WO2018038393A1 - Water treatment apparatus using magnetite and water treatment method using same - Google Patents
Water treatment apparatus using magnetite and water treatment method using same Download PDFInfo
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- WO2018038393A1 WO2018038393A1 PCT/KR2017/007591 KR2017007591W WO2018038393A1 WO 2018038393 A1 WO2018038393 A1 WO 2018038393A1 KR 2017007591 W KR2017007591 W KR 2017007591W WO 2018038393 A1 WO2018038393 A1 WO 2018038393A1
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- Prior art keywords
- water
- phosphorus
- tank
- magnetic force
- washing
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Classifications
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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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/02—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration
- B01D24/10—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being held in a closed container
- B01D24/16—Upward filtration
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/46—Regenerating the filtering material in the filter
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/48—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/48—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration
- B01D24/4807—Handling the filter cake for purposes other than regenerating
- B01D24/4815—Handling the filter cake for purposes other than regenerating for washing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/30—Combinations with other devices, not otherwise provided for
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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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- 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
-
- 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
- C02F2101/105—Phosphorus compounds
-
- 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
- C02F2303/16—Regeneration of sorbents, filters
Definitions
- the present invention relates to a water treatment apparatus, and more particularly, to a water treatment apparatus using magnetite (Fe 3 O 4 ) and a water treatment method using the same.
- Phosphorus is the main cause of eutrophication. When phosphorus is excessively introduced into lakes, rivers or seas, microorganisms multiply, resulting in the rapid depletion of dissolved oxygen, which kills aquatic organisms and destroys ecosystems.
- Conventional water treatment apparatuses use a method of removing contaminated water containing phosphorus by biological and physicochemical methods to remove such phosphorus.
- zeolite may be used instead of alumina sulfate (Al 2 (SO 4 ) 3 ) to improve the phosphorus removing effect
- zeolite has a problem in that the amount of chemical consumption is high in increasing alkalinity.
- the present invention was derived to solve the above problems, and to provide a water treatment apparatus for quickly removing the phosphorus of contaminated water through a filtration tank using a magnetite (Fe 3 O 4 ).
- the water treatment apparatus of the present invention can remove the phosphorus in the contaminated water without adding a separate chemical, and can also reduce the operating cost of the water treatment by using a semi-permanent magnetite (Fe 3 O 4 ) as a phosphorus adsorbent.
- a semi-permanent magnetite Fe 3 O 4
- the water treatment apparatus of the present invention does not generate by-products such as sludge in the phosphorus removal step.
- the present invention has been derived to solve the above problems, the water treatment device of the present invention to remove the phosphorus contained in the contaminated water, the filter part filled with the magnetite (Fe 3 O 4 ) powder which is a by-product of the steel rolling process
- An upward filtration tank 110 having a 111;
- a first flow passage (P1) for transferring the contaminated water to the filtration tank 110;
- the branch pipe line 150 includes a coupling part 151 coupled to the filtration tank 110;
- An inlet 155 coupled to the branch 153 of the outlet 154; and the magnetite (Fe 3 O 4 ) powder separated from the filtration unit 111
- a first adsorption device 160 formed on the coupling part 151 to recover the magnetic force;
- a first suction part (A) formed on the inner side of the coupling part 151 by the magnetic force of the first suction device 160;
- a second flow path (P2) coupled to the outlet portion 154 to discharge the contaminated water;
- a third flow path (P3) coupled to the inlet 155 to allow the washing water to flow therein;
- a washing tank 120 connected to the third flow path P3;
- a fourth flow passage (P4) connected to the filtration tank 110 to discharge the washing water;
- a phosphorus discharge tank 130 connected to the fourth flow path P4.
- the first adsorption device 160 includes a first fixing part 161 coupled to the coupling part 151 in a structure surrounding the outer side of the coupling part 151; A pair of first connectors 163, one side of which is coupled to the first fixing part 161 by a hinge structure and the other side of which rotates outward with respect to the first hinge part 162; It is preferable to include; a first magnetic force portion 164 is coupled to the other side of the pair of the first connection portion 163 and formed in a structure surrounding the coupling portion 151.
- the inner surface of the first magnetic portion 164 is in close contact with the outer surface of the coupling portion 151 in a structure corresponding to the outer surface of the coupling portion 151, the first magnetic portion 164 is the contaminated water It is preferable to generate magnetic force while being discharged through the second flow path P2 to adsorb the magnetite (Fe 3 O 4 ) powder included in the contaminated water to the first adsorption portion (A).
- the first adsorption device 160 loses magnetic force while the washing water is introduced through the inlet 155 so that the magnetite (Fe 3 O 4 ) adsorbed to the first adsorption unit A is filtered. It is preferable to re-introduce into 110.
- the washing water is preferably sodium hydroxide (NaOH) solution.
- the magnetite (Fe 3 O 4 ) powder is preferably installed in a size of less than 300 ⁇ m.
- the second storage device 170 for recovering the magnetite (Fe 3 O 4 ) powder passing through the first adsorption portion A is formed outside the bent portion 152.
- the second adsorption device 170 includes a second fixing part 171 coupled to the outlet part 154 adjacent to the bent part 152 in a structure surrounding the outlet part 154; A second connection part 173 having one side coupled to a hinge structure on an upper side of the second fixing part 171, and the other side rotatingly driven upward based on the second hinge part 172; It is preferable to include; a second magnetic force portion 174 coupled to the other side of the second connection portion 173 and formed to surround the upper portion of the outlet portion 154.
- the phosphorus discharge tank 130 is preferably interconnected by the phosphorus storage tank 140 and the sixth flow path (P6) for adjusting the concentration of the phosphorus.
- the phosphorus discharge tank 130 is interconnected by the washing tank 120 and the fifth flow path (P5), and to transfer the washing water of the phosphorus discharge tank 130 to the washing water tank 120 to reuse the washing water. desirable.
- Water treatment method using a water treatment device includes a contaminated water transfer step of transferring the contaminated water to the filtration tank 110; A filtration step of removing the phosphorus contained in the contaminated water from the filtration unit 111; A first adsorption part magnetic force forming step of forming a magnetic force on the first adsorption part A; A contaminated water discharge step of blocking the inlet part 155 and opening the outlet part 154 to discharge the contaminated water; A first adsorption part magnetic force removing step of removing a magnetic force to the first adsorption part A; A washing step of opening the inlet 155 and blocking the outlet 154 to deliver the washing water to the filtration tank; After washing the filtration unit 111, the washing water transport step for sending the washing water containing the phosphorus to the phosphorus discharge tank 130; includes.
- Water treatment method using a water treatment device includes a contaminated water transfer step of transferring the contaminated water to the filtration tank 110; A filtration step of removing the phosphorus contained in the contaminated water from the filtration unit 111; Magnetic force forming step of forming a magnetic force on the first and second adsorption portion (A) and (B); A contaminated water discharge step of blocking the inlet part 155 and opening the outlet part 154 to discharge the contaminated water; Magnetic force removal step of removing the magnetic force of the first and second adsorption portion (A) and (B); A washing step of opening the inlet 155 and blocking the outlet 154 to deliver the washing water to the filtration tank; After washing the filtration unit 111, the washing water transport step for sending the washing water containing the phosphorus to the phosphorus discharge tank 130; includes.
- Water treatment method using a water treatment device includes a contaminated water transfer step of transferring the contaminated water to the filtration tank 110; A filtration step of removing the phosphorus contained in the contaminated water from the filtration unit 111; A first adsorption part magnetic force forming step of forming a magnetic force on the first adsorption part A; A contaminated water discharge step of blocking the inlet part 155 and opening the outlet part 154 to discharge the contaminated water; A first adsorption part magnetic force removing step of removing a magnetic force to the first adsorption part A; A washing step of opening the inlet 155 and blocking the outlet 154 to deliver the washing water to the filtration tank; After washing the filtration unit 111, the washing water transport step of sending the washing water containing the phosphorus to the phosphorus discharge tank 130; In order to use the washing water as an agricultural fertilizer, the phosphorus concentration step of sending the washing water of the phosphorus discharge tank 130 to the phosphorus storage tank 140, and further supply
- the initial construction cost can be minimized because the water treatment apparatus can be operated using the existing general water purification facility.
- the water treatment process can be adjusted according to the turbidity of the mixed water or brackish water mixed with surface water and seawater and the concentration of TDS (Total Dissolved Solid, Total Dissolved Solids), reasonable and economical water treatment is possible. .
- the mixed water or brackish water mixed with the seawater since the mixed water or brackish water mixed with the seawater is used, it is an effective water treatment method in coastal areas with insufficient water.
- FIG. 1 is a block diagram of a combination of magnetite and phosphorus of the present invention.
- Figure 2 is a side view of the water treatment device according to an embodiment of the present invention.
- Figure 3 is a branch pipe coupling diagram according to an embodiment of the present invention.
- Figure 4 is a second adsorption device coupling diagram according to an embodiment of the present invention.
- FIG. 5 is a magnetic force forming and magnetic force removal process of the first adsorption apparatus according to an embodiment of the present invention.
- Figure 6 is a side view of the first adsorption device according to an embodiment of the present invention.
- A first adsorption part B: second adsorption part
- washing water tank 130 phosphorus discharge tank
- inlet 160 first adsorption device
- first connection portion 164 first magnetic portion
- first and second used below are merely identification symbols for distinguishing the same or corresponding components, and the same or corresponding components are limited by terms such as the first and second components. no.
- the coupling does not only mean the case where the physical contact is directly between the components in the contact relationship between the components, other components are interposed between the components, the components in the other components Use it as a comprehensive concept until each contact.
- the present invention has been derived to solve the above problems, the water treatment device of the present invention to remove the phosphorus contained in the contaminated water, the filter part filled with the magnetite (Fe 3 O 4 ) powder which is a by-product of the steel rolling process
- a first flow path P1 transferring contaminated water to the filtration tank 110;
- the washing water for washing the phosphorus adsorbed on the surface of the magnetite (Fe 3 O 4 ) having a magnetic force flows downward into the filtration tank 110, to the filtration tank 110 to discharge the contaminated water passing through the filtration unit 111.
- branch pipe line 150 It comprises a; branch pipe line 150; includes, the branch pipe line 150 is a coupling portion 151 is coupled to the filtration tank 110; An outlet portion 154 coupled to the coupling portion 151 by the bent portion 152; An inlet 155 coupled to the branch 153 of the outlet 154 and recovering the magnetite (Fe 3 O 4 ) powder contained in the contaminated water separated from the filtration unit 111 by magnetic force.
- the branch pipe line 150 includes, the branch pipe line 150 is a coupling portion 151 is coupled to the filtration tank 110; An outlet portion 154 coupled to the coupling portion 151 by the bent portion 152; An inlet 155 coupled to the branch 153 of the outlet 154 and recovering the magnetite (Fe 3 O 4 ) powder contained in the contaminated water separated from the filtration unit 111 by magnetic force.
- magnetite Fe 3 O 4
- the water treatment apparatus of the present invention uses magnetite (Fe 3 O 4 ), which is excellent in adsorption of phosphorus or heavy metal, from iron oxides (Fe 2 O 3 , Fe 3 O 4 , FeO), which are by-products generated in the steel making process, as an adsorbent. By-products can be recycled.
- magnetite has a strong magnetic force, and mono-dentate and bi-dentate with phosphate ions are formed on the surface of the particles, so that the phosphorous adsorption performance is excellent (see FIG. 1), so that phosphorus in contaminated water can be effectively removed.
- the water treatment apparatus of the present invention removes the phosphorus of the contaminated water only by passing the contaminated water flowing upward into the filtration unit 111 filled with the powder of magnetite, so that the phosphorus of the contaminated water is earlier than the water treatment time of the conventional phosphorus removal method. It can eliminate the need for a large water treatment plant, and can reduce the manufacturing cost of the water treatment plant.
- the water treatment apparatus of the present invention is excellent in environmental friendliness since sludge does not occur after the water treatment and no environmentally harmful by-products are generated.
- a feature of the water treatment device of the present invention is that some magnetite powder separated from the filtration part 11 is adsorbed in the first adsorption device so as not to flow out through the outlet part.
- Magnetite powder having a strong magnetic force adheres to the first adsorption portion having magnetic force, thereby preventing the loss of magnetite.
- the first suction part may be formed of a solenoid valve structure or may be formed of a structure that can be opened and closed manually.
- the first adsorption device 160 includes: a first fixing part 161 coupled to the coupling part 151 in a structure surrounding the outer side of the coupling part 151; A pair of first connectors 163, one side of which is coupled to the first fixing part 161 by a hinge structure, and the other side of which rotates outward with respect to the first hinge part 162; It is preferable to include; a first magnetic force portion 164 coupled to the other side of the pair of first connection portion 163 and formed in a structure surrounding the coupling portion 151.
- the inner surface of the first magnetic force portion 164 is in close contact with the outer surface of the coupling portion 151 in a structure corresponding to the outer surface of the coupling portion 151, the first magnetic portion 164 is contaminated water second flow path (P2) It is preferable to generate a magnetic force while being discharged through to adsorb the magnetite (Fe 3 O 4 ) powder contained in the contaminated water to the first adsorption portion (A).
- the first magnetic force unit 164 may be automatically or manually detached from the outer surface of the coupling unit 151 by the first hinge fixing unit 162.
- the first magnetic force unit 164 that is automatically or manually detached forms a strong magnetic force on the first adsorption unit A because the first magnetic force unit 164 is closely coupled to the outer surface of the coupling unit 151 in a structure corresponding to the outer surface of the coupling unit 151. can do.
- the first adsorption device 160 loses magnetic force while the washing water is introduced through the inlet 155 so that the magnetite (Fe 3 O 4 ) adsorbed to the first adsorption unit A is re-introduced into the filtration tank 110. It is preferred to be introduced.
- the magnetite (Fe 3 O 4 ) powder adsorbed on the first adsorption unit A is blocked by the outflow of the contaminated water, and then returned to the filtration tank 110 by the washing water introduced downward through the inlet 155. Is committed.
- the washing water is preferably sodium hydroxide (NaOH) solution.
- magnetite Fe 3 O 4
- phosphorus desorption is facilitated by OH ⁇ .
- Magnetite (Fe 3 O 4 ) powder is preferably installed in a size of 300 ⁇ m or less.
- the magnetite (Fe 3 O 4 ) powder is formed to a size of 300 ⁇ m or less to effectively adsorb the phosphorus contained in the contaminated water.
- a second storage device 170 is formed outside the bent portion 152 to recover the magnetite (Fe 3 O 4 ) powder that has passed through the first adsorption portion (A).
- the second adsorption device 170 may include: a second fixing part 171 coupled to the outlet part 154 adjacent to the bent part 152 in a structure surrounding the outlet part 154; A second connection part 173 having one side coupled to a hinge structure at an upper side of the second fixing part 171, and the other side rotatingly driven upward based on the second hinge part 172; It is preferable to include a second magnetic force portion (174) formed in a structure coupled to the other side of the second connection portion 173 to surround the upper portion of the outlet portion (154).
- the phosphorus discharge tank 130 is preferably interconnected by the phosphorus storage tank 140 and the sixth flow path (P6) for adjusting the phosphorus concentration.
- Phosphorus discharge tank 130 is interconnected by the washing water tank 120 and the fifth flow path (P5), it is preferable to transfer the washing water of the phosphorus discharge tank 130 to the washing water tank 120 to reuse the washing water.
- the washing water of the washing tank 120 is reused until a constant concentration.
- Water treatment method using a water treatment device is a contaminated water transfer step of transporting the contaminated water upward to the filtration tank 110; A filtration step of removing phosphorus contained in the contaminated water from the filtration unit 111; A first adsorption part magnetic force forming step of forming a magnetic force in the first adsorption part A; A contaminated water discharge step of blocking the inlet 155 and opening the outlet 154 to discharge the contaminated water; A first adsorption part magnetic force removing step of removing a magnetic force to the first adsorption part A; An inlet 155 is opened and an outlet 154 is blocked so that the washing water is delivered to the filtration tank; After washing the filtration unit 111, the washing water transport step of sending the washing water containing phosphorus to the discharge tank 130; includes.
- a magnetic force is formed in the first adsorption part to prevent the magnetite (Fe 3 O 4 ) powder from escaping to the outlet part.
- the magnetite (Fe 3 O 4 ) powder which was opened and attached to the first adsorption part by washing water, is re-injected into the filtration tank 110.
- Water treatment method using a water treatment device includes a contaminated water transfer step of transferring the contaminated water to the filtration tank 110; A filtration step of removing phosphorus contained in the contaminated water from the filtration unit 111; Magnetic force forming step of forming a magnetic force on the first and second adsorption portion (A) and (B); A contaminated water discharge step of blocking the inlet 155 and opening the outlet 154 to discharge the contaminated water; Magnetic force removal step of removing the magnetic force of the first and second adsorption portion (A) and (B); An inlet 155 is opened and an outlet 154 is blocked so that the washing water is delivered to the filtration tank; After washing the filtration unit 111, the washing water transport step of sending the washing water containing phosphorus to the discharge tank 130; includes.
- magnetic force may be formed in the first and second adsorption portions A and B to prevent the magnetite (Fe 3 O 4 ) powder from escaping to the outlet portion more effectively.
- Water treatment method using a water treatment device includes a contaminated water transfer step of transferring the contaminated water to the filtration tank 110; A filtration step of removing phosphorus contained in the contaminated water from the filtration unit 111; A first adsorption part magnetic force forming step of forming a magnetic force in the first adsorption part A; A contaminated water discharge step of blocking the inlet 155 and opening the outlet 154 to discharge the contaminated water; A first adsorption part magnetic force removing step of removing a magnetic force to the first adsorption part A; An inlet 155 is opened and an outlet 154 is blocked so that the washing water is delivered to the filtration tank; After washing the filtration unit 111, the washing and transporting step of sending the washing water containing phosphorus to the phosphorus discharge tank 130; In order to use the washing water as an agricultural fertilizer, the washing water of the phosphorus discharge tank 130 is sent to the phosphorus storage tank 140, the phosphorus concentration step of supplying additional phosphorus
- the washed water reused a number of times is transferred to the phosphorus storage tank 140 to be improved as a fertilizer.
- the wash water in the phosphorus storage tank 140 is improved by adding additional phosphorus as agricultural fertilizer and then flows out.
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Abstract
Description
본 발명은 수처리 장치에 관한 것으로서, 보다 상세하게는 마그네타이트(Fe3O4)를 이용한 수처리장치 및 이를 이용한 수처리방법에 관한 것이다.The present invention relates to a water treatment apparatus, and more particularly, to a water treatment apparatus using magnetite (Fe 3 O 4 ) and a water treatment method using the same.
인은 부영양화의 주원인으로서, 호수나 강 또는 바다에 인이 과량으로 유입되면 미생물이 증식되고, 이로 인해 용존산소가 급격히 고갈되어 수중생물이 폐사하고, 생태계가 파괴된다.Phosphorus is the main cause of eutrophication. When phosphorus is excessively introduced into lakes, rivers or seas, microorganisms multiply, resulting in the rapid depletion of dissolved oxygen, which kills aquatic organisms and destroys ecosystems.
지금까지의 수처리 장치는 이러한 인을 제거하기 위해, 인을 포함하고 있는 오염수를 생물학적인 방법과 물리화학적인 방법으로 제거하는 방법을 사용하고 있다.Conventional water treatment apparatuses use a method of removing contaminated water containing phosphorus by biological and physicochemical methods to remove such phosphorus.
그러나 생물학적인 방법은 인의 제거 과정에 많은 시간이 소요되고, 대형 체류 시설 및 저류시설을 갖추어야 하는 문제가 있다.However, biological methods require a long time for the removal of phosphorus and have a large residence and storage facilities.
응집침전법을 이용하여 인을 제거하는 물리적인 방법은 생물학적인 방법보다 비교적 인 제거공정이 짧은 시간에 이루어지는 장점이 있지만 통상적인 응집제로 사용되는 황산반토(Al2(SO4)3)의 인 제거 효율이 높지 않고, 응집과정에서 많은 양의 슬러지가 발생하는 문제점이 있다.Although the physical method of removing phosphorus by using flocculation sedimentation method has the advantage that the process of removing phosphorus is relatively shorter than biological method, phosphorus removal of alumina sulfate (Al 2 (SO 4 ) 3 ) used as a conventional flocculant The efficiency is not high, there is a problem that a large amount of sludge occurs in the flocculation process.
인 제거효과를 향상시키기 위해 황산반토(Al2(SO4)3) 대신 제올라이트를 사용하기도 하지만, 제올라이트는 알칼리도를 높이는 데 있어서 약품소모량이 많은 문제점이 있다.Although zeolite may be used instead of alumina sulfate (Al 2 (SO 4 ) 3 ) to improve the phosphorus removing effect, zeolite has a problem in that the amount of chemical consumption is high in increasing alkalinity.
본 발명은 상기와 같은 문제점을 해결하기 위하여 도출된 것으로서, 마그네타이트(Fe3O4)를 이용한 여과조를 통해 신속하게 오염수의 인을 제거하는 수처리장치를 제공하는 것에 있다.The present invention was derived to solve the above problems, and to provide a water treatment apparatus for quickly removing the phosphorus of contaminated water through a filtration tank using a magnetite (Fe 3 O 4 ).
또한, 본 발명의 수처리장치는 별도의 약품을 첨가하지 않고 오염수의 인을 제거함과 아울러, 인 흡착제로서 반 영구적인 마그네타이트(Fe3O4) 사용하여 수처리의 운영비를 절감할 수 있다.In addition, the water treatment apparatus of the present invention can remove the phosphorus in the contaminated water without adding a separate chemical, and can also reduce the operating cost of the water treatment by using a semi-permanent magnetite (Fe 3 O 4 ) as a phosphorus adsorbent.
마지막으로 본 발명의 수처리 장치는 인 제거단계에서 슬러지 등의 부산물이 발생하지 않는다.Finally, the water treatment apparatus of the present invention does not generate by-products such as sludge in the phosphorus removal step.
본 발명은 상기와 같은 문제점을 해결하기 위하여 도출된 것으로서, 본 발명의 수처리장치는 오염수에 포함된 인을 제거하기 위해, 강재 압연공정의 부산물인 마그네타이트(Fe3O4) 분말이 채워진 여과부(111)를 구비한 상향 여과조(110); 상기 여과조(110)로 상기 오염수를 이송하는 제1유로(P1); 자기력을 갖는 상기 마그네타이트(Fe3O4)의 표면에 흡착된 상기 인을 세척하기 위한 세척수를 상기 여과조(110)로 하향 유입시키고, 상기 여과부(111)를 통과한 상기 오염수를 배출시키기 위해 상기 여과조(110)에 결합된 분기관로(150);를 포함하고, 상기 분기관로(150)는 상기 여과조(110)와 결합되는 결합부(151); 절곡부(152)에 의해 상기 결합부(151)에 결합되는 유출부(154); 상기 유출부(154)의 분기부(153)에 결합된 유입부(155);를 구비하며, 상기 여과부(111)에서 이탈되어 상기 오염수에 포함된 상기 마그네타이트(Fe3O4) 분말을 자기력으로 회수하기 위해 상기 결합부(151)에 형성된 제1흡착장치(160); 상기 제1흡착장치(160)의 자기력에 의해 상기 결합부(151) 내측면에 형성된 제1흡착부(A); 상기 오염수를 배출하기 위해 상기 유출부(154)에 결합된 제2유로(P2); 상기 세척수가 유입되도록 상기 유입부(155)에 결합된 제3유로(P3); 상기 제3유로(P3)에 연결된 세척수조(120); 상기 세척수를 유출하도록 상기 여과조(110)에 연결된 제4유로(P4); 상기 제4유로(P4)에 연결된 인배출조(130);를 포함한다.The present invention has been derived to solve the above problems, the water treatment device of the present invention to remove the phosphorus contained in the contaminated water, the filter part filled with the magnetite (Fe 3 O 4 ) powder which is a by-product of the steel rolling process An
상기 제1흡착장치(160)는 상기 결합부(151)의 외측을 감싸는 구조로 상기 결합부(151)에 결합되는 제1고정부(161); 일측이 상기 제1고정부(161)에 힌지 구조로 결합되어 제1힌지고정부(162)를 기준으로 타측이 외측으로 회전구동하는 한 쌍의 제1연결부(163); 한 쌍의 상기 제1연결부(163)의 타측에 각각 결합되어 상기 결합부(151)를 감싸는 구조로 형성된 제1자력부(164);를 포함하는 것이 바람직하다.The
상기 제1자력부(164)의 내면은 상기 결합부(151)의 외면에 대응하는 구조로 상기 결합부(151)의 외면에 밀착결합되고, 상기 제1자력부(164)는 상기 오염수가 상기 제2유로(P2)를 통해 배출되는 동안 자기력을 발생하여 상기 오염수에 포함된 상기 마그네타이트(Fe3O4) 분말을 상기 제1흡착부(A)에 흡착시키는 것이 바람직하다.The inner surface of the first
상기 제1흡착장치(160)는 상기 유입부(155)를 통해 상기 세척수가 유입되는 동안 자기력을 상실하여 상기 제1흡착부(A)에 흡착된 상기 마그네타이트(Fe3O4)가 상기 여과조(110)의 내부로 재투입되는 것이 바람직하다.The
상기 세척수는 수산화나트륨(NaOH) 용액인 것이 바람직하다.The washing water is preferably sodium hydroxide (NaOH) solution.
상기 마그네타이트(Fe3O4) 분말은 300㎛ 이하의 크기로 설치되는 것이 바람직하다.The magnetite (Fe 3 O 4 ) powder is preferably installed in a size of less than 300㎛.
상기 절곡부(152)의 외측에는 제1흡착부(A)를 통과한 상기 마그네타이트(Fe3O4) 분말을 회수하기 위한 제2흡장장치(170)가 형성된 것이 바람직하다.It is preferable that the
상기 제2흡착장치(170)는 상기 절곡부(152)에 인접한 상기 유출부(154)에 상기 유출부(154)를 감싸는 구조로 결합되는 제2고정부(171); 일측이 상기 제2고정부(171)의 상측에 힌지 구조로 결합되고, 제2힌지고정부(172)를 기준으로 타측이 상측으로 회전구동하는 제2연결부(173); 상기 제2연결부(173)의 타측에 결합되어 상기 유출부(154)의 상부를 감싸는 구조로 형성된 제2자력부(174);를 포함하는 것이 바람직하다.The
상기 인배출조(130)는 상기 인의 농도를 조절하기 위한 인저장조(140)와 제6유로(P6)에 의해 상호 연결된 것이 바람직하다.The
상기 인배출조(130)는 상기 세척수조(120)와 제5유로(P5)에 의해 상호 연결되고, 상기 인배출조(130)의 세척수를 상기 세정수조(120)로 이송하여 상기 세척수를 재사용 하는 것이 바람직하다.The
본 발명의 일 실시 예에 따른 수처리장치를 이용한 수처리방법은 상기 여과조(110)로 상기 오염수를 이송하는 오염수이송단계; 상기 오염수에 포함된 상기 인을 상기 여과부(111)에서 제거하는 여과단계; 상기 제1흡착부(A)에 자기력을 형성하는 제1흡착부 자기력 형성단계; 상기 유입부(155)는 차단하고, 상기 유출부(154)는 개방하여 상기 오염수를 배출하는 오염수배출단계; 상기 제1흡착부(A)에 자기력을 제거하는 제1흡착부 자기력 제거단계; 상기 유입부(155)는 개방하고, 상기 유출부(154)는 차단하여 상기 세척수를 상기 여과조로 송수하는 세척단계; 상기 여과부(111)를 세척한 후, 상기 인을 포함하는 상기 세척수를 상기 인배출조(130)로 송수하는 세척수송수단계;를 포함한다.Water treatment method using a water treatment device according to an embodiment of the present invention includes a contaminated water transfer step of transferring the contaminated water to the
본 발명의 또 다른 실시 예에 따른 수처리장치를 이용한 수처리방법은 상기 여과조(110)로 상기 오염수를 이송하는 오염수이송단계; 상기 오염수에 포함된 상기 인을 상기 여과부(111)에서 제거하는 여과단계; 상기 제1흡착부(A)와 제2흡착부(B)에 자기력을 형성하는 자기력 형성단계; 상기 유입부(155)는 차단하고, 상기 유출부(154)는 개방하여 상기 오염수를 배출하는 오염수배출단계; 상기 제1흡착부(A)와 제2흡착부(B)의 자기력을 제거하는 자기력 제거단계; 상기 유입부(155)는 개방하고, 상기 유출부(154)는 차단하여 상기 세척수를 상기 여과조로 송수하는 세척단계; 상기 여과부(111)를 세척한 후, 상기 인을 포함하는 상기 세척수를 상기 인배출조(130)로 송수하는 세척수송수단계;를 포함한다.Water treatment method using a water treatment device according to another embodiment of the present invention includes a contaminated water transfer step of transferring the contaminated water to the
본 발명의 또 다른 실시 예에 따른 수처리장치를 이용한 수처리방법은 상기 여과조(110)로 상기 오염수를 이송하는 오염수이송단계; 상기 오염수에 포함된 상기 인을 상기 여과부(111)에서 제거하는 여과단계; 상기 제1흡착부(A)에 자기력을 형성하는 제1흡착부 자기력 형성단계; 상기 유입부(155)는 차단하고, 상기 유출부(154)는 개방하여 상기 오염수를 배출하는 오염수배출단계; 상기 제1흡착부(A)에 자기력을 제거하는 제1흡착부 자기력 제거단계; 상기 유입부(155)는 개방하고, 상기 유출부(154)는 차단하여 상기 세척수를 상기 여과조로 송수하는 세척단계; 상기 여과부(111)를 세척한 후, 상기 인을 포함하는 상기 세척수를 상기 인배출조(130)로 송수하는 세척수송수단계; 상기 세척수를 농업용 비료로 사용하기 위해, 상기 인배출조(130)의 세척수를 상기 인저장조(140)로 송수하고, 인을 추가로 공급하는 인농축단계; 상기 인농축단계 이후, 상기 인저장조(130)의 세척수를 유출하는 농축수유출단계;를 포함한다. Water treatment method using a water treatment device according to another embodiment of the present invention includes a contaminated water transfer step of transferring the contaminated water to the
상기 세척수송수단계 이후, 상기 인배출조(130)의 상기 세척수를 상기 세척수조(120)로 송수하여 상기 세척수를 재사용 하는 세척수리턴단계;를 더 포함하는 것이 바람직하다.After the washing water transport step, the washing water returning step of sending the washing water of the
본 발명에 따르면 기존 운영되고 있는 일반정수시설을 이용하여 수처리장치를 운영할 수 있기 때문에 초기 건설비용을 최소화할 수 있다.According to the present invention, the initial construction cost can be minimized because the water treatment apparatus can be operated using the existing general water purification facility.
본 발명에 따르면 지표수와 해수가 혼합된 혼합수 또는 기수의 탁도(Turbidity) 및 TDS(Total Dissolved Solid, 총용존고형물질)의 농도에 따라 수처리공정을 조절할 수 있기 때문에 합리적이고 경제적인 수처리가 가능하다.According to the present invention, since the water treatment process can be adjusted according to the turbidity of the mixed water or brackish water mixed with surface water and seawater and the concentration of TDS (Total Dissolved Solid, Total Dissolved Solids), reasonable and economical water treatment is possible. .
본 발명에 따르면 해수가 혼합된 혼합수 또는 기수를 활용하기 때문에 물부족 연안지역에 효과적인 수처리 방법이다.According to the present invention, since the mixed water or brackish water mixed with the seawater is used, it is an effective water treatment method in coastal areas with insufficient water.
도 1은 본 발명의 마그네타이트와 인의 결합 구성도.1 is a block diagram of a combination of magnetite and phosphorus of the present invention.
도 2는 본 발명의 일 실시 예에 따른 수처리장치 측면도.Figure 2 is a side view of the water treatment device according to an embodiment of the present invention.
도 3은 본 발명의 일 실시 예에 따른 분기관로 결합도.Figure 3 is a branch pipe coupling diagram according to an embodiment of the present invention.
도 4는 본 발명의 일 실시 예에 따른 제2흡착장치 결합도.Figure 4 is a second adsorption device coupling diagram according to an embodiment of the present invention.
도 5는 본 발명의 일 실시 예에 따른 제1흡착장치의 자기력 형성 및 자기력 제거 공정도.5 is a magnetic force forming and magnetic force removal process of the first adsorption apparatus according to an embodiment of the present invention.
도 6은 본 발명의 일 실시 예에 따른 제1흡착장치 측면도.Figure 6 is a side view of the first adsorption device according to an embodiment of the present invention.
*** 부호의 설명 ****** Explanation of Codes ***
A : 제1흡착부 B : 제2흡착부A: first adsorption part B: second adsorption part
P1 : 제1유로 P2 : 제2유로P1: Euro 1 P2: Euro 2
P3 : 제3유로 P4 : 제4유로P3: Euro 3 P4: Euro 4
P5 : 제5유로 100 : 수처리장치P5: Euro 5 100: Water treatment device
110 : 여과조 111 : 여과부110: filtration tank 111: filtration unit
120 : 세척수조 130 : 인배출조120: washing water tank 130: phosphorus discharge tank
140 : 인저장조 150 : 분기관로140: storage tank 150: branch pipe
151 : 결합부 152 : 절곡부151: coupling portion 152: bending portion
153 : 분기부 154 : 유출부153: branch portion 154: outlet portion
155 : 유입부 160 : 제1흡착장치155: inlet 160: first adsorption device
161 : 제1고정부 162 : 제1힌지고정부161: First Government 162: First Hingo Government
163 : 제1연결부 164 : 제1자력부163: first connection portion 164: first magnetic portion
170 : 제2흡착장치 171 : 제2고정부170: second adsorption device 171: second fixing part
172 : 제2힌지고정부 173 : 제2연결부172 Second Hinge
174 : 제2자력부174: Second magnetic force
본 발명에 따른 마그네타이트(Fe3O4)를 이용한 수처리장치 및 이를 이용한 수처리방법의 일 실시 예를 첨부도면을 참조하여 상세히 설명하기로 하며, 첨부 도면을 참조하여 설명함에 있어, 동일하거나 대응하는 구성 요소는 동일한 도면 번호를 부여하고 이에 대해 중복되는 설명은 생략하기로 한다.An embodiment of a water treatment apparatus using a magnetite (Fe 3 O 4 ) and a water treatment method using the same according to the present invention will be described in detail with reference to the accompanying drawings, in the following description, the same or corresponding configuration Elements are given the same reference numerals and redundant description thereof will be omitted.
또한, 이하 사용되는 제1, 제2 등과 같은 용어는 동일 또는 상응하는 구성 요소들을 구별하기 위한 식별 기호에 불과하며, 동일 또는 상응하는 구성 요소들이 제1, 제2 등의 용어에 의하여 한정되는 것은 아니다.In addition, terms such as first and second used below are merely identification symbols for distinguishing the same or corresponding components, and the same or corresponding components are limited by terms such as the first and second components. no.
또한, 결합이라 함은, 각 구성 요소 간의 접촉 관계에 있어, 각 구성 요소 간에 물리적으로 직접 접촉되는 경우만을 뜻하는 것이 아니라, 다른 구성이 각 구성 요소 사이에 개재되어, 그 다른 구성에 구성 요소가 각각 접촉되어 있는 경우까지 포괄하는 개념으로 사용하도록 한다.In addition, the coupling does not only mean the case where the physical contact is directly between the components in the contact relationship between the components, other components are interposed between the components, the components in the other components Use it as a comprehensive concept until each contact.
이하, 첨부도면을 참조하여 본 발명의 일 실시 예에 따른 마그네타이트(Fe3O4)를 이용한 수처리장치 및 이를 이용한 수처리방법에 관하여 상세히 설명한다.Hereinafter, a water treatment apparatus using magnetite (Fe 3 O 4 ) and a water treatment method using the same will be described in detail with reference to the accompanying drawings.
본 발명은 상기와 같은 문제점을 해결하기 위하여 도출된 것으로서, 본 발명의 수처리장치는 오염수에 포함된 인을 제거하기 위해, 강재 압연공정의 부산물인 마그네타이트(Fe3O4) 분말이 채워진 여과부(111)를 구비한 상향 여과조(110); 여과조(110)로 오염수를 이송하는 제1유로(P1); 자기력을 갖는 마그네타이트(Fe3O4)의 표면에 흡착된 인을 세척하기 위한 세척수를 여과조(110)로 하향 유입시키고, 여과부(111)를 통과한 오염수를 배출시키기 위해 여과조(110)에 결합된 분기관로(150);를 포함하고, 분기관로(150)는 여과조(110)와 결합되는 결합부(151); 절곡부(152)에 의해 결합부(151)에 결합되는 유출부(154); 유출부(154)의 분기부(153)에 결합된 유입부(155);를 구비하며, 여과부(111)에서 이탈되어 오염수에 포함된 마그네타이트(Fe3O4) 분말을 자기력으로 회수하기 위해 결합부(151)에 형성된 제1흡착장치(160); 제1흡착장치(160)의 자기력에 의해 결합부(151) 내측면에 형성된 제1흡착부(A); 오염수를 배출하기 위해 유출부(154)에 결합된 제2유로(P2); 세척수가 유입되도록 유입부(155)에 결합된 제3유로(P3); 제3유로(P3)에 연결된 세척수조(120); 세척수를 유출하도록 상기 여과조(110)에 연결된 제4유로(P4); 제4유로(P4)에 연결된 인배출조(130);를 포함한다.The present invention has been derived to solve the above problems, the water treatment device of the present invention to remove the phosphorus contained in the contaminated water, the filter part filled with the magnetite (Fe 3 O 4 ) powder which is a by-product of the steel rolling process An
이 경우, 본 발명의 수처리장치는 제철 공정에서 발생하는 부산물인 산화철(Fe2O3 , Fe3O4, FeO) 중 인 또는 중금속 흡착이 뛰어난 마그네타이트(Fe3O4)를 흡착제로 사용하기 때문에 부산물을 재활용할 수 있다.In this case, since the water treatment apparatus of the present invention uses magnetite (Fe 3 O 4 ), which is excellent in adsorption of phosphorus or heavy metal, from iron oxides (Fe 2 O 3 , Fe 3 O 4 , FeO), which are by-products generated in the steel making process, as an adsorbent. By-products can be recycled.
특히, 마그네타이트는 자기력이 강하고, 입자 표면에 phosphate 이온과의 mono-dentate, bi-dentate가 형성되어 있어 인 흡착성능이 우수하기 때문에(도 1 참고) 오염수의 인을 효과적으로 제거할 수 있다.In particular, magnetite has a strong magnetic force, and mono-dentate and bi-dentate with phosphate ions are formed on the surface of the particles, so that the phosphorous adsorption performance is excellent (see FIG. 1), so that phosphorus in contaminated water can be effectively removed.
또한, 본 발명의 수처리 장치는 마그네타이트의 분말이 채워진 여과부(111)에 상향 유입되는 오염수를 통과시키는 것만으로 오염수의 인을 제거하기 때문에 기존 인 제거 방식의 수처리 시간보다 빨리 오염수의 인을 제거할 수 있고, 대형 수처리 시설이 필요하지 않기 때문에 수처리 시설의 제작단가를 절감할 수 있다.In addition, the water treatment apparatus of the present invention removes the phosphorus of the contaminated water only by passing the contaminated water flowing upward into the
뿐만아니라 본원발명의 수처리장치는 수처리 이후에 슬러지가 발생하지 않고, 환경적으로 유해한 부산물을 발생하지 않기 때문에 환경 친화력이 우수하다.In addition, the water treatment apparatus of the present invention is excellent in environmental friendliness since sludge does not occur after the water treatment and no environmentally harmful by-products are generated.
본원발명의 수처리장치의 특징은 여과부(11)에서 이탈된 일부 마그네타이트 분말을 제1흡착장치에서 흡착하여 유출부를 통하여 유출되지 않도록 함에 있다.A feature of the water treatment device of the present invention is that some magnetite powder separated from the
자기력이 강한 마그네타이트 분말은 자기력을 갖는 제1흡착부에 부착되기 때문에 마그네타이트의 손실을 방지할 수 있다.Magnetite powder having a strong magnetic force adheres to the first adsorption portion having magnetic force, thereby preventing the loss of magnetite.
제1흡착부는 솔레노이드 벨브 구조로 형성되거나 수동으로 개폐할 수 있는 구조로 형성될 수 있다.The first suction part may be formed of a solenoid valve structure or may be formed of a structure that can be opened and closed manually.
제1흡착장치(160)는 결합부(151)의 외측을 감싸는 구조로 결합부(151)에 결합되는 제1고정부(161); 일측이 제1고정부(161)에 힌지 구조로 결합되어 제1힌지고정부(162)를 기준으로 타측이 외측으로 회전구동하는 한 쌍의 제1연결부(163); 한 쌍의 제1연결부(163)의 타측에 각각 결합되어 결합부(151)를 감싸는 구조로 형성된 제1자력부(164);를 포함하는 것이 바람직하다.The
제1자력부(164)의 내면은 결합부(151)의 외면에 대응하는 구조로 결합부(151)의 외면에 밀착결합되고, 제1자력부(164)는 오염수가 제2유로(P2)를 통해 배출되는 동안 자기력을 발생하여 오염수에 포함된 마그네타이트(Fe3O4) 분말을 제1흡착부(A)에 흡착시키는 것이 바람직하다.The inner surface of the first
이 경우, 제1자력부(164)는 제1힌고정정부(162)에 의해 결합부(151)의 외측면에 자동 또는 수동으로 탈착이 가능하다.In this case, the first
자동 또는 수동으로 탈착되는 제1자력부(164)는 결합부(151)의 외면에 대응하는 구조로 결합부(151)의 외면에 밀착 결합되기 때문에 제1흡착부(A)에 강한 자기력을 형성할 수 있다.The first
제1흡착장치(160)는 유입부(155)를 통해 세척수가 유입되는 동안 자기력을 상실하여 제1흡착부(A)에 흡착된 마그네타이트(Fe3O4)가 여과조(110)의 내부로 재투입되는 것이 바람직하다.The
이 경우, 제1흡착부(A)에 흡착된 마그네타이트(Fe3O4) 분말은 오염수의 유출이 차단된 이후, 유입부(155)를 통해 하향 유입되는 세척수에 의해 여과조(110)로 재투입된다.In this case, the magnetite (Fe 3 O 4 ) powder adsorbed on the first adsorption unit A is blocked by the outflow of the contaminated water, and then returned to the
상기 세척수는 수산화나트륨(NaOH) 용액인 것이 바람직하다.The washing water is preferably sodium hydroxide (NaOH) solution.
이 경우, 마그네타이트(Fe3O4)는 양쪽성(amphoteric) 성질을 갖기 때문에 OH-에 의해 인의 탈착이 용이해 진다. In this case, since magnetite (Fe 3 O 4 ) has an amphoteric property, phosphorus desorption is facilitated by OH − .
따라서 표면에 인이 흡착된 마그네타이트(Fe3O4) 분말이 수산화나트륨(NaOH) 용액에 잠기면 즉시 인이 탈락한다.Therefore, when the magnetite (Fe 3 O 4 ) powder having phosphorus adsorbed on the surface is immersed in sodium hydroxide (NaOH) solution, phosphorus is immediately eliminated.
마그네타이트(Fe3O4) 분말은 300㎛ 이하의 크기로 설치되는 것이 바람직하다.Magnetite (Fe 3 O 4 ) powder is preferably installed in a size of 300㎛ or less.
이 경우, 마그네타이트(Fe3O4) 분말은 300㎛ 이하의 크기로 형성되어 오염수에 포함된 인을 효과적으로 흡착한다.In this case, the magnetite (Fe 3 O 4 ) powder is formed to a size of 300㎛ or less to effectively adsorb the phosphorus contained in the contaminated water.
절곡부(152)의 외측에는 제1흡착부(A)를 통과한 마그네타이트(Fe3O4) 분말을 회수하기 위한 제2흡장장치(170)가 형성된 것이 바람직하다.It is preferable that a
제2흡착장치(170)는 절곡부(152)에 인접한 유출부(154)에 유출부(154)를 감싸는 구조로 결합되는 제2고정부(171); 일측이 제2고정부(171)의 상측에 힌지 구조로 결합되고, 제2힌지고정부(172)를 기준으로 타측이 상측으로 회전구동하는 제2연결부(173); 제2연결부(173)의 타측에 결합되어 유출부(154)의 상부를 감싸는 구조로 형성된 제2자력부(174);를 포함하는 것이 바람직하다.The
이 경우, 도 4 와 같이 제2자력부(174)는 절국부(152)의 외측면에 밀착되어 설치되기 때문에 절곡부(152)를 통과하면서 속도가 절감된 마그네타이트(Fe3O4) 분말의 회수가 용이하다.In this case, as shown in FIG. 4, since the second
또한, 오염수는 절곡부(152)를 통과하면서 절곡부(152)의 외측면에 부딪치기 때문에 오염수에 포함된 인을 효과적으로 흡착할 수 있다.In addition, since the contaminated water collides with the outer surface of the
상기 인배출조(130)는 인 농도를 조절하기 위한 인저장조(140)와 제6유로(P6)에 의해 상호 연결된 것이 바람직하다.The
인배출조(130)는 세척수조(120)와 제5유로(P5)에 의해 상호 연결되고, 인배출조(130)의 세척수를 세정수조(120)로 이송하여 세척수를 재사용 하는 것이 바람직하다.
이 경우, 세척수조(120)의 세척수는 일정 인 농도가 될 때까지 재사용 된다.In this case, the washing water of the
본 발명의 일 실시 예에 따른 수처리장치를 이용한 수처리방법은 여과조(110)로 오염수를 상향 이송하는 오염수이송단계; 오염수에 포함된 인을 여과부(111)에서 제거하는 여과단계; 제1흡착부(A)에 자기력을 형성하는 제1흡착부 자기력 형성단계; 유입부(155)는 차단하고, 유출부(154)는 개방하여 오염수를 배출하는 오염수배출단계; 제1흡착부(A)에 자기력을 제거하는 제1흡착부 자기력 제거단계; 유입부(155)는 개방하고, 유출부(154)는 차단하여 세척수를 여과조로 송수하는 세척단계; 여과부(111)를 세척한 후, 인을 포함하는 세척수를 인배출조(130)로 송수하는 세척수송수단계;를 포함한다.Water treatment method using a water treatment device according to an embodiment of the present invention is a contaminated water transfer step of transporting the contaminated water upward to the
이 경우, 오염수의 배출단계에서는 제1흡착부에 자기력을 형성하여 마그네타이트(Fe3O4) 분말이 유출부로 빠저나가는 것을 방지하고, 세척단계에서는 제1흡착부에 자기력을 제거함과 동시에 유입부를 개방하여 세척수에 의해 제1흡착부에 부착되었던 마그네타이트(Fe3O4) 분말을 여과조(110)로 재투입시킨다.In this case, in the discharge step of the contaminated water, a magnetic force is formed in the first adsorption part to prevent the magnetite (Fe 3 O 4 ) powder from escaping to the outlet part. The magnetite (Fe 3 O 4 ) powder, which was opened and attached to the first adsorption part by washing water, is re-injected into the
본 발명의 또 다른 실시 예에 따른 수처리장치를 이용한 수처리방법은 여과조(110)로 오염수를 이송하는 오염수이송단계; 오염수에 포함된 인을 여과부(111)에서 제거하는 여과단계; 제1흡착부(A)와 제2흡착부(B)에 자기력을 형성하는 자기력 형성단계; 유입부(155)는 차단하고, 유출부(154)는 개방하여 오염수를 배출하는 오염수배출단계; 제1흡착부(A)와 제2흡착부(B)의 자기력을 제거하는 자기력 제거단계; 유입부(155)는 개방하고, 유출부(154)는 차단하여 세척수를 여과조로 송수하는 세척단계; 여과부(111)를 세척한 후, 인을 포함하는 세척수를 인배출조(130)로 송수하는 세척수송수단계;를 포함한다.Water treatment method using a water treatment device according to another embodiment of the present invention includes a contaminated water transfer step of transferring the contaminated water to the
이 경우, 제1흡착부(A)와 제2흡착부(B)에 자기력을 형성하여 마그네타이트(Fe3O4) 분말이 유출부로 빠저나가는 것을 더욱 효과적으로 방지할 수 있다.In this case, magnetic force may be formed in the first and second adsorption portions A and B to prevent the magnetite (Fe 3 O 4 ) powder from escaping to the outlet portion more effectively.
본 발명의 또 다른 실시 예에 따른 수처리장치를 이용한 수처리방법은 여과조(110)로 오염수를 이송하는 오염수이송단계; 오염수에 포함된 인을 여과부(111)에서 제거하는 여과단계; 제1흡착부(A)에 자기력을 형성하는 제1흡착부 자기력 형성단계; 유입부(155)는 차단하고, 유출부(154)는 개방하여 오염수를 배출하는 오염수배출단계; 제1흡착부(A)에 자기력을 제거하는 제1흡착부 자기력 제거단계; 유입부(155)는 개방하고, 유출부(154)는 차단하여 세척수를 여과조로 송수하는 세척단계; 여과부(111)를 세척한 후, 인을 포함하는 세척수를 인배출조(130)로 송수하는 세척수송수단계; 세척수를 농업용 비료로 사용하기 위해, 인배출조(130)의 세척수를 인저장조(140)로 송수하고, 인을 추가로 공급하는 인농축단계단계; 인농축단계 이후, 인저장조(130)의 세척수를 유출하는 농축수유출단계;를 포함한다.Water treatment method using a water treatment device according to another embodiment of the present invention includes a contaminated water transfer step of transferring the contaminated water to the
이 경우, 많은 횟수로 재사용된 세척수는 인저장조(140)로 이송되어 비료로 개량된다. In this case, the washed water reused a number of times is transferred to the
인저장조(140)에서 세척수는 농업용 비료로 추가의 인을 첨가하여 개량된 후 유출된다.The wash water in the
세척수송수단계 이후, 인배출조(130)의 세척수를 세척수조(120)로 송수하여 세척수를 재사용 하는 세척수리턴단계;를 더 포함하는 것이 바람직하다.After the washing water transport step, the washing water returning step of sending the washing water of the
Claims (14)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020160106666A KR101746134B1 (en) | 2016-08-23 | 2016-08-23 | Water treating apparatus and method using magnetite |
| KR10-2016-0106666 | 2016-08-23 |
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| WO2018038393A1 true WO2018038393A1 (en) | 2018-03-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| PCT/KR2017/007591 Ceased WO2018038393A1 (en) | 2016-08-23 | 2017-07-14 | Water treatment apparatus using magnetite and water treatment method using same |
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| Country | Link |
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| KR (1) | KR101746134B1 (en) |
| WO (1) | WO2018038393A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109603261B (en) * | 2019-01-28 | 2021-09-03 | 辽宁工程技术大学 | Turbid liquid concentrating device and using method thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111298749B (en) * | 2020-03-19 | 2022-02-22 | 中国热带农业科学院湛江实验站 | Bagasse cellulose and lignin centrifugal separation synchronous processing screening equipment |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004057962A (en) * | 2002-07-30 | 2004-02-26 | Network:Kk | Magnetic processing unit |
| JP2005144365A (en) * | 2003-11-17 | 2005-06-09 | Japan Organo Co Ltd | Regeneration method of fluorine or phosphoric acid adsorbent |
| JP2009136784A (en) * | 2007-12-06 | 2009-06-25 | Tokyo Metropolitan Univ | Phosphorus removing device, phosphorus collecting device, phosphorus removing method and phosphorus collecting method |
| KR101568107B1 (en) * | 2015-05-29 | 2015-11-11 | 주식회사 포스코건설 | The method for water treatment |
-
2016
- 2016-08-23 KR KR1020160106666A patent/KR101746134B1/en active Active
-
2017
- 2017-07-14 WO PCT/KR2017/007591 patent/WO2018038393A1/en not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004057962A (en) * | 2002-07-30 | 2004-02-26 | Network:Kk | Magnetic processing unit |
| JP2005144365A (en) * | 2003-11-17 | 2005-06-09 | Japan Organo Co Ltd | Regeneration method of fluorine or phosphoric acid adsorbent |
| JP2009136784A (en) * | 2007-12-06 | 2009-06-25 | Tokyo Metropolitan Univ | Phosphorus removing device, phosphorus collecting device, phosphorus removing method and phosphorus collecting method |
| KR101568107B1 (en) * | 2015-05-29 | 2015-11-11 | 주식회사 포스코건설 | The method for water treatment |
Non-Patent Citations (1)
| Title |
|---|
| ZACH-MAOR, A.: "Adsorption-desorption mechanism of phosphate by immobilized nano-sized magnetite layer: Interface and bulk interactions", JOURNAL OF COLLOID AND INTERFACE SCIENCE, vol. 363, 27 July 2011 (2011-07-27), pages 608 - 614, XP028288417 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109603261B (en) * | 2019-01-28 | 2021-09-03 | 辽宁工程技术大学 | Turbid liquid concentrating device and using method thereof |
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| Publication number | Publication date |
|---|---|
| KR101746134B1 (en) | 2017-06-12 |
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