WO2020141791A1 - Apparatus and method for treating ship exhaust gas in combination with ballast water - Google Patents

Apparatus and method for treating ship exhaust gas in combination with ballast water Download PDF

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Publication number
WO2020141791A1
WO2020141791A1 PCT/KR2019/018427 KR2019018427W WO2020141791A1 WO 2020141791 A1 WO2020141791 A1 WO 2020141791A1 KR 2019018427 W KR2019018427 W KR 2019018427W WO 2020141791 A1 WO2020141791 A1 WO 2020141791A1
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Prior art keywords
ballast water
exhaust
pipe
valve
water
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PCT/KR2019/018427
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French (fr)
Korean (ko)
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손을택
손덕순
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(주)나노에스텍수산
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    • AHUMAN NECESSITIES
    • A41WEARING APPAREL
    • A41BSHIRTS; UNDERWEAR; BABY LINEN; HANDKERCHIEFS
    • A41B11/00Hosiery; Panti-hose
    • A41B11/10Stocking protectors
    • AHUMAN NECESSITIES
    • A41WEARING APPAREL
    • A41BSHIRTS; UNDERWEAR; BABY LINEN; HANDKERCHIEFS
    • A41B11/00Hosiery; Panti-hose
    • A41B11/005Hosiery made essentially of a multi-ply construction
    • AHUMAN NECESSITIES
    • A41WEARING APPAREL
    • A41BSHIRTS; UNDERWEAR; BABY LINEN; HANDKERCHIEFS
    • A41B11/00Hosiery; Panti-hose
    • A41B11/008Hosiery with an anti-slip coating
    • AHUMAN NECESSITIES
    • A41WEARING APPAREL
    • A41BSHIRTS; UNDERWEAR; BABY LINEN; HANDKERCHIEFS
    • A41B2400/00Functions or special features of shirts, underwear, baby linen or handkerchiefs not provided for in other groups of this subclass
    • A41B2400/80Friction or grip reinforcement
    • AHUMAN NECESSITIES
    • A41WEARING APPAREL
    • A41BSHIRTS; UNDERWEAR; BABY LINEN; HANDKERCHIEFS
    • A41B2500/00Materials for shirts, underwear, baby linen or handkerchiefs not provided for in other groups of this subclass
    • A41B2500/50Synthetic resins or rubbers

Definitions

  • the present invention relates to a ballast water treatment and discharge exhaust treatment of a ship, and relates to an apparatus and method for the combined treatment of microorganisms and discharge exhaust in the ballast water in a single device.
  • a ship generates power by burning liquid fuel as air, loads ballast water to secure the stability of the ship, discharges ballast water at the time of cargo entering the port, or repeats loading.
  • the combustion exhaust of fuel oil contains carbon dioxide (CO2), which is a cause of global warming, and has a problem of disturbing the marine ecosystem by discharging ballast water containing microorganisms.
  • CO2 carbon dioxide
  • the present invention decomposes carbon dioxide (CO2) contained in the exhaust gas generated during the combustion of fuel oil in a ship into extremely fine foam and disperses it into the ballast water, while the extremely fine foam dispersed in water bursts due to its unique action. Hotspots are formed, water molecules are decomposed in extreme reaction fields, hydroxyl groups (OH-) are formed to kill microorganisms, and carbon dioxide (CO2) in the exhaust is calcium hydrogen carbonate (Ca(HCO3)2), It is synthesized with magnesium hydrogen carbonate (Mg(HCO3)2) and dissolved in water with nitrogen oxides (NOx) and sulfur oxides (SOx).
  • CO2 carbon dioxide
  • the present invention enables to treat both the exhaust exhaust which combusts liquid fuel with air, the exhaust exhaust which combusts liquid fuel with oxygen, the exhaust exhaust which combusts natural gas with air, and the exhaust exhaust which combusts natural gas with oxygen.
  • the exhaust exhaust which combusts liquid fuel with air the exhaust exhaust which combusts liquid fuel with oxygen
  • the exhaust exhaust which combusts natural gas with air the exhaust exhaust which combusts natural gas with oxygen
  • the present invention is to install the device in the vessel as follows.
  • the exhaust compression device (C) is connected to the exhaust inlet pipe (1), and a compressed exhaust transfer pipe (2) is attached.
  • the first ultra-fine foam generator (A) is provided with a compressed exhaust supply pipe (3), connected to the compressed exhaust transfer pipe (2) through an open/close valve (4), and connected to the processing tank (D) from the opposite side to provide a very fine exhaust.
  • a discharge pipe (5) for discharging catcher is laid, and a ballast water supply pipe (6) is laid on the same side to be connected to the ballast water transfer pipe (8) through an open/close valve (7).
  • the second ultrafine foam generator (B) is provided with a compressed exhaust supply pipe (3-1), connected to the compressed exhaust transfer pipe (2) through an open/close valve (4-1), and connected to the treatment tank (D) from the opposite side.
  • the discharge pipe (9) for discharging the ultra-fine exhaust gas gun is laid, and the ballast water supply pipe (6-1) is laid on the same side, connected to the ballast water transfer pipe (8) through an on-off valve (7-1),
  • the ballast water transfer pipe (8) is branched into two pipes at the inflow side, and an on/off valve (17) and an on/off valve (19) are respectively attached to the ballast water inlet pipe (18) and on/off valve (19).
  • the seawater inflow pipe 20 is connected.
  • the treatment tank (D) is divided into an inflow chamber (14), a reaction chamber (15), and a stabilization chamber (16) by partition plates (12, 13), and a ballast water supply pipe (11) is installed in the inflow chamber (14).
  • a ballast water transfer pipe 8 Is connected to the ballast water transfer pipe 8 through the opening/closing valve 10, the discharge pipe 5 attached to the first microscopic bubble generation device A is connected, and the reaction chamber 15 has the second microscopic strength
  • the discharge pipe (9) attached to the gun generator (B) is connected, and to the stabilization chamber (16) is connected to the on/off valve (21) connected to the ballast water discharge pipe (22) at the rear and the seawater discharge pipe (24) facing the sea.
  • the connected opening/closing valve 23 is laid in close proximity so that the device is constructed.
  • ballast water refers to the water stored in the ballast water or fresh water tank, the ballast water is not limited to sea water and can be used by replacing it with fresh water.
  • the seawater inflow pipe 20 and the seawater discharge pipe 24 inflow the seawater when it is difficult to supply the ballast water and dissolve the discharged exhaust into the seawater to discharge it into the seawater.
  • ballast water is supplied from the ballast water tank of the ship to the treatment tank (D) and loaded, and the ballast water is supplied to the first and second ultra-fine foam generators to operate the apparatus;
  • Ballast water is pressurized to 8 atmospheres or more by the operation of the ultrafine foam generators 1 and 2, and the compressed exhaust is pressurized from the exhaust compressor to finely decompose and processed into ultrafine exhaust gunners;
  • Steps 1 and 2 of the ultra-fine air bubble generation devices A and B which are pressurized at a high pressure of 8 atmospheres or more, are discharged and diffused at normal pressure in the inlet chamber and the reaction chamber of the treatment tank, respectively;
  • H2O Water molecules
  • H+ hydrogen ions
  • OH- hydroxyl groups
  • Carbon dioxide (CO2) is reacted with inorganic substances such as calcium (Ca) and magnesium (Mg) in water by rupture of the ultrafine air bubbles, calcium hydrogen carbonate (Ca(HCO3)2), magnesium hydrogen carbonate (Mg(HCO3)2 ) And dissolved in water;
  • inorganic substances such as calcium (Ca) and magnesium (Mg) in water by rupture of the ultrafine air bubbles, calcium hydrogen carbonate (Ca(HCO3)2), magnesium hydrogen carbonate (Mg(HCO3)2 ) And dissolved in water;
  • a step in which the microorganisms are killed and the ballast water in which carbon dioxide (CO2) is dissolved is discharged to the ballast tank of the ship through the discharge pipe;
  • the seawater is introduced through the seawater inflow pipe and then discharged into the seawater through the seawater discharge pipe through the above steps.
  • the present invention is capable of contributing to the prevention of global warming by protecting the ecosystem and preventing the emission of carbon dioxide into the atmosphere by reducing costs by performing a combined treatment of dissolving the combustion exhaust gas containing carbon dioxide in water while killing microorganisms in the ballast water.
  • 1 is a connection plan view of a device.
  • Figure 1 is a connection plan view of the device, A is the first micro-bubble generator, B is the second micro-bubble generator, C is the exhaust compression device, D is the treatment tank.
  • Compressed exhaust supply pipe (3) is attached to the first ultrafine foam generator (A) and is connected to the compressed exhaust transfer pipe (2) through an open/close valve (4) to receive compressed exhaust from the exhaust compression system (C),
  • a discharge pipe (5) for discharging ultra-fine exhaust gas catchers is connected to the inlet chamber (14) of the treatment tank (D), and a ballast water supply pipe (6) for supplying ballast water is installed to open and close the valve (7).
  • a ballast water supply pipe (6) for supplying ballast water is installed to open and close the valve (7).
  • Compressed exhaust supply pipe (3-1) is attached to the second ultrafine foam generator (B), which is connected to the compressed exhaust transfer pipe (2) through an open/close valve (4-1) to receive compressed exhaust, and is extremely fine to the opposite side.
  • a discharge pipe (9) for discharging the device catcher is attached to the reaction chamber (15) of the treatment tank (C), and a ballast water supply pipe (6-1) for supplying ballast water is installed to open and close a valve (7-1) ) Is connected to the ballast water transfer pipe (8) to receive the ballast water.
  • the ballast water transfer pipe 8 connected to the on-off valve 7-1 is branched into two pipes at the inflow side, and the on-off valve 17 and the on-off valve 19 are attached to the ballast water inlet pipe to the on-off valve 17 (18) is connected, the seawater inlet pipe (20) is connected to the on-off valve (19), and when the supply of ballast water is difficult, the seawater is introduced through the seawater inlet pipe.
  • ballast water refers to the water stored in the ballast tank, and can be used as ballast water without distinction between sea water and fresh water.
  • ballast water inlet pipe 18 is not shown, but is connected to the ballast water tank of the ship, and the sea water inlet pipe 20 is connected into the sea water of the sea.
  • the on-off valve 17 is opened at the time of ballast water inflow and closed at the time of seawater inflow, and on the contrary, the on-off valve 19 is closed at the time of ballast water inflow and is opened at the time of seawater inflow to select the ballast water and seawater inflow. do.
  • No. 1 and No. 2 micro-bubble generators are devices of the micro-bubble generators (10-1022612) registered with the Korean Intellectual Property Office, and the devices are pressurized pumps, mixing pipes equipped with brackets It is composed of a plurality of tubes that contract and expand while varying the diameter, and it functions to decompose a cluster of molecules into extremely fine bubbles while repeating mixing, pressurization, crushing, expansion, collision, and turning of liquid and gas. .
  • micro-bubble generators A, B
  • the microscopically disintegrated microscopic micropore shrinks while shrinking in water and bursts when it reaches the limit, and when it bursts, it forms hot spots on the outer peripheral surface of the micro micropore and exists in this extreme reaction field.
  • the substance to be decomposed is decomposed, and the water molecules are also decomposed into hydrogen ions (H+) and hydroxyl groups (OH-).
  • the ultra-fine century bubble refers to a nano-sized bubble.
  • Exhaust compression device (C) is integrated to connect the equipment for cooling and filtering of the incoming exhaust, and the exhaust inlet pipe (1) and the compressed exhaust transfer pipe (2) is attached, the exhaust inlet pipe (1) is the ship exhaust It is connected to the discharge pipe of the source to introduce combustion exhaust, and compresses the incoming exhaust gas at a high pressure of 8 atmospheres or more to supply it to the first and second ultrafine foam generators (A, B) through the compressed exhaust transfer pipe (2).
  • the exhaust can be divided into an exhaust exhaust in which liquid fuel is combusted with air, an exhaust exhaust in which liquid fuel is combusted with oxygen, an exhaust exhaust in which natural gas is combusted with air, an exhaust exhaust in which natural gas is combusted with oxygen, and the like.
  • the exhaust is reduced by the amount of nitrogen contained in the air.
  • the exhaust compressor (C) can be miniaturized. Can be. Therefore, the size of the exhaust compression device (C) is configured by adjusting according to the amount of exhaust exhaust.
  • the present invention can treat both the exhaust exhaust which combusts liquid fuel with air, the exhaust exhaust which combusts liquid fuel with oxygen, the exhaust exhaust which combusts natural gas with air, and the exhaust exhaust which combusts natural gas with oxygen.
  • the treatment tank (D) is divided into an inlet chamber (14), a reaction chamber (15), and a stabilization chamber (15) by the partition plates (12, 13), and the partition plates (12, 13) have a ballast water flowing in to the upper side.
  • the height is adjusted to smoothly flow, and a drain pipe (not shown) is provided at the bottom.
  • the inlet chamber 14 is connected to the discharge pipe 5 of the first micro-strength bubble generating device B, and a ballast water supply pipe 11 is attached to the ballast water transfer pipe 8 through the on-off valve 10.
  • the discharge pipe 9 of the second ultra-fine foam generator B is connected, and the stabilization chamber 16 is provided with an on-off valve 21 and an on-off valve 23.
  • the open/close valve 21 is connected to a ballast water discharge pipe 22 connected to a ballast water tank and a seawater discharge pipe 24 directed to the sea to the open/close valve 23, respectively.
  • the ultra-fine exhaust air bubbles are discharged from the first and second ultra-fine bubble generators A and B in the inlet chamber 14 and the reaction chamber 15, and are diffused.
  • the on-off valve 19 connecting the seawater inlet pipe 20 and the on-off valve 23 connecting the seawater discharge pipe 24 are closed when the ballast water is introduced, and open when the seawater is introduced, The on-off valve 17 and the on-off valve 21 are closed.
  • the inflow of seawater is reduced to a small amount of the ballast water in the ship or when the ballast water is not available, and the exhaust gas containing carbon dioxide is dissolved in the seawater through the same treatment steps as the ballast water inflow. It is discharged into the sea water.
  • the apparatus is operated to adjust the ballast water to be discharged from the ballast water discharge pipe 22 of the stabilization chamber 16 while the ballast water flows into the inlet chamber 14, the reaction chamber 15, and the stabilization chamber 16.
  • the inlet chamber 14 and the reaction chamber 15 are discharged and diffused by the ultra-fine exhaust air bubbles from the first and second ultra-fine bubble generators A and B, and the inlet chamber 14 and the reaction chamber 15
  • the micro-exhaust air bubbles diffused in) are shrunk as shrinkage progresses to reach the limit and rupture, and extreme reaction fields (hotspots) are formed at the boundary surface of the micro-exhaust air bubbles that burst, and water present in the extreme reaction field Silver decomposes into hydrogen ions (H+) and hydroxyl groups (OH-), which attack microorganism cells and kill microorganisms.
  • the carbon dioxide (CO2) contained in the ultra-fine exhaust gas diffused in the inflow chamber 14 and the reaction chamber 15 is combined with inorganic substances such as calcium (Ca) and magnesium (Mg) contained in sea water to form calcium carbonate.
  • inorganic substances such as calcium (Ca) and magnesium (Mg) contained in sea water to form calcium carbonate.
  • Ca(CO3)), calcium hydrogen carbonate (Ca(HCO3)2), or magnesium carbonate (Mg(CO3)), magnesium hydrogen carbonate (Mg(HCO3)2), combined with nitrogen oxide (NOx), sulfur oxide ( SOx) and the like is discharged through the ballast water discharge pipe 22 of the stabilization chamber 16 and flows into the ballast water tank.
  • the exhaust gas is dissolved in the seawater and discharged into the seawater while passing through the same treatment steps as the ballast water treatment even when the seawater is introduced.
  • the present invention reduces the cost by performing a combined treatment of dissolving carbon dioxide (CO2) in water while killing microorganisms in the ballast water, while preventing the ecological disturbance caused by the discharge of ballast water while preventing the emission of carbon dioxide (CO2) into the atmosphere. It will contribute to the prevention of warming.
  • CO2 dissolving carbon dioxide
  • the ballast water of the ship is not limited to seawater, and fresh water containing inorganic materials can also be used as ballast water.
  • the present invention is not limited to a ship, and can be used for any combustion device that generates combustion exhaust.

Abstract

The present invention pertains to an apparatus and a method for treating ship exhaust gas in combination with ballast water. When exhaust gas produced from the combustion of fuel oils in a ship are discharged in the form of ultra-fine exhaust gas bubbles into water, microorganisms are killed by hydroxyl groups (OH-) generated by the decomposition of water molecules, and carbon dioxide (CO₂) contained in the exhaust gas is combined into calcium hydrogen carbonate (Ca(HCO3)2) or magnesium hydrogen carbonate (Mg(HCO3)2) and the like, and dissolved into the water.

Description

선박의 배출배기와 평형수 병합처리장치 및 방법Apparatus and method for combined discharge and ballast water from ships
본 발명은 선박의 평형수 처리와 배출배기 처리에 관한 것으로서, 단일 장치에서 평형수중의 미생물과 배출배기를 병합처리하는 장치 및 방법에 관한 것이다.The present invention relates to a ballast water treatment and discharge exhaust treatment of a ship, and relates to an apparatus and method for the combined treatment of microorganisms and discharge exhaust in the ballast water in a single device.
종래로부터 선박은 공기로서 액체연료를 연소시켜 동력을 발생시키고, 선박의 안정성 확보를 위해 평형수를 적재하며, 항구에 입항하여 화물의 적하시에 평형수를 배출하거나 적재를 반복하게 된다. Conventionally, a ship generates power by burning liquid fuel as air, loads ballast water to secure the stability of the ship, discharges ballast water at the time of cargo entering the port, or repeats loading.
그런데, 연료유 연소배기에는 지구온난화의 원인 물질인 이산화탄소(CO₂)가 함유되어 있고, 미생물이 함유된 평형수를 배출하여 해양생태계를 교란시키는 문제점을 가지고 있다. However, the combustion exhaust of fuel oil contains carbon dioxide (CO₂), which is a cause of global warming, and has a problem of disturbing the marine ecosystem by discharging ballast water containing microorganisms.
이러한 문제점 해결을 위해, 세계는 이산화탄소의 대기중 배출 삭감을 위한 지구 온난화방지조약과 평형수중의 미생물체 제거를 위한 평형수관리협약 등을 체결하면서 공동으로 노력하고 있다.In order to solve these problems, the world is working jointly by signing a global warming prevention treaty to reduce carbon dioxide emissions into the atmosphere and a ballast water management agreement to remove microorganisms from ballast water.
이와 같은 문제점 해결을 위한 기술개발이 요구되고, 이에 따라 선박의 배기가스처리장치 및 방법(공개번호 10-2015-0028136), 선박 평형수처리장치 및 방법(공개번호 10-2014-0108740) 등의 기술이 개발되어 특허출원으로 제시되고 있다.Technology development for solving such problems is required, and accordingly technologies such as a ship exhaust gas treatment device and method (Publication No. 10-2015-0028136), a ship ballast water treatment system and method (Publication No. 10-2014-0108740), etc. It has been developed and proposed as a patent application.
그리고, 근래에 와서, 액체연료유 대신 LNG등 천연가스 연료를 이용하는 선박건조가 제안되고 있다.And, in recent years, shipbuilding using natural gas fuel such as LNG instead of liquid fuel oil has been proposed.
그런데, 선박은 선내면적이 한정되고, 한정된 면적에서 평형수처리, 배기처리 장치를 각각 설치하게 되면 소요면적과 비용이 많이 소요되는 문제점을 가지고 있고, 천연가스를 연료로 이용하더라도 배출배기는 발생하게 된다. However, ships have a limited area on board, and if ballast water treatment and exhaust treatment devices are installed in a limited area, they have a problem of requiring a large area and cost, and even when using natural gas as fuel, exhaust emission occurs. .
본 발명은 선박의 연료유 연소과정에서 발생한 배출배기중에 함유된 이산화탄소(CO₂)를 극미세기포로 분해하여 평형수 수중에 토출확산시키며, 수중에 확산된 극미세기포는 고유의 작용에 의해 파열하면서 극한반응장(Hotspots)을 형성시키고, 극한반응장에서 물분자가 분해되어 수산기(OH-)가 생성되어 미생물을 사멸시키고, 배기중의 이산화탄소(CO₂)는 탄산수소칼슘(Ca(HCO3)2), 탄산수소마그네슘(Mg(HCO3)2) 등으로 합성되어 질소산화물(NOx), 황산화물(SOx) 등과 함께 수중에 용해되어, 평형수중의 미생물과 배출배기를 병합처리하는데 목적이 있다.The present invention decomposes carbon dioxide (CO₂) contained in the exhaust gas generated during the combustion of fuel oil in a ship into extremely fine foam and disperses it into the ballast water, while the extremely fine foam dispersed in water bursts due to its unique action. Hotspots are formed, water molecules are decomposed in extreme reaction fields, hydroxyl groups (OH-) are formed to kill microorganisms, and carbon dioxide (CO₂) in the exhaust is calcium hydrogen carbonate (Ca(HCO3)2), It is synthesized with magnesium hydrogen carbonate (Mg(HCO3)2) and dissolved in water with nitrogen oxides (NOx) and sulfur oxides (SOx).
그리고, 본 발명은 액체연료를 공기로 연소시킨 배출배기, 액체연료를 산소로 연소시킨 배출배기, 천연가스를 공기로 연소시킨 배출배기, 천연가스를 산소로 연소시킨 배출배기를 공히 처리할 수 있게 하는데 목적이 있다. In addition, the present invention enables to treat both the exhaust exhaust which combusts liquid fuel with air, the exhaust exhaust which combusts liquid fuel with oxygen, the exhaust exhaust which combusts natural gas with air, and the exhaust exhaust which combusts natural gas with oxygen. There is a purpose.
본 발명은 위의 과제해결을 위해, 선박내부에 아래와 같이 장치를 설치한다.In order to solve the above problems, the present invention is to install the device in the vessel as follows.
배기를 압축시키는 배기압축장치(C); 극미세기포를 생성시키는 1번 극미세기포발생장치(A)와 2번 극미세기포발생장치(B); 유입실(14), 반응실(15), 안정화실(16)로 구획되는 처리탱크(D); 가 주장치로 구성된다.An exhaust compressor (C) for compressing exhaust; A first micro-bubble generator (A) and a second micro-bubble generator (B) for generating micro-bubbles; A treatment tank (D) divided into an inflow chamber 14, a reaction chamber 15, and a stabilization chamber 16; Is composed of the main device.
배기압축장치(C)는 배기유입관(1)에 연결되고, 압축배기이송관(2)이 부설된다.The exhaust compression device (C) is connected to the exhaust inlet pipe (1), and a compressed exhaust transfer pipe (2) is attached.
1번 극미세기포발생장치(A)는 압축배기공급관(3)이 부설되어 개폐밸브(4)를 통해 압축배기이송관(2)에 연결되고, 반대측에서 처리탱크(D)로 연결되어 극미세배기기포수를 토출시키는 토출관(5)이 부설되며, 동일측에서 평형수공급관(6)이 부설되어 개폐밸브(7)를 통해서 평형수이송관(8)에 연결된다. The first ultra-fine foam generator (A) is provided with a compressed exhaust supply pipe (3), connected to the compressed exhaust transfer pipe (2) through an open/close valve (4), and connected to the processing tank (D) from the opposite side to provide a very fine exhaust. A discharge pipe (5) for discharging catcher is laid, and a ballast water supply pipe (6) is laid on the same side to be connected to the ballast water transfer pipe (8) through an open/close valve (7).
2번 극미세기포발생장치(B)는 압축배기공급관(3-1)이 부설되어 개폐밸브(4-1)를 통해서 압축배기이송관(2)에 연결되고, 반대측에서 처리탱크(D)로 연결되어 극미세배기기포수를 토출시키는 토출관(9)이 부설되며, 동일측에서 평형수공급관(6-1)이 부설되어 개폐밸브(7-1)을 통해서 평형수이송관(8)에 연결되고, The second ultrafine foam generator (B) is provided with a compressed exhaust supply pipe (3-1), connected to the compressed exhaust transfer pipe (2) through an open/close valve (4-1), and connected to the treatment tank (D) from the opposite side. The discharge pipe (9) for discharging the ultra-fine exhaust gas gun is laid, and the ballast water supply pipe (6-1) is laid on the same side, connected to the ballast water transfer pipe (8) through an on-off valve (7-1),
평형수이송관(8)은 유입측에서 2개의 관으로 분기되어 개폐밸브(17)과 개폐밸브(19)가 각각 부설되어 개폐밸브(17)에 평형수유입관(18), 개폐밸브(19)에 해수유입관(20)이 연결된다.The ballast water transfer pipe (8) is branched into two pipes at the inflow side, and an on/off valve (17) and an on/off valve (19) are respectively attached to the ballast water inlet pipe (18) and on/off valve (19). The seawater inflow pipe 20 is connected.
처리탱크(D)는 구획격판(12,13)에 의해서 유입실(14), 반응실(15), 안정화실(16)로 구획되며, 유입실(14)에는 평형수공급관(11)이 부설되어 개폐밸브(10)를 통해서 평형수이송관(8)에 연결되고, 1번 극미세기포발생장치(A)에 부설된 토출관(5)이 연결되며, 반응실(15)에는 2번 극미세기포발생장치(B)에 부설된 토출관(9)이 연결되고, 안정화실(16)에는 후미에 평형수배출관(22)에 연결되는 개폐밸브(21)와 바다로 향하는 해수방류관(24)에 연결된 개폐밸브(23)가 근접해서 부설되어 장치는 구성된다. The treatment tank (D) is divided into an inflow chamber (14), a reaction chamber (15), and a stabilization chamber (16) by partition plates (12, 13), and a ballast water supply pipe (11) is installed in the inflow chamber (14). Is connected to the ballast water transfer pipe 8 through the opening/closing valve 10, the discharge pipe 5 attached to the first microscopic bubble generation device A is connected, and the reaction chamber 15 has the second microscopic strength The discharge pipe (9) attached to the gun generator (B) is connected, and to the stabilization chamber (16) is connected to the on/off valve (21) connected to the ballast water discharge pipe (22) at the rear and the seawater discharge pipe (24) facing the sea. The connected opening/closing valve 23 is laid in close proximity so that the device is constructed.
위에서, 평형수는 해수 또는 담수가 평형수탱크에 저장된 물을 말하며, 평형수는 해수로 한정하지 않고 담수로 대체시켜 이용할 수 있다.Above, the ballast water refers to the water stored in the ballast water or fresh water tank, the ballast water is not limited to sea water and can be used by replacing it with fresh water.
위에서, 해수유입관(20) 과 해수방류관(24)은 평형수 공급이 어려울 때 해수를 유입시켜 배출배기를 해수에 용해시켜 바다의 해수중으로 방류시키게 된다.In the above, the seawater inflow pipe 20 and the seawater discharge pipe 24 inflow the seawater when it is difficult to supply the ballast water and dissolve the discharged exhaust into the seawater to discharge it into the seawater.
이하에서 장치의 작용에 대하여 설명한다.Hereinafter, the operation of the device will be described.
선박의 평형수탱크로부터 처리탱크(D)에 평형수가 공급되어 만재되고, 1번과 2번 극미세기포발생장치에 평형수가 공급되어 장치가 작동되는 단계;A step in which the ballast water is supplied from the ballast water tank of the ship to the treatment tank (D) and loaded, and the ballast water is supplied to the first and second ultra-fine foam generators to operate the apparatus;
1번과 2번 극미세기포발생장치의 작동에 의해서 평형수는 8기압 이상으로 가압되고, 배기압축장치로부터 압축배기가 압입되어 미세하게 분해되는 과정을 거쳐 극미세배기기포수로 가공되는 단계;Ballast water is pressurized to 8 atmospheres or more by the operation of the ultrafine foam generators 1 and 2, and the compressed exhaust is pressurized from the exhaust compressor to finely decompose and processed into ultrafine exhaust gunners;
1번, 2번 극미세기포발생장치(A,B)로부터 8기압 이상의 고압으로 가압된 극미세배기기포수가 처리탱크의 유입실 및 반응실 수중에 상압으로 각각 토출되어 확산되는 단계; Steps 1 and 2 of the ultra-fine air bubble generation devices A and B, which are pressurized at a high pressure of 8 atmospheres or more, are discharged and diffused at normal pressure in the inlet chamber and the reaction chamber of the treatment tank, respectively;
유입실 및 반응실 수중에 토출된 극미세배기기포는 수축하고 축소되어 파열되면서 극미세배기기포 경계면에 극한반응장(Hotspots)이 형성되는 단계;A step of forming extreme reaction fields (Hotspots) on the interface of the ultrafine exhaust gas bubbles as the microscopic exhaust air bubbles discharged into the inlet and reaction chambers shrink and shrink and rupture;
극한반응장(Hotspots)에서 물분자(H₂O)가 수소이온(H+), 수산기(OH-)로 분해되어 수중의 미생물을 사멸시키는 단계;Water molecules (H₂O) are decomposed into hydrogen ions (H+) and hydroxyl groups (OH-) in extreme reaction fields (Hotspots) to kill microorganisms in water;
극미세배기기포의 파열에 의해서 이산화탄소(CO₂)는 수중의 칼슘(Ca), 마그네슘(Mg)등의 무기물과 반응하여 탄산수소칼슘(Ca(HCO3)2), 탄산수소마그네슘(Mg(HCO3)2) 등으로 결합되어 수중에 용해되는 단계;Carbon dioxide (CO₂) is reacted with inorganic substances such as calcium (Ca) and magnesium (Mg) in water by rupture of the ultrafine air bubbles, calcium hydrogen carbonate (Ca(HCO3)2), magnesium hydrogen carbonate (Mg(HCO3)2 ) And dissolved in water;
미생물이 사멸되고, 이산화탄소(CO₂)가 용해된 평형수가 배출관을 통해서 선박의 평형수탱크로 배출되는 단계;A step in which the microorganisms are killed and the ballast water in which carbon dioxide (CO₂) is dissolved is discharged to the ballast tank of the ship through the discharge pipe;
위와 같은 단계를 거치면서 평형수중의 미생물의 사멸과 이산화탄소(CO₂)는 병합처리 된다.Through the above steps, the killing of microorganisms and carbon dioxide (CO₂) in the ballast water are combined.
위에서, 평형수가 감소하여 공급이 부족할 때는 해수유입관을 통해 해수를 유입하여 위와 같은 단계를 거쳐서 해수방류관을 통해 바다의 해수중으로 방류시킨다. In the above, when the supply of water is insufficient due to a decrease in the ballast water, the seawater is introduced through the seawater inflow pipe and then discharged into the seawater through the seawater discharge pipe through the above steps.
본 발명은 평형수중의 미생물을 사멸시키면서 이산화탄소를 함유한 연소배기를 수중에 용해시키는 병합처리를 행함으로서 비용절감은 물론, 생태계 보호와 이산화탄소의 대기중 배출을 방지하여 지구온난화 방지에 기여할 수 있게 된다.The present invention is capable of contributing to the prevention of global warming by protecting the ecosystem and preventing the emission of carbon dioxide into the atmosphere by reducing costs by performing a combined treatment of dissolving the combustion exhaust gas containing carbon dioxide in water while killing microorganisms in the ballast water.
도 1은 장치의 연결 평면도이다.1 is a connection plan view of a device.
본 발명은 도면상에서 구체적인 설명을 한다.The present invention will be described in detail on the drawings.
도 1은 장치의 연결 평면도로서, A는 1번 극미세기포발생장치, B는 2번 극미세기포발생장치이며, C는 배기압축장치, D는 처리탱크이다.Figure 1 is a connection plan view of the device, A is the first micro-bubble generator, B is the second micro-bubble generator, C is the exhaust compression device, D is the treatment tank.
1번 극미세기포발생장치(A)는 압축배기공급관(3)이 부설되어 개폐밸브(4)를 통해서 압축배기이송관(2)에 연결되어 배기압축장치(C)로부터 압축배기를 공급받게 되고, 반대측에는 극미세배기기포수를 토출시키는 토출관(5)이 부설되어 처리탱크(D)의 유입실(14)로 연결되며, 평형수를 공급하는 평형수공급관(6)이 부설되어 개폐밸브(7)를 통해서 평형수이송관(8)에 연결되어 평형수를 공급받게 된다.Compressed exhaust supply pipe (3) is attached to the first ultrafine foam generator (A) and is connected to the compressed exhaust transfer pipe (2) through an open/close valve (4) to receive compressed exhaust from the exhaust compression system (C), On the opposite side, a discharge pipe (5) for discharging ultra-fine exhaust gas catchers is connected to the inlet chamber (14) of the treatment tank (D), and a ballast water supply pipe (6) for supplying ballast water is installed to open and close the valve (7). ) Is connected to the ballast water transfer pipe (8) to receive the ballast water.
2번 극미세기포발생장치(B)는 압축배기공급관(3-1)이 부설되어 개폐밸브(4-1)를 통해서 압축배기이송관(2)으로 연결되어 압축배기를 공급받고, 반대측에 극미세배기기포수를 토출시키는 토출관(9)이 부설되어 처리탱크(C)의 반응실(15)로 연결되며, 평형수를 공급하는 평형수공급관(6-1)이 부설되어 개폐밸브(7-1)를 통해서 평형수이송관(8)에 연결되어 평형수를 공급받게 된다.Compressed exhaust supply pipe (3-1) is attached to the second ultrafine foam generator (B), which is connected to the compressed exhaust transfer pipe (2) through an open/close valve (4-1) to receive compressed exhaust, and is extremely fine to the opposite side. A discharge pipe (9) for discharging the device catcher is attached to the reaction chamber (15) of the treatment tank (C), and a ballast water supply pipe (6-1) for supplying ballast water is installed to open and close a valve (7-1) ) Is connected to the ballast water transfer pipe (8) to receive the ballast water.
위에서, 개폐밸브(7-1)에 연결된 평형수이송관(8)은 유입측에서 두개의 관으로 분기되어 개폐밸브(17)과 개폐밸브(19)가 부설되어 개폐밸브(17)에 평형수유입관(18)이 연결되고, 개폐밸브(19)에 해수유입관(20)이 연결되며, 평형수의 공급이 어려울 때, 해수유입관을 통해 해수를 유입시키게 된다.Above, the ballast water transfer pipe 8 connected to the on-off valve 7-1 is branched into two pipes at the inflow side, and the on-off valve 17 and the on-off valve 19 are attached to the ballast water inlet pipe to the on-off valve 17 (18) is connected, the seawater inlet pipe (20) is connected to the on-off valve (19), and when the supply of ballast water is difficult, the seawater is introduced through the seawater inlet pipe.
위에서, 평형수는 평형수탱크에 저장된 상태의 물을 말하며, 해수, 담수 구별없이 평형수로 이용될 수 있다.Above, the ballast water refers to the water stored in the ballast tank, and can be used as ballast water without distinction between sea water and fresh water.
위에서, 평형수유입관(18)은 도시되지 않았지만 선박의 평형수탱크로 연결되며, 해수유입관(20)은 바다의 해수중으로 연결된다.Above, the ballast water inlet pipe 18 is not shown, but is connected to the ballast water tank of the ship, and the sea water inlet pipe 20 is connected into the sea water of the sea.
위에서, 개폐밸브(17)은 평형수유입시에 개방되고 해수유입시에 폐쇄되며, 반대로 개폐밸브(19)는 평형수 유입시에는 폐쇄되고 해수유입시에 개방되어 평형수유입과 해수유입을 선택하게 된다.In the above, the on-off valve 17 is opened at the time of ballast water inflow and closed at the time of seawater inflow, and on the contrary, the on-off valve 19 is closed at the time of ballast water inflow and is opened at the time of seawater inflow to select the ballast water and seawater inflow. do.
위에서, 1번, 2번 극미세기포발생장치(A,B)는 한국 특허청에 등록된 극미세기포발생장치(10-1022612)의 장치가 이용되며, 장치는 가압펌프, 금구가 내장된 혼합관, 구경을 달리하면서 수축 및 팽창을 행하는 복수의 관으로 구성되고, 액체와 기체를 혼합, 가압, 분쇄, 팽창, 충돌, 선회를 반복하면서 분자집단(Cluster)을 극히 미세한 기포로 분해시키는 작용을 행한다. Above, No. 1 and No. 2 micro-bubble generators (A, B) are devices of the micro-bubble generators (10-1022612) registered with the Korean Intellectual Property Office, and the devices are pressurized pumps, mixing pipes equipped with brackets It is composed of a plurality of tubes that contract and expand while varying the diameter, and it functions to decompose a cluster of molecules into extremely fine bubbles while repeating mixing, pressurization, crushing, expansion, collision, and turning of liquid and gas. .
위에서, 1번, 2번 극미세기포발생장치(A,B)는 제시된 극미세기포발생장치(10-1022612)보다 우수한 장치로 대체시킬 수도 있다.Above, No. 1 and No. 2 micro-bubble generators (A, B) may be replaced with devices superior to the suggested micro-bubble generators (10-1022612).
위에서, 극히 미세하게 분해된 극미세기포는 수중에서 수축되면서 축소가 진행되어 한계점에 도달하면 파열하게 되고, 파열시에는 극미세기포 외주면에 극한반응장(Hotspots)을 형성시키며, 이 극한반응장에 존재하는 물질을 분해시키게 되고, 이 때 물분자도 수소이온(H+), 수산기(OH-)로 분해된다. From the top, the microscopically disintegrated microscopic micropore shrinks while shrinking in water and bursts when it reaches the limit, and when it bursts, it forms hot spots on the outer peripheral surface of the micro micropore and exists in this extreme reaction field. The substance to be decomposed is decomposed, and the water molecules are also decomposed into hydrogen ions (H+) and hydroxyl groups (OH-).
위에서, 극미세기포는 나노사이즈(nano size)의 기포를 말한다.Above, the ultra-fine century bubble refers to a nano-sized bubble.
배기압축장치(C)는 유입되는 배기의 냉각과 여과를 시키는 설비를 서로 연결하여 일체화시키고, 배기유입관(1)과 압축배기이송관(2)이 부설되고, 배기유입관(1)은 선박 배기발생원의 배출관으로 연결되어 연소배기를 유입시키며, 유입되는 배기를 8기압 이상의 고압으로 압축시켜 압축배기이송관(2)을 통해서 1번, 2번 극미세기포발생장치(A,B)에 공급하게 된다. Exhaust compression device (C) is integrated to connect the equipment for cooling and filtering of the incoming exhaust, and the exhaust inlet pipe (1) and the compressed exhaust transfer pipe (2) is attached, the exhaust inlet pipe (1) is the ship exhaust It is connected to the discharge pipe of the source to introduce combustion exhaust, and compresses the incoming exhaust gas at a high pressure of 8 atmospheres or more to supply it to the first and second ultrafine foam generators (A, B) through the compressed exhaust transfer pipe (2).
위에서, 배기는 액체연료를 공기로 연소시킨 배출배기, 액체연료를 산소로 연소시킨 배출배기, 천연가스를 공기로 연소시킨 배출배기, 천연가스를 산소로 연소시킨 배출배기 등으로 구분 될 수 있고, 액체연료, 천연가스 연료 공히 공기 대신 산소로 연소시키면 공기중에 함유된 질소량 만큼 배기는 감소하게 되고, 특히 천연가스를 산소로 연소시키면 배출배기는 크게 감소하게 되어, 배기압축장치(C)는 소형화할 수 있다. 따라서, 배기압축장치(C)의 크기는 배출배기량에 따라 조정하여 구성한다.In the above, the exhaust can be divided into an exhaust exhaust in which liquid fuel is combusted with air, an exhaust exhaust in which liquid fuel is combusted with oxygen, an exhaust exhaust in which natural gas is combusted with air, an exhaust exhaust in which natural gas is combusted with oxygen, and the like. When liquid fuel and natural gas fuel are burned with oxygen instead of air, the exhaust is reduced by the amount of nitrogen contained in the air. In particular, when the natural gas is burned with oxygen, the exhaust exhaust is greatly reduced, and the exhaust compressor (C) can be miniaturized. Can be. Therefore, the size of the exhaust compression device (C) is configured by adjusting according to the amount of exhaust exhaust.
본 발명은 액체연료를 공기로 연소시킨 배출배기, 액체연료를 산소로 연소시킨 배출배기, 천연가스를 공기로 연소시킨 배출배기, 천연가스를 산소로 연소시킨 배출배기를 공히 처리할 수 있다. The present invention can treat both the exhaust exhaust which combusts liquid fuel with air, the exhaust exhaust which combusts liquid fuel with oxygen, the exhaust exhaust which combusts natural gas with air, and the exhaust exhaust which combusts natural gas with oxygen.
처리탱크(D)는 구획격판(12,13)에 의해서 유입실(14), 반응실(15), 안정화실(15)로 구획되고, 구획격판(12,13)은 유입되는 평형수가 상부측으로 원활하게 월류할 수 있게 높이가 조정되며, 하부에는 도시되지 않은 드레인관이 부설된다.The treatment tank (D) is divided into an inlet chamber (14), a reaction chamber (15), and a stabilization chamber (15) by the partition plates (12, 13), and the partition plates (12, 13) have a ballast water flowing in to the upper side. The height is adjusted to smoothly flow, and a drain pipe (not shown) is provided at the bottom.
위에서, 유입실(14)에는 1번 극미세기포발생장치(B)의 토출관(5)이 연결되고, 평형수공급관(11)이 부설되어 개폐밸브(10)을 통해 평형수이송관(8)에 연결되며, 반응실(15)에는 2번 극미세기포발생장치(B)의 토출관(9)이 연결되고, 안정화실(16) 후미에 개폐밸브(21)와 개폐밸브(23)가 부설되어 개폐밸브(21)에 평형수탱크로 연결되는 평형수배출관(22), 개폐밸브(23)에 바다로 향하는 해수방류관(24)이 각각 연결된다.Above, the inlet chamber 14 is connected to the discharge pipe 5 of the first micro-strength bubble generating device B, and a ballast water supply pipe 11 is attached to the ballast water transfer pipe 8 through the on-off valve 10. Connected to the reaction chamber 15, the discharge pipe 9 of the second ultra-fine foam generator B is connected, and the stabilization chamber 16 is provided with an on-off valve 21 and an on-off valve 23. The open/close valve 21 is connected to a ballast water discharge pipe 22 connected to a ballast water tank and a seawater discharge pipe 24 directed to the sea to the open/close valve 23, respectively.
위에서, 유입실(14)과 반응실(15)에는 1번, 2번 극미세기포발생장치(A,B)에서 극미세배기기포수가 토출되어 확산된다.In the above, the ultra-fine exhaust air bubbles are discharged from the first and second ultra-fine bubble generators A and B in the inlet chamber 14 and the reaction chamber 15, and are diffused.
위에서, 해수유입관(20)을 연결하고 있는 개폐밸브(19)와 해수방류관(24)을 연결하고 있는 개폐밸브(23)는 평형수가 유입될 때는 폐쇄되고, 해수를 유입시킬 때 개방되고, 개폐밸브(17)과 개폐밸브(21)는 폐쇄된다.Above, the on-off valve 19 connecting the seawater inlet pipe 20 and the on-off valve 23 connecting the seawater discharge pipe 24 are closed when the ballast water is introduced, and open when the seawater is introduced, The on-off valve 17 and the on-off valve 21 are closed.
위에서, 해수의 유입은 선박에 평형수 보유량이 소량으로 감소하거나, 또는 평형수를 이용할 수 없을 때 유입시키며, 평형수 유입 때와 동일한 처리 단계를 거쳐 이산화탄소를 함유한 배출배기를 해수에 용해시켜 바다의 해수중으로 방류하게 된다.In the above, the inflow of seawater is reduced to a small amount of the ballast water in the ship or when the ballast water is not available, and the exhaust gas containing carbon dioxide is dissolved in the seawater through the same treatment steps as the ballast water inflow. It is discharged into the sea water.
이하 본 발명의 작용에 대하여 설명한다 Hereinafter, the operation of the present invention will be described.
먼저, 장치를 작동시켜 유입실(14), 반응실(15), 안정화실(16)에 평형수가 유입되어 만재되면서 안정화실(16)의 평형수배출관(22)에서 평형수가 배출되도록 조정한다.First, the apparatus is operated to adjust the ballast water to be discharged from the ballast water discharge pipe 22 of the stabilization chamber 16 while the ballast water flows into the inlet chamber 14, the reaction chamber 15, and the stabilization chamber 16.
그리고, 유입실(14)과 반응실(15)에는 1번, 2번 극미세기포발생장치(A,B)로부터 극미세배기기포수가 토출되어 확산되고, 유입실(14)과 반응실(15)에 확산된 극미세배기기포는 수축이 진행되면서 축소되어 한계점에 도달하여 파열되며, 파열되는 극미세배기기포의 외측면 경계면에는 극한반응장(Hotspots)이 형성되고, 극한반응장에 존재하는 물은 수소이온(H+)과 수산기(OH-)로 분해되며, 이 수산기(OH-)는 미생물의 세포를 공격하여 미생물을 사멸시키게 된다.Then, the inlet chamber 14 and the reaction chamber 15 are discharged and diffused by the ultra-fine exhaust air bubbles from the first and second ultra-fine bubble generators A and B, and the inlet chamber 14 and the reaction chamber 15 The micro-exhaust air bubbles diffused in) are shrunk as shrinkage progresses to reach the limit and rupture, and extreme reaction fields (hotspots) are formed at the boundary surface of the micro-exhaust air bubbles that burst, and water present in the extreme reaction field Silver decomposes into hydrogen ions (H+) and hydroxyl groups (OH-), which attack microorganism cells and kill microorganisms.
다음으로, 유입실(14)과 반응실(15)에 확산된 극미세배기기포에 함유된 이산화탄소(CO₂)는 해수중에 함유된 칼슘(Ca), 마그네슘(Mg) 등의 무기물과 결합하여 탄산칼슘(Ca(CO₃)), 탄산수소칼슘(Ca(HCO₃)₂), 또는 탄산마그네슘(Mg(CO₃)), 탄산수소마그네슘(Mg(HCO3)2)으로 결합되어 질소산화물(NOx), 황산화물(SOx) 등과 함께 안정화실(16)의 평형수배출관(22)을 통해 배출되어 평형수탱크로 유입된다. Next, the carbon dioxide (CO₂) contained in the ultra-fine exhaust gas diffused in the inflow chamber 14 and the reaction chamber 15 is combined with inorganic substances such as calcium (Ca) and magnesium (Mg) contained in sea water to form calcium carbonate. (Ca(CO₃)), calcium hydrogen carbonate (Ca(HCO₃)₂), or magnesium carbonate (Mg(CO₃)), magnesium hydrogen carbonate (Mg(HCO3)2), combined with nitrogen oxide (NOx), sulfur oxide ( SOx) and the like is discharged through the ballast water discharge pipe 22 of the stabilization chamber 16 and flows into the ballast water tank.
한편, 평형수를 이용할 수 없을 때, 해수를 유입시켜도 평형수처리와 동일한 처리단계를 거치면서 배기를 해수중에 용해시켜 바다의 해수중으로 방류한다.On the other hand, when the ballast water is not available, the exhaust gas is dissolved in the seawater and discharged into the seawater while passing through the same treatment steps as the ballast water treatment even when the seawater is introduced.
본 발명은 평형수중의 미생물을 사멸시키면서 이산화탄소(CO₂)를 수중에 용해시키는 병합처리를 행하여 비용을 절감시키고, 평형수방류에 의한 생태계교란을 방지하면서 대기중으로 이산화탄소(CO₂)의 배출이 방지되어 지구온난화 예방에 기여하게 된다. The present invention reduces the cost by performing a combined treatment of dissolving carbon dioxide (CO₂) in water while killing microorganisms in the ballast water, while preventing the ecological disturbance caused by the discharge of ballast water while preventing the emission of carbon dioxide (CO₂) into the atmosphere. It will contribute to the prevention of warming.
본 발명에서 선박의 평형수는 해수로 한정하지 않으며, 무기물질을 함유한 담수도 평형수로 이용할 수 있다. In the present invention, the ballast water of the ship is not limited to seawater, and fresh water containing inorganic materials can also be used as ballast water.
본 발명은 선박에 한정되지 않고, 연소배기를 발생시키는 모든 연소장치에 이용이 가능하다.The present invention is not limited to a ship, and can be used for any combustion device that generates combustion exhaust.

Claims (3)

  1. 배기유입관(1)에 연결되고, 압축배기이송관(2)이 부설된 배기압축장치(C); An exhaust compression device (C) connected to the exhaust inlet pipe (1) and provided with a compressed exhaust transfer pipe (2);
    압축배기공급관(3)이 부설되어 개폐밸브(4)를 통해 압축배기이송관(2)에 연결되고, 반대측에서 처리탱크(D)로 연결되는 토출관(5)이 부설되며, 동일측에서 평형수 공급관(6)이 부설되어 개폐밸브(7)를 통해서 평형수이송관(8)에 연결된 1번 극미세기포발생장치(A); Compressed exhaust supply pipe (3) is laid and connected to the compressed exhaust transfer pipe (2) through an open/close valve (4), and discharge pipe (5) connected to the treatment tank (D) on the opposite side is laid, and the ballast water is provided on the same side. No. 1 ultra-fine-strength generator (A) connected to the ballast water transfer pipe (8) through the on-off valve (7) is provided with a supply pipe (6);
    압축배기공급관(3-1)이 부설되어 개폐밸브(4-1)를 통해서 압축배기이송관(2)에 연결되고, 반대측에서 처리탱크(D)로 연결되는 토출관(9)이 부설되고, 동일측에서 평형수공급관(6-1)이 부설되어 개폐밸브(7-1)를 통해서 평형수이송관(8)에 연결된 2번 극미세기포발생장치(B); Compressed exhaust supply pipe (3-1) is laid and connected to the compressed exhaust transfer pipe (2) through an open/close valve (4-1), and the discharge pipe (9) connected to the treatment tank (D) from the opposite side is laid, and is the same A ballast water supply pipe (6-1) on the side is attached to the ballast water supply pipe (8) connected to the ballast water transfer pipe (8) through an on-off valve (7-1) (B);
    유입측에서 2개의 관으로 분기되어 개폐밸브(17)과 개폐밸브(19)에 각각 연결되고, 개폐밸브(17)에 선박의 평형수탱크로 연결되는 평형수유입관(18), 개폐밸브(19)에 바다로 향하는 해수유입관(20)이 연결된 평형수이송관(8);A ballast water inlet pipe (18) and an on-off valve (19) branched into two pipes at the inlet side and connected to the on-off valve (17) and the on-off valve (19), respectively, and connected to the on-off valve (17) to the ballast water tank of the ship ) Is connected to the sea water inlet pipe 20 is connected to the ballast water transfer pipe (8);
    구획격판(12,13)에 의해서 유입실(14), 반응실(15), 안정화실(16)로 구획되며, 유입실(14)에는 평형수공급관(11)이 부설되어 개폐밸브(10)를 통해서 평형수이송관(8)에 연결되고, 1번 극미세기포발생장치(A)에 부설된 토출관(5)이 연결되며, 반응실(15)에는 2번 극미세기포발생장치(B)에 부설된 토출관(9)이 연결되고, 안정화실(16)에는 후미에 평형수배출관(22)에 연결되는 개폐밸브(21)와 해수방류관(24)에 연결된 개폐밸브(23)가 근접 부설된 처리탱크(D); 가 서로 연결되어 구성되는 것을 특징으로 하는 선박의 배출배기와 평형수 병합처리장치.The partition plate (12, 13) is divided into an inlet chamber (14), a reaction chamber (15), and a stabilization chamber (16), and an inlet chamber (14) is provided with a ballast water supply pipe (11) to open and close a valve (10). It is connected to the ballast water transfer pipe (8), the discharge pipe (5) attached to the first microscopic bubble generator (A) is connected, the reaction chamber (15) is the second microscopic bubble generator (B) The discharge pipe (9) laid in the connection, the stabilization chamber (16) is connected to the on-off valve (21) connected to the ballast water discharge pipe (22) at the rear and the open/close valve (23) connected to the seawater discharge pipe (24) Treated tank (D); Combined discharge device and ballast water treatment device, characterized in that is configured to be connected to each other.
  2. 배기를 압축시키는 배기압축장치(C); 극미세기포를 생성시키는 1번 극미세기포발생장치와 2번 극미세기포발생장치; 유입실(14), 반응실(15), 안정화실(16)로 구획되는 처리탱크(D); 가 소요의 연결관으로 연결되어 구성되는 장치에서,An exhaust compressor (C) for compressing exhaust; A first micro-bubble generator and a second micro-bubble generator for generating micro-bubbles; A treatment tank (D) divided into an inflow chamber 14, a reaction chamber 15, and a stabilization chamber 16; In the device consisting of connected with the connector of the disturbance,
    선박의 평형수탱크로부터 처리탱크에 평형수가 공급되어 만재되고, 1번과 2번 극미세기포발생장치에 평형수가 공급되어 장치가 작동되는 단계; A step in which the ballast water is supplied from the ballast water tank of the ship to the treatment tank to be loaded, and the ballast water is supplied to the 1st and 2nd ultrafine foam generators to operate the apparatus;
    1번과 2번 극미세기포발생장치의 작동에 의해서 평형수는 8기압 이상으로 가압되고, 배기압축장치로부터 압축배기가 압입되어 미세하게 분해되는 과정을 거쳐 극미세배기기포수로 가공되는 단계; Ballast water is pressurized to 8 atmospheres or more by the operation of the ultrafine foam generators 1 and 2, and the compressed exhaust is pressurized from the exhaust compressor to finely decompose and processed into ultrafine exhaust gunners;
    1번, 2번 극미세기포발생장치(A,B)로부터 8기압 이상의 고압으로 가압된 극미세배기기포수가 처리탱크의 유입실 및 반응실 수중에 상압으로 각각 토출되어 확산되는 단계; Steps 1 and 2 of the ultra-fine air bubble generation devices A and B, which are pressurized at a high pressure of 8 atmospheres or more, are discharged and diffused at normal pressure in the inlet chamber and the reaction chamber of the treatment tank, respectively;
    유입실 및 반응실 수중에 토출된 극미세배기기포는 수축하고 축소되어 파열되면서 극미세배기기포 경계면에 극한반응장(Hotspots)이 형성되는 단계; A step of forming extreme reaction fields (Hotspots) on the interface of the ultrafine exhaust gas bubbles as the microscopic exhaust air bubbles discharged into the inlet and reaction chambers shrink and shrink and rupture;
    극한반응장(Hotspots)에서 물분자(H₂O)가 수소이온(H+), 수산기(OH-)로 분해되어 수중의 미생물을 사멸시키는 단계; Water molecules (H₂O) are decomposed into hydrogen ions (H+) and hydroxyl groups (OH-) in extreme reaction fields (Hotspots) to kill microorganisms in water;
    극미세배기기포의 파열에 의해서 이산화탄소(CO₂)는 수중의 칼슘(Ca), 마그네슘(Mg) 무기물과 반응하여 탄산수소칼슘(Ca(HCO3)2), 탄산수소마그네슘(Mg(HCO3)2) 으로 결합되어 수중에 용해되는 단계; The carbon dioxide (CO₂) reacts with calcium (Ca) and magnesium (Mg) minerals in water by the rupture of the ultra-fine exhaust air bubbles, resulting in calcium hydrogen carbonate (Ca(HCO3)2) and magnesium hydrogen carbonate (Mg(HCO3)2). Combined and dissolved in water;
    미생물이 사멸되고, 이산화탄소(CO₂)가 용해된 평형수가 배출관을 통해서 선박의 평형수탱크로 배출되는 단계; 를 거치면서 평형수중의 미생물의 사멸과 이산화탄소(CO₂)의 수중 용해처리를 병합처리하는 것을 특징으로 하는 선박의 배출배기와 평형수 병합처리방법.A step in which the microorganisms are killed and the ballast water in which carbon dioxide (CO₂) is dissolved is discharged to the ballast tank of the ship through the discharge pipe; A method of combining discharge and ballast of a ship, characterized in that the treatment of the destruction of microorganisms in the ballast water and the dissolution treatment of carbon dioxide (CO₂) in water are combined.
  3. 제 2항에 있어서, 선박의 평형수 이용이 불가능시에 해수를 유입시켜 평형수처리와 동일한 처리단계를 거쳐 이산화탄소(CO₂)를 함유한 배출배기를 해수에 용해시켜 바다의 해수로 방류시키는 것을 특징으로 하는 선박의 배출배기와 평형수 병합처리방법.The method according to claim 2, characterized in that when the ballast water of the ship is not available, the seawater is introduced and the exhaust gas containing carbon dioxide (CO₂) is dissolved in the seawater through the same treatment steps as the ballast water treatment, and discharged into the seawater. The combined discharge and ballast water treatment method of the vessel.
PCT/KR2019/018427 2019-01-01 2019-12-24 Apparatus and method for treating ship exhaust gas in combination with ballast water WO2020141791A1 (en)

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KR200141776Y1 (en) * 1997-02-15 1999-04-01 손을택 Microbubble generator for water treatment
KR101240305B1 (en) * 2012-11-08 2013-03-07 이춘우 Water treatment method and apparatus of ballast tank
KR20140057779A (en) * 2012-11-05 2014-05-14 주식회사 칼라카나 Water treatment apparatus of ballast tank
KR101563179B1 (en) * 2014-11-19 2015-10-27 한국해양과학기술원 The bypass line through type electrolysis ballast water treatment method and device designed to disinfect fresh water and seawater
KR101757766B1 (en) * 2015-10-26 2017-07-17 한국해양과학기술원 High efficiency ballast water treatment system using co2 and ozone micro-bubbles and treatment method thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200141776Y1 (en) * 1997-02-15 1999-04-01 손을택 Microbubble generator for water treatment
KR20140057779A (en) * 2012-11-05 2014-05-14 주식회사 칼라카나 Water treatment apparatus of ballast tank
KR101240305B1 (en) * 2012-11-08 2013-03-07 이춘우 Water treatment method and apparatus of ballast tank
KR101563179B1 (en) * 2014-11-19 2015-10-27 한국해양과학기술원 The bypass line through type electrolysis ballast water treatment method and device designed to disinfect fresh water and seawater
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