JP5132229B2 - Venturi pipe device and ballast water treatment apparatus using the venturi pipe device - Google Patents

Description

  The present invention relates to a venturi pipe device for efficiently killing harmful aquatic organisms and microorganisms contained in, for example, ballast water loaded in a ballast tank of a ship, and a ballast water treatment apparatus using the venturi pipe.

In general, a ship with an empty load or a small load carries water injection of ballast before leaving the port because of the necessity of ensuring the depth of submersion of the propeller and ensuring safe navigation during empty loading. Conversely, when loading in the port, the ballast water is discharged.
By the way, when ballast water is poured and drained by a ship that goes back and forth between loading and unloading ports in different environments, there is a concern that it may adversely affect the coastal ecosystem due to the difference in microorganisms contained in the ballast water. Has been.
Therefore, an international convention for the regulation and management of ship ballast water and sediment was adopted in February 2004 at an international conference on ship ballast water management, which required the treatment of ballast water.

The standard established by the International Maritime Organization (IMO) as a standard for the treatment of ballast water is that the number of organisms (mainly zooplankton) of 50 μm or more contained in the ballast water discharged from the ship is less than 10 in 1 m ³ , 10 μm or more The number of organisms less than 50 μm (mainly phytoplankton) is less than 10 in 1 ml, the number of Vibrio cholerae is less than 1 cfu in 100 ml, the number of E. coli is less than 250 cfu in 100 ml, and the number of enterococci is 100 cfu in 100 ml Is less than

As ballast water treatment technology, a filtration device that filters seawater to trap aquatic organisms, a bactericide supply device that supplies bactericides that kill bacteria in the seawater into the filtered seawater, and a bactericide supply A large amount of Venturi pipes that receive the supplied filtered water to generate cavitation in the filtered water to diffuse the disinfectant in the filtered water and damage or kill aquatic organisms in the filtered water, An apparatus in which a plurality of venturi pipes are arranged in parallel to treat ballast water has been proposed (for example, see Patent Document 1).
Patent Document 1 describes that a neutralizing agent is supplied to seawater to which a bactericidal agent is added to neutralize the bactericidal agent remaining in the seawater and then detoxify before discharging to the sea. .
JP 2007-105666 A

In the ballast water treatment apparatus described in Patent Document 1, as described above, a sterilizing agent supply apparatus for supplying the sterilizing agent into the filtered seawater, and the filtered water supplied with the sterilizing agent are supplied. And a venturi pipe 51 for generating cavitation in the filtered water (see FIG. 4).
The sterilizing agent supply device supplies the sterilizing agent to a drug injection unit 53 provided on the upstream side of the venturi 51 by a pump (not shown).
However, since the drug injection part 53 is provided as a separate device at a site away from the Venturi tube 51, the device becomes large, requires a large space for installation, and a ship that cannot secure a sufficient installation space for the equipment. There is a problem that trouble may occur when mounting.

  Patent Document 1 describes that a disinfectant decomposer is supplied to ballast water in order to detoxify the remaining disinfectant. However, when a disinfectant decomposer is supplied, the disinfectant decomposer is ballasted. There is also a problem that the amount of dissolved oxygen decreases by reacting with oxygen in the water, and draining such ballast water adversely affects the surrounding environment.

The present invention has been made to solve such a problem, and an object of the present invention is to provide a technique capable of realizing a ballast water treatment apparatus that does not require a large space as an installation place.
It also aims to provide technology that prevents adverse effects on the surrounding environment when ballast water is discharged.

(1) A venturi tube device according to the present invention is provided with a plurality of frustoconical or bowl-shaped openings, each of which includes a disk-shaped throttle member that serves as a throttle portion in the venturi pipe, and a plurality of columnar openings. A disc-shaped throat member provided with the opening serving as a throat portion in the venturi tube, and a diffuser member having a plurality of columnar openings, the inner surface of which is processed into a diffuser shape are accommodated, and the diffuser member is a venturi A plurality of venturi pipes formed by joining three members in series with a cylindrical diffuser member housing member serving as a diffuser portion in the pipe and communicating openings formed in the respective members are flow paths for the treated water are arranged in parallel, the inlet is provided in the throat portion of the plurality of venturi tubes and dispensing the drug to the plurality of venturi supplied with drugs The distribution pipe, is characterized in that the branches from 該分 pipe and an injection branch pipe connected to the inlet of said plurality of venturi tubes.

The venturi pipe device of the present invention can treat a large amount of treated water by adopting a structure in which a plurality of venturi pipes are arranged in parallel.
Further, since the drug is directly supplied to the throat of the venturi tube, the structure is compact and the installation place can be reduced as compared with the structure in which the drug is supplied upstream of the venturi tube.
Furthermore, since the drug is supplied to the throat of the venturi tube, the drug is self-primed by the ejector action of the venturi tube, the capacity of the supply pump for supplying the drug can be reduced, and the apparatus related to drug supply can be reduced in size and saved. Effective for space, energy saving and cost reduction.

(2) In the above-described (1), all or part of the plurality of venturi pipes are arranged concentrically and connected to the inlet of the venturi pipe arranged concentrically. The length is set to the same length.

  With the above configuration, the self-priming force of each Venturi tube arranged concentrically becomes equal, and an equal amount of medicine is supplied from the distribution pipe to each Venturi pipe, so that effective medicine supply can be realized.

(3) A ballast water treatment apparatus according to the present invention is a ballast water treatment apparatus provided with the venturi pipe device according to (1) or (2) above, and is provided on the upstream side of the venturi pipe device to supply seawater. A filtration device for filtering and capturing aquatic organisms; a bactericide supply pipe connected to a distribution pipe for supplying a bactericide to the distribution pipe; a bactericide storage tank for storing a bactericide supplied to the bactericide supply pipe; , Provided.

By providing the above-described configuration, aquatic organisms and bacteria in seawater can be killed or removed, and ballast water that does not contain pests can be supplied to the ship.
The main function of each component is as follows, and the function of each component acts organically to enhance the killing effect of aquatic organisms in seawater.
The filtration device captures and removes relatively large aquatic organisms such as zooplankton in seawater, and the germicide is supplied from the germicide storage tank to the venturi tube device through the germicide supply pipe, killing bacteria in the seawater. Perish.
In addition, cavitation is generated in the filtered water supplied with the bactericide by the Venturi tube to damage or kill relatively small aquatic organisms such as phytoplankton, and further, the sterilizer is put into the filtered water by cavitation. It diffuses rapidly and promotes the bactericidal action of bacteria by bactericides. In this way, diffusing action of cavitation promotes mixing of bactericides into seawater, so the amount of bactericides supplied can be reduced compared to the case of just injecting bactericides, and the impact on the environment can be reduced. Furthermore, it is possible to eliminate or reduce the supply of the disinfectant disinfectant for detoxifying the disinfectant.

(4) Further, in the above (3), an air supply pipe that communicates with the distribution pipe and supplies air to the distribution pipe, and an air supply device that supplies air to the air supply pipe are provided. It is characterized by that.

Dissolved oxygen in seawater where oxygen is consumed and reduced by supplying disinfectant by supplying disinfectant by decomposing the disinfectant by supplying disinfectant to seawater where the disinfectant remains. Restore the amount. Since air is supplied to the throat of the venturi tube, a large amount of air can be brought into contact with a large amount of seawater in a short time, and cavitation occurs in the diffuser portion 28 of the venturi tube, resulting in a large disturbance in the flow of seawater. Therefore, since the injected bubbles are miniaturized and the contact area of the gas and liquid is greatly increased, the air can be very efficiently dissolved in the seawater. For this reason, the amount of dissolved oxygen in seawater can be easily and quickly recovered to a level that does not adversely affect the surrounding environment while flowing through the pipeline.
Moreover, since it is not necessary to provide an aeration apparatus separately, the whole apparatus can be made compact.
Furthermore, since the injection mechanism for supplying the sterilizing agent and the injection mechanism for supplying air are used in combination, the ballast water treatment apparatus can be made more compact.

  The air supply pipe connected to the distribution pipe may be directly connected to the distribution pipe, or may be connected to the disinfectant supply pipe and connected to the distribution pipe via the disinfectant supply pipe. In the case where the air supply pipe is connected to the sterilizing agent supply pipe, a switching valve for switching between when the sterilizing agent is supplied to the sterilizing agent supply pipe and when air is supplied is provided. Good.

In the venturi tube device according to the present invention, since the drug injection mechanism is provided in the venturi tube, the device becomes compact. By using this as a ballast water treatment device, the ballast water treatment does not require a large space as an installation place. A device can be realized.
Moreover, according to the ballast water treatment apparatus according to the present invention, it is possible to provide a ballast water treatment apparatus that can efficiently process a large amount of ballast water and has a small installation location.
Moreover, when discharging ballast water, it is possible to prevent seawater having a reduced dissolved oxygen amount from being discharged and adversely affecting the surrounding environment.

[Embodiment 1]
Hereinafter, an example of the best mode of the ballast water treatment apparatus according to the present invention will be specifically described with reference to the drawings.
FIG. 1 is a diagram showing a configuration of a ballast water treatment apparatus according to an embodiment of the present invention. The ballast water treatment apparatus shown in FIG. 1 takes in seawater, performs a biocidal process on the taken-up seawater, and sends it to the ballast tank, and detoxifies the seawater in the ballast tank when drained into the sea. Has both functions.

As shown in FIG. 1, the ballast water treatment apparatus according to the present embodiment is a seawater intake line 1 for taking seawater into a ship, and a coarse filtration apparatus that removes coarse substances in seawater taken by the seawater intake line 1. 2. A pump 3 having a function of taking in seawater and a function of sending ballast water from a ballast tank 9 described later to the sea; a filtration apparatus 4 for removing planktons present in seawater from which coarse substances have been removed by the coarse filtration apparatus 2; , A bactericide supply device 5 that supplies a bactericide that kills bacteria to the seawater filtered by the filtration device 4, a venturi tube that receives the supply of filtered water filtered by the filtration device 4 and generates cavitation in the filtered water Device 6, Disinfectant supply device 7 for supplying disinfectant disinfectant to seawater added with disinfectant and stored in ballast tank 9, Ballast with disinfectant disinfectant added An air supply device 8 for supplying air to water, a treated water supply line 10 for supplying treated water to which a sterilizing agent is added to a ballast tank 9 described later, and a ballast tank for storing treated water supplied from the treated water supply line 10 9, a first ballast water supply line 11 for supplying ballast water in the ballast tank 9 to the disinfectant disinfectant supply device 7; A ballast water drain line 13 for draining ballast water supplied with air by the venturi pipe device 6 and the air supply device 8 to the sea.
Hereinafter, each device will be described in more detail.

1. Coarse filter device Coarse filter device 2 is comprised of a large amount of various contaminants and aquatic organisms contained in seawater taken from a sea chest (seawater inlet) provided on the side of the ship through seawater intake line 1 by pump 3. This is for removing coarse materials of about 10 mm or more.
The coarse filtration device 2 includes a cylindrical strainer (strainer) having a hole of about 10 mm, a hydrocyclone that separates coarse matter in the water flow by the difference in specific gravity, a device that captures and collects the coarse matter with a rotating screen, and the like. Can be used.

2. Filtration device The filtration device 4 removes planktons present in the seawater from which coarse substances have been removed by the coarse filtration device 2, and has a mesh size of 10 to 200 μm.
The reason why the mesh opening is 10 to 200 μm is to reduce the frequency of backwashing and shorten the ballast water treatment time in the port of call while keeping the capture rate of zooplankton and phytoplankton at a certain level. In other words, if the mesh size is larger than 200 μm, the capture rate of zooplankton and phytoplankton is remarkably reduced. If the mesh size is smaller than 10 μm, the frequency of backwashing increases and the ballast water treatment time at the port of call becomes longer. Therefore, it is not preferable. In particular, it is preferable to use one having an opening of about 50 μm because the capture rate and the backwashing frequency can be set optimally.

As a specific example of the filtration device 4, it is preferable to use a notch wire filter or a wedge wire filter.
A notch wire filter is a cylindrical element that is formed by winding a wire with a notch (protrusion) around a frame body. The casing is provided with valves and pipes for water supply and reverse cleaning. It is a thing. The cylindrical element keeps the distance between the wires at 10 to 200 μm which is the size of the filtration passage by the notch.
A specific example of this notch wire filter is a notch wire filter manufactured by Kanagawa Kikai Kogyo.
A wedge wire filter is a cylinder-shaped element formed by winding a wire with a triangular cross section around a frame body, and this casing is provided with valves and pipes for water supply and reverse cleaning. is there. In the cylindrical element, the distance between the wires is adjusted to be 10 to 200 μm which is the size of the filtration passage.
As a specific example of this wedge wire filter, there is a wedge wire filter manufactured by Toyo Screen Industries.

Another preferred specific example of the filtration device 4 is a laminated disk type filter. A laminated disk type filter is a donut-shaped disk having a plurality of oblique grooves formed on both sides thereof, which is laminated by pressing in the axial direction, and is formed by a gap between adjacent disks. The aquatic organisms are filtered through the water. In the laminated disk type filter, the opening can be made 10 to 200 μm by appropriately adjusting the size of the oblique groove.
In the laminated disk type filter, the disk pressure is released during backwashing to increase the gap and remove the filtration residue.
A specific example of this laminated disk type filter is Spin Klin Filter Systems manufactured by Arkal Filtration Systems.

3. Disinfectant supply device The disinfectant supply device 5 supplies a disinfectant that kills bacteria to the seawater filtered by the filtration device 4. FIG. 2 is an explanatory diagram of the configuration of the sterilizing agent supply device 5, the venturi tube device 6 and the air supply device 8. FIG. 2 shows an axial section of the flow path of the venturi tube device 6. In FIG. 3 is a cross-sectional view taken along line AA in FIG.
The sterilizing agent supply device 5 includes a sterilizing agent storage tank 15 for storing the sterilizing agent, and a sterilizing agent stored in the sterilizing agent storage tank 15 with one end connected to the sterilizing agent storing tank 15 and the other end connected to a distribution pipe 35 described later. The sterilizing agent supply pipe 17 that supplies the sterilizing agent to the distribution pipe 35, the sterilizing agent supply pump 19 that is provided in the sterilizing agent supply pipe 17 and sends out the sterilizing agent, and the sterilizing agent supply pipe 17 that is provided with the sterilizing agent supply amount And an adjusting valve 20 for adjusting.

As the disinfectant, chlorine, chlorine dioxide, sodium hypochlorite, hydrogen peroxide, ozone, peracetic acid or a mixture of two or more of these can be used, but other disinfectants can also be used. .
The supply amount of the bactericidal agent is adjusted on the downstream side of the venturi tube device 6 so that the bactericidal agent concentration in the seawater is sufficient to kill the bacteria. Adjustment of the supply amount of the bactericide is performed by measuring the bactericide concentration in seawater with a bactericide concentration meter (not shown) on the downstream side of the venturi tube device 6 and killing the measured bactericide concentration and bacteria. The necessary bactericidal supply amount is calculated by comparing the concentration of the bactericidal agent with a sufficient amount, and the output of the bactericidal agent supply pump 19 or the opening of the adjusting valve 20 is adjusted so that the calculated bactericidal agent supply amount is obtained. By doing.

4). Venturi tube device Venturi tube device 6 is for introducing seawater that has passed through filtration device 4 to damage or kill organisms that have passed through filtration device 4.
As shown in FIGS. 2 and 3, the venturi pipe device 6 of the present embodiment is formed by a plurality of venturi pipes 23 formed in parallel in a cylindrical protective outer cylinder 21. Although the aspect of the parallel arrangement of the venturi tubes 23 is not particularly limited, in this example, as shown in FIGS. 2 and 3, one venturi tube 23 is disposed at the center of the flow path, and the venturi tubes 23 are arranged on a concentric circle around the center. In this embodiment, a single venturi tube 23 is arranged.

The nine venturi tubes 23 include a disk-shaped throttle member 25 provided with nine truncated cone-shaped or bowl-shaped openings and a disk-shaped throat member 27 provided with nine cylindrical openings. And a cylindrical diffuser member housing member 29 provided with nine columnar openings are joined in series to communicate the openings formed in each member.
That is, the frustoconical or bowl-shaped opening formed in the throttle member 25 becomes the throttle part 22 in the venturi tube 23, and the columnar opening formed in the throat member 27 becomes the throat part 24 in the venturi pipe 23. A diffuser member 26 whose inner surface is processed into a diffuser shape is accommodated in a cylindrical opening formed in the accommodating member 29 to become a diffuser portion 28 in the venturi tube 23, and the throttle portion 22 in which the cross-sectional area of the pipe gradually decreases as a whole. The venturi tube 23 is provided with the throat portion 24, which is the minimum cross-sectional area portion, and the diffuser portion 28 in which the pipe cross-sectional area gradually increases.
The throat portion 24 is provided with an injection port 30 for injecting a sterilizing agent into the throat portion 24. The injection port 30 is formed by forming pores in the throat member 27 that allow communication between the peripheral wall of the cylindrical opening that forms the throat portion 24 and the outer peripheral portion of the throat member 27.

The throttle portion 22 and the throat portion 24 in the venturi tube device 6 are made of a plastic material having high chemical resistance (for example, a hard vinyl chloride resin with respect to sodium hypochlorite), and the diffuser member 26 has cavitation bubbles. It is desirable to form a metal material (for example, SUS316L, Ti, etc.) having high durability against erosion due to the collapse of the material.
Moreover, it is desirable that the diffuser member housing member 29 be formed of a hard vinyl chloride resin.

  The protective outer cylinder 21 in the venturi pipe device 6 is made of seawater piping material (for example, SUS316L, galvanized steel pipe), and flanges made of seawater piping material (for example, SUS316L, galvanized steel) at both ends of the protective outer cylinder 21. 31 is formed. The venturi pipe device 6 is connected to the upstream and downstream pipes 33 a and 33 b by the flange 31.

  A distribution pipe 35 is installed at a portion of the protective outer cylinder 21 corresponding to the throat portion 24 of the venturi pipe 23 so as to wrap around the outer periphery of the protective outer cylinder 21. The distribution pipe 35 is provided with an injection branch pipe 37 that connects the distribution pipe 35 and the injection port 30 of each venturi pipe 23.

In each venturi tube 23, cavitation bubbles are generated due to a rapid decrease in static pressure accompanying a rapid increase in flow velocity at the throat 24, and the cavitation bubbles grown due to a pressure increase due to a decrease in flow velocity at the diffuser portion 28 are collapsed. . Aquatic organisms in seawater are damaged or destroyed and killed by the action of OH radicals with impact pressure, shearing force, high temperature, strong oxidizing power due to the collapse of cavitation bubbles.
According to the cavitation of the Venturi tube 23, the outer shell of a protozoan or zooplankton having a relatively hard shell can be destroyed and killed.

  In the venturi tube device 6 configured as described above, cavitation is generated by each of the venturi tubes 23 to damage or kill relatively small aquatic organisms such as phytoplankton, and the venturi tube is formed by cavitation. 23 is rapidly diffused in seawater to promote the bactericidal action of bacteria by the bactericidal agent. In this way, mixing of fungicides into seawater is promoted by the diffusion action of cavitation, so that the amount of fungicides supplied can be reduced and the impact on the environment can be reduced compared to the case of simply injecting fungicides. The supply of the disinfectant disinfectant for detoxifying the disinfectant can be eliminated or reduced.

5. Disinfectant decomposer supply device The disinfectant decomposer supply device 7 detoxifies the disinfectant by supplying the disinfectant decomposer to the seawater to which the disinfectant is added to decompose the disinfectant remaining in the seawater.
It is desirable to use sodium thiosulfate, sodium sulfite, or sodium bisulfite as the disinfectant decomposing agent to be supplied from the viewpoint of price and ease of handling, but it is not particularly limited thereto.

  When the seawater is drained from the ballast tank 9 to the sea, the concentration of the residual sterilizing agent in the seawater is measured, and the sterilizing agent decomposing agent is injected more than the equivalent amount or equivalent amount necessary for decomposing the sterilizing agent. Seawater is fed from the ballast tank 9 by the pump 3 to the first ballast water supply line 11, a disinfectant is injected into the pipe on the upstream side of the pump 3, and sufficiently diffused by the stirring action of the pump 3. Let the disinfectant break down.

6). Air supply device The air supply device 8 supplies air to the seawater supplied with the bactericide decomposing agent in order to recover the amount of dissolved oxygen in the seawater in which the oxygen is consumed by the disinfectant decomposing agent and the dissolved oxygen concentration is reduced. It is a device.
As shown in FIG. 2, the air supply device 8 includes an air supply pipe 43 connected to the sterilizing agent supply pipe 17 via the switching valve 41, a blower 45 (or an air pump) that sends air to the air supply pipe 43, And an air amount adjusting valve 47 that adjusts the amount of air that is provided and sent to the air supply pipe 43.

  In the air supply device 8 configured as described above, the air sent from the blower 45 to the air supply pipe 43 is sent to the sterilizing agent supply pipe 17 via the switching valve 41, and the distribution pipe 35, the injection branch pipe 37 is supplied to the inlet 30 of the throat 24 of each Venturi tube 23. Thus, the venturi tube device 6 is used for both the supply of the bactericide and the supply of air.

  In the air supply device 8 of the present embodiment, since air is supplied to the throat portion 24 of the venturi tube 23, a large amount of air can be brought into contact with a large amount of seawater in a short time. Further, since cavitation occurs in the diffuser portion 28 of the venturi pipe 23 and large-scale turbulence occurs in the flow of seawater, the injected bubbles are miniaturized and the contact area of the gas and liquid is greatly increased. Because of these effects, air can be dissolved into seawater very efficiently, and the amount of dissolved oxygen in seawater can be easily and quickly reduced to a level that does not adversely affect the surrounding environment while flowing through the pipeline. I can recover.

  In addition, the dissolved oxygen concentration is measured by a dissolved oxygen concentration meter (not shown) on the downstream side of the venturi pipe device 6, and the air supply amount is adjusted so that the dissolved oxygen amount does not adversely affect the surrounding environment.

The operation of the present embodiment configured as described above will be described.
<Biological killing process during water intake>
First, the biological killing process in seawater performed when seawater is taken from the sea and supplied to the ballast tank 9 will be described. (See Figure 1)
The switching valve 41 is operated so that the sterilizing agent can be supplied to the venturi pipe device 6.
In this state, the pump 3 is operated. Thereby, seawater is taken into the ship from the seawater intake line 1. At that time, the coarse filter 2 removes large and small contaminants and aquatic organisms of about 10 mm or more from seawater.
Seawater from which coarse substances have been removed is supplied to the filtration device 4, and zooplankton, phytoplankton, and the like having a size corresponding to the opening of the filtration device 4 are removed.
Aquatic organisms and the like captured by the coarse filtration device 2 and the filtration device 4 are washed away by backwashing the filters of the coarse filtration device 2 and the filtration device 4 and returned to the sea. Even if it is returned to the sea, it is the same sea area, so there is no adverse effect on the ecosystem. That is, in this example, since the treatment is performed when the ballast water is loaded, the backwash water of the coarse filtration device 2 and the filtration device 4 can be discharged as it is.

Seawater filtered by the filtration device 4 is supplied to the venturi tube device 6, and a sterilizer is supplied to the throat portion 24 of each venturi tube 23 by the disinfectant supply device 5.
By supplying the disinfectant to the throat portion 24 of the venturi tube 23, the diffusion of the disinfectant into the seawater is promoted by cavitation in the venturi tube device 6, and the killing effect of the bacteria is enhanced. Further, in the venturi tube device 6, cavitation bubbles are generated and grown in the seawater introduced into the venturi tube 23 by the above-described mechanism, and further, the grown cavitation bubbles rapidly collapse, so that the aquatic organisms in the seawater It exerts the action of impact pressure, shear force, high temperature, strong oxidative OH radical, damages or destroys aquatic organisms and kills them.

Seawater that has been subjected to biocidal treatment by the venturi pipe device 6 is supplied to the ballast tank 9 through the treated water supply line 10 and stored.
The concentration of the bactericidal agent in the seawater is measured downstream of the venturi pipe device 6, and the output of the bactericidal agent supply pump 19 or the opening of the regulating valve 20 is set so that the bactericidal concentration is sufficient to kill bacteria. To adjust the amount of fungicide supplied.
In addition, when seawater is stored in the ballast tank 9, it is preferable that the disinfectant supplied from the disinfectant supply device 5 remains. This is because even if harmful microorganisms remain in the ballast tank 9, these microorganisms can be killed by the effect of the remaining fungicide. The concentration at which the disinfectant remains is appropriately determined according to the type and concentration of the disinfectant, and the material of the ballast tank 9 and the type of coating, and the supply amount of the disinfectant is adjusted based on this determination.

<Disinfecting disinfectant and recovering dissolved oxygen during drainage to the sea>
Next, the disinfectant decomposition process and the dissolved oxygen recovery process performed when the seawater in which the disinfectant remains from the ballast tank 9 is discharged to the sea will be described.
When this processing is performed, the switching valve 41 is switched so that air is injected into the venturi tube device 6 which is also used as a sterilizing agent.
Seawater stored in the ballast tank 9 is supplied to the first ballast water supply line 11 by the pump 3, and the disinfectant in the pipe upstream of the first ballast water supply line 11 by the disinfectant decomposer supply device 7. Inject degradation agent. As a result, the disinfectant decomposition agent is sufficiently diffused in the seawater by the stirring action of the pump 3 to decompose the disinfectant in the pipe. Measure the residual fungicide concentration in the sea water and inject an amount of fungicide decomposer equal to or greater than the equivalent required to decompose the fungicide.

  The ballast water to which the disinfectant is added is supplied to the venturi pipe device 6 through the second ballast water supply line 12, and further air is supplied to the throat portion 24 of the venturi pipe 23 by the air supply device 8. The ballast water supplied with air is drained to the sea through the ballast water drain line 13.

As a result, air is injected into the throat portion 24 of the venturi tube 23, and the above-described action allows the air to dissolve into the seawater very efficiently, so that dissolved oxygen in the seawater flows through the pipeline. The amount can be easily and quickly restored to a level that does not adversely affect the surrounding environment.
The amount of air supply is adjusted so that the amount of dissolved oxygen is measured on the downstream side of the venturi pipe device 6 and the amount of dissolved oxygen does not adversely affect the surrounding environment.

  The above example is a case where processing is performed when seawater is loaded into the ballast tank 9, but processing is not performed when seawater is loaded into the ballast tank 9, and processing may be performed when seawater is discharged from the ballast tank 9. is there. In this case, untreated ballast water is supplied from the ballast tank 9 to the filtration device 4, and thereafter the same biological killing process as that described above is performed, and the disinfectant discharged from the venturi tube device 6 remains in the seawater. It is only necessary to supply a disinfectant-decomposing agent and further supply air to perform disinfecting agent decomposition treatment and dissolved oxygen recovery treatment.

As described above, in the present embodiment, zooplankton and phytoplankton having a size of 10 to 200 μm or more are removed by the filtration device 4 and the bactericide is supplied to the throat portion 24 of the venturi tube 23 of the venturi tube device 6. As a result, the plankton and bacteria are killed, so that it is possible to reliably and inexpensively treat ballast water satisfying the ballast water standards set by IMO regardless of the water quality.
Further, since the mechanism for injecting the bactericide into the venturi tube device 6 is incorporated, the ballast water treatment device can be made compact and the installation location can be reduced. Furthermore, since the air supply device 8 for supplying air to the throat portion 24 of the venturi tube 23 is provided together with the disinfectant decomposition agent supply device 7, the remaining disinfectant can be rendered harmless, and the dissolved oxygen amount in the seawater is brought into the surrounding environment. It can be easily and quickly recovered to a level that does not have an adverse effect. In addition, since the ventilator device 6 is used as both the sterilizing agent injection mechanism and the air injection mechanism, the entire ballast water treatment device can be made more compact and the installation location can be reduced.

  The mechanism for injecting a bactericidal agent or air into the throat 24 of the venturi tube 23 in the venturi tube device 6 of the present invention is a chemical that renders harmful substances harmless to a large amount of liquid containing harmful substances in addition to the ballast water treatment device. Can be diverted to a device for supplying and diffusing air, an aeration device for supplying a gas such as air to a large amount of liquid, a device for refining bubbles, and the like.

It is explanatory drawing of the ballast water treatment apparatus which is one embodiment of this invention. It is explanatory drawing of the disinfectant supply apparatus and venturi pipe apparatus which concern on one embodiment of this invention. It is explanatory drawing of the AA cross section of FIG. It is explanatory drawing of the conventional venturi pipe.

Explanation of symbols

  2 Coarse filtration device, 3 pump, 4 filtration device, 5 disinfectant supply device, 6 venturi tube device, 7 disinfectant decomposition agent supply device, 8 air supply device, 9 ballast tank, 15 disinfectant storage tank, 23 venturi tube, 35 Distribution pipe, 37 injection branch pipe.

Claims (4)

A disc-shaped throttle member in which a plurality of frustoconical or bowl-shaped openings are provided, and the openings serve as throttle parts in the venturi tube, and a plurality of columnar openings are provided, and the openings serve as throat parts in the venturi pipe. A disk-shaped throat member and a cylindrical diffuser member housing a plurality of columnar openings in which a diffuser member whose inner surface is processed into a diffuser shape is housed and the diffuser member serves as a diffuser portion in a venturi tube A plurality of venturi pipes formed by joining three members in series with each other and communicating the openings formed in each member are arranged in parallel in the flow path of the treated water ,
Inlet is provided in the throat portion of the plurality of venturi tubes,
A distribution pipe for receiving the supply of the drug and distributing the drug to the plurality of venturi pipes; and an injection branch pipe branched from the distribution pipe and connected to the inlets of the plurality of venturi pipes. Venturi tube device.   All or some of the plurality of venturi pipes are arranged concentrically, and the lengths of the injection branch pipes connected to the inlets of the venturi pipes arranged concentrically are set to the same length. The venturi device according to claim 1.   A ballast water treatment apparatus comprising the venturi pipe device according to claim 1, wherein the ballast water treatment apparatus is provided upstream of the venturi pipe device and filters the seawater to capture aquatic organisms, and is connected to a distribution pipe A ballast water treatment apparatus comprising: a sterilizing agent supply pipe that supplies the sterilizing agent to the distribution pipe; and a sterilizing agent storage tank that stores the sterilizing agent supplied to the sterilizing agent supply pipe. The ballast water treatment according to claim 3, further comprising: an air supply pipe that communicates with the distribution pipe and supplies air to the distribution pipe; and an air supply device that supplies air to the air supply pipe. apparatus.

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