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WO2016208978A1 - Waste gas-treating scrubber formed of combination of gas-liquid contact means having multiple functions so as to be appropriate for treating according to waste gas properties - Google Patents

Waste gas-treating scrubber formed of combination of gas-liquid contact means having multiple functions so as to be appropriate for treating according to waste gas properties Download PDF

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Publication number
WO2016208978A1
WO2016208978A1 PCT/KR2016/006662 KR2016006662W WO2016208978A1 WO 2016208978 A1 WO2016208978 A1 WO 2016208978A1 KR 2016006662 W KR2016006662 W KR 2016006662W WO 2016208978 A1 WO2016208978 A1 WO 2016208978A1
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WO
WIPO (PCT)
Prior art keywords
gas
liquid contact
contact means
liquid
waste gas
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/KR2016/006662
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French (fr)
Korean (ko)
Inventor
서익환
박대연
박승철
김지영
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hyojin Ids Co Ltd
Samsung E&A Co Ltd
Original Assignee
Hyojin Ids Co Ltd
Samsung Engineering Co Ltd
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Publication date
Application filed by Hyojin Ids Co Ltd, Samsung Engineering Co Ltd filed Critical Hyojin Ids Co Ltd
Publication of WO2016208978A1 publication Critical patent/WO2016208978A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to a scrubber for treating waste gas, and more particularly, to a waste gas treating scrubber combined with a multi-functional gas-liquid contact means suitable for treatment according to the properties of toxic exhaust gas discharged from a semiconductor manufacturing process.
  • the exhaust gas (waste gas) discharged from a process of forming or etching a thin film on a wafer of a semiconductor manufacturing process includes acidic gases such as hydrogen fluoride, sulfur oxides, nitrogen oxides, hydrogen sulfide and sulfurous acid gas, and alkaline gases such as ammonia. Since these components are not only harmful to human body but also cause environmental pollution, the exhaust gas emitted from the semiconductor manufacturing process should be discharged to the atmosphere after purification.
  • a cleaning solution is sprayed on the exhaust gas (waste gas), which is a wet method, to make gas-liquid contact.
  • the scrubber method to be used is widely known, and in the related art, for example, in the case of installing a gas flow path device, a gas-liquid reaction device, and a dehumidification device in a housing in Korean Patent Publication No. 10-0816822, the gas flow path device is used.
  • a multi scrubber for simultaneously treating a complex pollutant characterized in that No. 10-1020258 includes a waste gas inlet formed on one side and a waste gas outlet formed on the other side, and a housing formed in a box shape and an acid gas introduced into one side of the housing and introduced into the housing.
  • It is formed to include a first injection unit for removing the acid gas by injecting water to the waste gas to be included and a discharge dust collector for collecting the acid mist introduced from the first injection unit by the corona discharge formed inside the other side of the housing
  • An acidic waste gas treatment system is disclosed.
  • the gas-liquid contact device used for the scrubber plate-shaped body 10 made of a predetermined shape in the Korean Patent Publication No. 10-1320638; It is composed of a bent portion 20 having a certain curvature by folding the center of the plate 10, the plate 10 is a polyolefin such as polyethylene, polypropylene, vinylidene chloride, polyester, nylon And organic fibers such as aramid and carbon fiber, inorganic fibers, and metal fibers, and the grid 10 has a grid 12 having a predetermined shape therein, and the grid 12 2 to 10 mm in width and 2 to 10 mm in length, and the bent portion 20 discloses a porous filter and a gas-liquid contact device using the same, wherein the cross-sectional shape is formed in a U shape or a V shape.
  • the plate 10 is a polyolefin such as polyethylene, polypropylene, vinylidene chloride, polyester, nylon And organic fibers such as aramid and carbon fiber, inorganic fibers, and metal fibers
  • the prior art has a problem in the separation and removal efficiency of the waste gas according to the type of waste gas because it is a technology for uniformly separating and removing waste gas by the gas-liquid contact regardless of the type of the waste gas, that is, component, concentration.
  • the present invention differs in function according to the types and concentrations of toxic gas components such as hydrogen fluoride, sulfur oxides, nitrogen oxides, hydrogen sulfide, ammonia sulfite and the like in the exhaust gases emitted from the semiconductor manufacturing process.
  • the present invention has been confirmed by improving the exhaust gas removal efficiency by applying a plurality of unit gas-liquid contact means in combination.
  • An object of the present invention is to provide a scrubber for removing toxic waste gas.
  • the gas is exhausted by a multi-layer gas-liquid contact means combination of a plurality of unit gas-liquid contact means having different gas-liquid contact functions so as to be suitable for treatment according to the properties of the waste gas. It aims at providing the scrubber which processes a gas.
  • the present invention is a multi-layer gas-liquid contact means combination of a plurality of unit gas-liquid contact means having different gas-liquid contact functions so as to be suitable for the treatment according to the concentration of perfluorocarbon (PFC) exhaust gas discharged from the semiconductor manufacturing process.
  • An object of the present invention is to provide a scrubber for treating exhaust gas.
  • Exhaust gas, HF, HCl, Cl 2 Toxic waste gases which are acidic exhaust gases containing and the like, alkaline exhaust gases containing NH 3 , and combustible exhaust gases containing SiF 4 , HF and the like, are discharged, and the perfluorocarbon (PFC) exhaust gases, acidic exhaust gases, Alkaline exhaust gas and combustible exhaust gas are not only discharged depending on the conditions of the semiconductor manufacturing process, operating hours, and products, but also emitted at high concentrations (50 to 500 ppm) to low concentrations (less than 50 ppm).
  • PFC perfluorocarbon
  • the present invention is a waste gas treatment scrubber that combines two or more gas-liquid contact means units having different functions of gas-liquid contact by geometrical differences in order to optimize the treatment according to the type and concentration of the waste gas (G) to improve treatment efficiency. Is done.
  • the waste gas treatment scrubber combined with a multi-functional gas-liquid contact means to fit the characteristics of the waste gas is provided with an exhaust pipe (1a) for discharging the purification gas upwards, the inside In the upper part of the cleaning liquid injection nozzle (1b) is installed, the middle part of the gas-liquid contact means combination (MS), the lower part of the scrubber (1), the waste liquid storage tank (1c) is installed, and the waste liquid storage tank (1c) of In the scrubber comprising a waste gas inlet pipe (2) connected to one side and a cleaning liquid supply pipe (3) connected to the cleaning liquid injection nozzle (1b) installed on the inside of the scrubber (1), the gas-liquid contact means combination (MS) Is a perfluorocarbon (PFC: Per) containing inflowing waste gases (G) containing NF 3 , CF 4 , C 2 F 6 , C 3 F 8 , F 2 , OF 2 , SiO 2 , SiF 4 , NH 3 ,
  • PFC perfluorocarbon
  • Geometry suitable for treatment with varying exhaust gas concentrations Structure is composed of a plurality of different gas-liquid contacting means unit (M1) to the gas-liquid contact means unit (M3) a multi-layered combination of two or more gas-liquid contact device unit selected from a.
  • the present invention is combined with the gas-liquid contact means combination (MS) according to the present invention in order to optimize the treatment according to the concentration of the waste gas (G), that is, per-flourocompounds (PFC) exhaust gas, and to increase the treatment efficiency.
  • the plurality of gas-liquid contact means units M1 to gas-liquid contact means units M3 are different in geometric structure from each other, and the function of gas-liquid contact is different due to the difference in geometric structure.
  • the gas-liquid contact means unit (M1) is a structure of a filter structure in which a network sheet having a predetermined thickness intertwined in two layers is arranged in a zigzag manner between a plurality of vertical partition walls, and induces foaming to contaminate particles contained in waste gas by bubbles.
  • (B) having a function of filtering and absorbing particulate matter, mist, etc. generated when the substance and the gas-liquid contact.
  • Gas-liquid contact means unit (M2) is a bar-shaped circular rods are arranged in a plurality of layers while being arranged in parallel with a plurality of intervals, and the gap and the circular rods are alternately arranged between the layers, re-split and Coarsening is repeated to promote the absorption of gas, (c).
  • the liquid contact means unit (M3) is bent a plurality of plate-like body and arranged up and down in parallel at a predetermined interval, the cross-sectional shape ' It is installed in a plurality, and the network sheet is a structure arranged in a zigzag while contacting the lower surface of the bent plate-shaped upper body, and has a function of extending the gas-liquid contact time while inverting and retaining the flow of gas.
  • the scrubber 1 contains waste gas G, that is, NF 3 , CF 4 , C 2 F 6 , C 3 F 8 , F 2 , OF 2 , SiO 2 , SiF 4 , NH 3 , HF, and the like.
  • Waste gas G that is, NF 3 , CF 4 , C 2 F 6 , C 3 F 8 , F 2 , OF 2 , SiO 2 , SiF 4 , NH 3 , HF, and the like.
  • PFC Per-Fluorocompounds
  • the gas-liquid contact means assembly MS according to the present invention is equal to the cleaning solution according to the present invention when two or more gas-liquid contact means units selected from the gas-liquid contact means unit M1 to the gas-liquid contact means unit M3 are combined.
  • the dispersion (S1) having one distribution function and the dispersion (S2) having an even distribution function of the cleaning liquid are mounted between the uppermost layer of the gas-liquid contact means assembly (MS) and the gas-liquid contact means unit.
  • Dispersion (S1) having an even distribution function of the cleaning solution is formed in a quadrangular through-hole is formed in four directions continuously by the partition wall, the four rectangular through-holes adjacent to the distribution structure in the center, the equal distribution of the cleaning solution Dispersion (S2) having a function is made of a structure in which the rectangular through-holes are arranged continuously in all directions by the partition wall.
  • the waste gas treatment scrubber combined with a multi-functional gas-liquid contact means to be treated according to the characteristics of the waste gas according to the present invention described above is a toxic waste gas (G) that is discharged from the semiconductor manufacturing process, that is, perfluorofluorocarbons (PFC: Per-Fluorocompounds)
  • G toxic waste gas
  • PFC perfluorofluorocarbons
  • the present invention has the advantage that can be easily replaced by coping with the gas-liquid contact means combination suitable for the treatment of the change in the appearance of the waste gas has the advantage that the required cost of the change of the scrubber is also reduced.
  • FIG. 1 is a front view schematically showing a scrubber of one embodiment according to the present invention
  • Figure 2 is a rear view schematically showing a scrubber of one embodiment according to the present invention
  • 3 to 7 is a view schematically showing the gas-liquid contact means unit and the dispersion in the present invention
  • 1 and 2 are front and rear views schematically showing a scrubber for treating a high concentration of waste gas G containing 50 to 500 ppm of perfluorocarbon (PFC) exhaust gas according to an embodiment of the present invention.
  • PFC perfluorocarbon
  • the scrubber 1 of the present invention is provided with an exhaust pipe 1a through which the purge gas is discharged at the upper end and a waste liquid storage tank 1c at the lower end thereof, and a cleaning liquid injection nozzle 1b is installed at the upper side of the scrubber 1.
  • the gas-liquid contact means combination MS combined to be optimized for the treatment of the waste gas G, which is a high concentration of perfluorocarbon (PFC) exhaust gas, is introduced.
  • the gas-liquid contact means combination is a dispersion (S1) having an even distribution function of the cleaning liquid sequentially from the top, induces the generation of bubbles, particulate matter contained in the waste gas by the foam and particles generated when the gas-liquid contact , Gas-liquid contact means unit (M1) having a function of filtering and absorbing mist and the like, a dispersion (S2) having an equal distribution function of the cleaning liquid, contaminant particles and gas-liquid contained in the waste gas by foaming by inducing foaming Gas-liquid contact time while reversing and retaining the flow of gas-liquid contact means unit M1, which has a function of filtering and absorbing particulate matter, mist, etc. generated during contact, dispersion S2 having an equal distribution function of cleaning liquid, and gas.
  • the gas-liquid contact means unit M3 having a function of extending the pressure is laminated.
  • the cleaning liquid supply pipe (3) is connected to the cleaning liquid injection nozzle (1b) to one side of the upper portion of the scrubber (1), the waste liquid storage tank (1c) installed at the lower end is introduced into the waste gas inlet pump (P 1 )
  • the waste gas inlet pipe 2 is connected, and on the other side, a waste liquid discharge pipe 1d is installed, and the cleaning liquid supply pipe 3 is equipped with a cleaning liquid supply pump P 2 for introducing the cleaning liquid from the cleaning liquid storage tank 3a.
  • the waste gas (G) is introduced into the waste liquid of the waste liquid storage tank (1c) through the waste gas inflow pipe (2) by the waste gas inflow pump (P 1 ), and the washing liquid from the washing liquid storage tank (3a) is supplied with the washing liquid supply pump (P 2).
  • the cleaning liquid is lowered while being injected into the scrubber 1 while being supplied to the cleaning liquid injection nozzle 1b installed inside the scrubber 1 through the cleaning liquid supply pipe 3.
  • the waste gas introduced into the waste liquid of the waste liquid storage tank 1c is pretreated by the waste liquid of the waste liquid storage tank 1c, and is combined with the gas-liquid contact to be optimized for the treatment of the waste gas G which is a high concentration of perfluorocarbon (PFC) exhaust gas.
  • the waste gas is purged and discharged to the outside through the exhaust pipe 1a installed on the top of the scrubber 1 while the cleaning liquid descends while passing through the means combination MS.
  • the sprayed and descending washing liquid is first lowered while being dispersed more widely by the dispersion (S1) having an equal distribution function of the washing liquid, and the rising waste gas is inverted and retained by the gas-liquid contact means unit M3.
  • the gas-liquid contact means unit M1 having a function of filtering and absorbing the contaminant particles contained in the waste gas and the gas-liquid particles generated by the foam and mist by inducing foam generation has two layers inside the frame F. It consists of a structure of the filter structure arranged while zigzag passing between the vertical partition wall (5) of approximately ' ⁇ ' shape arranged at regular intervals of the network sheet 4 of a predetermined thickness.
  • the gas-liquid contact means unit M2 having a function of promoting reabsorption and coarsening according to the flow rate of the gas to promote the absorption of the gas has a rod-shaped circular rod 6 inside the frame F at regular intervals. Dogs are arranged in parallel and arranged in a plurality of layers, and the gaps and the circular rods 6 are alternately arranged between the layers and the layers.
  • the liquid contact means unit body M3 having a function of extending the gas-liquid contact time while reversing and retaining the flow of gas is bent in a plurality of plate bodies 7 and 8 inside the frame F so as to be parallel to each other at a predetermined interval.
  • a cross section of " It consists of a plurality of ', and the network sheet (7a) is made of a structure arranged in a zigzag while contacting the lower surface of the upper plate bent (7).
  • the dispersion (S1) having an even distribution function of the cleaning liquid has a structure in which the rectangular through hole (Ha) consisting of partitions in the frame (F) is formed in all four directions continuously, and adjacent four rectangular through holes (Ha) flow in the center.
  • Dispersion (S2) has a structure in which the rectangular through hole (Hb) consisting of partition walls in the frame (F) is arranged in a continuous direction.
  • the waste gas to be treated (G) is a low concentration exhaust gas containing less than 50 ppm of perfluorocarbon (PFC) exhaust gas
  • the gas-liquid contact means assembly (MS) has a dispersion (S1) having an equal distribution function of the cleaning liquid sequentially from above.
  • Gas-liquid contact means unit (M1) having a function of filtering and absorbing the contaminated particulate matter contained in the waste gas and the gas-liquid particulate matter, mist, etc. by inducing foaming, and the ash according to the flow rate of the gas.
  • Gas-liquid contact means unit (M2) having a function of promoting the absorption of gas by repeated scattering and coarsening, contaminating particulate matter contained in waste gas by foaming by inducing foam, and particulate matter generated by gas-liquid contact, etc.
  • Gas-liquid contact means unit (M1) having a function of filtering and absorbing the liquid, a dispersion (S2) having an equal distribution function of the washing liquid, and gas-liquid contact while inverting and retaining the flow of gas.
  • S2 dispersion
  • the gas-liquid contact means units (M1) to (M3) is preferably manufactured to the same standard in order to be assembled integrally, the material of each gas-liquid contact means unit is preferably a synthetic resin material.
  • each gas-liquid contact means unit is not limited because it is determined according to the treatment capacity of the waste gas in the scrubber (1), if skilled in the art to which the present invention belongs can be produced without difficulty according to the waste gas treatment capacity. I will say.
  • Waste gas treatment scrubber using the multi-functional gas-liquid contact means according to the present invention described above is a gas-liquid contact optimized for treatment according to the concentration of toxic waste gas (G), that is, perfluorocarbon (PFC) exhaust gas discharged from the semiconductor manufacturing process
  • G toxic waste gas
  • PFC perfluorocarbon
  • the scrubber of the present invention described above has the advantage that it can be easily replaced by a combination of gas-liquid contact means suitable for treatment with respect to the change and concentration of the waste gas, thereby achieving the effect of improving the gas treatment efficiency of the scrubber and at the same time changing the scrubber Due to the advantage that the required cost is also reduced, the industrial availability is very high.

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  • Environmental & Geological Engineering (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • Manufacturing & Machinery (AREA)
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Abstract

The present invention relates to a scrubber treating exhaust gas by means of a multilayer gas-liquid contact means assembly formed by combining a plurality of unit gas-liquid contact means having different gas-liquid contact functions so as to be appropriate for treating perfluorocarbon (PFC) exhaust gas according to the properties and concentration thereof, the PFC exhaust gas being emitted from a semiconductor manufacturing process. The scrubber is a wet scrubber absorbing and purifying exhaust gas by having a cleaning solution come into contact with PFC exhaust gas, wherein the gas-liquid contact means installed inside the scrubber is formed of a multilayer structure formed by combining a plurality of gas-liquid contact means unit bodies having different gas-liquid contact functions.

Description

폐가스 성상에 따라 처리에 적합하도록 복수기능의 기액접촉수단으로 조합된 폐가스 처리 스크러버Waste gas treatment scrubber combined with multi-functional gas-liquid contact means suitable for treatment according to waste gas properties

본 발명은 폐가스를 처리하는 스크러버에 관한 것이며, 보다 구체적으로는 반도체 제조공정에서 배출하는 유독성 배기가스의 성상에 따라 처리에 적합하도록 복수기능의 기액접촉수단으로 조합한 폐가스 처리 스크러버에 관한 것이다.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a scrubber for treating waste gas, and more particularly, to a waste gas treating scrubber combined with a multi-functional gas-liquid contact means suitable for treatment according to the properties of toxic exhaust gas discharged from a semiconductor manufacturing process.

일반적으로, 반도체 제조공정의 웨이퍼 상에 박막을 형성 또는 식각 등의 공정으로부터 배출되는 배기가스(폐가스)에는 불화수소, 황산화물, 질소산화물, 황화수소, 아황산가스 등의 산성가스 및 암모니아 등의 알칼리성 가스들을 포함하고 있으므로 인체에 유해할 뿐만 아니라 환경오염을 유발시키기 때문에 반도체 제조공정에서 배출되는 배기가스는 정화시킨 후에 대기 중에 배출하여야 한다.In general, the exhaust gas (waste gas) discharged from a process of forming or etching a thin film on a wafer of a semiconductor manufacturing process includes acidic gases such as hydrogen fluoride, sulfur oxides, nitrogen oxides, hydrogen sulfide and sulfurous acid gas, and alkaline gases such as ammonia. Since these components are not only harmful to human body but also cause environmental pollution, the exhaust gas emitted from the semiconductor manufacturing process should be discharged to the atmosphere after purification.

상기 반도체 제조공정에서 배출되는 불화수소, 황산화물, 질소산화물, 황화수소, 아황산가스 암모나아 등과 같은 유독성 가스성분을 제거하기 위한 방법으로 습식방법인 배기가스(폐가스)에 세정용액을 분무하여 기액접촉을 이용하는 스크러버 방식이 널리 알려져 있으며, 이와 관련된 선행기술로 예를 들면, 국내 등록특허공보 제10-0816822호에 하우징에 가스유로장치와 기액반응장치 및 제습장치를 설치하여서 된 것에 있어서, 가스유로장치를 굴곡 유로판(21)과 사선 유로판(22)으로 구성시키고, 기액반응장치를 충전재층을 가진 반응기(31)와 분사장치로 형성시키되 분사장치를 기액반응장치의 상부와 입측에 설치하여 구성시켜서 된 것을 특징으로 하는 복합오염물질을 동시에 처리하는 멀티스크러버를 개시하고 있으며, 국내 등록특허공보 등록번호 제10-1020258호에는 일측에 형성되는 폐가스 유입구와, 타측에 형성되는 폐가스 유출구를 포함하며, 내부가 박스 형상으로 형성되는 하우징과 상기 하우징의 일측 내부에 형성되어 하우징의 내부로 유입되는 산성가스를 포함하는 폐가스에 물을 분사하여 산성 가스를 제거하는 제1분사부 및 상기 하우징의 타측 내부에 형성되어 코로나 방전에 의하여 상기 제1분사부로부터 유입되는 산미스트를 집진하는 방전 집진부를 포함하여 형성되는 것을 특징으로 하는 산성 폐가스 처리 시스템을 개시하고 있다.In order to remove toxic gas components such as hydrogen fluoride, sulfur oxides, nitrogen oxides, hydrogen sulfide, sulfurous acid ammonia, etc. discharged from the semiconductor manufacturing process, a cleaning solution is sprayed on the exhaust gas (waste gas), which is a wet method, to make gas-liquid contact. The scrubber method to be used is widely known, and in the related art, for example, in the case of installing a gas flow path device, a gas-liquid reaction device, and a dehumidification device in a housing in Korean Patent Publication No. 10-0816822, the gas flow path device is used. It consists of a curved flow path plate 21 and an oblique flow path plate 22, and the gas-liquid reaction device is formed of a reactor 31 having a filler layer and an injection device, the injection device is installed on the top and inlet side of the gas-liquid reaction device Disclosed is a multi scrubber for simultaneously treating a complex pollutant, characterized in that No. 10-1020258 includes a waste gas inlet formed on one side and a waste gas outlet formed on the other side, and a housing formed in a box shape and an acid gas introduced into one side of the housing and introduced into the housing. It is formed to include a first injection unit for removing the acid gas by injecting water to the waste gas to be included and a discharge dust collector for collecting the acid mist introduced from the first injection unit by the corona discharge formed inside the other side of the housing An acidic waste gas treatment system is disclosed.

또 스크러버에 이용되는 기액접촉장치와 관련하여 국내 등록특허공보 등록번호 제10-1320638호에 소정의 형상으로 이루어진 판상체(10)와; 상기 판상체(10)의 가운데를 접어서 일정한 곡률을 갖는 절곡부(20)로 구성되고, 상기 판상체(10)는 폴리에틸렌, 폴리프로필렌 등의 폴리올레핀(polyolefin)이나, 염화비닐리덴, 폴리에스테르, 나일론, 아라미드, 탄소섬유 등의 유기섬유나, 무기섬유, 금속섬유로 구성되며, 상기 판상체(10)에는 내부에 소정의 형상으로 이루어진 격자망(12)이 형성되며, 상기 격자망(12)은 가로 2∼10㎜, 세로 2∼10㎜로 형성되며, 상기 절곡부(20)는 단면형상이 U형 또는 V형으로 형성됨을 특징으로 하는 다공성 필터 및 이를 이용한 기액접촉장치를 개시하고 있다.In addition, with respect to the gas-liquid contact device used for the scrubber plate-shaped body 10 made of a predetermined shape in the Korean Patent Publication No. 10-1320638; It is composed of a bent portion 20 having a certain curvature by folding the center of the plate 10, the plate 10 is a polyolefin such as polyethylene, polypropylene, vinylidene chloride, polyester, nylon And organic fibers such as aramid and carbon fiber, inorganic fibers, and metal fibers, and the grid 10 has a grid 12 having a predetermined shape therein, and the grid 12 2 to 10 mm in width and 2 to 10 mm in length, and the bent portion 20 discloses a porous filter and a gas-liquid contact device using the same, wherein the cross-sectional shape is formed in a U shape or a V shape.

상기 선행기술들은 폐가스의 유형 즉 성분, 농도와 상관없이 일률적으로 기액접촉체에 의해 폐가스를 분리 제거하는 기술이므로 폐가스의 유형에 따라 폐가스의 분리 제거효율에 문제점을 지니고 있다.The prior art has a problem in the separation and removal efficiency of the waste gas according to the type of waste gas because it is a technology for uniformly separating and removing waste gas by the gas-liquid contact regardless of the type of the waste gas, that is, component, concentration.

본 발명은 폐가스의 유형 특히, 반도체 제조공정에서 배출되는 배기가스 중에 불화수소, 황산화물, 질소산화물, 황화수소, 아황산가스 암모니아 등과 같은 유독성 가스성분의 종류 및 농도에 따라 그 처리에 적합하게 기능이 상이한 단위 기액접촉수단을 복수개 조합하여 다층으로 적용함으로써 배기가스 제거효율을 향상시키는 것을 확인하고 본 발명을 완성하였다.The present invention differs in function according to the types and concentrations of toxic gas components such as hydrogen fluoride, sulfur oxides, nitrogen oxides, hydrogen sulfide, ammonia sulfite and the like in the exhaust gases emitted from the semiconductor manufacturing process. The present invention has been confirmed by improving the exhaust gas removal efficiency by applying a plurality of unit gas-liquid contact means in combination.

본 발명은 유독성 폐가스를 제거하는 스크러버의 제공을 목적으로 하며, 구체적으로는 폐가스의 성상에 따라 처리에 적합하도록 기액접촉 기능이 상이한 단위 기액접촉수단을 복수개 조합한 다층의 기액접촉수단 조합체에 의해 배기가스를 처리하는 스크러버의 제공을 목적으로 하는 것이다.An object of the present invention is to provide a scrubber for removing toxic waste gas. Specifically, the gas is exhausted by a multi-layer gas-liquid contact means combination of a plurality of unit gas-liquid contact means having different gas-liquid contact functions so as to be suitable for treatment according to the properties of the waste gas. It aims at providing the scrubber which processes a gas.

보다 구체적으로는 본 발명은 반도체 제조공정에서 배출하는 과불화탄소(PFC) 배기가스의 농도에 따라 그 처리에 적합하도록 기액접촉 기능이 상이한 단위 기액접촉수단을 복수개 조합한 다층의 기액접촉수단 조합체에 의해 배기가스를 처리하는 스크러버의 제공을 목적으로 하는 것이다.More specifically, the present invention is a multi-layer gas-liquid contact means combination of a plurality of unit gas-liquid contact means having different gas-liquid contact functions so as to be suitable for the treatment according to the concentration of perfluorocarbon (PFC) exhaust gas discharged from the semiconductor manufacturing process. An object of the present invention is to provide a scrubber for treating exhaust gas.

일반적으로 반도체 제조공정에서는 NF3, CF4, C2F6, C3F8, F2, OF2, SiO2, SiF4, NH3, HF 등을 함유하는 과불화탄소(PFC: Per-Fluorocompounds) 배기가스, HF, HCl, Cl2 등을 함유하는 산성 배기가스, NH3 등을 함유하는 알칼리성 배기가스 및 SiF4, HF 등을 함유하는 가연 배기가스인 유독성 폐가스가 배출되고 있으며, 상기 과불화탄소(PFC) 배기가스, 산성 배기가스, 알칼리성 배기가스, 가연 배기가스는 반도체 제조공정의 조건, 가동시간, 생산제품에 따라 유형을 달리하여 배출되고 있을 뿐 아니라 고농도(50~500ppm) 내지 저농도(50ppm 미만)로 배출되고 있다.Generally, in the semiconductor manufacturing process, perfluorofluorocompounds containing NF 3 , CF 4 , C 2 F 6 , C 3 F 8 , F 2 , OF 2 , SiO 2 , SiF 4 , NH 3 , HF, etc. ) Exhaust gas, HF, HCl, Cl 2 Toxic waste gases, which are acidic exhaust gases containing and the like, alkaline exhaust gases containing NH 3 , and combustible exhaust gases containing SiF 4 , HF and the like, are discharged, and the perfluorocarbon (PFC) exhaust gases, acidic exhaust gases, Alkaline exhaust gas and combustible exhaust gas are not only discharged depending on the conditions of the semiconductor manufacturing process, operating hours, and products, but also emitted at high concentrations (50 to 500 ppm) to low concentrations (less than 50 ppm).

본 발명은 상기 폐가스(G)의 유형과 농도에 따라 그 처리를 최적화하여 처리효율을 향상시키기 위하여 기하학적 구조의 상이성에 의해 기액접촉의 기능이 상이한 기액접촉수단 단위체를 2이상 조합한 폐가스 처리 스크러버로 이루어진다.The present invention is a waste gas treatment scrubber that combines two or more gas-liquid contact means units having different functions of gas-liquid contact by geometrical differences in order to optimize the treatment according to the type and concentration of the waste gas (G) to improve treatment efficiency. Is done.

구체적으로는 본 발명의 목적을 달성하기 위한 해결수단으로서, 폐가스의 성상에 적합하도록 복수기능의 기액접촉수단으로 조합한 폐가스 처리 스크러버는 상측으로 정화가스가 배출되는 배기관(1a)이 설치되며, 내부에는 상부에 세정액 분사노즐(1b)이 설치되고, 중간부에 기액접촉수단 조합체(MS)가 장착되며, 하부에 폐액저장조(1c)가 설치되는 스크러버(1)와, 상기 폐액저장조(1c)의 일측에 연결되는 폐가스 유입관(2) 및 스크러버(1)의 내부의 상부에 설치된 세정액 분사노즐(1b)에 연결되는 세정액 공급관(3)을 포함하는 스크러버에 있어서, 상기 기액접촉수단 조합체(MS)는 유입되는 폐가스(G)인 NF3, CF4, C2F6, C3F8, F2, OF2, SiO2, SiF4, NH3, HF 등을 함유하는 과불화탄소(PFC: Per-Fluorocompounds) 배기가스의 농도 변화에 따라 처리에 적합하도록 기하학적 구조가 상이한 복수개의 기액접촉수단 단위체(M1) 내지 기액접촉수단 단위체(M3)로부터 선택되는 2이상의 기액접촉수단 단위체를 조합한 다층구조로 이루어진다.Specifically, as a solution for achieving the object of the present invention, the waste gas treatment scrubber combined with a multi-functional gas-liquid contact means to fit the characteristics of the waste gas is provided with an exhaust pipe (1a) for discharging the purification gas upwards, the inside In the upper part of the cleaning liquid injection nozzle (1b) is installed, the middle part of the gas-liquid contact means combination (MS), the lower part of the scrubber (1), the waste liquid storage tank (1c) is installed, and the waste liquid storage tank (1c) of In the scrubber comprising a waste gas inlet pipe (2) connected to one side and a cleaning liquid supply pipe (3) connected to the cleaning liquid injection nozzle (1b) installed on the inside of the scrubber (1), the gas-liquid contact means combination (MS) Is a perfluorocarbon (PFC: Per) containing inflowing waste gases (G) containing NF 3 , CF 4 , C 2 F 6 , C 3 F 8 , F 2 , OF 2 , SiO 2 , SiF 4 , NH 3 , HF, etc. Fluorocompounds: Geometry suitable for treatment with varying exhaust gas concentrations Structure is composed of a plurality of different gas-liquid contacting means unit (M1) to the gas-liquid contact means unit (M3) a multi-layered combination of two or more gas-liquid contact device unit selected from a.

본 발명은 상기한 폐가스(G) 즉 과불화탄소(PFC: Per-Fluorocompounds) 배기가스의 농도에 따라 그 처리를 최적화하고, 처리효율을 높이기 위하여 본 발명에 따른 상기 기액접촉수단 조합체(MS)에 조합되는 복수개의 기액접촉수단 단위체(M1) 내지 기액접촉수단 단위체(M3)들은 상호 기하학적 구조를 달리하고 있으며, 기하학적 구조의 상이성에 의해 기액접촉의 기능이 상이하게 나타난다.The present invention is combined with the gas-liquid contact means combination (MS) according to the present invention in order to optimize the treatment according to the concentration of the waste gas (G), that is, per-flourocompounds (PFC) exhaust gas, and to increase the treatment efficiency. The plurality of gas-liquid contact means units M1 to gas-liquid contact means units M3 are different in geometric structure from each other, and the function of gas-liquid contact is different due to the difference in geometric structure.

상기 본 발명에 따른 기액접촉수단 단위체(M1) 내지 기액접촉수단 단위체(M3)의 기능 및 구조를 구체적으로 설명하면, (a). 기액접촉수단 단위체(M1)는 2겹으로 엮어진 일정두께의 망상시트가 다수의 수직하는 격벽사이로 지그재그식으로 배치된 필터구조체의 구조이며, 거품발생을 유도하여 거품에 의해 폐가스에 함유된 오염입자물질 및 기액 접촉시 발생하는 입자물질, 미스트 등을 여과 및 흡수하는 기능을 가지며, (b). 기액접촉수단 단위체(M2)는 막대형상의 원형봉이 간격을 두고 다수개 평행되게 배치되면서 다수의 층으로 설치되고, 층간에는 간격과 원형봉이 교대로 배치된 구조이며, 기체의 유속에 따라 재비산과 조대화가 반복되어 기체의 흡수를 촉진시키는 기능을 가지며, (c). 액접촉수단 단위체(M3)는 다수의 판상체를 절곡하여 일정간격으로 평행되게 상하로 배치하되 단면형상이 ‘

Figure PCTKR2016006662-appb-I000001
’가 되게 복수로 설치하고, 망상시트가 상부의 절곡된 판상체의 하면에 접하면서 지그재그식으로 배치된 구조이며, 기체의 흐름을 반전 및 체류시키면서 기액접촉시간을 연장시키는 기능을 가지는 것으로 이루어진다.Referring to the function and structure of the gas-liquid contact means unit (M1) to the gas-liquid contact means unit (M3) according to the present invention in detail, (a). The gas-liquid contact means unit (M1) is a structure of a filter structure in which a network sheet having a predetermined thickness intertwined in two layers is arranged in a zigzag manner between a plurality of vertical partition walls, and induces foaming to contaminate particles contained in waste gas by bubbles. (B) having a function of filtering and absorbing particulate matter, mist, etc. generated when the substance and the gas-liquid contact. Gas-liquid contact means unit (M2) is a bar-shaped circular rods are arranged in a plurality of layers while being arranged in parallel with a plurality of intervals, and the gap and the circular rods are alternately arranged between the layers, re-split and Coarsening is repeated to promote the absorption of gas, (c). The liquid contact means unit (M3) is bent a plurality of plate-like body and arranged up and down in parallel at a predetermined interval, the cross-sectional shape '
Figure PCTKR2016006662-appb-I000001
It is installed in a plurality, and the network sheet is a structure arranged in a zigzag while contacting the lower surface of the bent plate-shaped upper body, and has a function of extending the gas-liquid contact time while inverting and retaining the flow of gas.

그리고 본 발명에 따른 스크러버(1)는 폐가스(G) 즉 NF3, CF4, C2F6, C3F8, F2, OF2, SiO2, SiF4, NH3, HF 등이 함유된 과불화탄소(PFC: Per-Fluorocompounds) 배기가스의 농도 즉 고농도(50 ~ 500ppm) 내지 저농도(50ppm 미만)에 따라 상기 기액접촉수단 단위체(M1) 내지 기액접촉수단 단위체(M3)로부터 선택되는 2 이상의 기액접촉수단 단위체를 조합함으로써 본 발명에 따른 기액접촉수단 조합체(MS)가 이루어진다.The scrubber 1 according to the present invention contains waste gas G, that is, NF 3 , CF 4 , C 2 F 6 , C 3 F 8 , F 2 , OF 2 , SiO 2 , SiF 4 , NH 3 , HF, and the like. Two or more selected from the gas-liquid contact unit (M1) to the gas-liquid contact unit (M3) according to the concentration of Per-Fluorocompounds (PFC) exhaust gas, that is, a high concentration (50 to 500 ppm) to a low concentration (less than 50 ppm). By combining the gas-liquid contact means unit body, the gas-liquid contact means assembly MS according to the present invention is achieved.

또 본 발명에 따른 기액접촉수단 조합체(MS)는 상기 기액접촉수단 단위체(M1) 내지 기액접촉수단 단위체(M3)로부터 선택되는 2 이상의 기액접촉수단 단위체가 조합될 때, 본 발명에 따른 세정액의 균등한 분배기능을 갖는 분산체(S1) 및 세정액의 균등한 분배기능을 갖는 분산체(S2)가 기액접촉수단 조합체(MS)의 최상층 및 기액접촉수단 단위체 사이에 장착되는 것으로 이루어진다.In addition, the gas-liquid contact means assembly MS according to the present invention is equal to the cleaning solution according to the present invention when two or more gas-liquid contact means units selected from the gas-liquid contact means unit M1 to the gas-liquid contact means unit M3 are combined. The dispersion (S1) having one distribution function and the dispersion (S2) having an even distribution function of the cleaning liquid are mounted between the uppermost layer of the gas-liquid contact means assembly (MS) and the gas-liquid contact means unit.

상기 세정액의 균등한 분배기능을 갖는 분산체(S1)은 격벽에 의해 4각형 통공이 사방연속으로 형성되며, 인접하는 4개의 사각형 통공이 중앙에서 유통되는 구조로 이루어지며, 상기 세정액의 균등한 분배기능을 갖는 분산체(S2)는 격벽에 의해 사각형 통공이 사방연속으로 배열된 구조로 이루어진다.Dispersion (S1) having an even distribution function of the cleaning solution is formed in a quadrangular through-hole is formed in four directions continuously by the partition wall, the four rectangular through-holes adjacent to the distribution structure in the center, the equal distribution of the cleaning solution Dispersion (S2) having a function is made of a structure in which the rectangular through-holes are arranged continuously in all directions by the partition wall.

상기한 본 발명에 따른 폐가스의 성상에 따라 처리가 적합하도록 복수기능의 기액접촉수단으로 조합한 폐가스 처리 스크러버는 반도체 제조공정에서 배출되는 유독성 폐가스(G) 즉 과불화탄소(PFC: Per-Fluorocompounds) 배기가스의 농도에 따라 처리에 적합하도록 최적화된 기액접촉수단 조합체를 적용함으로써 스크러버의 가스처리 효율을 향상시키는 작용효과를 나타낸다.The waste gas treatment scrubber combined with a multi-functional gas-liquid contact means to be treated according to the characteristics of the waste gas according to the present invention described above is a toxic waste gas (G) that is discharged from the semiconductor manufacturing process, that is, perfluorofluorocarbons (PFC: Per-Fluorocompounds) By applying the gas-liquid contact means combination optimized for treatment according to the concentration of the gas exhibits the effect of improving the gas treatment efficiency of the scrubber.

또한 본 발명은 폐가스의 성상변화에 대하여 처리에 적합한 기액접촉수단 조합체로 간편하게 교체하여 대처할 수 있는 장점이 있으므로 스크러버의 변경에 따른 소요경비도 감소되는 장점이 있다.In addition, the present invention has the advantage that can be easily replaced by coping with the gas-liquid contact means combination suitable for the treatment of the change in the appearance of the waste gas has the advantage that the required cost of the change of the scrubber is also reduced.

도 1은 본 발명에 따른 일 실시예의 스크러버를 개략적으로 나타내는 정면도 1 is a front view schematically showing a scrubber of one embodiment according to the present invention

도 2는 본 발명에 따른 일 실시예의 스크러버를 개략적으로 나타내는 배면도Figure 2 is a rear view schematically showing a scrubber of one embodiment according to the present invention

도 3 내지 도 7는 본 발명에 기액접촉수단 단위체 및 분산체를 개략적으로 나타내는 도면3 to 7 is a view schematically showing the gas-liquid contact means unit and the dispersion in the present invention

이하에서는 본 발명을 첨부한 도면에 의해 구체적으로 설명하기로 하겠으나, 본 발명은 하기의 설명에 의하여 제한되는 것은 아니다.Hereinafter, the present invention will be described in detail with reference to the accompanying drawings, but the present invention is not limited to the following description.

<실시예 1><Example 1>

도 1 및 도 2는 본 발명에 따른 일 실시예로 과불화탄소(PFC) 배기가스를 50 ~ 500ppm 함유하는 고농도의 폐가스(G)를 처리하기 위한 스크러버를 개략적으로 나타내는 정면도 및 배면도로써, 도 1 및 도 2를 참조하여, 본 발명에 따른 스크러버를 설명한다. 1 and 2 are front and rear views schematically showing a scrubber for treating a high concentration of waste gas G containing 50 to 500 ppm of perfluorocarbon (PFC) exhaust gas according to an embodiment of the present invention. 1 and 2, a scrubber according to the present invention will be described.

본 발명의 스크러버(1)는 그 상단에 정화가스가 배출되는 배기관(1a)과 하단에 폐액저장조(1c)가 설치되고, 스크러버(1)의 내측으로 상부에 세정액 분사노즐(1b)이 설치되고, 폐액저장조(1c)의 상측에는 유입되는 고농도의 과불화탄소(PFC) 배기가스인 폐가스(G)의 처리에 최적화되도록 조합된 기액접촉수단 조합체(MS)가 장착된다.The scrubber 1 of the present invention is provided with an exhaust pipe 1a through which the purge gas is discharged at the upper end and a waste liquid storage tank 1c at the lower end thereof, and a cleaning liquid injection nozzle 1b is installed at the upper side of the scrubber 1. On the upper side of the waste liquid storage tank 1c, the gas-liquid contact means combination MS combined to be optimized for the treatment of the waste gas G, which is a high concentration of perfluorocarbon (PFC) exhaust gas, is introduced.

상기 기액접촉수단 조합체(MS)는 위에서부터 순차적으로 세정액의 균등한 분배기능을 갖는 분산체(S1), 거품발생을 유도하여 거품에 의해 폐가스에 함유된 오염입자물질 및 기액 접촉시 발생하는 입자물질, 미스트 등을 여과 및 흡수하는 기능을 갖는 기액접촉수단 단위체(M1), 세정액의 균등한 분배기능을 갖는 분산체(S2), 거품발생을 유도하여 거품에 의해 폐가스에 함유된 오염입자물질 및 기액 접촉시 발생하는 입자물질, 미스트 등을 여과 및 흡수하는 기능을 갖는 기액접촉수단 단위체(M1), 세정액의 균등한 분배기능을 갖는 분산체(S2) 및 기체의 흐름을 반전 및 체류시키면서 기액접촉시간을 연장시키는 기능을 갖는 기액접촉수단 단위체(M3)가 적층되어 있다.The gas-liquid contact means combination (MS) is a dispersion (S1) having an even distribution function of the cleaning liquid sequentially from the top, induces the generation of bubbles, particulate matter contained in the waste gas by the foam and particles generated when the gas-liquid contact , Gas-liquid contact means unit (M1) having a function of filtering and absorbing mist and the like, a dispersion (S2) having an equal distribution function of the cleaning liquid, contaminant particles and gas-liquid contained in the waste gas by foaming by inducing foaming Gas-liquid contact time while reversing and retaining the flow of gas-liquid contact means unit M1, which has a function of filtering and absorbing particulate matter, mist, etc. generated during contact, dispersion S2 having an equal distribution function of cleaning liquid, and gas. The gas-liquid contact means unit M3 having a function of extending the pressure is laminated.

또 상기 스크러버(1)의 상부에는 일 측으로 세정액 분사노즐(1b)에 세정액 공급관(3)이 연결되고, 그 하단에 설치된 폐액저장조(1c)에는 일 측으로 폐가스 유입펌프(P1)에 의해 유입되는 폐가스 유입관(2)이 접속되고, 타 측에는 폐액배출관(1d)이 설치되어 있으며, 상기 세정액 공급관(3)에는 세정액 저장조(3a)로부터 세정액을 유입시키기 위한 세정액 공급펌프(P2)가 장착되어 있다.In addition, the cleaning liquid supply pipe (3) is connected to the cleaning liquid injection nozzle (1b) to one side of the upper portion of the scrubber (1), the waste liquid storage tank (1c) installed at the lower end is introduced into the waste gas inlet pump (P 1 ) The waste gas inlet pipe 2 is connected, and on the other side, a waste liquid discharge pipe 1d is installed, and the cleaning liquid supply pipe 3 is equipped with a cleaning liquid supply pump P 2 for introducing the cleaning liquid from the cleaning liquid storage tank 3a. have.

상기 도 1 및 도 2를 참조하여, 상기한 본 발명에 따른 복수기능의 기액접촉수단(MS)을 이용하여 과불화탄소(PFC) 배기가스를 50 ~ 500ppm 함유하는 고농도의 폐가스(G)를 처리하는 과정을 설명하면,1 and 2, by using the multi-functional gas-liquid contact means (MS) according to the present invention to process a high concentration of waste gas (G) containing 50 to 500ppm perfluorocarbon (PFC) exhaust gas In describing the process,

폐가스(G)를 폐가스 유입펌프(P1)에 의해 폐가스 유입관(2)을 통하여 폐액저장조(1c)의 폐액 내부로 유입시키고, 이와 함께 세정액 저장조(3a)로부터 세정액이 세정액 공급펌프(P2)에 의해 세정액 공급관(3)을 통하여 스크러버(1) 내부에 설치된 세정액 분사노즐(1b)에 공급되면서 세정액이 스크러버(1) 내부에 분사되면서 하강한다.The waste gas (G) is introduced into the waste liquid of the waste liquid storage tank (1c) through the waste gas inflow pipe (2) by the waste gas inflow pump (P 1 ), and the washing liquid from the washing liquid storage tank (3a) is supplied with the washing liquid supply pump (P 2). The cleaning liquid is lowered while being injected into the scrubber 1 while being supplied to the cleaning liquid injection nozzle 1b installed inside the scrubber 1 through the cleaning liquid supply pipe 3.

상기 폐액저장조(1c)의 폐액 내부로 유입된 폐가스는 폐액저장조(1c)의 폐액에의해 예비 처리되고, 고농도의 과불화탄소(PFC) 배기가스인 폐가스(G)의 처리에 최적화되도록 조합된 기액접촉수단 조합체(MS)를 통과하면서 하강하는 세정액과 기액접촉이 이루어지면서 폐가스는 정화되어 스크러버(1) 상단에 설치된 배기관(1a)을 통하여 외부로 배출된다.The waste gas introduced into the waste liquid of the waste liquid storage tank 1c is pretreated by the waste liquid of the waste liquid storage tank 1c, and is combined with the gas-liquid contact to be optimized for the treatment of the waste gas G which is a high concentration of perfluorocarbon (PFC) exhaust gas. The waste gas is purged and discharged to the outside through the exhaust pipe 1a installed on the top of the scrubber 1 while the cleaning liquid descends while passing through the means combination MS.

상기 폐가스가 복수기능의 기액접촉수단(MS)을 통과하면서 하강하는 세정액과 기액접촉이 이루어지는 과정을 보다 구체적으로 설명하면,When the waste gas is passed through the gas-liquid contact means (MS) having a plurality of functions to be described in more detail the process of making the gas-liquid contact with the falling down liquid,

상기 분사되어 하강하는 세정액은 1차적으로 세정액의 균등한 분배기능을 갖는 분산체(S1)에 의해 보다 더 넓게 분산되면서 하강하고, 상승하는 폐가스는 기액접촉수단 단위체(M3)에 의해 반전 및 체류하는 과정에서 기액접촉시간이 연장되고 또 세정액의 균등한 분배기능을 갖는 분산체(S2)에 의해 균등하게 분배되어 상승하게 되고, 2단으로 적층된 여과 및 흡수하는 기능을 갖는 기액접촉수단 단위체(M1)에 의해 거품이 발생되어 거품에 의해 폐가스에 함유된 오염입자물질 및 기액 접촉시 발생하는 입자물질, 미스트 등을 여과 및 흡수 작용이 반복적으로 수행되면서 고농도의 과불화탄소(PFC) 배기가스가 보다 효율적으로 처리된다.The sprayed and descending washing liquid is first lowered while being dispersed more widely by the dispersion (S1) having an equal distribution function of the washing liquid, and the rising waste gas is inverted and retained by the gas-liquid contact means unit M3. The gas-liquid contact means unit (M1) having a function of filtration and absorption stacked in two stages, which is evenly distributed and raised by the dispersion (S2) having an extended distribution of the gas-liquid contact time and an equal distribution function of the cleaning liquid. Bubbles are generated by the foam, and the particles repeatedly filter and absorb the polluted particles contained in the waste gas and gas-liquid, and mists.The high concentration of PFC exhaust gas is more efficient. Is processed.

<기액접촉단위체 및 분산체의 구체적 예><Specific examples of gas-liquid contact unit and dispersion>

그리고 3 도 내지 7도를 참조하여 본 발명에 따른 기액접촉수단 단위체(M1) 내지 (M3)와 세정액의 균등한 분배기능을 갖는 분산체(S1) 및 (S2)를 아래에서 구체적으로 설명하면, (a). 거품발생을 유도하여 거품에 의해 폐가스에 함유된 오염입자물질 및 기액 접촉시 발생하는 입자물질, 미스트 등을 여과 및 흡수하는 기능을 갖는 기액접촉수단 단위체(M1)는 프레임(F) 내부에 2겹으로 엮어진 일정두께의 망상시트(4)가 일정간격으로 배치된 대략‘Π’형상의 수직하는 격벽(5)들 사이로 지그재그식으로 통과하면서 배치된 필터구조체의 구조로 이루어져 있다.And the dispersion (S1) and (S2) having an even distribution function of the gas-liquid contact means unit (M1) to (M3) and the cleaning liquid according to the present invention with reference to 3 to 7 in detail below, (a). The gas-liquid contact means unit M1 having a function of filtering and absorbing the contaminant particles contained in the waste gas and the gas-liquid particles generated by the foam and mist by inducing foam generation has two layers inside the frame F. It consists of a structure of the filter structure arranged while zigzag passing between the vertical partition wall (5) of approximately 'π' shape arranged at regular intervals of the network sheet 4 of a predetermined thickness.

(b). 기체의 유속에 따라 재비산과 조대화가 반복되어 기체의 흡수를 촉진시키는 기능을 갖는 기액접촉수단 단위체(M2)는 프레임(F) 내부에 막대형상의 원형봉(6)이 일정간격을 두고 다수개 평행되게 배치되면서 다수의 층으로 설치되고, 층과 층간에는 간격과 원형봉(6)이 교대로 배치된 구조로 이루어져 있다.(b). The gas-liquid contact means unit M2 having a function of promoting reabsorption and coarsening according to the flow rate of the gas to promote the absorption of the gas has a rod-shaped circular rod 6 inside the frame F at regular intervals. Dogs are arranged in parallel and arranged in a plurality of layers, and the gaps and the circular rods 6 are alternately arranged between the layers and the layers.

(c). 기체의 흐름을 반전 및 체류시키면서 기액접촉시간을 연장시키는 기능을 갖는 액접촉수단 단위체(M3)는 프레임(F) 내부에 다수의 판상체(7, 8)를 절곡하여 일정간격으로 평행되게 상하로 배치하되, 단면형상이 ‘

Figure PCTKR2016006662-appb-I000002
’가 되게 복수로 설치하고, 망상시트(7a)가 상부의 절곡된 판상체(7)의 하면에 접하면서 지그재그식으로 배치된 구조로 이루어져 있다.(c). The liquid contact means unit body M3 having a function of extending the gas-liquid contact time while reversing and retaining the flow of gas is bent in a plurality of plate bodies 7 and 8 inside the frame F so as to be parallel to each other at a predetermined interval. With a cross section of "
Figure PCTKR2016006662-appb-I000002
It consists of a plurality of ', and the network sheet (7a) is made of a structure arranged in a zigzag while contacting the lower surface of the upper plate bent (7).

그리고 세정액의 균등한 분배기능을 갖는 분산체(S1)은 프레임(F) 내에 격벽으로 이루어진 사각형 통공(Ha)이 사방연속으로 형성되고, 인접하는 4개의 사각형 통공(Ha)이 중앙에서 유통되는 구조이며, 분산체(S2)는 프레임(F) 내에 격벽으로 이루어진 사각형 통공(Hb)이 사방연속으로 배열된 구조로 이루어진다.And the dispersion (S1) having an even distribution function of the cleaning liquid has a structure in which the rectangular through hole (Ha) consisting of partitions in the frame (F) is formed in all four directions continuously, and adjacent four rectangular through holes (Ha) flow in the center. Dispersion (S2) has a structure in which the rectangular through hole (Hb) consisting of partition walls in the frame (F) is arranged in a continuous direction.

<실시예 2><Example 2>

처리되는 폐가스(G)가 과불화탄소(PFC) 배기가스를 50ppm 미만으로 함유하는 저농도의 배기가스이고, 기액접촉수단 조합체(MS)가 위에서부터 순차적으로 세정액의 균등한 분배기능을 갖는 분산체(S1), 거품발생을 유도하여 거품에 의해 폐가스에 함유된 오염입자물질 및 기액 접촉시 발생하는 입자물질, 미스트 등을 여과 및 흡수하는 기능을 갖는 기액접촉수단 단위체(M1), 기체의 유속에 따라 재비산과 조대화가 반복되어 기체의 흡수를 촉진시키는 기능을 갖는 기액접촉수단 단위체(M2), 거품발생을 유도하여 거품에 의해 폐가스에 함유된 오염입자물질 및 기액 접촉시 발생하는 입자물질, 미스트 등을 여과 및 흡수하는 기능을 갖는 기액접촉수단 단위체(M1), 세정액의 균등한 분배기능을 갖는 분산체(S2) 및 기체의 흐름을 반전 및 체류시키면서 기액접촉시간을 연장시키는 기능을 갖는 기액접촉수단 단위체(M3)가 적층되어 있는 것을 제외하고는 위 <실시예 1>과 동일한 스크러버(1)에 의해 폐가스를 처리하였다. The waste gas to be treated (G) is a low concentration exhaust gas containing less than 50 ppm of perfluorocarbon (PFC) exhaust gas, and the gas-liquid contact means assembly (MS) has a dispersion (S1) having an equal distribution function of the cleaning liquid sequentially from above. ), Gas-liquid contact means unit (M1) having a function of filtering and absorbing the contaminated particulate matter contained in the waste gas and the gas-liquid particulate matter, mist, etc. by inducing foaming, and the ash according to the flow rate of the gas. Gas-liquid contact means unit (M2) having a function of promoting the absorption of gas by repeated scattering and coarsening, contaminating particulate matter contained in waste gas by foaming by inducing foam, and particulate matter generated by gas-liquid contact, etc. Gas-liquid contact means unit (M1) having a function of filtering and absorbing the liquid, a dispersion (S2) having an equal distribution function of the washing liquid, and gas-liquid contact while inverting and retaining the flow of gas. Was treated with the waste gas and is by the above <Example 1> and the same scrubber 1, except that in which the gas-liquid contact means unit (M3) laminate having a function of extending.

상기한 기액접촉수단 단위체(M1) 내지 (M3)은 일체로 조립되기 위하여 동일한 규격으로 제작되는 것이 바람직하며, 각각의 기액접촉수단 단위체의 재질은 합성수지 재질이 바람직하다.The gas-liquid contact means units (M1) to (M3) is preferably manufactured to the same standard in order to be assembled integrally, the material of each gas-liquid contact means unit is preferably a synthetic resin material.

또 상기 각각의 기액접촉수단 단위체의 규격의 크기 및 높이는 스크러버(1)에서 폐가스의 처리용량에 따라 정하여지므로 한정되는 것은 아니며, 본 발명이 속하는 기술분야의 숙련가이면 폐가스 처리용량에 따라 어려움 없이 제작할 수가 있다고 하겠다.In addition, the size and height of the standard of each gas-liquid contact means unit is not limited because it is determined according to the treatment capacity of the waste gas in the scrubber (1), if skilled in the art to which the present invention belongs can be produced without difficulty according to the waste gas treatment capacity. I will say.

상기에서 설명한 본 발명에 따른 복수기능의 기액접촉수단을 이용한 폐가스 처리 스크러버는 반도체 제조공정에서 배출되는 유독성 폐가스(G) 즉 과불화탄소(PFC) 배기가스의 농도에 따라 처리에 적합하도록 최적화된 기액접촉수단 조합체를 적용함으로써 스크러버의 가스처리 효율을 향상시키는 작용효과를 나타내며, 폐가스의 성상변화에 대하여 처리에 적합한 기액접촉수단 조합체로 간편하게 대처할 수 있는 장점이 있다.Waste gas treatment scrubber using the multi-functional gas-liquid contact means according to the present invention described above is a gas-liquid contact optimized for treatment according to the concentration of toxic waste gas (G), that is, perfluorocarbon (PFC) exhaust gas discharged from the semiconductor manufacturing process By applying the combination of means has the effect of improving the gas treatment efficiency of the scrubber, there is an advantage that can easily cope with the gas-liquid contact means combination suitable for treatment against the change in the properties of the waste gas.

상기한 본 발명의 스크러버는 폐가스의 성상변화 및 농도에 대하여 처리에 적합한 기액접촉수단 조합체로 간편하게 교체하여 대처할 수 있는 장점이 있으므로 스크러버의 가스처리 효율을 향상시키는 작용효과를 달성함과 동시에 스크러버의 변경에 따른 소요경비도 감소되는 장점이 있어 산업상 이용가능이 매우 높다.The scrubber of the present invention described above has the advantage that it can be easily replaced by a combination of gas-liquid contact means suitable for treatment with respect to the change and concentration of the waste gas, thereby achieving the effect of improving the gas treatment efficiency of the scrubber and at the same time changing the scrubber Due to the advantage that the required cost is also reduced, the industrial availability is very high.

Claims (3)

상측으로 정화가스가 배출되는 배기관(1a)이 설치되며, 내부에는 상부에 세정액 분사노즐(1b)이 설치되고, 분사노즐(1b)의 하측으로 거품발생을 유도하여 거품에 의해 폐가스에 함유된 오염입자물질 및 기액 접촉시 발생하는 입자물질, 미스트를 여과 및 흡수하는 기능을 갖는 기액접촉수단 단위체(M1), 기체의 유속에 따라 재비산과 조대화가 반복되어 기체의 흡수를 촉진시키는 기능을 갖는 기액접촉수단 단위체(M2) 및 기체의 흐름을 반전 및 체류시키면서 기액접촉시간을 연장시키는 기능을 갖는 기액접촉수단 단위체(M3)로부터 선택되는 2이상의 기액접촉수단 단위체를 조합하여, 유입되는 반도체 제조공정에서 배출되는 과불화탄소(PFC) 배기가스인 폐가스(G)의 농도 변화에 따라 처리에 적합하도록 다층구조로 이루어진 기액접촉수단 조합체(MS)가 장착되고, 또 상기 기액접촉수단 조합체(MS)의 최상층에 세정액의 균등한 분배기능을 갖는 분산체(S1)가 장착되면서, 세정액의 균등한 분배기능을 갖는 분산체(S2)가 상기 기액접촉수단 단위체 사이에 장착되며, 하부에 폐액저장조(1c)가 설치되는 스크러버(1)와, 상기 폐액저장조(1c)의 일측에 연결되는 폐가스 유입관(2) 및 스크러버(1)의 내부의 상부에 설치된 세정액 분사노즐(1b)에 연결되는 세정액 공급관(3)을 포함하는 상기 폐가스(G)를 처리하는 스크러버(1)에 있어서, An exhaust pipe 1a through which the purge gas is discharged is installed upward, and a cleaning liquid injection nozzle 1b is installed at an upper portion thereof, and bubbles are contained in the waste gas by bubbles by inducing foaming to the lower side of the injection nozzle 1b. A gas-liquid contact means unit M1 having a function of filtering and absorbing particulate matter and mist generated when contacting particulate matter and gas-liquid, and having a function of promoting resorption and coarsening by re-spreading and coarsening according to the flow rate of gas. A semiconductor manufacturing process introduced by combining a gas-liquid contact means unit M2 and two or more gas-liquid contact means units selected from the gas-liquid contact means unit M3 having a function of extending the gas-liquid contact time while reversing and retaining the flow of gas. Equipped with a multi-layer gas-liquid contact assembly (MS), which is suitable for treatment according to the concentration change of waste gas (G), which is a perfluorocarbon (PFC) exhaust gas discharged from In addition, while the dispersion (S1) having an even distribution function of the cleaning liquid is mounted on the uppermost layer of the gas-liquid contact means assembly (MS), the dispersion (S2) having an even distribution function of the cleaning liquid is the gas-liquid contact means unit. The scrubber 1 is installed between the scrubber 1, the waste liquid storage tank 1c is installed at the bottom, and the waste gas inlet pipe 2 connected to one side of the waste liquid storage tank 1c and the cleaning liquid installed in the upper part of the scrubber 1. In the scrubber (1) for treating the waste gas (G) comprising a cleaning liquid supply pipe (3) connected to the injection nozzle (1b), 상기 기액접촉수단 단위체(M1)는 프레임(F) 내부에 2겹으로 엮어진 일정두께의 망상시트(4)가 일정간격으로 배치된 ‘Π’형상의 수직하는 격벽(5)들 사이로 지그재그식으로 통과하면서 배치된 필터구조체의 구조이고, 상기 기액접촉수단 단위체(M2)는 프레임(F) 내부에 막대형상의 원형봉(9)이 일정간격을 두고 다수개 평행되게 배치되면서 다수의 층으로 설치되고, 층과 층간에는 간격과 원형봉(9)이 교대로 배치된 구조이고, 상기 기액접촉수단 단위체(M3)는 프레임(F) 내부에 다수의 판상체(7,8)를 절곡하여 일정간격으로 평행되게 상하로 배치하되, 단면형상이 ‘
Figure PCTKR2016006662-appb-I000003
’가 되게 복수로 설치하고, 망상시트(7a)가 상부의 절곡된 판상체(7)의 하면에 접하면서 지그재그식으로 배치된 구조이고,
The gas-liquid contact means unit (M1) is zigzag between the vertical partition wall (5) of the 'Π' shape in which the network sheet (4) of a certain thickness woven in two layers in the frame (F) is arranged at regular intervals. It is a structure of the filter structure arranged while passing, the gas-liquid contact means unit (M2) is installed in a plurality of layers while being arranged in parallel with a plurality of bar-shaped circular rods 9 in a predetermined interval in the frame (F) The gap between the layers and the layers and the circular rods 9 are arranged alternately, the gas-liquid contact means unit (M3) is bent a plurality of plate members (7, 8) in the frame (F) at a predetermined interval Placed up and down in parallel, the cross-sectional shape is'
Figure PCTKR2016006662-appb-I000003
It is a structure in which a plurality of 'to be installed, the network sheet (7a) is arranged in a zigzag form while contacting the lower surface of the upper curved plate 7,
또 상기 분산체(S1)는 프레임(F) 내에 격벽으로 이루어진 사각형 통공(Ha)이 사방연속으로 형성되고, 인접하는 4개의 사각형 통공(Ha)이 중앙에서 유통되는 구조이며, 상기 분산체(S2)는 프레임(F) 내에 격벽으로 이루어진 사각형 통공(Hb)이 사방연속으로 배열된 구조로 이루어진 것을 특징으로 하는 폐가스 성상에 따라 처리에 적합하도록 복수기능의 기액접촉수단으로 조합된 폐가스 처리 스크러버.In addition, the dispersion (S1) is a structure in which a rectangular through hole (Ha) consisting of partition walls in the frame (F) is formed in all four directions continuously, and adjacent four rectangular through holes (Ha) are distributed in the center, the dispersion (S2) ) Is a waste gas treatment scrubber combined with a plurality of gas-liquid contact means suitable for treatment according to the waste gas properties characterized in that the rectangular through hole (Hb) consisting of partition walls arranged in a continuous direction in a frame (F).
청구항 1에 있어서, 폐가스(G)가 과불화탄소(PFC) 배기가스를 50 ~ 500ppm 고농도로 함유하고, 기액접촉수단 조합체(MS)가 상기 분산체(S1), 상기 기액접촉수단 단위체(M1), 상기 분산체(S2), 상기 기액접촉수단 단위체(M1), 상기 분산체(S2) 및 상기 기액접촉수단 단위체(M3)가 위로부터 순차 적층되는 것을 특징으로 하는 폐가스 성상에 따라 처리에 적합하도록 복수기능의 기액접촉수단으로 조합된 폐가스 처리 스크러버.The method according to claim 1, the waste gas (G) contains perfluorocarbon (PFC) exhaust gas at a high concentration of 50 ~ 500ppm, the gas-liquid contact means assembly (MS) is the dispersion (S1), the gas-liquid contact means unit (M1), The dispersion (S2), the gas-liquid contact means unit (M1), the dispersion (S2) and the gas-liquid contact means unit (M3) are sequentially stacked from above a plurality of to suit the treatment according to the waste gas properties. Waste gas treatment scrubber combined with a functional gas-liquid contact means. 청구항 1에 있어서, 폐가스(G)가 과불화탄소(PFC) 배기가스를 50ppm 미만의 저농도로 함유하고, 기액접촉수단 조합체(MS)가 상기 분산체(S1), 상기 기액접촉수단 단위체(M1), 상기 기액접촉수단 단위체(M2), 상기 기액접촉수단 단위체(M1), 상기 분산체(S2) 및 기액접촉수단 단위체(M3)가 위로부터 순차 적층되는 것을 특징으로 하는 폐가스 성상에 따라 처리에 적합하도록 복수기능의 기액접촉수단으로 조합된 폐가스 처리 스크러버.The waste gas G contains perfluorocarbon (PFC) exhaust gas at a low concentration of less than 50 ppm, and the gas-liquid contact means assembly (MS) comprises the dispersion (S1), the gas-liquid contact means unit (M1), The gas-liquid contact means unit (M2), the gas-liquid contact means unit (M1), the dispersion (S2) and the gas-liquid contact means unit (M3) are sequentially stacked from above to be suitable for treatment according to the waste gas properties. Waste gas treatment scrubber combined with a multi-functional gas-liquid contact means.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272034A (en) * 2005-03-28 2006-10-12 Kurita Water Ind Ltd Contaminating gas treatment apparatus and method using photocatalyst
KR100816822B1 (en) * 2006-01-13 2008-03-31 신도건공 주식회사 Multi Scrubber to process complex pollutants at the same time
KR101320638B1 (en) * 2013-06-04 2013-10-23 엔텍이앤씨 주식회사 Porous filter and using the gas-liquid contact device
KR101478973B1 (en) * 2014-09-05 2015-01-05 (주)효진엔지니어링 Scrubber for removing acidic gases using multi gas-liquid contact device
KR101513682B1 (en) * 2014-12-19 2015-04-21 (주)한국테크 Cleansing-type Multistage Deodorising Apparatus

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272034A (en) * 2005-03-28 2006-10-12 Kurita Water Ind Ltd Contaminating gas treatment apparatus and method using photocatalyst
KR100816822B1 (en) * 2006-01-13 2008-03-31 신도건공 주식회사 Multi Scrubber to process complex pollutants at the same time
KR101320638B1 (en) * 2013-06-04 2013-10-23 엔텍이앤씨 주식회사 Porous filter and using the gas-liquid contact device
KR101478973B1 (en) * 2014-09-05 2015-01-05 (주)효진엔지니어링 Scrubber for removing acidic gases using multi gas-liquid contact device
KR101513682B1 (en) * 2014-12-19 2015-04-21 (주)한국테크 Cleansing-type Multistage Deodorising Apparatus

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