JP2011092821A - Method and system for suppressing adhesion of marine organism, and method for inhibiting swimming of marine organism - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method and system for effectively suppressing the adhesion of marine organisms to a heat exchange water flow passage by injecting a chlorine-based agent and CO<SB>2</SB>microbubbles into the water for heat exchange when heat is exchanged with a heat exchange object equipment using the water containing marine organisms. <P>SOLUTION: The method for suppressing the adhesion of marine organisms to the heat exchange water flow passage includes the steps of: supplying the water containing marine organisms to the heat exchange object equipment; exchanging heat with the heat exchange object equipment using the supplied water; discharging the water after the heat exchange with the heat exchange object equipment from the heat exchange object equipment; and injecting the chlorine-based agent and CO<SB>2</SB>microbubbles into at least one of the water containing marine organisms, the supplied water and the water after the heat exchange with the heat exchange object equipment. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

The present invention, a chlorine-based agent and CO ₂ microbubbles and suppressing method and system of attachment of marine organisms to the heat exchanger water flow path with, and, of marine organisms using the chlorine-based agent and CO ₂ microbubbles The present invention relates to a system that inhibits swimming.

  In power plants such as thermal power plants and nuclear power plants that use seawater as cooling water, intake water that takes seawater from the sea and supplies it to the condenser, and discharges seawater that passes through the condenser to the sea Marine organisms such as barnacles and mussels are likely to adhere to the inside of the spillway. When the adhesion amount of marine organisms increases, there is a risk of causing problems such as blocking the cooling water flow path and reducing cooling performance. Therefore, conventionally, for example, as disclosed in Patent Documents 1 to 5, by injecting a chlorine-based chemical such as sodium hypochlorite solution or chlorine dioxide into the cooling water, Inhibition of adhesion is performed.

JP-A-7-265867 JP-A-11-37666 JP-A-2005-144212 JP 2005-144213 A JP 2005-244214 A

However, as mentioned above, seawater after being used as cooling water in power plants is released into the sea, and chlorinated chemicals injected into the cooling water are also released into the sea. Therefore, the chlorine concentration (residual chlorine concentration) contained in the cooling water released to the sea is required to be below a certain agreed value. Therefore, the amount of chlorinated chemicals for removing marine organisms must also be limited so that the above requirements can be satisfied, and it has not been easy to obtain a sufficient removal effect within the limits. .
The present invention has been made in view of the above points, and in exchanging heat with the facility subject to heat exchange using water containing marine organisms, the chlorine-based chemical and the CO ₂ microbubbles are used for heat exchange. It is an object of the present invention to provide a method and system for effectively suppressing adhesion of marine organisms to a heat exchange water flow path by injecting into water.

In order to solve the above-mentioned problem, a method for suppressing the attachment of marine organisms to a heat exchange water flow path according to the present invention includes supplying water containing marine organisms to a heat exchange target facility, Using water, exchanging heat with the heat exchange target equipment, releasing the water after heat exchange with the heat exchange target equipment from the heat exchange target equipment, water containing the marine organisms, A step of injecting chlorine-based chemicals and CO ₂ microbubbles into any one or more of the supplied water and the heat exchange target equipment and the water after heat exchange.

According to the present invention, marine organisms contained in the injected water adhere to the heat exchange water flow path by combining the chlorine-based chemical and the CO ₂ microbubbles and injecting them into the water for heat exchange. It can be effectively suppressed. Further, by using a combination of a chlorine-based agent and CO ₂ microbubbles are released from the heat exchange relevant equipment since it is possible to reduce the amount of chlorine-based agent than when using only chlorine agent Further, it is possible to more efficiently prevent marine organisms from adhering to the heat exchange water flow path while reducing the chlorine concentration of the water after heat exchange with the heat exchange target equipment.

Here, the heat exchange target equipment is not particularly limited, but may be, for example, a condenser or an LNG (liquefied natural gas) vaporizer provided in a power plant such as a thermal power plant.
Further, where a rather CO ₂ microbubbles, the particle size of the event refers bubbles of carbon dioxide 5 m to 50 m. The method for generating CO ₂ microbubbles is not particularly limited. For example, it is generated by using an ejector type, a venturi type, a line mixer type, a pressure dissolution type, a swirl type, or a cavitation type microbubble generator. Can be made.

  The chlorinated drug is not particularly limited as long as it can suppress the attachment of marine organisms to the heat exchange water flow path, and may be, for example, sodium hypochlorite, chlorine dioxide, or chlorine.

Even small amount of injection amount of the chlorine-based agent and CO ₂ microbubbles in water for heat exchange, because it can effectively prevent the marine organisms from adhering to the heat exchange water channel, CO ₂ microbubbles It is preferable that the pH of the water into which is injected is 7.9 or more.

  Although the kind of marine organism is not specifically limited, For example, shellfishes, such as barnacles and mussels, may be sufficient, and among these, it is more preferable that it is a larva of barnacles.

  Although the kind of water containing a marine organism is not specifically limited, For example, seawater may be sufficient.

The method for inhibiting swimming of marine organisms according to the present invention includes a step of injecting a chlorine-based drug and CO ₂ microbubbles into water containing the marine organisms.

According to the present invention, by injecting a chlorinated drug and CO ₂ microbubbles into water containing marine organisms, marine organisms contained in the injected water can be efficiently paralyzed. As a result, the swimming of marine life can be effectively inhibited.
If the swimming of marine organisms is inhibited, for example, marine organisms can be prevented from adhering to a water container containing marine organisms, and marine organisms can be easily recovered and removed from the water.

  The chlorinated drug is not particularly limited as long as it can inhibit the swimming of marine organisms. For example, it may be sodium hypochlorite, chlorine dioxide, or chlorine.

Even small amount of injection amount of the chlorine-based agent and CO ₂ microbubbles in water containing marine life, since it can be effectively suppressed swimming marine life, pH of the water injected with CO ₂ microbubbles It is preferable that it is 7.9 or more.

On the other hand, the system for suppressing the attachment of marine organisms to the heat exchange water flow path according to the present invention uses a supply device for supplying marine organism-containing water to the heat exchange target equipment and the supplied water. A heat exchanger for exchanging heat with the heat exchange target equipment, a discharge device for discharging the heat exchange target equipment and water after heat exchange from the heat exchange target equipment, and the marine organisms Water containing the marine organisms, a chemical injection device for injecting a chlorine-based chemical into one or more of the water to be supplied, the supplied water, and the water after heat exchange with the heat exchange target facility And a microbubble injection device for injecting CO ₂ microbubbles into any one or more of the supplied water and the heat exchange target equipment and the water after heat exchange.

  The chlorinated chemical | medical agent using this system will not be specifically limited if the adhesion | attachment of the marine organism to a heat exchange water flow path can be suppressed, For example, sodium hypochlorite, chlorine dioxide, or chlorine may be sufficient.

According to the present invention, in exchanging heat with the facility for heat exchange using water containing marine organisms, the chlorine-based chemical and the CO ₂ microbubble are effectively injected into the water for heat exchange. A method and system for suppressing the attachment of marine organisms to the heat exchange water flow path can be provided.

It is a figure which shows the whole structure of the system which suppresses adhesion of the marine organism to the heat exchange water flow path demonstrated as one Embodiment of this invention. It is a figure which shows typically the heat exchange water flow path which consists of a water intake channel, a water discharge channel, an LNG vaporizer flow path, and a condenser flow path in one Embodiment of this invention. It is a figure which shows the detailed structure of the chemical injection device in one Embodiment of this invention. It is a figure which shows the structural example of the chemical injection port which the chemical injection tube provides in one Embodiment of this invention. It is a figure which shows another structural example of the chemical | medical agent injection port which a chemical | medical agent injection tube provides in one Embodiment of this invention. In an embodiment of the present invention, it is a diagram illustrating a detailed configuration of a CO ₂ microbubble infusion device.

Hereinafter, embodiments of the present invention completed based on the above knowledge will be described in detail with reference to the accompanying drawings. The objects, features, advantages, and ideas of the present invention will be apparent to those skilled in the art from the description of the present specification, and those skilled in the art can easily reproduce the present invention from the description of the present specification. it can. The embodiments and specific examples of the invention described below show preferred embodiments of the present invention and are shown for illustration or explanation, and the present invention is not limited to them. It is not limited. It will be apparent to those skilled in the art that various modifications and variations can be made based on the description of the present specification within the spirit and scope of the present invention disclosed herein.
== Configuration of system for suppressing adhesion of marine organisms to heat exchange water flow path according to the present invention ==
FIG. 1 is a diagram illustrating an overall configuration of a system that suppresses the attachment of marine organisms to a heat exchange water flow path, which will be described as an embodiment of the present invention. As shown in FIG. 1, a system (hereinafter simply referred to as “system”) 100 for suppressing the attachment of marine organisms to a heat exchange water flow path according to the present invention was constructed on a site facing the sea 2. A thermal power plant 10 is provided. The thermal power plant 10 includes a fuel storage facility 12, an LNG tank 14, a power generation facility 16, an LNG vaporizer 17, a water intake channel 20, a water discharge channel 22, and the like.

  The power generation facility 16 further includes condensers 18A and 18B. The condensers 18A and 18B are devices that are connected to a steam prime mover, condense the steam, create a high vacuum, and assist the expansion action of the steam. In order to cool and condense water vapor in the condensers 18A and 18B, the condensers 18A and 18B include condenser flow paths 29A and 29B as heat exchange water flow paths through which the cooling water passes. Note that, as the condensers 18A and 18B, surface condensers in which cooling water passes through the condenser flow paths 29A and 29B are illustrated, but the cooling water is directly introduced into the condenser, It may be a direct contact condenser that mixes steam with steam.

  The LNG vaporizer 17 is a device that vaporizes LNG by heat exchange. In order to heat and vaporize LNG in the LNG vaporizer 17, the LNG vaporizer 17 further includes an LNG vaporizer flow path 27 as a heat exchange water flow path through which water serving as a heating heat source passes.

  The intake channel 20 is a channel for supplying the water for heat exchange that has been taken into the heat exchange target facility. The intake channel 20 further includes an intake port 24 for taking water. The intake channel 20 takes in seawater containing marine organisms from the sea 2 through the intake port 24, and cools the condensers 18A and 18B, which are heat exchange target equipment, from the seawater thus taken. Supply to condenser channels 29A and 29B.

The water discharge path 22 is a flow path for discharging water after heat exchange with the heat exchange target equipment to the outside of the heat exchange target equipment. The water discharge channel 22 further includes a discharge port 26 for discharging the water after heat exchange to the sea. That is, the water discharge channel 22 discharges the seawater flowing through the condenser channels 29A and 29B heated by heat exchange with the condensers 18A and 18B to the sea through the discharge port 26.
In the present embodiment, a part of the water discharge channel 22 leads to the LNG vaporizer channel 27 in order to effectively use the seawater heated by the condensers 18A and 18B. Thereby, since the seawater heated by the condensers 18A and 18B is sent to the LNG vaporizer 17, the LNG vaporizer 17 is heated using the heat generated by the condensers 18A and 18B. be able to. Seawater flowing through the LNG vaporizer flow path 27 after heat exchange with the LNG vaporizer 17 joins the water discharge path 22. The water discharge channel 22 discharges the seawater flowing inside the merged LNG vaporizer flow channel 27 to the sea through the discharge port 26.

As described above, since the seawater flows through the intake channel 20, the discharge channel 22, the LNG vaporizer channel 27, and the condenser channels 29A and 29B, which are heat exchange channels, the inside of the heat exchange channel , It is easy for marine organisms such as shellfish to attach and propagate. If a large amount of marine organisms adhere to the heat exchange water flow path, the heat exchange function may be deteriorated because the flow path is blocked and a sufficient flow rate cannot be obtained.
In particular, with regard to the intake channel 20, the intake channel 20 is very far away from the land so that the low-temperature seawater can be taken in in order to efficiently cool the condensers 18 </ b> A and 18 </ b> B. It is long and susceptible to marine life. In addition, the LNG vaporizer flow path 27 is in a state in which marine organisms are likely to breed due to the flow of seawater heated by the condensers 18A and 18B, and further heat exchange with the LNG vaporizer 17 In order to improve the efficiency, the diameter of the flow path is smaller than that of the water discharge path 22, so that it is easily affected when marine organisms adhere.

Therefore, in the present embodiment, the water intake channel 20, the water discharge channel 22, and the LNG vaporizer channel 27 are injected by injecting chlorine-based chemicals and CO ₂ microbubbles into the seawater for heat exchange taken from the water intake 24. And, adhesion of marine organisms such as shellfish on the inner wall surfaces of the condenser flow paths 29A and 29B is suppressed. In addition, by injecting chlorinated chemicals and CO ₂ microbubbles into the seawater for heat exchange heated by the condensers 18A and 18B, shells, particularly on the inner wall surface of the LNG vaporizer channel 27, The adhesion of marine organisms such as is further suppressed.
In addition, the kind of chlorinated chemical | medical agent is not specifically limited, For example, sodium hypochlorite, chlorine dioxide, chlorine, etc. may be sufficient. The form of the chlorinated drug is not particularly limited. For example, if sodium hypochlorite is used, it is preferable to use a stable sodium hypochlorite aqueous solution. Further, chlorine or sodium hypochlorite obtained by electrolyzing seawater may be used.
The type of chlorinated chemical injected into the seawater taken from the intake port 24 and the type of chlorinated chemical injected into the seawater heated by the condensers 18A and 18B may be the same, and are toxic depending on the combination. It may be different as long as it does not produce a new material.

When injecting chlorine-based chemicals and CO ₂ microbubbles into seawater taken from the water intake 24, heat is generated by injecting chlorine-based chemicals and CO ₂ microbubbles at a location near the water intake 24 in the intake channel 20. Since it is possible to inhibit the swimming of marine organisms upstream of the exchange water flow path, it is possible to suppress the attachment of marine organisms to the entire heat exchange water flow path downstream from the injection site of the chlorinated drug and the CO ₂ microbubble. Can do.
In addition, when injecting chlorine-based chemicals into the seawater heated by the condensers 18A and 18B, by injecting chlorine-based chemicals and CO ₂ microbubbles at a location near the entrance of the LNG vaporizer flow path 27. The adhesion of marine organisms to the inner wall surface of the LNG vaporizer flow path 27 in which heat exchange with the LNG vaporizer 17 is performed can be suppressed, and the deterioration of the heat exchange function of the LNG vaporizer flow path 27 can be effectively prevented.

Note that it is not necessary to inject the chlorine-based chemical and the CO ₂ microbubble at the same location. For example, the chlorine-based chemical is injected at a location close to the intake port 24 of the intake channel 20, and enters the inlet of the LNG vaporizer channel 27. It may be at any different location in the heat exchange water flow path, such as injecting CO ₂ microbubbles at a nearby location. For example, a chlorinated chemical is injected at a location near the water intake 24 of the intake channel 20, and the CO ₂ micro is located downstream of the location where the chlorinated chemical is injected in the intake channel 20, and particularly upstream of the location where adhesion is desired to be prevented. If a bubble is injected, the adhesion of marine organisms to the heat exchange water flow path particularly at a location where it is desired to prevent the adhesion can be more effectively suppressed.

FIG. 2 is a diagram schematically showing a heat exchange water channel 80 including the intake channel 20, the discharge channel 22, the LNG vaporizer channel 27, and the condenser channels 29A and 29B.
As shown in FIG. 2, the intake channel 20 includes first seawater pumps 30 </ b> A and 30 </ b> B at a connection portion with the condensers 18 </ b> A and 18 </ b> B, that is, a connection portion with the condenser flow paths 29 </ b> A and 29 </ b> B, respectively. . The first seawater pumps 30 </ b> A and 30 </ b> B suck the seawater from the sea 2 into the intake channel 20 through the intake port 24.

The intake channel 20 is provided with a drug injection device 32A and a CO ₂ microbubble injection device 34A for injecting a chlorine-based drug, preferably at a location close to the water intake 24. Furthermore, LNG vaporizer channel 27 is preferably a position close to the entrance, that is, the connecting portion between the spillway 22, and a drug infusion device 32B and CO ₂ microbubble infusion device 34B.

  FIG. 3 shows a detailed configuration of the drug injection device 32A. As illustrated in FIG. 3, the drug injection device 32 </ b> A includes a drug supply tank 40 that supplies a chlorine-based drug and the chlorine-based drug supplied from the drug supply tank 40 to seawater for heat exchange that flows through the intake channel 20. And a drug injection tube 42 for injection.

The drug injection tube 42 includes a valve 44 that controls the supply amount of the chlorinated drug from the drug supply tank 40. By using this valve 44, in combination with CO ₂ microbubbles, an amount of a chlorine-based drug that can inhibit the migration of marine organisms and suppress the adhesion of marine organisms to the heat exchange water channel, It can inject | pour into the seawater for the heat exchange which flows through the intake channel 20 as needed.
It should be noted that the amount of the chlorinated drug that can inhibit the swimming of marine organisms and suppress the adhesion of marine organisms to the heat exchange water flow path in combination with the CO ₂ microbubbles has been tested in advance, for example. In addition, an observation device (not shown) may be provided at an arbitrary location in the heat exchange water flow path, and control may be performed while observing the state of marine life through the observation device.

The drug injection pipe 42 includes a drug injection port 43 for injecting the chlorine-based drug supplied from the drug supply tank 40 to the drug injection pipe 42 into seawater for heat exchange flowing through the intake channel 20. .
In the example shown in FIG. 3, the tip of the drug injection tube 42 on the side not connected to the drug supply tank 40 is bent toward the downstream side of the intake channel 20, and a drug injection port 43 is provided at the forefront thereof. . In this case, as shown in FIG. 4, the cross section of the distal end portion of the drug injection tube 42 on the side not connected to the drug supply tank 40 may be configured to gradually expand toward the drug injection port 43. Good.
Further, as shown in FIG. 5, the tip of the drug injection tube 42 that is not connected to the drug supply tank 40 is not bent, and a hole provided in the side surface of the drug injection tube 42 may be used as the drug injection port 43. . As described above, various configurations of the drug injection tube 42 and the drug injection port 43 are conceivable.

Note that a plurality of drug injection tubes 42 may be provided at the same place or at a plurality of places.
Moreover, it is preferable that the chemical | medical agent injection port 43 is located along these wall surfaces so that the chlorine-type chemical | medical agent density | concentration in the wall surface vicinity of the intake channel 20 and the LNG vaporizer flow path 27 may become high. In this case, since the sludge accumulates at the bottom of the intake channel 20, the intake channel 20 is more preferably located along the side or upper part.

Incidentally, after injection of the chlorinated agent and CO ₂ microbubbles, as the pH of the sea water after the heat exchange is 7.9 or more, from the infusion port 43 may be injected chlorine based agents.

FIG. 6 shows a detailed configuration of the CO ₂ microbubble injection device 34A. As shown in FIG. 6, the CO ₂ microbubble injecting device 34A includes a CO ₂ microbubble generating device 46 and the heat that flows through the intake channel 20 from the CO ₂ microbubble generated by using the CO ₂ microbubble generating device 46. fed microbubble injection pipe 48 for injecting the seawater after the replacement, the second seawater pump 50 for supplying sea water to the CO ₂ microbubble generator 46, the CO ₂ in the CO ₂ microbubble generator 46 And a CO ₂ cylinder 52.

The second seawater pump 50 takes seawater from the intake channel 20 and supplies the taken seawater to the CO ₂ microbubble generator 46.

The CO ₂ cylinder 52 includes a CO ₂ line 53 between the CO ₂ cylinder 52 and the CO ₂ microbubble generator 46. The CO ₂ line 53 includes a pressure reducing valve 54 and a flow rate adjusting valve 55 in order from the CO ₂ cylinder 52 side.
The pressure of carbon dioxide flowing from the CO ₂ cylinder 52 into the CO ₂ line 53 is adjusted to atmospheric pressure by the pressure reducing valve 54, the flow rate is adjusted by the flow rate adjusting valve 55, and the CO ₂ microbubble generator 46 is supplied. Sent. The CO ₂ is automatically taken into the apparatus by the negative pressure inside the apparatus due to the flowing water of the sea water taken in by the second sea water pump 50 into the CO ₂ microbubble generator 46.
In this way, using a CO ₂ microbubble generator CO ₂ supplied to 46, in combination with the chlorine-based agent injected from the drug infusion device 32A, inhibit swimming marine organisms, to the heat exchange water flow path An amount of CO ₂ microbubbles that can suppress the adhesion of marine organisms can be generated and injected into seawater for heat exchange flowing through the intake channel 20 as necessary.
It should be noted that the amount of CO ₂ microbubbles that can inhibit the migration of marine organisms and suppress the adhesion of marine organisms to the heat exchange water flow path in combination with a chlorinated drug is tested in advance, for example. In addition, an observation device (not shown) may be provided at an arbitrary location in the heat exchange water flow path, and adjustment may be performed while observing the state of marine life through the observation device.

The microbubble injection pipe 48 is a microbubble injection for exhausting CO ₂ microbubbles sent from the CO ₂ microbubble generator 46 to the microbubble injection pipe 48 into seawater after heat exchange flowing through the intake channel 20. An inlet 49 is provided. Microbubble infusion tube 48 by CO ₂ micro-bubble generator 46 with a flow rate regulating valve 55 regulates the flow rate of CO ₂ that sucks, CO ₂ microbubble generator CO ₂ that generated the required amount from 46 Microbubbles are injected into the seawater after heat exchange flowing through the intake channel 20 through the microbubble inlet 49.

The tip of the microbubble injection pipe 48 on the side not connected to the CO ₂ microbubble generator 46 is bent toward the downstream side of the water intake channel 20 in the same manner as the drug injection port 43, and the microbubble injection is at the forefront thereof. An inlet 49 may be provided. In this case, the cross section of the tip of the microbubble injection pipe 48 on the side not connected to the CO ₂ microbubble generator 46 is gradually directed toward the microbubble injection port 49. You may comprise so that it may spread. Instead of bending the tip of the microbubble injection tube 48 that is not connected to the CO ₂ microbubble generator 46, a hole provided in the side surface of the microbubble injection tube 48 may be used as the microbubble injection port 49. As described above, various configurations can be considered as the microbubble injection tube 48 and the microbubble injection port 49.

  A plurality of microbubble injection tubes 48 may be provided at the same place or at a plurality of places.

In addition, even if CO ₂ microbubbles are injected from the microbubble injection port 49 so that the pH of the seawater after heat exchange after injecting the chlorine-based chemical and CO ₂ microbubbles is 8.1 or less. good.

== Method for suppressing attachment of marine organisms to the heat exchange water flow path according to the present invention ==
Next, as one embodiment of the present invention, a method for suppressing the attachment of marine organisms to the heat exchange water flow path by injecting a chlorine-based chemical and CO ₂ microbubbles into water for heat exchange will be described.
First, using the first seawater pumps 30 </ b> A and 30 </ b> B, seawater containing marine organisms is sucked into the intake channel 20 from the sea 2 through the intake port 24.

It is possible to suppress adhesion of marine organisms to the heat exchange water flow path including the intake channel 20 by a combination with the CO ₂ microbubble injected from the CO ₂ microbubble injection device 34A from the drug supply tank 40 of the drug injection device 32A. A possible amount of chlorinated chemical is injected from the chemical injection port 43 into the seawater taken into the intake channel 20 through the chemical injection pipe 42 using the valve 44.
On the other hand, by using a second seawater pump 50, sea water flowing Tosuiro 20, it is supplied to the CO ₂ microbubble generator 46, a CO ₂ cylinder 52, automatically CO ₂ within the microbubble generator 46 captured, CO ₂ microbubbles generated.
In this way, the amount of CO that can inhibit marine life swimming and suppress adhesion of marine organisms to the heat exchange water flow path by the combination with the chlorine-based drug injected from the drug injection device 32A. ₂ microbubbles, generated from CO ₂ microbubble infusion device 34A of CO ₂ microbubble generator 46. The generated CO ₂ microbubbles are injected from the microbubble inlet 49 through the microbubble injection pipe 48 into the seawater taken into the intake channel 20.
By injecting a chlorine-based chemical and CO ₂ microbubbles into seawater containing marine organisms, the marine organisms contained can be effectively prevented from adhering to the heat exchange water flow path.

It should be noted that the amount of chlorinated chemicals that can inhibit the migration of marine organisms and suppress the adhesion of marine organisms to the heat exchange water flow path, and combinations with chlorinated chemicals, in combination with CO ₂ microbubbles Therefore, the amount of CO ₂ microbubbles that can inhibit the migration of marine organisms and suppress the adhesion of marine organisms to the heat exchange water flow path can be obtained, for example, by conducting experiments in advance. It is also possible to provide an observation device (not shown) at an arbitrary location in the heat exchange water flow path and adjust it while observing the state of marine organisms through the observation device.

After injecting the chlorine-based chemical and the CO ₂ microbubble, the chlorine-based chemical from the chemical injection port 43 and the CO from the micro-bubble injection port 49 so that the pH of the seawater containing marine organisms is 7.9 or higher. _Two microbubbles may be injected. This is because even if the injection amount of the chlorinated chemical and the CO ₂ microbubble is small, it is possible to effectively suppress marine organisms from adhering to the heat exchange water channel including the intake channel 20.

Seawater into which chlorinated chemicals and CO ₂ microbubbles are injected is supplied to the condenser flow paths 29A and 29B passing through the condensers 18A and 18B through the intake channel 20. The seawater supplied to the condenser channels 29A and 29B exchanges heat with the condensers 18A and 18B, respectively, thereby cooling the condensers 18A and 18B.

  The seawater after heat exchange with the condensers 18A and 18B is discharged from the condenser flow paths 29A and 29B to the water discharge path 22. A part of the seawater discharged to the discharge channel 22 is supplied to the LNG vaporizer flow path 27 passing through the inside of the LNG vaporizer.

In the seawater supplied to the LNG vaporizer flow path 27, the chlorine-based chemical supplied from the chemical injection device 32B as in the case of the chemical injection device 32A and the CO as in the case of the CO ₂ microbubble injection device 34A are used. _The CO ₂ microbubbles generated from the ₂ microbubble injection device 34B are injected. By injecting chlorine-based chemicals and CO ₂ microbubbles into the seawater supplied to the LNG vaporizer flow path 27, marine organisms are easily propagated because they are heated by the condensers 18 A and 18 B. It is possible to inhibit the swimming of marine organisms inside the LNG vaporizer channel 27 and to suppress the attachment of marine organisms to the heat exchange water channel including the LNG vaporizer channel 27 and the discharge channel 22.

Seawater in the LNG vaporizer channel 27 into which the chlorine-based chemical and CO ₂ microbubbles are injected heats the LNG vaporizer 17 by heat exchange with the LNG vaporizer 17. At this time, since the seawater inside the LNG vaporizer channel 27 is heated by the condensers 18A and 18B, the LNG vaporizer 17 is heated using the heat generated in the condensers 18A and 18B. can do.

  Seawater after heat exchange with the LNG vaporizer 17 is discharged from the LNG vaporizer flow path 27 to the water discharge path 22. Here, among the seawater released from the condenser channels 29A and 29B to the discharge channel 22, the seawater supplied to the LNG vaporizer channel 27 and the seawater not supplied to the LNG vaporizer channel 27 Join.

The merged seawater is discharged from the water outlet 26 to the sea 2 through the water discharge channel 22.
By using a combination of chlorinated chemicals and CO ₂ microbubbles, it is possible to more efficiently suppress the adhesion of marine organisms to the heat exchange water flow path than when only chlorinated chemicals are used. As a result of reducing the amount of chlorinated chemicals used compared to the case of using only chlorinated chemicals, the concentration of chlorine in the seawater discharged from the outlet 26 to the sea 2 is reduced. It is very good in that it has less load.

  Hereinafter, the present invention will be specifically described by way of examples. These examples are for explaining the present invention, and do not limit the scope of the present invention.

[Example 1] Preparation of 4th-5th stage larvae of the red barnacle nauplius A red barnacle adult was sampled from the natural sea area. The sampled red barnacle adult was transferred to 23 ° C. artificial seawater (Aquamarine S, manufactured by Yashima Pharmaceutical Co., Ltd.). Adult red barnacles were fed daily with Artemia larvae and watered daily. Nauplius larvae spawned during breeding in this way, so they were collected under light.

  After filtration through a 0.45 μm filter, the collected naprius larvae were placed at about 2 individuals / mL in natural seawater supplemented with 3 mg / L penicillin and 6.6 mg / L streptomycin, and were bred at 23 ° C. Nauplius larvae were fed daily with the cultured floating diatom Chaetoceros gracilis at a concentration of about 600,000 cells / mL, and were rearranged once every 2-3 days.

  Nauplius larvae that had grown to the 4th-5th stage of nauplius about one week after the start of raising the nauplius larvae were used in the swimming inhibition test of Examples 2 and 3.

[Example 2] Combined effect 1 of chlorinated drug and CO ₂ microbubble
5 L of artificial seawater was put into an 8.5 L water tank. T1 type microbubble generating device (swirl flow type, CO ₂ sufficiency rate: 700 mL / min) at a flow rate of 100 mL / min using to generate a CO ₂ microbubbles of CO ₂ microbubbles are generated, the water tank Injected into seawater.
CO ₂ microbubbles predetermined time after starting to inject into each of CO ₂ microbubbles injected seawater approximately 200 mL, was pumped from the water bath.

About 200 to 100 mL of pumped seawater was weighed and transferred to another container. In the state where the injected CO ₂ microbubbles (bubbles) were visible, about 5.0 g / L of sodium hypochlorite aqueous solution was added to this container so that the chlorine concentration was 0.2 mg / L. Subsequently, in a state where the bubbles were visible, about 30 Nauplius larvae of red barnacles prepared in Example 1 were added. The approximately 5.0 g / L sodium hypochlorite aqueous solution used was assumed to be a seawater electrolyzer widely used in seawater-based power generation plants, and a pen-type water purifier (made by Myox, USA) And prepared by electrolysis of 10% aqueous sodium chloride solution.
Moreover, the water temperature of the seawater, DO (Dissolved Oxygen, dissolved oxygen), and pH were measured at the stage where bubbles disappeared and the pH was stabilized using the remaining about 200 mL of the pumped seawater.

Calculate the inhibition rate of Nauplius larvae swimming by counting individuals that have been swimming and those that have stopped moving 1 min, 2 min, 3 min, and 5 min after adding Nauplius larvae did.
The results are shown in Table 1.

As a result, the swimming inhibition rate 3 minutes after adding the Nauplius larvae was 26% under the condition where no CO ₂ microbubbles were added (pH 8.54 (without chlorine)), and the condition under which a small amount of CO ₂ microbubbles were added ( At pH 8.22), the value was 62%. Even results after after 1 minute and 2 minutes, immobilization rate in small additions the conditions of CO ₂ microbubbles exceeded the immobilization rate without the addition of CO ₂ microbubbles. On the other hand, there was almost no difference in the swimming inhibition rate after 5 minutes. From these results, it was clarified that when a small amount of CO ₂ microbubbles was added, it was possible to accelerate the time until the inhibition of swimming, compared with the case where only chlorine was added.
Usually, since the chlorine concentration in water falls rapidly, when only chlorine is added, it will become a density | concentration which cannot inhibit the swimming of marine organisms effectively immediately. However, by injecting the CO ₂ microbubbles together, it has become possible to inhibit the swimming of marine organisms in a short time, and as a result, the attachment of marine organisms can be suppressed very effectively.

In addition, under the condition where a large amount of CO ₂ microbubbles were added (pH 7.43 or less), a relatively high result was obtained in the swimming inhibition rate 1 minute after adding the nauplius larvae, but after 5 minutes As a result, a tendency was observed that the swimming inhibition rate decreased as the pH decreased. This is considered to be due to the effect of the CO ₂ microbubbles and the chlorine scattering or reacting with organic matter in seawater other than the larvae, and the chlorine concentration in the water quickly decreased to a concentration having a low swimming inhibition effect.

  The dissolved oxygen concentration in this test is 7.9 mg / L or more, which greatly exceeds 4.0 mg / L, which is the concentration at which swimming inhibition was confirmed in the test of Comparative Example 1 described later. There is no effect on test results due to the decrease in oxygen concentration.

[Example 3] Combined effect 2 of a chlorine-based drug and CO ₂ microbubbles 2
5 L of artificial seawater was put into an 8.5 L water tank. Using a T1-type microbubble generator, CO ₂ microbubbles were generated at a flow rate of 100 mL / min, and the generated CO ₂ microbubbles were injected into seawater in a water tank.
CO ₂ microbubbles predetermined time after starting to inject into each of CO ₂ microbubbles injected seawater approximately 200 mL, was pumped from the water bath.

About 200 to 100 mL of pumped seawater was weighed and transferred to another container. To this container, about 30 individuals of the red barnacle larvae prepared in Example 1 were added in a state where the injected CO ₂ microbubbles were visible. Subsequently, in a state where the bubbles were visible, about 5.0 g / L of sodium hypochlorite aqueous solution was added so that the chlorine concentration was 0.2 mg / L.
Moreover, the water temperature, DO, and pH of the seawater were measured at the stage where the bubbles disappeared and the pH was stabilized, using the remaining about 200 mL of the pumped seawater.

Inhibition of Nauplius larvae swimming by counting individuals swimming and individuals that have stopped moving 1 minute, 2 minutes, 3 minutes, and 5 minutes after adding sodium hypochlorite aqueous solution The rate was calculated. Moreover, 5 minutes after adding sodium hypochlorite aqueous solution, the chlorine concentration of seawater was measured using the residual chlorine meter (the HINA Instruments Japan Co., Ltd. make, HI95711 type | mold).
The results are shown in Table 2.

As a result, as in Example 2, it was clarified that under the condition (pH 7.91 or more) to which a small amount of CO ₂ microbubbles were added, the time until the marine organisms became unable to swim was shortened.
In addition, under conditions where a large amount of CO ₂ microbubbles were added (pH 7.30 or less), the chlorine concentration after 5 minutes from the addition of the sodium hypochlorite aqueous solution increases the amount of CO ₂ microbubbles added (pH Therefore, when the amount of CO ₂ microbubbles added increases, the concentration of chlorine decreases to a level where it does not act effectively on marine organisms, and the swimming inhibition rate on marine organisms decreases accordingly. It was confirmed to do.

  In addition, the dissolved oxygen concentration in this test is 7.6 mg / L or more, and greatly exceeds 4.0 mg / L, which is the concentration at which swimming inhibition performed in the test of Comparative Example 1 described later was confirmed. There is no effect on test results due to the decrease in dissolved oxygen concentration.

Comparative Example 1 Effect of Dissolved Oxygen Concentration The following experiment was conducted in order to examine the effect of the dissolved oxygen concentration of seawater on the inhibition of marine life swimming.
2 L of artificial seawater (manufactured by Yashima Pharmaceutical Co., Ltd., Aquamarine S) was placed in a 2 L beaker. N ₂ was injected into the sea water by placing the air stone in sea water in a beaker and supplying N ₂ to the air stone in sea water at a flow rate of 100 mL / min.
DO of seawater, the _{N 2} before injection 7.6 mg / L, respectively, 5.1,4.0,3.0, or 2.0 and until, continued to inject _{N 2.}

100 mL of seawater with a DO of 5.1, 4.0, 3.0, or 2.0 was pumped from a 2 L beaker into a 100 mL beaker. About 30 individuals of the red barnacle nauplii larva prepared in Example 1 were added to this container in a state where the injected N ₂ bubbles were visible. Moreover, the pH of the seawater in this container was measured.

The percentage of inhibition of swimming of the nauplius larvae was calculated by counting the individuals that had been swimming and those that had stopped moving 1 min and 5 min after adding the nauplius larvae.
The results are shown in Table 3.

  As a result, it was found that when DO was lowered to 4.0 mg / L or less, a swimming inhibition effect of marine organisms was obtained. However, when DO exceeded 4.0 mg / L, no swimming inhibition effect was observed.

  Therefore, it was revealed that the marine organisms swimming inhibition effect obtained in Examples 2 and 3 was not due to the influence of dissolved oxygen concentration.

2 Sea 10 Thermal power plant 12 Fuel storage facility 14 LNG tank 16 Power generation facility 17 LNG vaporizer 18A, 18B Condenser 20 Intake channel 22 Discharge channel 24 Intake port 26 Discharge port 27 LNG vaporizer channel 29A, 29B Condenser Flow path 30A, 30B First seawater pump 32A, 32B Drug injection device 34A, 34B CO ₂ microbubble injection device 40 Drug supply tank 42 Drug injection tube 43 Drug injection port 44 Valve 46 CO ₂ microbubble generator 48 Micro bubble injection Pipe 49 Microbubble inlet 50 Second seawater pump 52 CO ₂ cylinder 53 CO ₂ line 54 Pressure reducing valve 55 Flow control valve 80 Heat exchange water flow path

Claims (10)

A method for suppressing the attachment of marine organisms to a heat exchange water flow path,
Supplying water containing marine organisms to the facility subject to heat exchange;
Using the supplied water to exchange heat with the heat exchange target equipment;
Discharging the heat exchange target equipment and water after heat exchange from the heat exchange target equipment;
Injecting chlorine-based chemicals and CO ₂ microbubbles into any one or more of the water containing the marine organisms, the supplied water, and the heat exchange target equipment and the water after heat exchange; A suppression method characterized by comprising.   The suppression method according to claim 1, wherein the chlorinated drug is sodium hypochlorite, chlorine dioxide, or chlorine. The suppression method according to any one of claims 1 and 2, wherein the pH of water into which the chlorine-based chemical and CO ₂ microbubbles are injected is 7.9 or more.   The said marine organism is barnacles, The suppression method of any one of Claims 1-3 characterized by the above-mentioned.   The suppression method according to any one of claims 1 to 4, wherein the water containing the marine organisms is seawater. A method for inhibiting the swimming of marine life,
An inhibition method comprising a step of injecting a chlorine-based drug and CO ₂ microbubbles into water containing the marine organisms.   The inhibition method according to claim 6, wherein the chlorinated drug is sodium hypochlorite, chlorine dioxide, or chlorine. The inhibition method according to any one of claims 6 and 7, wherein the pH of the water into which the chlorinated drug and CO ₂ microbubbles are injected is 7.9 or more. A system for suppressing the attachment of marine organisms to the heat exchange water flow path,
A supply device for supplying water containing marine organisms to the facility for heat exchange;
A heat exchanger for exchanging heat with the heat exchange target facility using the supplied heat exchange water;
A discharge device for discharging the heat exchange target equipment and water after heat exchange from the heat exchange target equipment;
A drug injection device for injecting a chlorine-based drug into any one or more of the water containing the marine organisms, the supplied water, and the heat exchange target equipment and the water after the heat exchange;
A microbubble injection device for injecting CO ₂ microbubbles into any one or more of the water containing the marine organisms, the supplied water, and the heat exchange target equipment and the water after heat exchange; A system characterized by comprising.   The system according to claim 9, wherein the chlorinated drug is sodium hypochlorite, chlorine dioxide, or chlorine.

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