The present invention relates to a ship ballast water treatment system, and more particularly, to a ship ballast water treatment system, which can sterilize ballast water stored in a plurality of ballast tanks disposed in a ship and receiving seawater to improve stability of the ship.
Generally, ships such as LNG carriers, LPG carriers, container ships, bulk carriers, and tankers are designed to transport cargo in navigation. Thus, when cargo is unloaded from a ship, the center of gravity of the ship can be shifted upwards, causing instability of the ship.
In other words, when the draft (that is, the depth to which a ship is immersed when bearing a given load) becomes shallow by unloading cargo from the ship, the degree of hogging (referring to upward bending of a ship as the center of the ship is raised while the bow and the stern are lowered due to heavier weights thereof by intensively loading cargo at the bow and the stem of the ship) increases during navigation, and shearing force and longitudinal bending moment applied to the ship also increase.
In addition, during navigation, the ship can be exposed to impact of waves striking the bottom of the ship, that is, a slamming phenomenon, and also suffers from a propeller racing phenomenon in which the propeller is not fully submerged in water and emerges from a water surface, causing decrease in propulsion performance or increase in load fluctuation on the propeller and main engines, and a problem of deterioration in maneuverability due to insufficient submersion of a rudder in the water.
Accordingly, in order to resolve such problems, ships such as LNG carriers, LPG carriers, container ships, bulk carriers, and tankers are provided with a plurality of ballast tanks storing seawater in order to improve stability of the ships. Herein, the water stored in the ballast tank is referred to as ballast water.
Ballast water serves to provide stable adjustment of draft and trim (defined as a longitudinal inclination of a ship) depending upon the amount of cargo loaded on the ship. As described above, if ballast water is not supplied into the ship after cargo is completely unloaded from the ship, it is difficult for the ship to maintain a sufficient draft only with an inherent weight thereof.
As a result, the bow of the ship can severely emerge from the water surface, or the propeller of the ship can be insufficiently submerged in the seawater, thereby causing bow slamming, deterioration of propulsion performance, or deterioration in maneuverability. Therefore, it is necessary for ships to use'the ballast water.
However, use of ballast water provides a problem. That is, marine contamination can occur due to microorganisms or marine organisms in the course of supplying or discharging the ballast water into or from the ballast tanks.
That is, when ballast water supplied into a ship in one nation is discharged therefrom in another nation having a completely different environment, various foreign substances, microorganisms, viruses, and other organic materials of the one nation can disturb the marine ecosystem of the other nation.
In consideration of such danger, strengthened international regulations on ballast water and sediments, enforced starting in 2009, require that ballast water be discharged only after sterilization of 99% microorganisms in the ballast water in order to prevent propagation of toxic microorganisms included in the ballast water. As such, the strengthened international regulations on ballast water and sediments increase difficulty in treatment of ballast water and promote development of various techniques related to a ballast water treatment apparatus.
Among conventional techniques, in a conventional filtration type ballast water treatment apparatus, underwater creatures such as plankton are deposited. In order to remove the deposited underwater creatures, the apparatus must be disassembled before cleaning, thereby providing a complicated cleaning process and difficulty in removal of toxic viruses other than some plankton.
Further, in a ballast water treatment apparatus wherein sodium hypochlorite generated through electrolysis of seawater is added to ballast water for sterilization of the ballast water, only some microorganisms can be removed through an indirect method, thereby providing low sterilization efficiency and difficulty in control of a sterilization material.
Further, a ballast water treatment apparatus separately employing a filtration device and an electrolysis device performs sterilization of ballast water through many processes, thereby requiring a very complicated operation mechanism and a large space.
Moreover, this apparatus can sterilize some microorganisms through an indirect method, thereby providing low sterilization efficiency and difficulty in control of a sterilization material.
It is an aspect of the present invention to provide a ship ballast water treatment system, which is a direct injection type system allowing direct supply of ozone into a ballast conduit and can achieve efficient dissolution of ozone in ballast water through generation of ozone bubbles.
In accordance with one aspect of the present invention, a ship ballast water treatment system includes: an ozone bubbling unit disposed inside a conduit through which ballast water flows and converting ozone supplied thereto into bubbles; an ozone supply channel connected at one end thereof to the ozone bubbling unit and supplying the ozone to the ozone bubbling unit therethrough; and a seawater pumping unit provided to the conduit while being coupled at one end thereof to the ozone bubbling unit, and pumping the ballast water in the conduit into the ozone bubbling unit.
The ozone bubbling unit may include a bubble nozzle connected at one side thereof to the seawater pumping unit and converting the supplied ozone into ozone microbubbles using the seawater; and a spreading unit provided to an outlet of the bubble nozzle and spreading the ozone microbubbles.
The conduit may include a main conduit and a connecting conduit detachably connected between pieces of the main conduit, and the ozone bubbling unit may be disposed in the connecting conduit.
Both ends of the connecting conduit may have the same diameter as that of the main conduit, and a central portion of the connecting conduit may have a larger diameter than that of both ends thereof to allow the ozone microbubbles to be spread therethrough.
The ozone bubbling unit may be placed at the central portion of the connecting conduit.
The seawater pumping unit may include a pump coupled at one side thereof to the ozone bubbling unit and at the other side thereof to the conduit to pump the ballast water in the conduit into the ozone bubbling unit; a motor provided to the pump and operating the pump; and a bracket provided to the motor and coupling the motor to the conduit.
The ozone may be supplied from an ozone generating unit disposed on a deck, and the ozone generating unit may include an oxygen generator disposed on the deck; an oxygen storage tank disposed on the deck and storing oxygen generated by the oxygen generator; and an ozone generator disposed on the deck and generating ozone using oxygen supplied from the oxygen storage tank.
The oxygen generator, the oxygen storage tank and the ozone generator may be disposed inside a container placed on the deck.
The ozone generated by the ozone generator may be supplied into the ozone bubbling unit through a double-pipe.
In accordance with another aspect of the present invention, a ship ballast water treatment system includes: an ozone bubbling unit to which part of a conduit through which ballast water flows is detachably coupled, the ozone bubbling unit converting ozone supplied into the part of the conduit into microbubbles using the ballast water, wherein the ballast water is pumped into the ozone bubbling unit by a pump disposed inside the conduit.
Embodiments of the preset invention can achieve efficient sterilization of ballast water by directly supplying ozone bubbles into a conduit through which the ballast water flows, while producing the ozone bubbles directly using the ballast water flowing in the conduit as a medium for generating the ozone bubbles, thereby simplifying the structure of the ballast water treatment system.
The above and other aspects, features, and advantages of the present invention will become apparent from the detailed description of the following embodiments in conjunction with the accompanying drawings.
Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. Like components will be denoted by like reference numerals throughout the drawings.
Referring to these drawings, a ship ballast water treatment system 1 according to one embodiment of the invention includes: an ozone bubbling unit 100 disposed inside a conduit L through which ballast water flows and converting ozone supplied thereto into bubbles; an ozone supply channel 200 connected at one end thereof to the ozone bubbling unit 100 and supplying the ozone to the ozone bubbling unit 100 therethrough; a seawater pumping unit 300 provided to the conduit L while being coupled at one end thereof to the ozone bubbling unit 100, and pumping the ballast water in the conduit L into the ozone bubbling unit 100; and an ozone generating unit 400 disposed on a deck D of the ship.
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In this embodiment, as shown in
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In this embodiment, the bubble nozzle 110 is provided therein with an ozone flow passage (not shown) communicating with the ozone supply channel 200, and a seawater flow passage (not shown) communicating with the pump 310. In addition, a bottleneck portion having a narrower diameter than other portions of the seawater flow passage is formed in region of the seawater flow passage, at which the ozone flow passage meets the seawater flow passage. In the bottleneck portion, a negative pressure is generated and forces the supplied ozone to be suctioned from the ozone flow passage into the seawater flow passage such that the ozone is discharged together with the seawater through the outlet of the bubble nozzle.
Furthermore, the outlet of the bubble nozzle 110 may be provided with a bubble layer (not shown) having a plurality of fine holes, whereby the ozone microbubbles can be generated while the supplied ozone passes through the bubble layer.
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In this embodiment, the ozone bubbling unit 100 is illustrated as one example and may be replaced by any bubble nozzle known in the art.
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In addition, as shown in
Further, a flange may be disposed at an interface between the main conduit L1 and the connecting conduit L2 such that the main conduit L1 and the connecting conduit L2 can be coupled to each other by bolts and nuts through the flange.
Furthermore, for convenience of installation and coupling of the ozone bubbling unit 100, the ozone supply channel 200 and the seawater pumping unit 300, a portion of an upper side of the connecting conduit L2 may be cut and detachably coupled thereto by bolts and nuts.
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Further, ozone generated by the ozone generator 430 is supplied to the ozone bubbling unit 100 disposed at the bottom of the ship through the ozone supply channel 200, which passes through a closed space. An ozone transport pipe is likely to suffer from corrosion due to characteristics of ozone. Thus, in this embodiment, in order to prevent leakage of ozone using an ozone transport pipe for redundancy, even upon corrosion of one transport pipe, the ozone supply channel 200, through which ozone is transported, may be realized by a double-pipe, as shown in
The ozone supply channel 200 may be provided with, at least one valve (not, shown), which may be opened or closed by a controller (not shown). Further, the conduit L may be provided therein with at least one bubble sensor (not shown) capable of measuring the amount of bubbles generated, and the controller may regulate the degree of opening of the at least one valve provided to the ozone supply channel 200 and power of the pump 310 based on the amount of the generated bubbles measured by the bubble sensor.
The seawater pumping unit 300 supplies the ballast water into the bubble nozzle 110 by pumping the ballast water flowing in the conduit L, and includes: a pump 310 coupled at a left side thereof to the ozone bubbling unit 100 and at a right side thereof to the conduit L to pump the ballast water in the conduit L into the ozone bubbling unit 100; a motor 320 provided to the pump 310 and operating the pump 310; and a bracket 330 provided to the motor 320 and coupling the motor 320 to the conduit L via bolts and nuts, or welding, as shown in
As shown in
In this embodiment, the ozone generating unit 400 may be disposed inside a container C, as shown in
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The ozone generator 430 may generate ozone in a silent discharge manner wherein, with a dielectric material such as glass or a ceramic material interposed between electrodes, oxygen is supplied into a discharge space and a high voltage of 6 kV˜15 kV is applied to the electrodes to induce reaction for generating ozone in, the discharge space.
The ozone gas generated by the ozone generator 430 may be supplied at a flow rate of 1 L/min into the conduit L, through which ballast water flows, such that the conduit L has an ozone concentration of 170 g/cm3 and an ozone injection amount of 2 mg/L.
In this embodiment, in order to remove heat generated in the course of generating ozone, the ozone generator 430 may cool the ozone generator 430 using the water chiller 440, as shown in
Ozone generated in the ozone generating unit 400 is supplied to the ozone bubbling unit 100 through the ozone supply channel 200. The ozone bubbling unit 100 converts the supplied ozone into ozone microbubbles using seawater supplied through a seawater supply channel.
In addition, the ozone bubbling unit 100 spreads the ozone microbubbles such that the ozone microbubbles can be dissolved in a wide surface area in ballast water. It can be seen that the ozone microbubbles can be more efficiently spread due to decrease in inflow rate of the ballast water resulting from a larger diameter of the central portion of the connecting conduit L2 than that of the main conduit L1.
Further, in this embodiment, the pump 310 is directly coupled to the bubbling generating unit such that the ballast water in the conduit L can be directly supplied to the bubble nozzle 110 by the pump 310, thereby simplifying the structure of the ballast water treatment system through elimination of a separate component for bypassing the ballast water.
As such, in this embodiment, ozone is converted into bubbles, which in turn are directly supplied into the conduit through which ballast water flows, thereby enabling efficient sterilization of the ballast water, and the ballast water flowing in the conduit can be directly used as a medium for generation of the ozone bubbles, thereby simplifying the structure of the ballast water treatment system.
Although some embodiments have been described with reference to the drawings, it will be apparent to those skilled in the art that the present invention is not limited to above embodiment, and that various modifications, changes, and alterations can be made without departing from the spirit and scope of the invention. Therefore, the scope of the present invention should be limited only by the accompanying claims.
Number | Date | Country | Kind |
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10-2012-0117863 | Oct 2012 | KR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/KR2012/009342 | 11/7/2012 | WO | 00 |