID=48441695
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020110107606A KR20130043461A (en) | 2011-10-20 | 2011-10-20 | The coagulantion method and using floc coagulantion device |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR20130043461A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20200141646A (en) * | 2019-06-11 | 2020-12-21 | 세메스 주식회사 | Apparatus for dispensing droplet |
-
2011
- 2011-10-20 KR KR1020110107606A patent/KR20130043461A/en not_active Application Discontinuation
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20200141646A (en) * | 2019-06-11 | 2020-12-21 | 세메스 주식회사 | Apparatus for dispensing droplet |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101941759A (en) | Method for improving pollution resistance and flux of membrane by using weak electric field | |
CN106219858B (en) | Portable magnetic wrench of a force system settler | |
CN108793357A (en) | A kind of sewage-treatment plant using coagulant sedimentation | |
CN112591952A (en) | System for coal fired power plant desulfurization waste water is handled to magnetism coagulation | |
KR20130043461A (en) | The coagulantion method and using floc coagulantion device | |
CN102583874A (en) | Sewage treatment system | |
CN206783454U (en) | A kind of industrial sewage processing unit | |
CN202754885U (en) | Sludge concentration tank | |
CN205500982U (en) | Sewage quickly separating clarifier | |
CN111018064A (en) | Industrial sewage regeneration treatment equipment | |
KR101927302B1 (en) | Driving Apparatus for Cohesive Area | |
KR101259891B1 (en) | Sludge Concentration Apparutus of Multiple Circle Plate Type | |
CN102502929B (en) | Flocculation device, raw water purification device, flocculation method and raw water purification method | |
CN106630062A (en) | Chemical adding device for sewage treatment | |
CN113860573B (en) | Landfill leachate treatment device and technology based on reinforced Fenton oxidation method | |
CN205933459U (en) | Effluent treatment plant is used in alloy material production | |
CN107601777A (en) | Integrated equipment for sewage treatment | |
CN113120997A (en) | Superconducting magnetic coagulation separation waste water all-in-one machine | |
CN104310512B (en) | Discharge wavegenerator and using method | |
CN209117588U (en) | A kind of flocculant performance evaluation equipment | |
CN204138365U (en) | Discharge wavegenerator | |
CN219117224U (en) | Magnetic flocculation water purifying device | |
CN207356956U (en) | A kind of agitating device for sewage sludge processing | |
CN205886749U (en) | A laboratory installation that is used for mixing of high viscosity solution to join in marriage | |
CN219489823U (en) | Quick dewatering device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
E601 | Decision to refuse application |