WO2016174890A1 - バラスト水処理装置及びバラスト水処理方法 - Google Patents
バラスト水処理装置及びバラスト水処理方法 Download PDFInfo
- Publication number
- WO2016174890A1 WO2016174890A1 PCT/JP2016/053289 JP2016053289W WO2016174890A1 WO 2016174890 A1 WO2016174890 A1 WO 2016174890A1 JP 2016053289 W JP2016053289 W JP 2016053289W WO 2016174890 A1 WO2016174890 A1 WO 2016174890A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- ballast water
- sterilizing component
- ballast
- main pipe
- water treatment
- Prior art date
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63J—AUXILIARIES ON VESSELS
- B63J4/00—Arrangements of installations for treating ballast water, waste water, sewage, sludge, or refuse, or for preventing environmental pollution not otherwise provided for
- B63J4/002—Arrangements of installations for treating ballast water, waste water, sewage, sludge, or refuse, or for preventing environmental pollution not otherwise provided for for treating ballast water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING
- B63B13/00—Conduits for emptying or ballasting; Self-bailing equipment; Scuppers
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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
- C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
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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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/008—Originating from marine vessels, ships and boats, e.g. bilge water or ballast water
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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
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
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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
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Definitions
- the present invention relates to a ballast water treatment apparatus and a ballast water treatment method.
- ballast water treatment method bactericidal components such as chlorine are injected into seawater during flooding.
- ballast water is stored in the ballast tank, the concentration of the sterilizing component in the ballast water decreases, and microorganisms and bacteria start to grow again. This tendency of proliferation is particularly remarkable when the water temperature is high or when there are many dissolved organic substances.
- An object of the present invention is to provide a ballast water treatment apparatus and a ballast water treatment method capable of increasing the concentration of a sterilizing component of ballast water in a ballast tank.
- a ballast water treatment apparatus includes a ballast tank, a main pipe that guides the ballast water to the ballast tank, a circulation pipe that returns the ballast water stored in the ballast tank to the main pipe, and the main pipe A sterilizing component introduction section for introducing a sterilizing component on the downstream side of a connection portion of the piping with the circulation piping.
- the ballast water treatment method includes a circulation step of returning the ballast water stored in the ballast tank from the main pipe to the ballast tank via the circulation pipe.
- the ballast water containing the sterilizing component is returned to the ballast tank by introducing the sterilizing component downstream of the connection portion of the piping with the circulation piping.
- the ballast water treatment device 1 is a device for increasing the concentration of the sterilizing component of ballast water in the ballast tank 60 disposed in the ship.
- the ballast water treatment device 1 mainly includes a ballast tank 60, a main pipe 2, a circulation pipe 80, a ballast pump 10, a filter 20, a sterilizing component introduction unit 40, a bypass pipe 90, and a mixer 50. I have.
- the main pipe 2 is connected to the ballast tank 60 and constitutes a supply channel for guiding the seawater pumped into the ship to the ballast tank 60.
- the main pipe 2 has one pipe port 2 ⁇ / b> A into which seawater flows and the other pipe port 2 ⁇ / b> B connected to the ballast tank 60.
- Seawater flows into the main pipe 2 from one piping port 2A, and is guided to the ballast tank 60 by flowing in the main piping 2 toward the other piping port 2B along the flow direction D of the seawater. This seawater is stored as ballast water for stabilizing the hull in the ballast tank 60.
- the circulation piping 80 mentioned later is connected to the main piping 2.
- the main pipe 2 and the circulation pipe 80 constitute a circulation passage for circulating ballast water in the ballast tank 60.
- the circulation pipe 80 is connected to the main pipe 2 so that a part of the ballast water stored in the ballast tank 60 is returned to the main pipe 2 and passes through the sterilizing component introduction part 40.
- one end of the circulation pipe 80 is connected to the ballast tank 60, and the other end of the circulation pipe 80 is located on the upstream side of the ballast pump 10 and the sterilizing component introduction part 40 in the main pipe 2. Connected to 2C.
- the pump pressure by the ballast pump 10 can be used by connecting the circulation pipe 80 to the above position.
- a part of the ballast water in the ballast tank 60 flows into the main pipe 2 from the first connecting portion 2C via the circulation pipe 80.
- the ballast water that has flowed into the main pipe 2 is returned to the ballast tank 60 by flowing in the main pipe 2 along the flow direction D toward the other pipe port 2B.
- the sterilizing component introduction part 40 when the ballast water passes through the sterilizing component introduction part 40, the sterilizing component is introduced into the ballast water from the sterilizing component introduction part 40.
- the concentration of the sterilizing component of the ballast water in the ballast tank 60 is increased.
- the ballast pump 10 is disposed in the main pipe 2 on the side of one pipe port 2A.
- the ballast pump 10 also has a function of supplying seawater that has flowed into the main pipe 2 to the ballast tank 60, and the ballast water in the ballast tank 60 is transferred from the main pipe 2 to the ballast tank 60 via the circulation pipe 80. There is also a function to return.
- the filter 20 is disposed downstream of the ballast pump 10 in the main pipe 2 in the seawater flow direction D (on the ballast tank 60 side).
- the filter 20 removes foreign matters and microorganisms contained in seawater by filtration. Since the filter 20 can sufficiently remove foreign substances and microorganisms by passing seawater when it is taken into the ballast tank 60, the ballast water returned to the main pipe 2 via the circulation pipe 80 does not necessarily pass the filter 20. It does not have to pass.
- the bypass pipe 90 is connected to the main pipe 2 so that the ballast water can avoid the filter 20 (bypass) when the ballast water flows through the main pipe 2.
- one end of the bypass pipe 90 is connected to the second connection portion 2D located on the upstream side of the filter 20, and the other end of the bypass pipe 90 is connected to the third connection portion 2 ⁇ / b> E located on the downstream side of the filter 20. It is connected to the.
- the ballast water does not need to pass through the filter 20 again because the filter 20 passes through the ballast water 60 when the seawater is taken into the ballast tank 60 to remove foreign matters and microorganisms.
- a bypass pipe 90 connected to the upstream side and the downstream side of the filter 20 is provided so that ballast water can bypass the filter 20 through the bypass pipe 90.
- the sterilizing component introduction part 40 is disposed downstream of the filter 20 in the main pipe 2 and is a part that introduces the sterilizing component into seawater or ballast water flowing in the main pipe 2. By injecting the sterilizing component into seawater or ballast water, microorganisms, sterilizers, etc. present in the seawater or ballast water can be eradicated.
- the sterilizing component introduction unit 40 may be any unit that can introduce a sterilizing component into the ballast water passing through the main pipe 2.
- the method of introducing the sterilizing component by the sterilizing component introducing unit 40 is, for example, a method of directly injecting the sterilizing component into the main pipe 2, and after preparing a high-concentration chlorine solution, the required amount of the prepared solution is set to the main pipe 2.
- a method of injecting into the main pipe 2 a method of disposing a sterilizing agent for generating hypochlorous acid as a sterilizing component in the main pipe 2 (embodiment 4), a method of generating hypochlorous acid by electrolyzing seawater or ballast water
- a method of injecting sterilizing component ozone into the main pipe 2 by an ozone generator a method of injecting sterilizing component ozone into the main pipe 2 by an ozone generator.
- the sterilization component introduction part 40 introduce
- a method for injecting a necessary amount of a sterilizing component into the main pipe 2 will be described.
- the mixer 50 is arranged downstream of the sterilizing component introduction part 40 in the main pipe 2.
- the mixer 50 agitates the ballast water after the sterilizing component is injected in the sterilizing component introducing unit 40, thereby uniformizing the concentration of the sterilizing component in the ballast water.
- the position of the concentration measuring unit 41 is not limited as long as the concentration of the sterilizing component in the ballast tank 60 can be measured.
- the concentration measurement unit 41 may be attached to the circulation pipe 80, the concentration measurement unit 41 may be attached to the bypass pipe 90, or the main pipe 2 between the first connection portion 2C and the second connection portion 2D.
- the concentration measuring unit 41 may be attached.
- the ballast water treatment apparatus 1 further includes a sterilizing component adjusting means 70.
- the sterilizing component adjusting means 70 is based on the measurement result of the sterilizing component concentration (chlorine concentration) of the ballast water by the concentration measuring unit 41 and the amount of the sterilizing component injected into the main pipe 2 from the sterilizing component introducing unit 40 and the ballast tank 60. The amount of ballast water to be flowed to the circulation pipe 80 is determined.
- the configuration of the sterilizing component adjusting means 70 will be described in detail.
- the sterilizing component adjusting means 70 includes a sterilizing component adjusting unit 71 and a sterilizing component control unit 72.
- the sterilizing component adjustment unit 71 adjusts the amount of ballast water flowing from the ballast tank 60 to the circulation pipe 80 and adjusts the amount of the sterilizing component introduced into the main pipe 2.
- the sterilization component control unit 72 receives the measurement result of the concentration of the sterilization component of the ballast water from the concentration measurement unit 41, and controls the sterilization component adjustment unit 71 based on the measurement result.
- the sterilizing component adjustment unit 71 includes a first on-off valve 71A, a second on-off valve 71B, and a third on-off valve 71C.
- the first opening / closing valve 71A is disposed in the circulation pipe 80, and adjusts the circulation amount of the ballast water flowing through the circulation pipe 80 by opening / closing the first opening / closing valve 71A.
- the first on-off valve 71A is preferably arranged at a position close to the first connection portion 2C in the circulation pipe 80. By disposing at this position, it is possible to reduce the dead volume of seawater flowing through the circulation pipe 80 when the first connection portion 2C is closed during normal flooding.
- the second on-off valve 71B is disposed upstream of the first connection portion 2C, and adjusts the amount of seawater taken into the main pipe 2 by opening and closing the second on-off valve 71B.
- the third on-off valve 71C is disposed downstream of the second connection portion 2D and upstream of the third connection portion 2E, and the seawater flows through the filter 20 by opening / closing the third on-off valve 71C, or ballast It adjusts whether the water flows into the bypass pipe 90.
- the sterilizing component control unit 72 closes the first on-off valve 71A and opens the second on-off valve 71B and the third on-off valve 71C. Conversely, when the ballast water in the ballast tank 60 is circulated, the sterilizing component control unit 72 opens the first on-off valve 71A and closes the second on-off valve 71B and the third on-off valve 71C.
- the sterilizing component control unit 72 mainly includes a determination unit 72A, a control unit 72B, and a storage unit 72C.
- the sterilizing component control unit 72 electromagnetically controls the amount of the sterilizing component introduced from the sterilizing component introducing unit 40 into the main pipe 2 by these configurations.
- the determination result of the concentration of the sterilizing component of the ballast water by the concentration measurement unit 41 is input to the determination unit 72A.
- the storage unit 72C stores reference value data for the concentration of the sterilizing component of the ballast water.
- the determination unit 72A compares the measurement result input from the concentration measurement unit 41 with the reference value stored in the storage unit 72C, and based on the comparison result, the sterilization component is introduced into the main pipe 2 from the sterilization component introduction unit 40.
- the determination unit 72C determines that the sterilizing component needs to be introduced into the main pipe 2 from the sterilizing component introducing unit 40. On the other hand, when the measured value is higher than the reference value, the determination unit 72C determines that it is not necessary to introduce the sterilizing component into the main pipe 2 from the sterilizing component introducing unit 40.
- the control unit 72B receives the determination result from the determination unit 72A, adjusts the operations of the first to third on-off valves 71A, 71B, 71C, and the ballast pump 10 based on the result, and supplies the main piping from the sterilizing component introduction unit 40.
- the amount of the sterilizing component to be introduced into 2 is adjusted. More specifically, when the determination unit 72A determines that the concentration of the sterilizing component of the ballast water needs to be increased, the control unit 72B opens the first on-off valve 71A to open the second and third on-off valves. 71B and 71C are closed, and a sterilizing component is introduced into the main pipe 2 from the sterilizing component introducing section 40.
- the control unit 72B closes the first on-off valve 71A and the second on-off valve 71B, or disinfects the sterilizing component. No sterilizing component is introduced into the main pipe 2 from the introduction part 40. In this way, the control unit 72B measures the concentration of the sterilizing component of the ballast water in the ballast tank 60, and determines whether it is necessary to introduce the sterilizing component by feeding back the result. And the control part 72B can adjust so that the density
- control unit 72B causes the concentration measuring unit 41 to measure the concentration of the sterilizing component of the ballast water in the ballast tank 60 at a preset measurement cycle (for example, every 12 hours) (S1).
- concentration measuring unit 41 measures the concentration of the sterilizing component of the ballast water in the ballast tank 60 at a preset measurement cycle (for example, every 12 hours) (S1).
- the measurement data acquired here is input to the determination unit 72A.
- the determination unit 72A compares the input measurement data with the reference value data stored in the storage unit 72C, and determines whether or not the measurement data is greater than or equal to the reference value (for example, 1 mg / L or more). Whether or not there is) is determined (S2). When it is determined that the measurement data is less than the reference value (S2: NO), the determination result is input to the control unit 72B. Then, the controller 72B opens the first on-off valve 71A and closes the second and third on-off valves 71B and 71C so that the concentration of the sterilizing component is equal to or higher than the reference value (S3), and then the ballast pump 10 Is activated (S4).
- the reference value for example, 1 mg / L or more
- the ballast water in the ballast tank 60 flows through the main pipe 2 through the circulation pipe 80 and is returned to the ballast tank 60 through the bypass pipe 90.
- the amount of the sterilizing component of the ballast water in the ballast tank 60 can be adjusted by introducing the sterilizing component from the sterilizing component introducing unit 40 to the main pipe 2 (S5).
- the ballast water treatment apparatus 1 includes a ballast tank 60, a main pipe 2 that guides the ballast water to the ballast tank 60, and the main pipe 2 that guides the ballast water stored in the ballast tank 60 to the ballast tank 60.
- a circulation pipe 80 to be returned and a sterilization component introduction section 40 for introducing a sterilization component downstream of the connection portion 2C of the main pipe 2 with the circulation pipe 80 are provided.
- ballast water treatment apparatus it is possible to circulate ballast water by returning a part of the ballast water in the ballast tank 60 to the main pipe 2 via the circulation pipe 80 and returning the ballast water from the main pipe 2 to the ballast tank 60.
- the sterilizing component introduction part 40 is arranged on the downstream side of the connecting part 2C with the circulation pipe 80 in the main pipe 2 to inject the sterilizing component into the ballast water from the sterilizing component introduction part 40. Can do. Thereby, the ballast water containing a sterilizing component can be returned to the ballast tank 60.
- the ballast water in the ballast tank 60 can be circulated and the sterilizing component can be additionally introduced into the ballast water by introducing the sterilizing component from the sterilizing component introducing unit 40. Thereby, regrowth of microorganisms can be controlled.
- ballast water treatment apparatus needs only to add a simple facility only to newly provide a circulation pipe 80 to the configuration of the conventional ballast water treatment apparatus, the ballast water treatment apparatus can be used even in a ship where it is difficult to secure an installation space.
- the device 1 is easy to apply.
- ballast water treatment device 1 When the ballast water treatment device 1 returns the ballast water from the ballast tank 60 to the ballast tank 60 via the circulation pipe 80 and the main pipe 2, the amount of the sterilizing component introduced into the main pipe 2 from the sterilizing ingredient introduction unit 40 is determined.
- a sterilizing component adjusting means 70 for adjusting is provided. By providing the sterilizing component adjusting means 70, the amount of the sterilizing component introduced into the main pipe 2 from the sterilizing component introducing portion 40 can be adjusted. As a result, the ballast water in the ballast tank 60 can be adjusted to an appropriate concentration of the sterilizing component. Thereby, corrosion can be prevented from occurring in the main pipe 2 and the circulation pipe 80 through which the ballast tank 60 and the ballast water flow.
- the ballast water treatment apparatus 1 includes a concentration measuring unit 41 that measures the concentration of the sterilizing component of the ballast water stored in the ballast tank 60.
- the concentration measuring unit 41 measures the concentration of the sterilizing component of the ballast water in the ballast tank 60 and feeds back the measurement result to the sterilizing component adjusting means 70.
- the sterilizing component adjusting means 70 can introduce an appropriate amount of the sterilizing component into the main pipe 2, and can appropriately increase the concentration of the sterilizing component in the ballast tank 60.
- the ballast water treatment method using the ballast water treatment apparatus 1 includes a circulation step of returning the ballast water stored in the ballast tank 60 from the main pipe 2 to the ballast tank 60 via the circulation pipe 80.
- the sterilizing component can be injected from the sterilizing component introduction part 40 arranged on the downstream side of the connecting portion with the circulation piping 80 in the main piping 2, and the ballast water into which the sterilizing component is injected It can be returned to the ballast tank 60.
- concentration of the disinfection component of the ballast water in the ballast tank 60 can be raised, and the re-growth of microorganisms can be suppressed.
- the ballast water treatment method includes a step of measuring the concentration of the sterilizing component of the ballast water stored in the ballast tank 60 and a sterilizing component introduced into the main pipe 2 in the circulation step based on the result obtained by the measurement. Adjusting the amount. Through these steps, the measurement result of the concentration of the sterilizing component of the ballast water in the ballast tank 60 is fed back, and the amount of the sterilizing component introduced into the main pipe 2 can be adjusted. The concentration can be increased moderately.
- the amount of the sterilizing component to be introduced into the main pipe 2 is adjusted based on the measurement result by the concentration measuring unit 41.
- the amount of the sterilizing component of the ballast water is adjusted as described above. It is not limited only to the adjustment.
- the ballast water is adjusted by flowing the ballast water through the circulation pipe 80 and adjusting the amount of the sterilizing component introduced into the main pipe 2 based on the time until the scheduled port entry date and time of the ship equipped with the ballast water treatment apparatus 1.
- the concentration of the sterilizing component may be adjusted.
- the concentration of the sterilizing component of the ballast water at the time of ship call can be made appropriate by flowing back the ballast water through the circulation pipe 80 several hours to several tens of hours before the time when the ship calls at the port.
- ballast water can be processed just before a ship's call.
- Embodiment 2 A ballast water treatment apparatus 1 ′ according to Embodiment 2, which is another embodiment of the present invention, will be described.
- the ballast water treatment apparatus 1 ′ of the second embodiment replaces the circulation amount control unit 72 that adjusts the opening / closing of the on-off valves 71 ⁇ / b> A, 71 ⁇ / b> B, 71 ⁇ / b> C with respect to that of the first embodiment
- the second embodiment is the same as the first embodiment except that an input unit 72 ′ for inputting an opening / closing command for each of the opening / closing valves 71A, 71B, 71C is provided manually by the operator.
- an operator inputs a command for flowing ballast water from the ballast tank 60 to the circulation pipe 80 to the input unit 72 ′.
- the ballast water can be returned to the main pipe 2 via the circulation pipe 80 by controlling the opening and closing of each of the first to third on-off valves 71A, 71B, 71C and the ballast pump 10 based on the command.
- the concentration of the sterilizing component of the ballast water in the ballast tank 60 can be increased by injecting the sterilizing component from the sterilizing component introducing unit 40 into the main pipe 2.
- a notification device 42 for transmitting the measurement result of the concentration measuring unit 41 to the operator is connected to the concentration measuring unit 41.
- the ballast water gradually consumes sterilizing components according to the storage time in the ballast tank 60.
- the concentration of the sterilizing component falls below the reference value due to this consumption
- the information is input from the concentration measuring unit 41 to the notification device 42.
- the information is displayed on the notification device 42 or the sterilizing component adjusting means 70 or the like. Thereby, the worker can grasp that the concentration of the sterilizing component is lower than the reference value.
- the operator operates the input unit 72 ′ based on the information transmitted from the notification device 42, so that the input unit 72 ′ issues a command to open the first on-off valve 71 A, and the second and third on-off valves 71 B and 71 C.
- a command for closing, a command for starting the ballast pump 10, and a command for injecting a sterilizing component into the main pipe 2 from the sterilizing component introducing unit 40 are issued.
- the operator opens and closes each on-off valve and the ballast pump 10 is activated to flow the ballast water in the ballast tank 60 to the circulation pipe 80.
- the sterilizing component can be injected into the main pipe 2 from the sterilizing component introducing section 40, and the concentration of the sterilizing component of the ballast water can be increased at an appropriate timing.
- the concentration measurement result of the sterilization component of the ballast water by the concentration measurement unit 41 exceeds the reference value by increasing the concentration of the sterilization component of the ballast water
- the information is input from the concentration measurement unit 41 to the notification device 42.
- the information is displayed on the notification device 42. Thereby, the operator can grasp that the concentration of the sterilizing component is equal to or higher than the reference value.
- the concentration measuring unit 41 only needs to be able to detect the concentration of the sterilizing component stored in the ballast tank 60, and other types of sensors can be used in the same manner.
- the display by the notification device 42 is not limited to the form in which the concentration of the sterilizing component of the ballast water is displayed as described above, and the concentration is a reference value for the worker by an alarm such as a sound or a light signal such as red or blue. It is possible to communicate that the value has fallen below.
- ballast water treatment device ⁇ Operational effects of ballast water treatment device> Also in the description of the function and effect, only the function and effect unique to the ballast water treatment apparatus 1 ′ of the second embodiment will be described, and the same function and effect as those of the first embodiment will be omitted.
- the input unit 72 ′ instructs the ballast water to flow from the ballast tank 60 to the circulation pipe 80. Accordingly, the ballast water can be returned to the main pipe 2 via the circulation pipe 80 at a timing at which the concentration of the sterilizing component of the ballast water should be increased, and the sterilizing ingredient can be injected from the sterilizing ingredient introduction unit 40 into the main pipe 2.
- the concentration of the sterilizing component of the ballast water inside can be increased moderately.
- the timing and amount of circulation of the ballast water in the ballast tank 60 to the circulation pipe 80 are determined by the operator based on notification (alarm or the like) from the notification device 42.
- the ballast water treatment method using the ballast water treatment apparatus 1 ′ according to the second embodiment is based on a step of inputting a command for flowing ballast water from the ballast tank 60 to the circulation pipe 80 to the input unit 72 ′, and the input command. And adjusting the amount of the sterilizing component to be injected from the sterilizing component introducing unit 40 into the main pipe 2.
- the ballast water can be returned to the main pipe 2 via the circulation pipe 80, and the concentration of the sterilizing component of the ballast water in the ballast tank 60 can be increased.
- the ballast water treatment apparatus of the third embodiment has the same configuration as that of the first embodiment except that the concentration measuring unit 41 is provided in the circulation pipe 80.
- the concentration measuring unit 41 When the concentration measuring unit 41 is provided at such a position, the first on-off valve 71A is opened and the second and third on-off valves 71B and 71C are opened regardless of whether or not the sterilizing component is injected from the sterilizing component introduction unit 40. Keep closed. In this way, the ballast water stored in the ballast tank 60 continues to flow through the circulation pipe 80 at all times. And the density
- a concentration measuring device other than the concentration measuring unit 41 may be connected to the ballast tank 60. Thereby, the density
- the ballast water is circulated for a time necessary for the ballast water in the ballast tank 60 to be replaced. Thereafter, the concentration of the sterilizing component of the ballast water in the ballast tank 60 is measured, and the ballast water in the ballast tank is confirmed while confirming whether or not the measured value is within a set range including the reference value (for example, 3 ⁇ 1 mg / L). Adjust the concentration of sterilizing ingredients.
- a concentration measuring device different from the concentration measuring unit 41 may be connected to the downstream side of the mixer 50 in the main pipe 2.
- the sterilizing component introduction unit 40 is controlled so as to reduce the concentration of the sterilizing component injected into the main pipe 2 accordingly. . This adjusts the concentration of the sterilizing component of the ballast water in the ballast tank.
- the ballast water treatment apparatus according to the fourth embodiment is different from the sterilizing component introduction unit 40 in that a chemical container 40 ′ including the sterilizing agent 3 is disposed instead of injecting a sterilizing component.
- the sterilizing component adjusting means 70 adjusts the introduction amount of the sterilizing component by adjusting the circulation amount of the ballast water flowing through the circulation pipe 80. That is, as the sterilizing component adjusting means 70 increases the circulation amount of the ballast water that passes through the chemical container 40 ′, the sterilizing agent 3 dissolves in the ballast water and the sterilizing component can be added.
- the bactericidal agent 3 is a normal temperature solid chemical, and dissolves in the seawater flowing through the main pipe 2, thereby killing microorganisms and bacteria existing in the seawater.
- the sterilizing agent 3 is preferably a chlorine-based sterilizing agent.
- the chlorinated fungicide it is preferable to use one or more selected from the group consisting of chlorinated isocyanurate and hypochlorite.
- hypochlorite include calcium hypochlorite.
- the sterilizing agent 3 is preferably a chlorinated isocyanurate from the viewpoint of high storage stability in a temperature range exceeding room temperature and no side products.
- the chlorinated isocyanurate is a compound having a structure in which a hydrogen atom bonded to a nitrogen atom of isocyanuric acid is substituted with a chlorine atom, and trichloroisocyanuric acid in which a hydrogen atom is substituted with three chlorine atoms (the following structure) Formula (1)) and sodium dichloroisocyanurate in which a hydrogen atom is substituted by two chlorine atoms (the following structural formula (2)) are included.
- These chlorinated isocyanurates generate sterilizable hypochlorous acid (HOCl) by dissolving in seawater, which sterilizes seawater flowing in the main pipe 2.
- the amount of the sterilizing agent 3 is determined according to the amount of ballast water and the concentration of the sterilizing component of the ballast water. For example, when preparing 1,000 tons of ballast water having an effective chlorine concentration of the disinfectant of 50% and a disinfectant concentration of 5 mg / L, the amount of the necessary disinfectant is calculated as 10 kg.
- the form of the bactericidal agent is not particularly limited, and any form such as a granular form, a powder form, or a tablet form may be used, but considering the ease of handling, the granular form or tablet having a diameter of 1 to 100 mm.
- the shape is preferred.
- the form of the disinfectant is preferably appropriately determined according to the seawater uptake speed, the capacity of the ballast tank, the amount of ballast water, the number of voyages, and the like. For example, when it is desired to increase the TRO concentration in a short time or when the management temperature of the ballast water is high, it is preferable to use a granular form. When it is desired to maintain the effect for a relatively long time or when the control concentration of ballast water is low, it is preferable to use a tablet.
- the configuration of the chemical container 40 ′ filled with the sterilizing agent 3 will be described in detail with reference to FIG. 7.
- the mesh member 40B is filled with a plurality of bactericides 3.
- a slit (not shown) is provided on the side surface of the container body 40A, and ballast water flows into the container body 40A through the slit.
- the mesh-like member 40B holds the disinfectant 3 inside and has an opening enough to allow seawater (which may be ballast water) to flow in sufficiently.
- ballast pump 10 is turned on. to start.
- the ballast water in the ballast tank 60 flows through the main pipe 2 through the circulation pipe 80 and is returned to the ballast tank 60 through the bypass pipe 90.
- the sterilizing component is dissolved from the sterilizing agent 3, so that the sterilizing component is introduced into the ballast water in the ballast tank 60.
- ballast water treatment apparatus and a ballast water treatment method that can increase the concentration of the sterilizing component of the ballast water in the ballast tank.
- the ballast water treatment apparatus includes a ballast tank, a main pipe for guiding ballast water to the ballast tank, a circulation pipe for returning the ballast water stored in the ballast tank to the main pipe, and the main pipe.
- a sterilizing component introduction section for introducing a sterilizing component downstream of a connection portion of the piping with the circulation piping.
- ballast water treatment device it is possible to circulate ballast water by returning a part of the ballast water in the ballast tank to the main pipe via the circulation pipe and returning the ballast water from the main pipe to the ballast tank.
- a sterilizing component introduction part is disposed downstream of the main pipe connected to the circulation pipe, and the sterilizing component is introduced into the main pipe from the sterilizing component introduction part, thereby including the sterilizing component.
- Ballast water can be returned to the ballast tank. That is, according to the said ballast water treatment apparatus, a bactericidal component can be additionally introduce
- the sterilizing component can be introduced into the ballast water by returning the ballast water in the ballast tank to the circulation pipe, it is not necessary to adjust the amount of the sterilizing agent in advance. There is also.
- ballast water treatment device since it is only necessary to add a simple facility for newly providing a circulation pipe to the configuration of the conventional ballast water treatment device, the above-described ballast water treatment device can be easily applied even to a ship in which installation space is difficult to secure. .
- the ballast water treatment apparatus may further include a sterilizing component adjusting means for adjusting the amount of the sterilizing component introduced into the main pipe.
- the amount of the sterilizing component introduced into the main pipe from the sterilizing component introducing portion can be adjusted.
- the ballast water in the ballast tank can be adjusted to an appropriate concentration of the sterilizing component.
- the sterilizing component adjusting means by measuring the concentration of the sterilizing component of the ballast water in the ballast tank and feeding back the measurement result to the sterilizing component adjusting means, an appropriate amount of the sterilizing component can be introduced into the main pipe.
- the concentration of the sterilizing component of the ballast water in the ballast tank can be increased moderately.
- the ballast water treatment apparatus has an input unit that receives a command for flowing ballast water from the ballast tank to the circulation pipe, and the sterilizing component adjustment unit is received by the input unit. Based on the command, the amount of the sterilizing component introduced into the main pipe from the sterilizing component introducing unit may be adjusted.
- the amount of the sterilizing component introduced into the ballast water can be adjusted by inputting the amount of the sterilizing component that the operator introduces into the main pipe from the sterilizing component introducing unit,
- the concentration of the sterilizing component of the ballast water can be increased moderately.
- an appropriate amount of the sterilizing component is flowed through the circulation pipe in the ballast water in the ballast tank according to the date and time (for example, several hours to several tens of hours before the call). Ballast water can be treated. Therefore, even when the ballast water is inspected when draining the ballast water, the risk that the number of microorganisms exceeds the standard is very low.
- the ballast water treatment method includes a circulation step of returning the ballast water stored in the ballast tank from the main piping to the ballast tank via the circulation piping, and in the circulation step, the main piping
- the ballast water containing the sterilizing component is returned to the ballast tank by introducing the sterilizing component downstream of the connection portion with the circulation pipe in the.
- the sterilizing component is introduced into the main pipe in the circulation step, and the ballast water containing the sterilizing component can be returned to the ballast tank.
- concentration of the disinfection component of the ballast water in a ballast tank can be raised, and the re-growth of microorganisms and bacteria can be suppressed.
- the ballast water treatment method includes a step of measuring the concentration of a sterilizing component of ballast water stored in the ballast tank, and a sterilizing component to be introduced into the main pipe in the circulation step based on a result obtained by the measurement. And a step of adjusting the amount of.
- the ballast water treatment method includes a step of inputting a command for flowing ballast water from the ballast tank to the circulation piping, and a main piping in the circulation step based on the input command. And a step of adjusting the amount of the sterilizing component to be introduced.
- the ballast water can be returned to the main pipe via the circulation pipe when the operator inputs a command for flowing the ballast water from the ballast tank to the circulation pipe. Accordingly, an appropriate amount of the sterilizing component can be introduced into the ballast water, and the concentration of the sterilizing component of the ballast water in the ballast tank can be increased by returning the ballast water to the ballast tank.
- the ballast water treatment method is based on the time until the scheduled port entry date and time of a ship equipped with the ballast water treatment apparatus, and the amount of the sterilizing component to be introduced into the main pipe in the circulation step
- the process of adjusting may be further included.
- ballast water is treated immediately before the ship calls by introducing an appropriate amount of sterilizing components into the main pipe in accordance with the ship's call date (for example, several hours to several tens of hours before the call). be able to. Therefore, even when the ballast water is inspected when draining the ballast water, the risk that the number of microorganisms exceeds the standard is very low.
- 100 m 3 of seawater was supplied to the ballast tank 60 having a capacity of about 200 m 3 using the ballast water treatment apparatus 100 shown in FIG. Specifically, first, the ballast pump 10 was started, and seawater was taken in from the piping port 2A of the main piping 2 by the pump pressure. By passing this seawater through the filter 20, microorganisms and particles in the seawater were removed.
- a chlorine component was contained in the seawater by injecting a solution of TRO 2000 mg / L in which sodium dichloroisocyanurate was dissolved from the sterilizing component introduction part 40 into the seawater after the filter filtration.
- the seawater containing the chlorine component was stirred with the mixer 50 to make the chlorine component in the seawater uniform, so that the ballast water was poured into the ballast tank 60.
- the ballast pump 10 is started to start the ballast in the ballast tank 60.
- Water was passed through the main pipe 2 via the circulation pipe 80.
- the ballast water flowing into the main pipe 2 was returned to the ballast tank 60 through the sterilizing component introduction unit 40 and the mixer 50 via the bypass pipe 90 without passing through the filter 20.
- the injection amount of the sterilizing component by the sterilizing component introducing unit 40 was adjusted so that the TRO concentration of the ballast water immediately after passing through the sterilizing component introducing unit 40 was 3 mg / L.
- 100 tons of ballast water was returned from the main pipe 2 to the ballast tank 60 via the circulation pipe 80.
- the ballast water that finished this circulation was sampled.
- TRO concentration and the number of heterotrophic bacteria for each of the three types of ballast water sampled above (ballast water immediately after drowning, ballast water after 10 days from dredging, and ballast water in the ballast tank after ballast water circulation) (Seawater medium) was measured.
- the number of heterotrophic bacteria in seawater was measured.
- TRO concentration a value measured by a DPD type chlorimeter II (manufactured by HACH) was adopted. The results are shown in Table 1 below.
- the chlorine component was introduce
- the TRO concentration of the ballast water was increased to 3.2 mg / L, the bacterial count was reduced to about 1.2 ⁇ 10 1 cfu / cc as shown in the data of “post-circulation” bacterial count in Table 1. I was able to suppress it.
- the ballast water in the ballast tank 60 is sterilized by returning the ballast water in the ballast tank 60 to the main pipe 2 via the circulation pipe 80 and additionally introducing a sterilizing component from the sterilizing component introduction unit 40.
- the concentration of ingredients could be increased.
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Abstract
Description
<バラスト水処理装置の構成>
まず、本発明の一実施形態である実施形態1に係るバラスト水処理装置1の構成について、図1を参照して説明する。
次に、上記バラスト水処理装置1における殺菌成分の濃度(塩素濃度)の調整方法について、図3に示すフローチャートに沿って説明する。
次に、上記バラスト水処理装置1による作用効果について説明する。上記バラスト水処理装置1は、バラストタンク60と、バラストタンク60にバラスト水を導く主配管2と、バラストタンク60内に貯留されたバラスト水を、バラストタンク60にバラスト水を導く主配管2に戻す循環配管80と、主配管2における循環配管80との接続部分2Cよりも下流側に殺菌成分を導入する殺菌成分導入部40と、を備えている。上記バラスト水処理装置では、バラストタンク60内のバラスト水の一部を循環配管80経由で主配管2に戻し、当該主配管2からバラストタンク60に戻すというバラスト水の循環を行うことができる。このバラスト水の循環において、主配管2における循環配管80との接続部分2Cよりも下流側に殺菌成分導入部40を配置することにより、殺菌成分導入部40からバラスト水に殺菌成分を注入することができる。これにより殺菌成分を含むバラスト水をバラストタンク60に戻すことができる。つまり、上記バラスト水処理装置1によれば、バラストタンク60内のバラスト水を循環させるとともに殺菌成分導入部40から殺菌成分を導入することによりバラスト水に殺菌成分を追加で導入することができる。これにより、微生物の再増殖を抑制することができる。
実施形態1のバラスト水処理装置1においては、濃度測定部41による測定結果に基づいて主配管2に導入する殺菌成分の分量を調整していたが、このようにバラスト水の殺菌成分の分量を調整する場合のみに限られない。例えば、上記バラスト水処理装置1を搭載した船舶の入港予定日時までの時間に基づいて、循環配管80にバラスト水を流すとともに主配管2に導入する殺菌成分の分量を調整することによってバラスト水の殺菌成分の濃度を調整してもよい。つまり、船舶が寄港する時間から逆算して、数時間から数十時間前に循環配管80にバラスト水を流すことにより、船舶寄港時のバラスト水の殺菌成分の濃度を適正にすることができ、これにより船舶の寄港直前にバラスト水を処理することができる。
本発明の他の実施形態である実施形態2のバラスト水処理装置1’について説明する。実施形態2のバラスト水処理装置1’は、図4に示されるように、実施形態1のそれに対して、各開閉弁71A,71B,71Cの開閉を調整する循環量制御部72に代えて、作業者の手動により各開閉弁71A,71B,71Cの開閉の指令を入力する入力部72’を設けたことが異なる他は実施形態1と同一である。
作用効果の説明においても、実施形態2のバラスト水処理装置1’特有の作用効果のみを説明し、実施形態1と同一の作用効果は割愛する。
次に、本発明の他の実施形態である実施形態3のバラスト水処理装置について説明する。実施形態3のバラスト水処理装置は、図5に示されるように、濃度測定部41を循環配管80に設けたことが異なる他は実施形態1と同一の構成である。
次に、本発明の他の実施形態である実施形態4のバラスト水処理装置について説明する。実施形態4のバラスト水処理装置は、図6に示されるように、殺菌成分導入部40として、殺菌成分を注入するのではなく、殺菌剤3を含む薬品容器40’を配置したことが異なる他は実施形態1のバラスト水処理装置と同一の構成である。本実施形態では、殺菌成分調整手段70は、循環配管80に流すバラスト水の循環量を調整することによって殺菌成分の導入量を調整する。つまり、殺菌成分調整手段70が、薬品容器40’を通過させるバラスト水の循環量を多くすればするほど殺菌剤3がバラスト水に溶け出して殺菌成分を追加することができる。
本実施形態のバラスト水処理装置1における殺菌成分の濃度(塩素濃度)の調整は、以下のようにして行われる。まず、予め設定された測定周期(例えば12時間ごと)にバラストタンク60内のバラスト水の殺菌成分の濃度を濃度測定部41で測定する。そして、この測定データと基準値データとを比較し、当該測定データが基準値以上であるか否か(例えば、3mg/L以上であるか否か)を判定する。そして、基準値未満であると、殺菌成分の濃度が基準値以上となるように第1開閉弁71Aを開けて、第2、第3開閉弁71B,71Cを閉めた上で、バラストポンプ10を起動する。これによりバラストタンク60内のバラスト水が循環配管80を通じて主配管2を流れ、迂回配管90を経由してバラストタンク60に戻される。このとき、循環したバラスト水が薬品容器40’内の殺菌剤3を通過することにより、殺菌剤3から殺菌成分が溶け出すことで、バラストタンク60内のバラスト水に殺菌成分が導入される。
上記でサンプリングした3種のバラスト水(漲水直後のバラスト水、漲水から10日経過後のバラスト水、及びバラスト水循環後のバラストタンク内のバラスト水)のそれぞれについて、TRO濃度及び従属栄養細菌数(海水培地)を測定した。また比較として、海水の従属栄養細菌数を測定した。TRO濃度は、DPD方式のクロリメーターII(HACH社製)によって測定した値を採用した。この結果を以下の表1に示す。
Claims (9)
- バラストタンクと、
前記バラストタンクにバラスト水を導く主配管と、
前記バラストタンク内に貯留されたバラスト水を前記主配管に戻す循環配管と、
前記主配管における前記循環配管との接続部分よりも下流側に殺菌成分を導入する殺菌成分導入部と、を備えた、バラスト水処理装置。 - 前記殺菌成分導入部から前記主配管に導入する殺菌成分の分量を調整する殺菌成分調整手段をさらに備えた、請求項1に記載のバラスト水処理装置。
- 前記バラストタンクに貯留されたバラスト水の殺菌成分の濃度を測定する濃度測定部をさらに備え、
前記殺菌成分調整手段は、前記濃度測定部による測定結果に基づいて、前記殺菌成分導入部から前記主配管に導入する殺菌成分の分量を調整する、請求項2に記載のバラスト水処理装置。 - 前記バラストタンクから前記循環配管にバラスト水を流す指令を受け付ける入力部を有し、
前記殺菌成分調整手段は、前記入力部で受け付けた指令に基づいて、前記殺菌成分導入部から前記主配管に導入する殺菌成分の分量を調整する、請求項2に記載のバラスト水処理装置。 - 請求項2又は3のバラスト水処理装置を搭載した船舶の入港予定日時までの時間に基づいて、前記殺菌成分導入部から前記主配管に導入する殺菌成分の分量を調整する、請求項2又は3に記載のバラスト水処理装置。
- バラストタンクに貯留したバラスト水を、循環配管を経由して主配管から前記バラストタンクに戻す循環工程を含み、
前記循環工程において、前記主配管における前記循環配管との接続部分よりも下流側に殺菌成分を導入することにより、前記殺菌成分を含む前記バラスト水を前記バラストタンクに戻す、バラスト水処理方法。 - 前記バラストタンクに貯留されたバラスト水の殺菌成分の濃度を測定する工程と、
前記測定により得られた結果に基づいて、前記循環工程における前記主配管に導入する殺菌成分の分量を調整する工程と、をさらに含む、請求項6に記載のバラスト水処理方法。 - 前記バラストタンクから前記循環配管にバラスト水を流す指令を入力する工程と、
前記入力された指令に基づいて、前記循環工程における前記主配管に導入する殺菌成分の分量を調整する工程と、をさらに含む、請求項6に記載のバラスト水処理方法。 - 請求項1~5のいずれか一項に記載されたバラスト水処理装置を搭載した船舶の入港予定日時までの時間に基づいて、前記循環工程における前記主配管に導入する殺菌成分の分量を調整する工程をさらに含む、請求項6に記載のバラスト水処理方法。
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EP16786167.3A EP3290394B1 (en) | 2015-04-30 | 2016-02-03 | Ballast water treatment device and ballast water treatment method |
KR1020197022190A KR20190091386A (ko) | 2015-04-30 | 2016-02-03 | 밸러스트수 처리 장치 및 밸러스트수 처리 방법 |
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Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009112978A (ja) * | 2007-11-08 | 2009-05-28 | Mitsubishi Heavy Ind Ltd | バラスト水処理システム |
JP2015016761A (ja) * | 2013-07-10 | 2015-01-29 | 栗田工業株式会社 | バラスト水の処理システムおよびバラスト水の処理方法 |
Family Cites Families (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4330412A (en) * | 1977-07-05 | 1982-05-18 | International Telephone And Telegraph Corporation | Hydrotherapy device, method and apparatus |
WO2002072478A2 (en) * | 2000-11-06 | 2002-09-19 | Larry Russell | Ballast water treatment for exotic species control |
AU2005212085A1 (en) * | 2004-02-13 | 2005-08-25 | Mitsubishi Heavy Industries, Ltd. | Method of liquid detoxification and apparatus therefor |
AU2005320350B8 (en) * | 2005-01-24 | 2009-11-19 | Nutech 03, Inc. | Ozone injection method and system |
KR20060088576A (ko) * | 2005-02-02 | 2006-08-07 | 이상렬 | 황동금속사를 이용한 선박의 밸러스트수 처리장치 |
KR101724166B1 (ko) * | 2009-02-16 | 2017-04-18 | 주식회사 쿠라레 | 여과 유닛 및 이것을 구비한 밸러스트수 제조 장치 |
WO2010093025A1 (ja) | 2009-02-16 | 2010-08-19 | 株式会社クラレ | ろ過ユニットおよびこれを備えたバラスト水製造装置 |
JP5431208B2 (ja) * | 2010-02-24 | 2014-03-05 | 三洋電機株式会社 | バラスト水処理装置 |
CN101948204A (zh) * | 2010-09-07 | 2011-01-19 | 中国船舶重工集团公司第七一八研究所 | 一种高效的船舶压载水处理*** |
JP2012254415A (ja) * | 2011-06-09 | 2012-12-27 | Kurita Water Ind Ltd | 船舶バラスト水の処理システム |
JP2013017936A (ja) * | 2011-07-08 | 2013-01-31 | Gaia:Kk | 電解水製造装置 |
CN102515400A (zh) * | 2011-12-21 | 2012-06-27 | 青岛双瑞海洋环境工程股份有限公司 | 高效船舶压载水处理方法 |
CA2864381C (en) * | 2012-02-15 | 2016-08-02 | Mitsubishi Heavy Industries, Ltd. | Seawater desalination system |
JP5701325B2 (ja) * | 2013-02-25 | 2015-04-15 | 三菱重工業株式会社 | バラスト水処理システム |
KR101584051B1 (ko) * | 2013-05-20 | 2016-01-11 | 주식회사 파나시아 | 밸러스트수의 탁도를 고려한 밸러스트수 처리장치 및 그 방법 |
-
2016
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Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009112978A (ja) * | 2007-11-08 | 2009-05-28 | Mitsubishi Heavy Ind Ltd | バラスト水処理システム |
JP2015016761A (ja) * | 2013-07-10 | 2015-01-29 | 栗田工業株式会社 | バラスト水の処理システムおよびバラスト水の処理方法 |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2019044769A1 (ja) | 2017-08-31 | 2019-03-07 | 株式会社クラレ | バラスト水処理方法 |
JP6529706B1 (ja) * | 2017-08-31 | 2019-06-12 | 株式会社クラレ | バラスト水処理方法 |
EP3666737A4 (en) * | 2017-08-31 | 2021-04-21 | Kuraray Co., Ltd. | BALLAST WATER TREATMENT DEVICE |
US11530144B2 (en) | 2017-08-31 | 2022-12-20 | Kuraray Co., Ltd. | Ballast water treatment method |
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EP3290394A1 (en) | 2018-03-07 |
JPWO2016174890A1 (ja) | 2018-02-22 |
EP3290394A4 (en) | 2018-11-21 |
CN107531521A (zh) | 2018-01-02 |
EP3290394B1 (en) | 2021-06-09 |
KR20190091386A (ko) | 2019-08-05 |
JP6730263B2 (ja) | 2020-07-29 |
KR20170140384A (ko) | 2017-12-20 |
US20180312237A1 (en) | 2018-11-01 |
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