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WO2020050477A1 - Wet scrubber for ship, and composite cleaning water spray system inside absorption tower, including same - Google Patents

Wet scrubber for ship, and composite cleaning water spray system inside absorption tower, including same Download PDF

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Publication number
WO2020050477A1
WO2020050477A1 PCT/KR2019/006371 KR2019006371W WO2020050477A1 WO 2020050477 A1 WO2020050477 A1 WO 2020050477A1 KR 2019006371 W KR2019006371 W KR 2019006371W WO 2020050477 A1 WO2020050477 A1 WO 2020050477A1
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WO
WIPO (PCT)
Prior art keywords
absorption tower
flue gas
filler
washing water
cleaning water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/KR2019/006371
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French (fr)
Korean (ko)
Inventor
김근배
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Hiair Korea Co Ltd
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Hiair Korea Co Ltd
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Filing date
Publication date
Application filed by Hiair Korea Co Ltd filed Critical Hiair Korea Co Ltd
Publication of WO2020050477A1 publication Critical patent/WO2020050477A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/04Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust using liquids
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/037Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of inertial or centrifugal separators, e.g. of cyclone type, optionally combined or associated with agglomerators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/0807Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents
    • F01N3/0828Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents characterised by the absorbed or adsorbed substances
    • F01N3/085Sulfur or sulfur oxides
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N2570/00Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
    • F01N2570/04Sulfur or sulfur oxides
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N2590/00Exhaust or silencing apparatus adapted to particular use, e.g. for military applications, airplanes, submarines
    • F01N2590/02Exhaust or silencing apparatus adapted to particular use, e.g. for military applications, airplanes, submarines for marine vessels or naval applications
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/14Arrangements for the supply of substances, e.g. conduits
    • F01N2610/1433Pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/14Arrangements for the supply of substances, e.g. conduits
    • F01N2610/1453Sprayers or atomisers; Arrangement thereof in the exhaust apparatus

Definitions

  • the present invention relates to a wet scrubber system for ships, after the flue gas sucked through the suction port at the bottom of the absorption tower passes through the first filling material and the second filling material after passing through the quenching process, it goes up toward the flue gas outlet.
  • the washing water spray method in the upper space of the second filler is a combination of counter-current and counter-current methods. It relates to a method of spraying the washing water inside the absorption tower to which the spraying method is applied.
  • the toxic substances contained in the flue gas discharged from ships are not only harmful to the human body, but also cause environmental pollution when discharged into the atmosphere without filtration, especially sulfur compounds (sulfur oxides) contained in flue gas.
  • the oxide of sulfur (S) is collectively called, but mainly SO2 (sulfur dioxide) and SO3 (sulfur trioxide) are both produced when fuel containing sulfur or sulfur is burned, but in general, there are many SO2 in the exhaust gas. It must be removed.
  • flue gas treatment devices are installed in the flue gas line of the vessel to desulfurize the ship flue gas and discharge it into the atmosphere.
  • a wet scrubber system for ships is used to treat such flue gas.
  • Korean Registered Patent No. 10-1804418 sprays washing water onto flue gas containing contaminants, and dissolves the contaminants of flue gas by contacting the contaminants with droplets, liquid films, and bubbles generated therefrom, or It relates to a wet scrubber system for collecting vessels.
  • the wet scrubber system for ships is an absorption tower that absorbs and treats pollutants of flue gas by spraying washing water, a washing water treatment system that processes the washing water discharged after absorbing pollutants, and each system while operating the scrubber system. It consists of three parts: a control system that monitors and controls functions.
  • the absorption tower is a core device of a wet scrubber system, and there are various types, in particular, a packing material is installed inside the absorption tower so that the pollutants of flue gas are absorbed in the washing water sprayed on the filling material, Alternatively, a method of removing pollutants from the flue gas by spraying the washing water directly into the flue gas is used.
  • an object of the present invention is to provide a wet scrubber for a ship which has improved the efficiency of removing sulfur compounds from a ship exhaust gas and a complex type washing water injection system including an absorption tower.
  • the present invention is provided with an intake port through which the flue gas is sucked, and after the pollutants contained in the flue gas are absorbed, the exhaust gas from which the pollutants are absorbed is discharged.
  • the absorption tower has a pollutant absorption space therein;
  • a first filler and a second filler which are installed at intervals of upper / lower in the absorption tower to sequentially absorb sulfur compounds contained in flue gas passing through the absorption tower;
  • a supply line connected to the absorption tower and including a plurality of injection nozzles and a supply pump to supply / inject cleaning water into the absorption tower; It is installed in the interior of the absorption tower and the upper portion of the suction port, the center is formed in a conical shape inclined upward to include an inflow prevention portion to prevent the inflow of cleaning water to the suction port, the supply line of the first filler
  • a first injection nozzle module connected to a pipe located at an upper portion and having a plurality of injection nozzles for spraying cleaning
  • outlet and the first injection nozzle module further comprises a gas-liquid separation device for inducing rotation in the flow of gas in a linear direction to separate gas and liquid by using centrifugal force to discharge only gas to the outlet. do.
  • the bottom side of the absorption tower is characterized in that the washing water sprayed by the injection nozzle module absorbs and removes the sulfur compound contained in the flue gas, and then discharges to the outside of the absorption tower.
  • FIG. 1 is a schematic view showing a wet scrubber for a ship according to the present invention and a complex type washing water injection system inside the absorption tower including the same.
  • Figure 2 is an enlarged view showing a part of the structure in the wet scrubber for ships according to the present invention and the complex type washing water injection system including the absorption tower.
  • the wet scrubber for ships of the present invention and the complex-type washing water injection system inside the absorption tower including the same spray the washing water, that is, sea water, into the flue gas to dissolve the sulfur compounds contained in the flue gas in the droplets, liquid film, and bubbles generated therefrom. , Is to capture.
  • the filler is installed in two stages. Separation and installation method of the filling material can increase the absorption efficiency of sulfur compounds in the cleaning water (5) by spraying fresh cleaning water (5) at each step. By mixing and applying the (Packing) cleaning step, sulfur compounds can be more effectively removed.
  • the intake port 101 is provided with the flue gas is suction is provided at the bottom, the pollutants contained in the flue gas is absorbed and treated, the pollutant is absorbed treatment is discharged exhaust gas (102) ) Is provided on the upper side, and an absorption tower 100 having a space in which a washing water injection nozzle module and a filler is installed is provided.
  • the filler is installed at intervals above and below the absorption tower 100, and the first filler 140a and the second sequentially absorbing sulfur compounds contained in flue gas passing through the absorption tower 100. It is divided into a filling material (140b).
  • the pipe inside the absorption tower 100 is connected to the pipe inside the absorption tower 100 and includes a plurality of injection nozzles 122 and a supply pump 123 to supply / dispensing the washing water 5 into the absorption tower 100.
  • a supply line 120 is provided.
  • the center for preventing the washing water 5 from entering the suction port 101 is inclined upwardly conical shape inflow preventing unit 110 Are spaced apart.
  • the supply line 120 is connected to a pipe located above the first filler 140a and has a plurality of spray nozzles 122 for spraying washing water 5 upward toward the second filler 140b.
  • the second injection nozzle module 120b having a plurality of injection nozzles 122 connected to a pipe located above the second filling material 140b and spraying the washing water 5 upward toward the gas-liquid separation device 150 and;
  • the second filling material 140b is divided into a third injection nozzle module 120c having an injection nozzle 122 that is connected to a pipe located on the upper part and sprays the washing water 5 downward toward the second filling material 140b. Can be.
  • the step of spraying the washing water 5 in the upper space of the second filler 140b is the final washing water injection step for absorbing and removing sulfur compounds before the flue gas is discharged outside the absorption tower. As, it directly affects the removal efficiency of the sulfur compound in the entire absorption tower (100).
  • a complex type washing water spraying method was devised and applied so that the efficiency of removing sulfur compounds in the upper space of the second filler 140b was maximized.
  • the second injection module 120b and the third injection module 120c are divided and installed, and the second injection module 120b is a parallel flow in the same direction as the flow direction of flue gas.
  • (Co-Current) sprays the washing water (5)
  • the third injection module (120c) injects the washing water (5) in a counter-current (Count-Current) method opposite to the flow direction of the flue gas do.
  • the droplets of the sprayed water which are divided up and down, collide in the interior space, dispersing into smaller droplets of cleaning water, and at the same time, the flow state of the cleaning water changes to a turbulent flow state.
  • washing water reaching the upper portion of the washing water sprayed from the second injection module 120b falls, and again contacts the flue gas rising to the top, through which the removal efficiency of sulfur compounds may be further increased.
  • the supply line 120 is connected to the pipe to spray the washing water 5 toward the first filling material 140a to cool the flue gas sucked into the absorption tower.
  • a cooling injection nozzle module 120d having a plurality of injection nozzles 122 may be included.
  • Device 150 may be included.
  • the bottom of one side of the absorption tower 100 is characterized in that a drain 103 is discharged after the washing water 5 sprayed by the spray nozzle 122 absorbs and removes the sulfur compound contained in the flue gas. do.
  • the washing water 5 is sprayed upward in the same direction as the flue gas flow direction in the second injection nozzle module 120b installed on the top of the second filling material 140b, and the sprayed washing water (5) is primarily in contact with the flue gas passing through the second filler 140b, and removes the sulfur compound.
  • the washing water droplets sprayed downward from the third injection nozzle module 120c and the washing water droplets sprayed upward from the second injection nozzle module 120b collide, and the washing water droplets are finely divided and scattered. , Due to this, the contact opportunity between the washing water droplet and the flue gas is further expanded, and accordingly, the removal efficiency of the sulfur compound may be further increased.
  • the present invention relates to a wet scrubber system for ships, a suction port through which flue gas is sucked is provided at the bottom, and after the pollutants contained in the flue gas are absorbed, the exhaust gas from which the pollutants are absorbed is discharged.
  • a first filler and a second filler which are installed at intervals of upper / lower in the absorption tower to sequentially absorb sulfur compounds contained in flue gas passing through the absorption tower;
  • a supply line including a plurality of injection nozzles and a supply pump to be connected to the absorption tower to supply / inject cleaning water into the interior of the absorption tower; It is installed on the inside of the absorption tower and above the suction port, and is formed in a conical shape with a center inclined upward toward the discharge port, and includes an inflow prevention unit to prevent the inflow of cleaning water into the flue gas intake port, and the supply line.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

The present invention relates to a wet scrubber system for a ship, and to a wet scrubber for a ship and a composite cleaning water spray system inside an absorption tower, including same, the wet scrubber comprising: an absorption tower having, at the lower part thereof, a suction port through which flue gas is suctioned, having, at the upper part thereof, a discharge port through which the flue gas, from which pollutants have been treated to be absorbed, is discharged after the pollutants included in the flue gas are treated to be absorbed, and having a space in which a cleaning water spray nozzle and packing are provided; a first filler and a second filler, which are provided inside the absorption tower with a vertical gap therebetween so as to sequentially absorb sulfur compounds included in the flue gas passing through the absorption tower; a supply line including a plurality of spray nozzles and a supply pump such that a pipe is connected to the absorption tower so as to enable cleaning water to be supplied/sprayed into the absorption tower; and an inflow prevention part which is provided inside the absorption tower so as to be spaced from the upper part of the suction port, and which is formed in a conical shape having a center upwardly inclined toward the discharge port, so as to prevent the inflow of the cleaning water into the flue gas suction port, wherein the supply line is divided into: a first spray nozzle module having a plurality of spray nozzles, which are connected to a pipe positioned at the upper part of the first packing, so as to spray the cleaning water toward the second packing; a second spray nozzle module having a plurality of spray nozzles, which are connected to two upper and lower rows of pipes positioned at the upper part of the second packing, so as to upwardly spray the cleaning water toward a gas-liquid separator; and a third spray nozzle module having a plurality of spray nozzles, which are connected to a pipe positioned at the upper part of the second packing, so as to downwardly spray the cleaning water toward the second packing, and thus the present invention can drastically increase the contact time and contact opportunity of the flue gas suctioned into the absorption tower and the cleaning water sprayed in the absorption tower, so as to effectively remove sulfur oxides contained in the flue gas, which is suctioned into the absorption tower, of a main engine, a power generator, and a boiler, thereby enabling installation costs and operating costs of the system to be reduced.

Description

선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템Wet scrubber for ships and the complex type washing water injection system inside the absorption tower including the same

본 발명은 선박용 습식 스크러버 시스템에 관한 것으로, 흡수탑 하단부 흡입구로 흡입된 배연가스가 냉각(Quenching) 과정을 거쳐, 제1충진재(Packing) 및 제2충진재를 통과한 후, 배연가스 배출구를 향해 올라가는 과정에서, 배연가스에 함유된 황화합물을 효과적으로 흡수 및 제거하기 위하여 제2충진재 상부 공간에서 세정수의 분사 방식을 대항류(Counter-Current) 방식과 평행류(Co-Current) 방식을 복합한 세정수 분사 방식을 적용한 흡수탑 내부 세정수 분사 방식에 관한 것이다. The present invention relates to a wet scrubber system for ships, after the flue gas sucked through the suction port at the bottom of the absorption tower passes through the first filling material and the second filling material after passing through the quenching process, it goes up toward the flue gas outlet. In the process, in order to effectively absorb and remove the sulfur compounds contained in the flue gas, the washing water spray method in the upper space of the second filler is a combination of counter-current and counter-current methods. It relates to a method of spraying the washing water inside the absorption tower to which the spraying method is applied.

최근에는 선박으로부터 배출되는 배연가스로 인한 환경오염 등의 문제가 야기되어 이를 처리하는 장치 또는 방법에 대한 관심이 집중되고 있다.Recently, problems such as environmental pollution caused by flue gas emitted from ships have been caused, and attention has been focused on an apparatus or a method for treating the problem.

선박에서 배출되는 배연가스에 포함된 유독 물질은 인체에 유해할 뿐만 아니라, 여과처리 없이 그대로 대기 중으로 배출되는 경우에는 환경오염을 유발하는 원인이 되며, 특히, 배연가스에 포함되는 황화합물(황산화물; 황(S)의 산화물을 일괄하여 칭하는 것이나 주로 SO₂(이산화황)와 SO₃(삼산화황)가 대부분. 황 또는 황을 함유하는 연료가 연소될 때 양쪽 모두 발생되나 일반적으로 배출가스 중에 SO₂가 많다. )은 반드시 제거되어야 한다.The toxic substances contained in the flue gas discharged from ships are not only harmful to the human body, but also cause environmental pollution when discharged into the atmosphere without filtration, especially sulfur compounds (sulfur oxides) contained in flue gas. The oxide of sulfur (S) is collectively called, but mainly SO₂ (sulfur dioxide) and SO₃ (sulfur trioxide) are both produced when fuel containing sulfur or sulfur is burned, but in general, there are many SO₂ in the exhaust gas. It must be removed.

한편, 국제해사기구(IMO, International Maritime Organization)에서는 해양오염 방지협약(MARPOL, Marine Pollution treaty)에 의해 선박의 연료 황함유량을 제한하고 있으며, 2015년부터 모든 배연가스 통제지역(ECA, Emission Control Area) 해역에 0.1% 이하 황함유 연료를 사용하도록 규제하고 있다.Meanwhile, the International Maritime Organization (IMO) has restricted the fuel sulfur content of ships by the Marine Pollution Treaty (MARPOL), and since 2015, all Emission Control Areas (ECAs) ) It is regulated to use less than 0.1% sulfur-containing fuel in the sea area.

또한, 연료비용 등의 문제로 0.1%를 초과하는 황함유 연료를 사용하는 선박의 경우에는 2015년부터 황화합물 저감장치의 설치가 법적으로 의무화되어 있다. 즉, 배연가스에 포함된 황화합물의 함량을 허용 농도 이하로 낮추는 탈황 처리 과정이 반드시 필요하며, 이와 같은 처리과정을 거친 배연 가스만을 대기 중으로 방출하도록 의무화되어 있다.In addition, for ships that use more than 0.1% sulfur-containing fuel due to problems such as fuel costs, the installation of sulfur compound abatement devices has been legally mandated since 2015. That is, a desulfurization treatment process that lowers the content of the sulfur compound contained in the flue gas to an allowable concentration is absolutely necessary, and it is mandatory to discharge only flue gas that has undergone such treatment into the atmosphere.

이에 따라, 선박의 배연 라인에는 선박 배연가스를 탈황 처리하여 대기 중으로 배출시키기 위한 다양한 형태의 배연가스 처리장치가 설치되고 있다.Accordingly, various types of flue gas treatment devices are installed in the flue gas line of the vessel to desulfurize the ship flue gas and discharge it into the atmosphere.

이러한 선박 배연가스를 처리하기 위해 선박용 습식 스크러버 시스템이 사용되고 있다.A wet scrubber system for ships is used to treat such flue gas.

한국등록특허 제10-1804418호는 오염물질을 포함하고 있는 배연가스에 세정수를 분사시켜, 이를 통해 생성되는 액적, 액막, 기포 등에 상기 오염물질들을 접촉시켜 배연가스의 오염물질을 용해시키거나 또는 포집하는 선박용 습식 스크러버 시스템에 관한 것이다.Korean Registered Patent No. 10-1804418 sprays washing water onto flue gas containing contaminants, and dissolves the contaminants of flue gas by contacting the contaminants with droplets, liquid films, and bubbles generated therefrom, or It relates to a wet scrubber system for collecting vessels.

상기 선박용 습식 스크러버 시스템은 세정수를 분사시켜 배연가스의 오염물질을 흡수 처리하는 흡수탑, 오염물질을 흡수한 후 배출되는 세정수를 처리하는 세정수 처리 시스템, 상기 스크러버 시스템을 운용하면서 각 시스템의 기능을 감시, 제어하는 제어시스템 등 크게 세 부분으로 구성된다.The wet scrubber system for ships is an absorption tower that absorbs and treats pollutants of flue gas by spraying washing water, a washing water treatment system that processes the washing water discharged after absorbing pollutants, and each system while operating the scrubber system. It consists of three parts: a control system that monitors and controls functions.

위 구성 중, 흡수탑은 습식 스크러버 시스템의 핵심 장치로서 여러 종류가 있는데, 특히, 충진재(packing)를 흡수탑 내부에 설치하여 상기 충진재에 분사된 세정수에 배연가스의 오염물질이 흡수되도록 하거나, 또는 세정수를 직접 배연가스에 분사시켜 배연가스의 오염물질을 제거하는 방식이 사용되고 있다.In the above configuration, the absorption tower is a core device of a wet scrubber system, and there are various types, in particular, a packing material is installed inside the absorption tower so that the pollutants of flue gas are absorbed in the washing water sprayed on the filling material, Alternatively, a method of removing pollutants from the flue gas by spraying the washing water directly into the flue gas is used.

그러나 흡수탑 내부에 흡입된 주기관, 발전기, 보일러의 배연가스에 함유된 황화합물을 효과적으로 제거하기 위하여 흡수탑 내부에 흡입된 배연가스와 흡수탑 내부에서 분사되는 세정수의 접촉시간 및 접촉기회를 더욱 확충시키기 위해 개선된 방식이 필요하다. However, in order to effectively remove the sulfur compounds contained in the flue gas of the main pipe, the generator, and the boiler sucked inside the absorption tower, the contact time and contact chance of the flue gas sucked inside the absorption tower and the washing water sprayed inside the absorption tower are further improved. An improved approach is needed to expand.

상기한 과제를 해결하기 위하여 본 발명은 제2충진재 상부공간에 설치된 세정수 분사노즐모듈을 상부와 하부로 분할하여 배치함으로써, 세정수를 상부와 하부 양방향에서 분사하도록 새로운 세정수 분사방식을 적용하였다. 이를 통해 상부노즐에서 하방향으로 분사된 세정수와 하부노즐에서 상방향으로 분사된 세정수가 맞부딪치게 되며, 이과정에서 세정수 물방울들의 덩어리짐 (Agglomeration) 현상이 없어지고, 잘게 쪼개져서 비산(Dispersion)하게 됨으로써, 세정수 물방울과 배연가스가 접촉할 수 있는 기회가 확충되고, 이를 토대로 세정수의 황화합물 제거효율을 더욱 향상시킬 수 있게 된다. 따라서 본 발명은 선박 배기가스의 황화합물 제거효율을 향상시킨 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템을 제공하는데 목적이 있다.In order to solve the above problems, the present invention applies a new washing water spraying method to spray washing water in both upper and lower directions by dividing and disposing the washing water spray nozzle module installed in the upper space of the second filler into upper and lower portions. . Through this, the washing water sprayed downward from the upper nozzle and the washing water sprayed upward from the lower nozzle collide, and in this process, the agglomeration phenomenon of the washing water droplets disappears, and it is finely split and scattered. As a result, the opportunity for contact between the washing water droplets and the flue gas is expanded, and based on this, the removal efficiency of the sulfur compound in the washing water can be further improved. Accordingly, an object of the present invention is to provide a wet scrubber for a ship which has improved the efficiency of removing sulfur compounds from a ship exhaust gas and a complex type washing water injection system including an absorption tower.

상기한 목적을 달성하기 위하여, 본 발명은 배연가스가 흡입되는 흡입구가 하부에 구비되고, 상기 배연가스에 포함된 오염물질이 흡수 처리된 후, 상기 오염물질이 흡수 처리된 배연가스가 배출되는 배출구가 상부에 구비되며, 내부에 오염물질 흡수처리 공간을 갖는 흡수탑과; 상기 흡수탑의 내부에 상/하 간격을 두고 설치되어 상기 흡수탑을 통과하는 배연가스에 포함된 황화합물을 순차적으로 흡수하는 제1충진재 및 제2충진재와; 상기 흡수탑에 배관 연결되어 흡수탑의 내부로 세정수를 공급/분사할 수 있도록 복수의 분사노즐과 공급펌프를 포함하는 공급라인과; 상기 흡수탑의 내부 및 상기 흡입구의 상부에 이격 설치되며, 중앙이 상향 경사진 원뿔형상으로 형성되어 상기 흡입구로 세정수의 유입을 방지하는 유입방지부를 포함하되, 상기 공급라인은 상기 제1충진재의 상부에 위치한 배관과 연결되어 상기 제2충진재를 향해 세정수를 상부로 분사하는 복수의 분사노즐을 갖는 제1분사노즐모듈과; 상기 제2충진재 상부에 위치한 상하 2열의 배관 과 연결되어 상기 기액분리장치를 향해 세정수를 상부로 분사하는 복수의 분사노즐을 갖는 제2분사노즐모듈과; 상기 제2충진재 상부에 위치한 배관과 연결되어 상기 제2충진재를 향해 하부로 분사하는 복수의 분사노즐을 갖는 제3분사노즐모듈; 상기 유입방지부 하단에 위치한 배관과 연결되어, 흡수탑에 흡입된 배연가스를 냉각하기 위해 냉각(Quenching)용 세정수를 상방향으로 분사하는 복수의 분사노즐을 갖는 냉각용 분사노즐모듈로 분할 구성된 것을 특징으로 하는 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템을 제공한다.In order to achieve the above object, the present invention is provided with an intake port through which the flue gas is sucked, and after the pollutants contained in the flue gas are absorbed, the exhaust gas from which the pollutants are absorbed is discharged. Is provided on the upper, and the absorption tower has a pollutant absorption space therein; A first filler and a second filler which are installed at intervals of upper / lower in the absorption tower to sequentially absorb sulfur compounds contained in flue gas passing through the absorption tower; A supply line connected to the absorption tower and including a plurality of injection nozzles and a supply pump to supply / inject cleaning water into the absorption tower; It is installed in the interior of the absorption tower and the upper portion of the suction port, the center is formed in a conical shape inclined upward to include an inflow prevention portion to prevent the inflow of cleaning water to the suction port, the supply line of the first filler A first injection nozzle module connected to a pipe located at an upper portion and having a plurality of injection nozzles for spraying cleaning water upward toward the second filler; A second injection nozzle module having a plurality of spray nozzles which are connected to the upper and lower rows of the piping located above the second filler to spray cleaning water upward toward the gas-liquid separator; A third injection nozzle module having a plurality of injection nozzles connected to a pipe located above the second filler and spraying downward toward the second filler; It is connected to the pipe located at the bottom of the inflow prevention part, and is divided into a cooling injection nozzle module having a plurality of injection nozzles that spray upward cooling water to cool the flue gas sucked into the absorption tower. Provided is a wet scrubber for a vessel, and a complex type washing water injection system inside the absorption tower including the same.

그리고, 상기 배출구와 제1분사노즐모듈의 사이에는 직선 방향의 가스의 흐름에 회전을 유도하여 원심력을 이용하여 기체와 액체를 분리하여 기체만 배출구로 배출시키는 기액분리장치를 더 포함하는 것을 특징으로 한다.And, between the outlet and the first injection nozzle module further comprises a gas-liquid separation device for inducing rotation in the flow of gas in a linear direction to separate gas and liquid by using centrifugal force to discharge only gas to the outlet. do.

한편, 상기 흡수탑의 하단 일측에는 상기 분사노즐모듈에 의해 분사된 세정수가 배연가스에 함유된 황화합물을 흡수, 제거한 후 흡수탑 외부로 배출되는 배수구가 설치된 것을 특징으로 한다.On the other hand, the bottom side of the absorption tower is characterized in that the washing water sprayed by the injection nozzle module absorbs and removes the sulfur compound contained in the flue gas, and then discharges to the outside of the absorption tower.

상기와 같이 구성된 본 발명을 제공함으로써, 흡수탑의 최상층에 위치하는 제2충진재 상부 공간에서 배연가스와 세정수와의 접촉시간 및 접촉기회를 대폭 확충할 수 있으며, 이를 토대로 흡수탑 내부에 흡입된 주기관, 발전기, 보일러의 배연가스에 함유된 황화합물을 효과적으로 제거할 수 있다.By providing the present invention configured as described above, it is possible to significantly increase the contact time and contact opportunity between the flue gas and the washing water in the upper space of the second filler located on the uppermost layer of the absorption tower, and based on this, the suction inside the absorption tower It can effectively remove sulfur compounds contained in the flue gas of main engine, generator, and boiler.

도 1은 본 발명에 따른 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템을 나타내는 구성도.1 is a schematic view showing a wet scrubber for a ship according to the present invention and a complex type washing water injection system inside the absorption tower including the same.

도 2는 본 발명에 따른 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템에서 일부 구성을 나타내는 확대도.Figure 2 is an enlarged view showing a part of the structure in the wet scrubber for ships according to the present invention and the complex type washing water injection system including the absorption tower.

이하, 본 발명에 대하여 동일한 기술분야에 속하는 통상의 지식을 가진 자가 용이하게 실시할 수 있도록 첨부도면을 참조하여 바람직한 실시 예를 상세하게 설명하기로 한다.Hereinafter, preferred embodiments will be described in detail with reference to the accompanying drawings so that a person having ordinary knowledge belonging to the same technical field can easily implement the present invention.

본 발명의 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템은 배연가스에 세정수 즉 해수를 분사시켜, 이를 통해 생성되는 액적, 액막, 기포에 배연가스에 함유되어 있는 황화합물을 용해시켜, 포집하는 것이다.The wet scrubber for ships of the present invention and the complex-type washing water injection system inside the absorption tower including the same spray the washing water, that is, sea water, into the flue gas to dissolve the sulfur compounds contained in the flue gas in the droplets, liquid film, and bubbles generated therefrom. , Is to capture.

따라서, 흡수탑의 황화합물 제거효율을 높이는 것이 선박용 스크러버 시스템 및 흡수탑 설계의 궁극적 목적이며, 이 때문에 흡수탑 내부에 충진재(Packing)를 설치하여, 충진재 상부에서 분사되어 충진재로 흘러 들어오는 세정수(5)와 충진재 하부로부터 충진재로 흘러 들어오는 배연가스가 서로 접촉하게 만들어 줌으로써, 세정수(5)와 배연가스의 접촉시간과 접촉거리를 확충시키는 충진재 적용 방식이 일반적으로 많이 적용되고 있다.Therefore, increasing the removal efficiency of sulfur compounds in the absorption tower is the ultimate purpose of the design of a ship scrubber system and an absorption tower, and for this reason, by installing a packing material inside the absorption tower, spray water sprayed from the top of the filling material and flowing into the filling material (5 ) And the flue gas flowing into the filler from the bottom of the filler make contact with each other, and thus, a method of applying a filler to increase the contact time and contact distance between the washing water 5 and the flue gas is generally applied.

본 발명에서는 충진재를 두 단계로 나누어 설치하고 있다. 충진재의 분리 설치 방식은 각 단계별로 신선한(Fresh) 세정수(5)를 분사하게 함으로써 세정수(5)의 황화합물 흡수효율을 증대시킬 수 있고, 각 단계별로 분사(Spray) 방식의 세정단계와 충진재(Packing) 방식의 세정단계를 혼합하여 적용함으로써, 보다 효과적으로 황화합물을 제거할 수 있다.In the present invention, the filler is installed in two stages. Separation and installation method of the filling material can increase the absorption efficiency of sulfur compounds in the cleaning water (5) by spraying fresh cleaning water (5) at each step. By mixing and applying the (Packing) cleaning step, sulfur compounds can be more effectively removed.

이에 따라 본 발명은 우선, 배연가스가 흡입되는 흡입구(101)가 하부에 구비되고 상기 배연가스에 포함된 오염물질이 흡수 처리된 후, 상기 오염물질이 흡수 처리된 배연가스가 배출되는 배출구(102)가 상부에 구비되며 내부에 세정수 분사노즐모듈과 충진재가 설치된 공간을 갖는 흡수탑(100)이 제공된다.Accordingly, the present invention, first, the intake port 101 is provided with the flue gas is suction is provided at the bottom, the pollutants contained in the flue gas is absorbed and treated, the pollutant is absorbed treatment is discharged exhaust gas (102) ) Is provided on the upper side, and an absorption tower 100 having a space in which a washing water injection nozzle module and a filler is installed is provided.

그리고 상기 충진재는 상기 흡수탑(100)의 내부에 상/하 간격을 두고 설치되어 상기 흡수탑(100)을 통과하는 배연가스에 포함된 황화합물을 순차적으로 흡수하는 제1충진재(140a) 및 제2충진재(140b)로 구분된다.In addition, the filler is installed at intervals above and below the absorption tower 100, and the first filler 140a and the second sequentially absorbing sulfur compounds contained in flue gas passing through the absorption tower 100. It is divided into a filling material (140b).

한편, 상기 흡수탑(100) 내부의 배관과 연결되어 흡수탑(100)의 내부로 세정수(5)를 공급/분사할 수 있도록 복수의 분사노즐(122)과 공급펌프(123)를 포함하는 공급라인(120)이 제공된다.On the other hand, it is connected to the pipe inside the absorption tower 100 and includes a plurality of injection nozzles 122 and a supply pump 123 to supply / dispensing the washing water 5 into the absorption tower 100. A supply line 120 is provided.

그리고 상기 흡수탑(100)의 내부 및 상기 흡입구(101)의 상부에는 상기 흡입구(101)로 세정수(5)가 유입되는 것을 방지하기 위한 중앙이 상향으로 경사진 원뿔형상의 유입방지부(110)가 이격 설치된다.And inside the absorption tower 100 and the upper portion of the suction port 101, the center for preventing the washing water 5 from entering the suction port 101 is inclined upwardly conical shape inflow preventing unit 110 Are spaced apart.

상기 공급라인(120)은 상기 제1충진재(140a)의 상부에 위치한 배관과 연결되어 상기 제2충진재(140b)를 향해 세정수(5)를 상부로 분사하는 복수의 분사노즐(122)을 갖는 제1분사노즐모듈(120a)과; 상기 제2충진재(140b) 상부에 위치한 배관과 연결되어 상기 기액분리장치(150)를 향해 세정수(5)를 상부로 분사하는 복수의 분사노즐(122)을 갖는 제2분사노즐모듈(120b)과; 상기 제2충진재(140b) 상부에 위치한 배관과 연결되어 제2충진재(140b)를 향해 세정수(5)를 하부로 분사하는 분사노즐(122)를 갖는 제3분사노즐모듈(120c)로 분할 구성될 수 있다.The supply line 120 is connected to a pipe located above the first filler 140a and has a plurality of spray nozzles 122 for spraying washing water 5 upward toward the second filler 140b. A first injection nozzle module 120a; The second injection nozzle module 120b having a plurality of injection nozzles 122 connected to a pipe located above the second filling material 140b and spraying the washing water 5 upward toward the gas-liquid separation device 150 and; The second filling material 140b is divided into a third injection nozzle module 120c having an injection nozzle 122 that is connected to a pipe located on the upper part and sprays the washing water 5 downward toward the second filling material 140b. Can be.

특히 본 발명에서 제시된 흡수탑에서는 상기 제2충진재(140b) 상부 공간에서의 세정수(5) 분사 단계는 배연가스가 흡수탑 외부로 배출되기 전, 황화합물 흡수 및 제거를 위한 최종적인 세정수 분사단계로서, 흡수탑(100) 전체의 황화합물의 제거효율에 직접적인 영향을 미친다. In particular, in the absorption tower proposed in the present invention, the step of spraying the washing water 5 in the upper space of the second filler 140b is the final washing water injection step for absorbing and removing sulfur compounds before the flue gas is discharged outside the absorption tower. As, it directly affects the removal efficiency of the sulfur compound in the entire absorption tower (100).

따라서, 본 발명에서는 상기 제2충진재(140b) 상부 공간에서의 황화합물 제거 효율이 극대화 되도록 복합방식의 세정수 분사 방식을 고안하여 적용하였다.Therefore, in the present invention, a complex type washing water spraying method was devised and applied so that the efficiency of removing sulfur compounds in the upper space of the second filler 140b was maximized.

더욱 상세하게 설명하면, 상기 제2분사모듈(120b)과 제3분사모듈(120c)을 상/하로 나누어 설치하며, 상기 제2분사모듈(120b)은 배연가스의 유동방향과 같은 방향인 평행류(Co-Current) 방식으로 세정수(5)를 분사하고, 상기 제3분사모듈(120c)은 배연가스의 유동방향과 반대 방향인 대항류(Count-Current) 방식으로 세정수(5)를 분사한다.In more detail, the second injection module 120b and the third injection module 120c are divided and installed, and the second injection module 120b is a parallel flow in the same direction as the flow direction of flue gas. (Co-Current) sprays the washing water (5), and the third injection module (120c) injects the washing water (5) in a counter-current (Count-Current) method opposite to the flow direction of the flue gas do.

상/하로 나누어져 분사된 세정수 방울들은 내부 공간에서 맞부딪치게 되어, 더 작은 세정수방울로 비산(Dispersion)하게 되며, 동시에 세정수의 유동상태가 난류(Turbulent Flow) 상태로 바뀌게 된다.The droplets of the sprayed water, which are divided up and down, collide in the interior space, dispersing into smaller droplets of cleaning water, and at the same time, the flow state of the cleaning water changes to a turbulent flow state.

이로 인해 배연가스와 세정수방울과의 접촉시간과 접촉기회가 대폭 확충되며, 이를 토대로 황화합물의 제거 효율이 증대될 수 있다.Due to this, the contact time and the chance of contact between the flue gas and the washing water droplets are greatly expanded, and on this basis, the removal efficiency of the sulfur compound can be increased.

그리고, 상기 제2분사모듈(120b)에서 분사된 세정수중 상부에 도달한 세정수는 낙하하면서, 상부로 올라오는 배연가스를 다시 접촉하게 되며, 이를 통해 황화합물 제거 효율이 추가적으로 증대될 수 있다. In addition, the washing water reaching the upper portion of the washing water sprayed from the second injection module 120b falls, and again contacts the flue gas rising to the top, through which the removal efficiency of sulfur compounds may be further increased.

그리고, 상기 유입방지부(110) 하단에는 상기 공급라인(120)이 배관과 연결되어 흡수탑에 흡입된 배연가스를 냉각시키기 위해 상기 제1충진재(140a)를 향해 세정수(5)를 분사하는 복수의 분사노즐(122)을 갖는 냉각용 분사노즐모듈(120d)를 포함할 수 있다.Then, at the bottom of the inflow prevention part 110, the supply line 120 is connected to the pipe to spray the washing water 5 toward the first filling material 140a to cool the flue gas sucked into the absorption tower. A cooling injection nozzle module 120d having a plurality of injection nozzles 122 may be included.

한편, 상기 배출구(102)와 제3분사모듈(120c)의 사이에는 직선 방향의 가스의 흐름에 회전을 유도하여 원심력을 이용하여 기체와 액체를 분리하여 기체만 배출구(102)로 배출시키는 기액분리장치(150)를 포함할 수 있다.On the other hand, between the discharge port 102 and the third injection module (120c) by inducing rotation in the flow of the gas in a straight direction to separate the gas and liquid using centrifugal force to separate gas-liquid to discharge only the gas to the discharge port (102) Device 150 may be included.

또한, 상기 흡수탑(100)의 하단 일측에는 상기 분사노즐(122)에 의해 분사된 세정수(5)가 배연가스에 함유된 황화합물을 흡수 제거한 후, 배출되는 배수구(103)가 설치된 것을 특징으로 한다.In addition, the bottom of one side of the absorption tower 100 is characterized in that a drain 103 is discharged after the washing water 5 sprayed by the spray nozzle 122 absorbs and removes the sulfur compound contained in the flue gas. do.

도 2에 도시된 바, 상기 제2충진재(140b)의 상단에 설치된 제2분사노즐모듈(120b)에서 세정수(5)는 배연가스 유동방향과 동일하게 상 방향으로 분사되며, 분사된 세정수(5)는 일차적으로 제2충진재(140b)를 통과한 배연가스와 접촉하면서, 황화합물을 제거한다.As shown in FIG. 2, the washing water 5 is sprayed upward in the same direction as the flue gas flow direction in the second injection nozzle module 120b installed on the top of the second filling material 140b, and the sprayed washing water (5) is primarily in contact with the flue gas passing through the second filler 140b, and removes the sulfur compound.

그리고, 제3분사노즐모듈(120c)에서 하부로 분사되는 세정수 물방울들과 제2분사노즐모듈(120b)에서 상부로 분사된 세정수 물방울들은 맞부딪치게 되어, 세정수 물방울들이 잘게 쪼개져서 비산되며, 이로 인해 세정수 물방울과 배연가스와의 접촉기회가 더욱 확충되고, 이에 따라 황화합물 제거효율이 더욱 증대될 수 있다.Then, the washing water droplets sprayed downward from the third injection nozzle module 120c and the washing water droplets sprayed upward from the second injection nozzle module 120b collide, and the washing water droplets are finely divided and scattered. , Due to this, the contact opportunity between the washing water droplet and the flue gas is further expanded, and accordingly, the removal efficiency of the sulfur compound may be further increased.

상기와 같이 구성된 본 발명을 적용함으로써, 상기 흡수탑(100)의 최상층에 위치하는 제2충진재(140b) 상부 공간에서 배연가스와 세정수의 접촉시간 및 접촉기회를 확충할 수 있으며, 이를 토대로 훕수탑 내부에 흡입된 주기관, 발전기, 보일러의 배연가스에 함유된 황화합물을 효과적으로 제거할 수 있다.By applying the present invention configured as described above, it is possible to increase the contact time and the contact time between the flue gas and the washing water in the upper space of the second filler 140b located on the uppermost layer of the absorption tower 100, based on this. It is possible to effectively remove the sulfur compounds contained in the flue gas of the main pipe, generator, and boiler sucked inside the water tower.

이상 설명한 본 명세서 및 청구범위에 사용되는 용어 및 단어는 통상적이거나 사전적인 의미로 한정해서 해석되어서는 아니 되며, 본 발명자는 그 자신의 발명을 가장 최선의 방법으로 설명하기 위해 용어의 개념을 적절하게 정의할 수 있다는 원칙에 입각하여 본 발명의 기술적 사상에 부합하는 의미와 개념으로 해석되어야만 한다.The terms and words used in the present specification and claims described above should not be construed as being limited to ordinary or lexical meanings, and the inventor appropriately explains the concept of terms in order to explain his or her invention in the best way. Based on the principle that it can be defined, it should be interpreted as meanings and concepts consistent with the technical spirit of the present invention.

따라서, 본 명세서에 기재된 도면 및 실시 예에 도시된 구성은 본 발명의 가장 바람직한 하나의 실시 예에 불과할 뿐이고, 본 발명의 기술적 사상을 모두 대변하는 것이 아니므로, 본 출원시점에 있어서 이들을 대체할 수 있는 다양한 균등물과 변형 예들이 있을 수 있음을 이해하여야 한다.Therefore, the configuration shown in the drawings and examples described in this specification is only one of the most preferred embodiments of the present invention, and does not represent all of the technical spirit of the present invention, and can be replaced at the time of this application. It should be understood that there may be various equivalents and variations.

* 부호의 설명* Explanation of codes

5: 세정수5: washing water

100: 흡수탑100: absorption tower

101: 흡입구101: intake

102: 배출구102: outlet

103: 배수구103: drain

110: 유입방지부110: inflow prevention part

120: 공급라인120: supply line

120a: 제1분사노즐모듈120a: first injection nozzle module

120b: 제2분사노즐모듈120b: second injection nozzle module

120c: 제3분사노즐모듈120c: third injection nozzle module

120d: 냉각용분사노즐모듈120d: spray nozzle module for cooling

122: 분사노즐122: spray nozzle

123: 공급펌프123: supply pump

140a: 제1충진재140a: first filler

140b: 제2충진재140b: second filler

150: 기액분리장치150: gas-liquid separator

본 발명은 선박용 습식 스크러버 시스템에 관한 것으로, 배연가스가 흡입되는 흡입구가 하부에 구비되고, 상기 배연가스에 포함된 오염물질이 흡수 처리된 후, 상기 오염물질이 흡수 처리된 배연가스가 배출되는 배출구가 상부에 구비되며, 내부에 세정수 분사노즐과 충진재가 설치된 공간을 갖는 흡수탑과; 상기 흡수탑의 내부에 상/하 간격을 두고 설치되어 상기 흡수탑을 통과하는 배연가스에 포함된 황화합물을 순차적으로 흡수하는 제1충진재 및 제2충진재와; 상기 흡수탑에 배관이 연결되어 흡수탑의 내부로 세정수를 공급/분사할 수 있도록 복수의 분사노즐과 공급펌프를 포함하는 공급라인과; 상기 흡수탑의 내부 및 상기 흡입구의 상부에 이격 설치되며, 상기 배출구를 향해 중앙이 상향 경사진 원뿔형상으로 형성되어 상기 배연가스 흡입구로 세정수의 유입을 방지하는 유입방지부를 포함하며, 상기 공급라인은 상기 제1충진재의 상부에 위치한 배관과 연결되어 상기 제2충진재를 향해 세정수를 분사하는 복수의 분사노즐을 갖는 제1분사노즐모듈과; 상기 제2충진재 상부에 위치한 상하 2열의 배관과 연결되어 상기 기액분리장치를 향해 향해 세정수를 상부로 분사하는 복수의 분사노즐을 갖는 제2분사노즐모듈과; 상기 제2충진재 상부에 위치한 배관과 연결되어 상기 제2충진재를 향해 세정수를 하부로 분사하는 복수의 분사노즐을 갖는 제3분사노즐모듈로 분할 구성되어; 흡수탑 내부에 흡입된 배연가스와 흡수탑 내부에서 분사되는 세정수의 접촉시간 및 접촉기회를 대폭 확충할 수 있고, 이를 토대로 흡수탑 내부에 흡입된 주기관, 발전기, 보일러의 배연가스에 함유된 황산화물을 효과적으로 제거할 수 있으며, 이를 통해 시스템의 설치비용 및 운용비용을 절감할 수 있는 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템에 관련하여 선박의 배연기관 관련 분야에 산업상 이용가능성이 있다.The present invention relates to a wet scrubber system for ships, a suction port through which flue gas is sucked is provided at the bottom, and after the pollutants contained in the flue gas are absorbed, the exhaust gas from which the pollutants are absorbed is discharged. Is provided on the upper, and the absorption tower having a space in which the washing water spray nozzle and filler is installed; A first filler and a second filler which are installed at intervals of upper / lower in the absorption tower to sequentially absorb sulfur compounds contained in flue gas passing through the absorption tower; A supply line including a plurality of injection nozzles and a supply pump to be connected to the absorption tower to supply / inject cleaning water into the interior of the absorption tower; It is installed on the inside of the absorption tower and above the suction port, and is formed in a conical shape with a center inclined upward toward the discharge port, and includes an inflow prevention unit to prevent the inflow of cleaning water into the flue gas intake port, and the supply line. Is a first injection nozzle module having a plurality of injection nozzles connected to a pipe located above the first filling material and spraying cleaning water toward the second filling material; A second spray nozzle module having a plurality of spray nozzles connected to the upper and lower rows of the pipes located above the second filler and spraying cleaning water upward toward the gas-liquid separator; It is connected to the pipe located above the second filler and is divided into a third injection nozzle module having a plurality of spray nozzles for spraying cleaning water downward toward the second filler; The contact time and the chance of contact between the flue gas sucked inside the absorption tower and the washing water sprayed from inside the absorption tower can be significantly expanded, and based on this, it is contained in the flue gas of the main pipe, generator, and boiler sucked inside the absorption tower. It is possible to effectively remove sulfur oxides, thereby reducing the installation cost and operating cost of the system. There is availability.

Claims (4)

배연가스가 흡입되는 흡입구(101)가 하부에 구비되고, 상기 배연가스에 함유된 황화합물이 흡수 처리된 후, 상기 오염물질이 흡수, 처리된 배연가스가 배출되는 배출구(102)가 상부에 구비되며, 내부에 공간을 갖는 흡수탑(100)과;The intake port 101 through which the flue gas is sucked is provided at the bottom, and after the sulfur compound contained in the flue gas is absorbed and treated, the exhaust port 102 through which the pollutants are absorbed and the treated flue gas is discharged is provided at the top. , An absorption tower 100 having a space therein; 상기 흡수탑(100)의 내부에 상/하 간격을 두고 설치되어 상기 흡수탑(100)을 통과하는 배연가스에 포함된 황산화물을 순차적으로 흡수하는 제1충진재(140a) 및 제2충진재(140b)와;The first filler 140a and the second filler 140b that are installed inside the absorption tower 100 at upper and lower intervals to sequentially absorb sulfur oxides contained in the flue gas passing through the absorption tower 100. )Wow; 상기 흡수탑(100) 내부에 배관과 연결되어 흡수탑(100)의 내부로 세정수(5)를 공급/분사할 수 있도록 복수의 분사노즐(122)과 공급펌프(123)를 포함하는 공급라인(120)과;Supply line including a plurality of spray nozzles 122 and a supply pump 123 to be connected to a pipe inside the absorption tower 100 to supply / dispensing the washing water 5 into the interior of the absorption tower 100 (120) and; 상기 흡수탑(100)의 내부 및 상기 흡입구(101)의 상부에 이격 설치되며, 중앙이 상향 경사진 원뿔형상으로 형성되어 상기 흡입구(101)로 세정수(5)의 유입을 방지하는 유입방지부(110)를 포함하며,It is installed in the interior of the absorption tower (100) and above the suction port (101), and the center is formed in a conical shape inclined upward to prevent inflow of the washing water (5) into the suction port (101). Contains 110, 상기 공급라인(120)은,The supply line 120, 상기 제1충진재(140a)의 상부에 위치한 배관과 연결되어 상기 제2충진재(140b)를 향해 세정수(5)를 분사하는 복수의 분사노즐(122)을 갖는 제1분사노즐모듈(120a)과;The first injection nozzle module (120a) having a plurality of injection nozzles 122 connected to the piping located on the upper portion of the first filler (140a) for spraying the washing water (5) toward the second filler (140b) and ; 상기 제2충진재(140b)의 상부에 위치한 배관과 연결되어 상기 제2충진재(140a)를 향해 세정수(5)를 상부로 분사하는 복수의 분사노즐(122)을 갖는 제2분사노즐모듈(120b)과;The second injection nozzle module 120b having a plurality of injection nozzles 122 connected to a pipe located on the upper portion of the second filler 140b and spraying the washing water 5 upward toward the second filler 140a )and; 상기 제2충진재(140b)의 상부에 위치한 배관과 연결되어 상기 제2충진재(140a)을 향해 하부로 세정수(5)를 분사하는 복수의 분사노즐(122)을 갖는 제3분사노즐모듈(120c)로 분할 구성된 것을 특징으로 하는 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템.The third injection nozzle module 120c having a plurality of injection nozzles 122 connected to a pipe located at the upper portion of the second filler 140b and spraying washing water 5 downward toward the second filler 140a ) Is composed of a wet scrubber for ships, and a composite water washing system inside the absorption tower including the same. 청구항 1에 있어서,The method according to claim 1, 상기 배출구(102)와 제3분사노즐모듈(120c)의 사이에는,Between the outlet 102 and the third injection nozzle module (120c), 직선 방향의 가스의 흐름에 회전을 유도하여 원심력을 이용하여 기체와 액체를 분리하여 기체만 배출구(102)로 배출시키는 기액분리장치(150)를 더 포함하는 것을 특징으로 하는 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사시스템.Including a gas-liquid separator 150 for separating gas and liquid by using a centrifugal force to induce rotation in the flow of gas in a linear direction and discharging only the gas to the outlet 102, including a wet scrubber for ships and the same Complex-type washing water injection system inside the absorption tower. 청구항 1에 있어서,The method according to claim 1, 상기 유입방지부(110) 하단에는 상기 공급라인(120)에 배관 연결되어 상기 제1충진재(140a)를 향해 배연가스 냉각용 세정수(5)를 분사하는 복수의 분사노즐(122)을 갖는 냉각용 분사노즐모듈(120d)을 포함하는 것을 특징으로 하는 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템.Cooling having a plurality of injection nozzles 122 connected to the supply line 120 at the bottom of the inflow prevention part 110 to inject the flue gas cooling washing water 5 toward the first filler 140a A wet scrubber for ships, characterized by including a spray nozzle module (120d) for use, and a composite water washing system inside the absorption tower including the same. 청구항 1에 있어서,The method according to claim 1, 상기 흡수탑(100)의 하단 일측에는,On the lower side of the absorption tower 100, 상기 분사노즐(122)에 의해 분사된 세정수(5)가 배연가스에 함유된 황화합물을 흡수, 제거한 후 흡수탑 외부로 배출되는 배수구(103)가 설치된 것을 특징으로 하는 선박용 습식 스크러버 및 이를 포함한 흡수탑 내부 복합방식 세정수 분사 시스템.Wet scrubber for ships and absorption including the same, characterized in that a drainage hole (103) discharged to the outside of the absorption tower is installed after the washing water (5) injected by the injection nozzle (122) absorbs and removes sulfur compounds contained in flue gas. Complex water cleaning system inside the tower.
PCT/KR2019/006371 2018-09-03 2019-05-28 Wet scrubber for ship, and composite cleaning water spray system inside absorption tower, including same Ceased WO2020050477A1 (en)

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