JP5386690B2 - Liquid detoxification treatment apparatus and ship equipped with this apparatus - Google Patents

Description

The present invention mainly removes microorganisms in untreated seawater to form clean treated seawater and stores it in a ballast water tank, or clean untreated seawater stored in a ballast water tank during voyage. It is applied to ballast water treatment that is performed when untreated seawater is discharged from the ballast water tank into clean treated seawater, etc., and mechanical treatment such as electrolytic treatment and filter treatment is applied to liquid containing untreated seawater. subjected to the microorganism separation treatment, to harmless Kasho MakotoSo location and ship equipped with the system for a liquid such as seawater to be converted to a clean processing liquid by removing microbes該海water.

  In ships such as tankers, when navigating without oil, the seawater stored in the ballast water tank, that is, ballast water, removes microorganisms in untreated seawater in order to avoid marine pollution and pollution. Detoxification treatment is performed to make clean treated seawater.

As such a detoxification method for seawater, the techniques of Patent Document 1 (Japanese Patent No. 2794537), Patent Document 2 (Japanese Patent Laid-Open No. 2002-192161), and Patent Document 3 (Japanese Patent Laid-Open No. 2003-200156) are provided. ing.
In the technique of Patent Document 1, the ballast water tank is emptied or water is left in the bottom, and then the temperature of precipitates remaining in the ballast water tank is raised to a temperature equal to or higher than the killing temperature of harmful plankton and bacteria. Heated to a predetermined time.

In the technique of Patent Document 2, a high voltage pulse is applied to the ballast water in the ballast water tank, the high voltage pulse is directly applied to the harmful microorganisms, and a discharge is generated therein to kill or delete the harmful microorganisms. The harmful microorganisms are sterilized or indirectly killed or sterilized by a shock wave generated by arc discharge between the electrodes.
In the technique of Patent Document 3, a slit plate having a plurality of elongated slits is attached in the cross-sectional direction in the middle of the flow path in the pipe, and untreated seawater is allowed to pass through the slit, thereby allowing the microorganisms of the untreated seawater to pass through. It is damaged and killed or sterilized.

Japanese Patent No. 2794537 JP 2002-192161 A JP 2003-200156 A

In the technique of Patent Document 1, since the ballast water tank is empty or in a state where water remains in the bottom, there is a risk of damaging the hull due to local stress concentration. Further, since the ballast water tank is heated over a wide range so as to raise the temperature of the sediment accumulated in the entire bottom of the ballast water tank, the heating work takes time and labor, and the processing cost increases.
Moreover, in the technique of patent document 2, since a large-scale high voltage pulse application equipment is required, an installation cost and an operating cost become high.
Furthermore, in the technique of Patent Document 3, large-sized microorganisms can be killed or sterilized by passing untreated seawater through a slit, but small-sized bacteria are killed or sterilized. Have difficulty.

Therefore, the inventors have proposed an invention that solves such a problem in Japanese Patent Application No. 2004-135389.
However, in such an invention, the microorganisms in the liquid containing untreated seawater are subjected to mechanical microorganism separation treatment such as electrolytic treatment and filter treatment to remove the microorganisms and accommodated in a treatment liquid tank such as a ballast water tank. It does not mention the following issues that need to be solved.

(1) All or part of the liquid is introduced into a storage tank, and the liquid is circulated through a circulation path between the storage tank and an electrolytic cell that electrolyzes the liquid to generate a chlorine-containing substance. When a chlorine-containing substance is produced from the liquid and the chlorine-containing substance is injected into an untreated liquid to kill or sterilize microorganisms, the liquid is rendered harmless. In the case of treatment, since the chlorine concentration in the untreated liquid is low, a chlorine-containing substance by electrolysis cannot be efficiently produced, and the treatment efficiency of the electrolytic equipment is lowered.
(2) When the surviving microorganisms are present in the ballast water in the ballast water tank at a concentration higher than the regulated concentration, it may not be possible to treat the surviving microorganisms especially during the navigation of the ship.
(3) When the residual chlorine concentration in the ballast water stored in the ballast water tank after chlorination becomes higher than the permissible value, the chlorine concentration in the ballast water tank cannot be reduced, and together with the ballast water There is a possibility of discharging chlorine above the specified value.
(4) During the electrolysis of seawater, hydrogen is generated from the electrode side that is paired with the electrode on the chlorine-containing substance side. If this hydrogen accumulates in the electrolytic cell or in the ballast water tank, there is a risk of explosion.
(5) Seawater after electrolytic treatment and untreated seawater may be supplied into the ballast water tank in a non-uniform state without being sufficiently mixed.

Accordingly, in view of the problems of the prior art, the present invention can remove liquids such as seawater that can be detoxified by removing living microorganisms in the ballast water tank at any time even during navigation of the ship. It is an object of the present invention to provide a detoxification processing apparatus and a ship equipped with this apparatus.

In order to achieve the above object, the present invention provides a liquid detoxification treatment apparatus configured to remove microorganisms in an untreated liquid, convert it into a clean treatment liquid, and store it in a ballast water tank. A microorganism separation treatment means for removing relatively large microorganisms in the liquid by a filtration method or a centrifugal separation method through which the liquid is passed, and an electrolysis apparatus configured to electrolyze all or part of the liquid; The liquid after processing in the microorganism separation processing means and the seawater electrolysis apparatus is supplied to the ballast water tank, and the liquid in the ballast water tank is disposed upstream of the microorganism separation processing means or the electrolytic device liquid reflux path for circulating on one of the upstream side of a pump for circulating the liquid in the ballast water tank in the liquid return path is provided, before Characterized in that a hydrotreater for burning or dilute hydrogen generated by the electrolysis apparatus (claim 1).

According to this invention, in the case where the microorganisms present in the ballast water tank after the detoxification treatment in the microorganism separation treatment means such as the filter treatment device and the electrolysis device are present in a concentration exceeding the regulated concentration, The liquid is circulated to the upstream side of the microorganism separation treatment means or the upstream side of the electrolysis apparatus through the seawater reflux path, and the viable microorganisms are removed by the electrolysis apparatus or the electrolysis apparatus and the microorganism separation treatment means. Since the treatment can be performed, it is possible to make the liquid harmless by removing the living microorganisms in the ballast water tank at any time even during the navigation of the ship.
Further, by introducing hydrogen generated during chlorination (electrolytic treatment) to a hydrogen treatment apparatus and burning or diluting in the hydrogen treatment apparatus, it is possible to eliminate the fear of explosion caused by the hydrogen.

In such invention, it is preferable to provide a chlorine deactivating agent adding means for adding chlorine deactivating agent for deactivating the chlorine to the ballast water tank to said ballast water tank (claim 2).
In this invention, preferably, sodium thiosulfate is used as the chlorine-inactivating substance (Claim 3 ).

According to this invention, even when the residual chlorine concentration in the liquid stored in the ballast water tank after chlorination (seawater electrolysis treatment) is higher than the allowable value, preferably sodium thiosulfate By adding a chlorine deactivating material comprising (Claim 3 ) to the treatment liquid in the ballast water tank and reducing chlorine with the chlorine deactivating material, the residual chlorine concentration in the ballast water tank is less than the allowable concentration. Or the residual chlorine concentration can be made zero. Thereby, the pollution of the sea area by discharging | emitting chlorine beyond a regulation value with a liquid can be avoided.
In addition, if chlorine deactivation material is added to the treatment liquid discharged from the ballast water tank, chlorine decreases in the ballast water tank, so that the amount of addition of chlorine deactivation material can be minimized, If a chlorine deactivating substance is added in the process of passing through the liquid pipe, mixing with the liquid can be promoted as compared with the case where it is added in the ballast water tank.

In this invention, an inert gas injection means for injecting an inert gas for degassing chlorine into the ballast water tank into the ballast water tank, and microorganisms in the inert gas before being supplied to the ballast water tank preferably Rukoto provided a microorganism removing means for removing (claim 4).

According to this invention, even when the residual chlorine concentration in the liquid stored in the ballast water tank after chlorination (seawater electrolysis treatment) becomes higher than the allowable value, the ballast is supplied by the inert gas injection means. By injecting an inert gas such as air or nitrogen into the water tank and degassing the chlorine in the ballast water tank with the inert gas, the residual chlorine concentration in the ballast water tank is kept below an allowable concentration. be able to. Thereby, the pollution of the sea area by discharging | emitting chlorine more than a regulation value with the liquid in a ballast water tank can be avoided.
Moreover, after killing microorganisms by letting the said inert gas pass through a microorganism removal means, it inject | pours in a ballast water tank, Therefore The purified inert gas can be supplied to a ballast water tank.

In this invention, the liquid in the liquid passage and the chlorine from the electrolysis device outlet passage between the junction of the liquid passage connected to the ballast water tank and the electrolytic device outlet passage and the ballast water tank. it is preferable to provide the mixing acceleration means for promoting mixing of the containing material (claim 5).

  According to this invention, the liquid passage connected to the ballast water tank is mixed in the liquid passage by the mixing promoting means such as a line mixer provided between the joining portion of the liquid circulation passage at the outlet of the electrolyzer and the ballast water tank. The mixture of the liquid and the chlorine-containing substance from the liquid circulation passage is promoted to quickly generate a uniform concentration treatment liquid and store it in the ballast water tank.

In the above invention, it is preferable that the untreated liquid is a liquid containing a seawater component. Furthermore, vessels of applying the non Gaika processing apparatus configured as described above is also within the scope of the present invention.

According to the present invention, it is possible to remove the living microorganisms in the ballast water tank at any time even during the navigation of the ship, thereby detoxifying the liquid in the ballast water tank.
Further, according to the present invention, by reducing chlorine with a chlorine deactivating substance, the residual chlorine concentration in the ballast water tank can be kept below an allowable concentration, and chlorine in the ballast water tank can be reduced by an inert gas. By degassing, the residual chlorine concentration in the ballast water tank can be kept below the allowable concentration, and these can avoid contamination of the sea area by discharging chlorine above the specified value together with the liquid in the ballast water tank. .

Further, according to the present invention, hydrogen generated by chlorination (electrolytic treatment) is generated by chlorination (electrolytic treatment) by injecting an inert gas into the upper space volume of the liquid in the ballast water tank. By replacing the hydrogen accumulated in the space volume with an inert gas, and by introducing the hydrogen to the hydrogen treatment device and burning or diluting the hydrogen in the hydrogen treatment device, there is concern about the retention of hydrogen and the associated explosion. Can be resolved.
Further, according to the present invention, mixing of the untreated liquid in the liquid passage and the liquid after the electrolytic treatment from the liquid circulation passage is promoted, so that treated water having a uniform concentration can be quickly generated and stored in the ballast water tank.

  Hereinafter, the present invention will be described in detail with reference to the embodiments shown in the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the component parts described in this example are not intended to limit the scope of the present invention only to specific examples unless otherwise specified. Only.

<Reference Example 1>
FIG. 1 is a system diagram of a detoxifying device for marine ballast water according to a first reference example of the present invention.
In FIG. 1, 1 is a screen for filtering untreated seawater to capture foreign matters such as dust, 2 is a pump for transporting seawater to the treatment line 6, and 5 is a ballast water tank in which treated seawater is accommodated. 20 is a filter processing device installed in the processing line 6, 21 is a backwash line of the filter processing device 20, and 22 is an on-off valve for opening and closing the backwash line 21.
In the first reference example , untreated seawater after foreign matters such as dust are captured by the screen 1 is introduced into the filter 20, and relatively large microorganisms in the seawater are removed by passing through the filter treatment device 20. To do.

In the first reference example , a liquid having a low chlorine concentration such as brackish water or fresh water is used instead of the untreated seawater.
That is, 04 is a liquid electrolysis apparatus having the same configuration as the seawater electrolysis apparatus, and is configured as follows.
43 is a storage tank, 44 is a pump, 41 is an electrolytic cell, and 42 is a power supply device for the electrolytic cell 41. A liquid for chlorination is introduced into the storage tank 43 through the extraction line 7.
Then, a circulation path 47 that returns from the storage tank 43 to the storage tank 43 through the pump 44 and the electrolytic tank 41 is formed, and the liquid in the storage tank 43 is circulated through the circulation path 47 by the pump 44. Hypochlorous acid, which is a chlorine-containing substance, is generated from the liquid, and the hypochlorous acid is injected into the treatment line 6 (see FIG. 1) through the injection line 8 in the middle of the circulation path 47. The processing liquid is accommodated in the ballast water tank 5. Reference numerals 45 and 46 are on-off valves.

Reference numeral 60 denotes a salt storage tank. In the salt storage tank 60, sodium chloride as an electrolysis promoter for increasing the chlorine concentration is accommodated. 61a is an electrolysis promoter supply pipe connecting the inside of the salt storage tank 60 and the storage tank 43, and 61 is a pump provided in the electrolysis promoter supply pipe 61a.
Sodium chloride in the salt storage tank 60 is injected into the storage tank 43 through the electrolysis promoter supply pipe 61a by the pump 61 and added to the liquid in the storage tank 43 to increase the chlorine concentration of the liquid. .
In this case, the sodium chloride in the salt storage tank 60 may be supplied into the electrolytic cell 41 as shown by the broken line in the figure, or the liquid flow path between the storage tank 43 and the electrolytic cell 41 or the storage. You may supply to the multiple places in the tank 43, the electrolytic vessel 41, and a liquid flow path.
Further, as the electrolysis promoter, high-concentration seawater having a salt concentration of a certain amount or more can be used instead of the sodium chloride.

According to the first reference example , even when a liquid having a low chlorine concentration, such as brackish water or fresh water, is detoxified by the liquid electrolysis apparatus 04, sodium chloride or high-concentration seawater having a salt concentration of a certain amount or more is used. Is injected into the storage tank 43, the electrolytic tank 41, or one or a plurality of portions of the liquid flow path between the storage tank 43 and the electrolytic tank 41. It is possible to increase the salt concentration during the electrolytic treatment.
Due to the increase in the salinity of the liquid to be treated, the electrolytic treatment can be performed while maintaining high current efficiency in the electrolytic cell 41 even during the electrolytic treatment of a liquid having a low chlorine concentration such as brackish water or fresh water. High processing efficiency can be maintained.

FIG. 2 is a system diagram of the detoxifying device for marine ballast water according to the first embodiment of the present invention.
In FIG. 2, 1 is a screen for filtering untreated seawater to capture foreign matters such as dust, 2 is a pump for transporting seawater to the treatment line 6, and 5 is a ballast water tank in which treated seawater is accommodated. Reference numeral 20 denotes a filter processing apparatus installed in the processing line 6. Reference numeral 27 denotes a discharge pipe for discharging foreign matter collected by the filter processing apparatus 20.
Reference numeral 4 denotes a seawater electrolysis apparatus having the same configuration as the liquid electrolysis apparatus 04 shown in FIG.
A circulation passage 41 circulates a part of the seawater at the outlet of the pump 2 to the inlet side of the screen 1. Reference numeral 40 denotes a circulation passage for detoxifying the filter treatment device 20 and the seawater electrolysis device 4 and circulating the treated seawater before being introduced into the ballast water tank 5 to the suction side of the pump 2.

  50 and 51 are on-off valves for opening and closing the inlet and outlet sides of the screen 1 of the processing line 6, 29 and 30 are on-off valves for opening and closing the inlet and outlet sides of the filter processing device 20, and 55 and 56 are the circulation valves. On-off valves for opening and closing the inlet side and outlet side of the passage 41, 53 and 57 are on-off valves for opening and closing the upstream and downstream sides of the branching portion of the circulation passage 40 of the processing line 6, and 53a is the inlet of the circulation passage 40. An on-off valve 52 for opening and closing the side is an on-off valve installed in the downstream of the branch portion of the circulation passage 41 of the processing line 6.

  A circulation passage 63 connects the ballast water tank and the inlet portion of the circulation passage 40, and 63 a is an open / close valve that opens and closes the circulation passage 63. 64 is branched from the middle of the circulation path 40 and connected to the outlet portion of the filter processing apparatus 20 of the processing line 6, and 62 is installed in the seawater circulation path 64 and passes through the circulation path 40. Booster pumps 64 a and 64 b for supplying circulating seawater to the processing line 6 are open / close valves that open and close the suction side and the discharge side of the booster pump 62.

In the first embodiment , a part of the seawater stored in the ballast water tank 5 is caused by opening the on-off valves 63a, 64a, 64b, 53, 57 and closing the on-off valve 64a. The pump 62 returns from the circulation passage 63 through the circulation passage 40 and the seawater recirculation passage 64 to the outlet portion of the filter processing device 20 in the treatment line 6, and then passes through the extraction line 7 and the seawater electrolysis. Introduced into the device 4. Then, the seawater electrolysis apparatus 4 generates hypochlorous acid as a chlorine-containing substance from the seawater, and the hypochlorous acid is injected into the treatment line 6 through the injection line 8. The seawater after the hypochlorous acid injection is circulated to the ballast water tank 5.
In addition, as shown with a broken line in FIG. 2, the seawater recirculation path 62 branched from the middle of the circulation passage 40 is connected to the inlet portion of the filter processing apparatus 20, and the microorganism filtration process in the filter processing apparatus 20 and You may make it circulate to the ballast water tank 5 after performing both chlorinations in the said seawater electrolyzer 4. FIG.

According to this 1st Example , when the microorganisms which survived exist in the ballast water accommodated in the ballast water tank 5 after the detoxification process by the filter processing apparatus 20 and the seawater electrolysis apparatus 4 more than a regulation object density | concentration. The ballast water is circulated to either the upstream side of the filter processing device 20 or the upstream side of the seawater electrolysis device 4 through the seawater return path 64, and the seawater electrolysis device 4 or the seawater electrolysis device 4 and the filter are circulated. Since the treatment apparatus 20 can perform the removal process of the living microorganisms, the removal process of the living microorganisms in the ballast water tank 5 can be performed at any time even during the navigation of the ship to render the ballast water harmless. it can.

FIG. 3 is a system diagram (corresponding to FIG. 2) of the detoxifying device for marine ballast water according to the second embodiment of the present invention.
In the second embodiment , the seawater is subjected to microbial separation treatment by the filter treatment device 20 and chlorination treatment by the seawater electrolysis treatment 4, and then the treated seawater is accommodated in the ballast water tank 5, and the treatment in the ballast water tank 5 is performed. Sodium thiosulfate, which is a chlorine deactivating material for deactivating chlorine, is added to seawater through a chlorine reducing agent injection pipe 65.
3, the same members as those in FIG. 2 in the first embodiment are denoted by the same reference numerals.
According to the second embodiment, the residual chlorine concentration in the ballast water tank 5 stored in the ballast water tank 5 after the microbial separation treatment by the filter treatment device 20 and the chlorination treatment by the seawater electrolysis treatment 4 becomes higher than the allowable value. Even in this case, a chlorine deactivation material such as sodium thiosulfate is added to the treated seawater in the ballast water tank 5 and the chlorine is reduced by the chlorine deactivation material, thereby remaining in the ballast water tank 5. The chlorine concentration can be kept below the allowable concentration. Thereby, the pollution of the sea area by discharging | emitting chlorine more than a regulation value with ballast water can be avoided.
Further, if sodium thiosulfate, which is the chlorine deactivating substance, is added to the treated seawater discharged from the ballast water tank 5, chlorine is reduced in the ballast water tank. When sodium thiosulfate is added in the course of passing through the seawater piping, mixing with ballast water can be promoted as compared with the case where it is added in the ballast water tank.

FIG. 4 is a system diagram (corresponding to FIG. 2) of the detoxifying device for marine ballast water according to the third embodiment of the present invention.
In the third embodiment , the seawater is subjected to microbial separation treatment by the filter treatment device 20 and chlorination treatment by the seawater electrolysis treatment 4, and then the treated seawater is stored in the ballast water tank 5, and the treatment in the ballast water tank 5 is performed. An inert gas such as air or nitrogen is injected into the sea water through an air supply pipe 66 by a blower 67. In FIG. 4, 67a is an air suction pipe to the blower 67, and 68 is activated carbon (microorganism removing means) for removing microorganisms in the inert gas from the blower 67.
4, the same members as those in FIG. 2 in the first embodiment are denoted by the same reference numerals.

According to the third embodiment, after the microorganism separation treatment by the filter treatment device 20 and the chlorination treatment by the seawater electrolysis treatment 4, the treated seawater is accommodated in the ballast water tank 5 and accommodated in the ballast water tank 5. Even when the residual chlorine concentration in the ballast water becomes higher than the allowable value, an inert gas such as air or nitrogen is injected into the ballast water tank 5 by the blower 67, and the inert gas By degassing the chlorine in the ballast water tank 5, the residual chlorine concentration in the ballast water tank can be kept below the allowable concentration. Thereby, the pollution of the sea area by discharging | emitting chlorine more than a regulation value with ballast water can be avoided.
Moreover, since the said inert gas is injected into the ballast water tank 5 after killing microorganisms by passing activated carbon (microorganism removal means), the purified inert gas can be supplied to the ballast water tank 5. .

FIG. 5 is a configuration diagram around the ballast water tank of the detoxifying apparatus for marine ballast water according to the fourth embodiment of the present invention.
In the fourth embodiment , the seawater is subjected to microbial separation treatment by the filter treatment device 20 and chlorination treatment by the seawater electrolysis treatment 4, and then the treated seawater is stored in the ballast water tank 5, and the gas in the ballast water tank 5 is stored. The gas accumulated in the part, specifically, the hydrogen gas generated in the seawater electrolysis process 4 is discharged from the discharge pipe 75, and an inert gas such as air or nitrogen is supplied into the volume of the gas part by the blower 67. Inject through tube 74. In FIG. 5, 67a is an air suction pipe to the blower 67, and 68 is activated carbon (microorganism removing means) for removing microorganisms in the inert gas from the blower 67.

According to the fourth embodiment, the chlorination treatment by the seawater electrolysis device 4 is performed in the upper space volume of the ballast water stored in the ballast water tank 5 after the microorganism separation treatment by the filter treatment device 20 and the chlorination treatment by the seawater electrolysis device 4. Hydrogen generated in (seawater electrolysis treatment) accumulates, and an inert gas such as air or nitrogen is injected into the volume, and the hydrogen gas accumulated in the volume is replaced with an inert gas, thereby the ballast. It is possible to eliminate the concern about the stagnation of hydrogen in the upper space volume of the water tank 5 and the associated explosion.

FIG. 6 is a system diagram (corresponding to FIG. 2) of the detoxifying device for marine ballast water according to the fifth embodiment of the present invention.
In FIG. 6, 4 is a seawater electrolyzer, and the main structure is the same as that of the seawater electrolyzer in each of the above embodiments, and is configured as follows.
43 is a storage tank, 44 is a pump, 41 is an electrolytic cell, and 42 is a power supply device for the electrolytic cell 41. A liquid for chlorination is introduced into the storage tank 43 through the extraction line 7. Then, a circulation path 47 that returns from the storage tank 43 to the storage tank 43 through the pump 44 and the electrolytic tank 41 is formed, and the liquid in the storage tank 43 is circulated through the circulation path 47 by the pump 44. Hypochlorous acid, which is a chlorine-containing substance, is generated from the liquid, and the hypochlorous acid is injected into the treatment line 6 (see FIG. 1) through the injection line 8 in the middle of the circulation path 47. The processing liquid is accommodated in the ballast water tank 5.

In the fifth embodiment , a hydrogen treatment apparatus 70 for combusting or diluting hydrogen generated in the seawater electrolysis apparatus 4 is additionally provided in the seawater electrolysis apparatus 4 configured as described above. In other words, hydrogen gas stored in the electrolytic cell 41 or the storage tank 43 is introduced into the hydrogen treatment apparatus 70 through a hydrogen extraction pipe 69, and can be exploded by burning or diluting in the hydrogen treatment apparatus 70. After removing the property, the pump 71 discharges it to the outside.
According to the fifth embodiment, hydrogen gas generated during the seawater electrolysis process in the seawater electrolysis apparatus 4 is guided to the hydrogen treatment apparatus 70 and burned or diluted in the hydrogen treatment apparatus 70, so that an explosion caused by the hydrogen is generated. Can eliminate concerns.

FIG. 7 is a system diagram (corresponding to FIG. 2) of the detoxifying device for marine ballast water according to the sixth embodiment of the present invention.
In the sixth embodiment , the treatment line 6 connected to the ballast water tank 6 is connected between the joining portion of the seawater electrolysis apparatus 4 outlet side injection line 8 and the ballast water tank 5. A line mixer 76 that promotes mixing of seawater in the line 6 and hypochlorous acid, which is a chlorine-containing substance from the seawater electrolysis apparatus 4, is provided.
According to the sixth embodiment, the line mixer 76 provided between the joining portion of the treatment line 6 connected to the ballast water tank 5 and the injection line 8 at the outlet of the seawater electrolysis apparatus 4 and the ballast water tank 5. By mixing the seawater in the treatment line 6 with hypochlorous acid (chlorine-containing substance) from the seawater electrolyzer 4, the treated seawater with a uniform concentration can be quickly generated and accommodated in the ballast water tank 5.

  According to the present invention, a chlorine-containing substance can be efficiently produced even in an untreated liquid with a low chlorine concentration, enabling treatment of living microorganisms in ballast water in the ballast water tank, and the chlorine concentration in the ballast water tank is always set to a prescribed value. Non-harmful for liquids such as seawater that can be maintained in the following, and can reliably treat hydrogen generated during electrolysis, and can be supplied to a ballast water tank by uniformly mixing seawater after electrolysis and untreated seawater The processing method and apparatus, and a ship equipped with the apparatus can be provided.

It is a systematic diagram of the detoxification processing apparatus for ship ballast water concerning the 1st reference example of the present invention. BRIEF DESCRIPTION OF THE DRAWINGS It is a systematic diagram of the detoxification processing apparatus for ship ballast water based on 1st Example of this invention. It is a figure corresponding to FIG. 2 which shows 2nd Example . It is a figure corresponding to FIG. 2 which shows 3rd Example . It is a block diagram of the ballast water tank periphery which shows 4th Example . FIG. 10 is a diagram corresponding to FIG. 2 illustrating a fifth embodiment . It is a figure corresponding to FIG. 2 which shows 6th Example .

DESCRIPTION OF SYMBOLS 1 Screen 2 Pump 4 Seawater electrolysis apparatus 5 Ballast water tank 6 Processing line 20 Filter processing apparatus 40 Circulation path 41 Electrolysis tank 42 Power supply apparatus 43 Storage tank 60 Salt storage tank 61a Electrolysis promoter supply pipe 62 Booster pump 63 Circulation path 64 Seawater reflux Path 65 Chlorine reducing agent injection pipe 66 Air supply pipe 67 Blower 68 Activated carbon (microorganism removal means)
69 Hydrogen Extraction Pipe 70 Hydrogen Treatment Equipment 71 Pump 74 Air Supply Pipe 76 Line Mixer

Claims (7)

In a liquid detoxification treatment apparatus configured to remove microorganisms in an untreated liquid and convert it to a clean treatment liquid and accommodate it in a ballast water tank, a filtration method or a centrifugal separation method in which the liquid is passed through the filter The microorganism separation processing means for removing the relatively large microorganisms in the liquid and the electrolysis apparatus configured to electrolyze all or part of the liquid, and the microorganism separation processing means and the electrolysis The liquid after the processing in the apparatus is configured to be supplied to the ballast water tank, and the liquid in the ballast water tank is circulated to either the upstream side of the microorganism separation processing means or the upstream side of the electrolyzer. A liquid recirculation path to be provided , and a pump for circulating the liquid in the ballast water tank to the liquid recirculation path ,
A liquid detoxification treatment apparatus comprising a hydrogen treatment apparatus for burning or diluting hydrogen generated in the electrolysis apparatus.   2. The liquid detoxification treatment according to claim 1, further comprising a chlorine deactivation material adding means for adding a chlorine deactivation material for deactivating chlorine in the ballast water tank. apparatus.   The liquid detoxification treatment apparatus according to claim 2, wherein sodium thiosulfate is used as the chlorine deactivating material.   An inert gas injection means for injecting an inert gas for degassing chlorine into the ballast water tank and a microorganism for removing microorganisms in the inert gas before being supplied to the ballast water tank The liquid detoxification treatment apparatus according to any one of claims 1 to 3, further comprising a removing unit. Between the junction of the liquid passage connected to the ballast water tank and the electrolyzer outlet passage and the ballast water tank, the liquid in the liquid passage and the chlorine-containing substance from the electrolyzer outlet passage The liquid detoxification processing apparatus according to any one of claims 1 to 4 , further comprising mixing promoting means for promoting mixing.   A ship provided with the detoxification processing apparatus according to any one of claims 1 to 5.   The liquid detoxification processing apparatus according to any one of claims 1 to 5, wherein the untreated liquid is a liquid containing a seawater component.

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