KR970058760A - Flue gas treatment device - Google Patents

Flue gas treatment device Download PDF

Info

Publication number
KR970058760A
KR970058760A KR1019960000753A KR19960000753A KR970058760A KR 970058760 A KR970058760 A KR 970058760A KR 1019960000753 A KR1019960000753 A KR 1019960000753A KR 19960000753 A KR19960000753 A KR 19960000753A KR 970058760 A KR970058760 A KR 970058760A
Authority
KR
South Korea
Prior art keywords
pipe
collector
particle
gas
tube
Prior art date
Application number
KR1019960000753A
Other languages
Korean (ko)
Other versions
KR0178256B1 (en
Inventor
한영수
김상철
Original Assignee
김상철
한영수
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 김상철, 한영수 filed Critical 김상철
Priority to KR1019960000753A priority Critical patent/KR0178256B1/en
Publication of KR970058760A publication Critical patent/KR970058760A/en
Application granted granted Critical
Publication of KR0178256B1 publication Critical patent/KR0178256B1/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/02Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/022Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
    • F23J15/027Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using cyclone separators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • 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
    • B01D53/24Separation 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 by centrifugal force
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/24Multiple arrangement thereof
    • B04C5/26Multiple arrangement thereof for series flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/24Multiple arrangement thereof
    • B04C5/28Multiple arrangement thereof for parallel flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C9/00Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Treating Waste Gases (AREA)
  • Cyclones (AREA)

Abstract

이 발명은 입자수거 과정에서 공해 가스의 대기방출을 차단하고 처리공기의 대기방출을 최소화하고, 처리장치를 단위장치로 블럭화 하므로 연도가스의 배출용량과 공해가스의 오염밀도에 맞추어 직렬 또는 병열로 배치 할 수 있게 함으로 설치 이용이 용이하게 하고, 액화수집관의 효율과 성능을 개선하는 연도가스 처리장치를 제공하는 것으로서, 연도가스발생원; 사이클론관; 다중사이클론관; 유해가스 액화수집관; 공기압축기 및 입자 수집관을 구비하여 연도가스 처리장치를 구성하되, 냉각된 연도가스를 공급받는 일차수집기(100)와; 일차수집기 배출가스를 공급받는 단위수집기로(200)로 구성하고; 하나이상의 단위수집기(200)를 중첩하여 설치하며; 일차수집기(100)를 구성하는 다중사이클론판, 사이클론관 및 액화수집관의 입자배출구 및 혼합배출구를 밀폐입자수집관(6a)에 가스배출구(61a)를 설치하며; 닫ㄴ위수짖ㅂ기(200)를 구성하는 사이클론관 및 액화수집관의 입자배출구 및 혼합배출구를 입자수집관(6d)에 가스배출구(61d)를 설치한 것을 특징으로 하는 연도가스 처리장치이다.The present invention disposes of air pollution gases in the process of collecting particles, minimizes the atmospheric release of the treated air, and blocks the treatment unit with unit devices, so that it can be arranged in series or parallel to the discharge capacity of the flue gas and pollution density of the polluting gas The present invention also provides a flue gas treating apparatus for facilitating installation and improving the efficiency and performance of a liquefaction collector, comprising: a flue gas generator; Cyclone tube; Multi cyclone tubes; Hazardous gas liquefaction collector; A primary collector (100) having an air compressor and a particle collecting tube to constitute a flue gas treating apparatus, wherein the primary collector (100) is supplied with cooled flue gas; Comprising a unit collector (200) which receives a primary collector discharge gas; One or more unit collectors (200) are stacked and installed; The particle discharge port and the mixed discharge port of the multiple cyclone plate, the cyclone pipe and the liquefying collection pipe constituting the primary collector 100 are provided with the gas discharge port 61a in the closed particle collection pipe 6a; Wherein the particle discharge port and the mixed discharge port of the cyclone pipe and the liquefying collecting pipe constituting the closed upper baffle 200 are provided with a gas discharge port 61d in the particle collecting pipe 6d.

Description

연도가스 처리장치Flue gas treatment device

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is a trivial issue, I did not include the contents of the text.

제1도는 일차수집기의 정면도로서 다중사이클론관, 액화수집관, 사이클론판 및 입자수집관으로 되어있다.Figure 1 shows a front view of the primary collector as a multi-cyclone tube, a liquefaction collector tube, a cyclone plate and a particle collection tube.

제2도는 단위수집기의 단면도로서 다중사이클론관, 사이클론관 및 입자수집기로 되어있다.FIG. 2 is a cross-sectional view of a unit collector comprising a multi-cyclone tube, a cyclone tube, and a particle collector.

Claims (11)

연도가스발생원; 냉각기; 사이클론관; 다중사이클론관; 유해가스 액화수집관; 공기압축기 및 입자수집관을 구비하여 연도가스 처리장치를 구성하되, 냉각된 연도가스를 공급받는 일차수집기(100)와; 일차수집기 배출가스를 공급받는 단위수집기로(200)로 구성하고; 하나 이상의 단위수집기(200)를 중첩하여 설치하며; 일차수집기(100)를 구성하는 다중사이클론판, 사이클론관 및 액화수집관의 입자배출구 및 혼합배출구를 밀폐 입자수집관(6a)에 연결하고, 입자수집관(6a)에 가스배출구(61a)를 설치하며; 단위수집기(200)를 구성하는 사이클론관 및 액화수집관의 입자배출구 및 혼합배출구를 입자수집관(6d)에 연결하고 입자수집과(6a)에 가스배출구(61d)를 설치한 것을 특징으로 하는 연도가스 처리장치.A flue gas source; cooler; Cyclone tube; Multi cyclone tubes; Hazardous gas liquefaction collector; A primary collector (100) having an air compressor and a particle collecting tube to constitute a flue gas treating apparatus, the primary collector (100) being supplied with cooled flue gas; Comprising a unit collector (200) which receives a primary collector discharge gas; One or more unit collectors (200) are stacked and installed; A particle discharge port and a mixed discharge port of the multiple cyclone plate, the cyclone pipe and the liquefaction collection pipe constituting the primary collector 100 are connected to the closed particle collection pipe 6a and the gas discharge port 61a is installed in the particle collection pipe 6a ; Characterized in that the particle outlet and the mixed outlet of the cyclone pipe and the liquefying collection pipe constituting the unit collector 200 are connected to the particle collecting pipe 6d and the gas outlet 61d is provided in the particle collecting passage 6a, Gas processing device. 청구범위 제1항에 있어서, 일차수집기(100)는 송풍기(11)로부터 일정한 온도로 냉각된 연도가스를 도입하는 다중사이클론관(3)에 설치된 하나 이상의 기체 배출구(31,31)에 액화수집관(4a,4b)을 설치하고, 액화수집관(4a,4b)의 혼합배출구(입자와 기체의 혼합 배출구)를 안내관 (32)으로 입자수집관(6a)에 연결하고, 다중사이클론(3)의 입자배출구(33)를 회전공급기(7a)를 통해 입자수집관(6a)에 연결하고, 사이클론관(3)의 입자배출구(33)를 회전공급기(7a)를 통해 입자수집관(6a)에 연결하고, 다중사이클론과(3)의 기체 배출구(35)를사이클론관(2a)에 연결하고, 사이클론관(2a)의 기체배출구(36)에 액화수집기(4c)를 연결하고, 액화수집기(4c)의 입자 및 가스 혼합배출구를 안내관(37)으로 입자수집관(6a)에 연결하고, 사이클론관(2a)의 입자배출구를 회전공급기(7b)를 통해 입자수집관(6a)에 연결하며, 입자수집관(6a)에 가스배출구(61a)를 설치하여 구성한 것을 특징으로 하는 연도가스처리장치.The primary collector (100) according to claim 1, wherein the primary collector (100) is connected to one or more gas outlets (31, 31) provided in a multi-cyclone pipe (3) for introducing flue gas cooled to a constant temperature from a blower The mixing outlet of the liquefaction collecting pipes 4a and 4b is connected to the particle collecting pipe 6a by the guide pipe 32, The particle outlet 33 of the cyclone tube 3 is connected to the particle collecting pipe 6a through the rotating feeder 7a and the particle outlet 33 of the cyclone pipe 3 is connected to the particle collecting pipe 6a through the rotating feeder 7a And the gas discharge port 35 of the multi cyclone 3 is connected to the cyclone tube 2a and the liquefying collector 4c is connected to the gas discharge port 36 of the cyclone tube 2a and the liquefaction collector 4c ) Is connected to the particle collecting pipe 6a through the guide pipe 37 and the particle outlet of the cyclone pipe 2a is connected to the particle feed port 7b through the rotating feeder 7b Is connected to the collector pipe (6a), and a gas discharge port (61a) is provided in the particle collecting pipe (6a). 청구범위 제1항에 있어서, 단위수집기(200)는 사이클론관(2d)으로 도입되는 연도가스의 기체배출구(21d)에 액화수집관(4d)을 연결하고, 액화수집관(4d)의 혼합배출구를 안내관(22d) 및 가스분리관(23d)을 거쳐 입자수집기(6d)에 연결하고, 사이클론관(2d)의 입자배출구를 회전공급기(7d)를 통해 입자수집관(6d)에 연결하고, 가스분리관(23d)과 입자수집관(6d)에 공유되는 가스배출구(61d)를 설치하여 구성한 것을 특징으로 하는 연도가스 처리장치.The unit collector (200) according to claim 1, wherein the unit collector (200) connects the liquefaction collection pipe (4d) to the gas discharge port (21d) of the flue gas introduced into the cyclone pipe (2d) Is connected to the particle collector 6d through the guide pipe 22d and the gas separation pipe 23d and the particle outlet of the cyclone pipe 2d is connected to the particle collection pipe 6d through the rotation feeder 7d, And a gas discharge port (61d) shared by the gas separation pipe (23d) and the particle collection pipe (6d). 청구범위 제1항에 있어서, 단위수집기는 병렬의 두 사이크론관(2e,2f)으로 도입되는 연도가스의 기체배출구(21e,21f)에 각각 액화수집관(4e,4f)을 연결하고 액화수집관(4e,4f)의 혼합배출구를 안내관(22e,22f), 합류관(24ef) 및 가스분리관 (23ef)을 거쳐 입자수집관(6ef)에 연결하고, 사이클론관(2e,2f)의 입자배출구를 회전공급기(7e,7f)를 통해 입자수집관(6ef)에 연결하고, 가스분리관(23ef)과 입자수집관(6ef)에 공유되는 가스배출구(61ef)를 설치하여 되는 것을 특징으로 하는 연도가스 처리장치.The unit collector according to claim 1, wherein the unit collector connects the liquefaction collection pipes (4e, 4f) to the gas outlets (21e, 21f) of the flue gas introduced into the two cyclone pipes (2e, 2f) The mixing outlet of the tubes 4e and 4f is connected to the particle collecting tube 6ef through the guide tubes 22e and 22f, the confluence tube 24ef and the gas separation tube 23ef, The particle outlet is connected to the particle collecting tube 6ef through the rotary feeders 7e and 7f and the gas outlet 61ef shared by the gas separating tube 23ef and the particle collecting tube 6ef is provided A flue gas treating device. 청구범위 제1항에 있어서, 단위수집기는 사이클론관(2g)으로 도입되는 연도가스의 기체배출구(21g)에 액화수집관(4g)을 연결하고 액화수집관(4g,4h)의 혼합배출구를 안내관(22g)을 통해 직렬의 사이클론관(2h)에 공급하고, 사이클론관(2h)의 기체배출구(21h)에 액화수집관(4h)을 연결하고, 액화수집관(4h)의 혼합배출구를 안내관(22h) 및 가스분리관(23gh)을 거쳐 입자수집관(6gh)에 연결하고, 사이클론관 (2g,2h)의 입자배출를 회전공급기(7g,7h)를 통해 각각 입자수집관(6gh)에 연결하고, 가스분리관(23gh)과 입자수집관(6gh)에 공유되는 가스배출구(61gh)를 설치하여 구성한 것을 특징으로 하는 연도가스 처리장치.The unit collector according to claim 1, wherein the unit collector connects the liquefaction collection pipe (4g) to the gas discharge port (21g) of the flue gas introduced into the cyclone pipe (2g) and guides the mixed discharge port of the liquefaction collection pipes (4g, 4h) The liquefying collection pipe 4h is connected to the gas discharge port 21h of the cyclone pipe 2h and the mixed discharge port of the liquefaction collection pipe 4h is connected to the cyclone pipe 2h through the pipe 22g, Is connected to the particle collecting pipe 6gh via the pipe 22h and the gas separating pipe 23gh and the particle discharge of the cyclone pipes 2g and 2h is supplied to the particle collecting pipe 6gh through the rotating feeders 7g and 7h, , And a gas discharge port (61gh) shared by the gas separation pipe (23gh) and the particle collection pipe (6gh) is provided. 청구범위 제1항에 있어서, 액화수집관은 외관(41)이 깔대기형 내관(42)을 포위하며 밸브(43)로 배기관을비례개폐할 수 있는 상부 덮개(48)와 저부 가스 도입관(49)을 구비하고, 외관(41)에 유입된 가스는 내관의상부에 분포되어 내관(42)의 내면을 따라 균일하게 아래로 흐르게 하는 하향환상유로(44)를 조성하며, 환상의노즐(45) 내벽에 2 내지 8개 등간격 나선방향의 팁(46)을 설치하고 압축공기를 팁(46)에서 내관(42)내에 분출시켜 내관내에 나사선방향의 강력한 외류를 발생할 수 있게 하며, 내관(42) 내의 강력한 희류가 내관(42)내벽면에 흐르는 공해가스를 미립상으로 액화시키고 액화 공해물질을 원심력으로에 의해 내관(42) 내벽면에 모여 낙하되는 입자에 흡수되어 가스와 함께 혼합배출구(47)로 배출되게 구성한 것을 특징으로 하는 연도가스 처리장치.The liquefied collection tube according to claim 1, wherein the liquefying collection tube includes an upper lid (48) capable of enclosing the funnel-shaped inner tube (42) and opening the exhaust pipe to the valve (43) And the gas introduced into the outer tube 41 is distributed in the upper portion of the inner tube to form a downward annular flow path 44 that uniformly flows down along the inner surface of the inner tube 42, Two to eight equally spaced spiral tips 46 are provided on the inner wall of the inner tube 42 and compressed air is blown into the inner tube 42 from the tip 46 to generate strong outward flow in the inner tube 42, Is liquefied in the form of fine particles flowing in the inner wall surface of the inner pipe 42 and the liquefied pollutant is collected on the inner wall surface of the inner pipe 42 by the centrifugal force to be absorbed by the falling particles, ) Of the flue gas. 청구범위 제1항에 있어서, 액화수집관은 외관(41a)이 상판(42b)이 덮힌 깔대기형(42a)을 포위하며 밸브(43a)로 배기관(43')을 비례개폐할 수 있는 상부 덮개(48a)와 저부 가스 도입관(49a)을 구비하고, 외관(41a)에 유입된 가스는 내관의 상부에서 상판(42a)에 분포시킨 분산구멍(44a) 및 경사 안내깃(44b)에 안내되어 내관(42a)의 내벽면에서 균일하게 나사선방향으로 흐르게 하며, 환상의 노즐(45a) 저부에 2 내지 8개 등간격 나사선방향의 팁(46a)을 설치하고 팁(46a)을 통해 압축공기를내관(42a)에 분출시켜 내관내에 나사선방향의 강력한 희루를 발생할 수 있게 하며, 내관(42a)내의 강력한 희류가 내관 내벽면을 나사선방향으로 흐르는 공해가스를 미립상으로 액화시키고 액화 공해물질은 원심력으로 내관(42a)에 내벽면에 모여 낙하되는 입자에 흡수되어 가스와 함께 내관(42a)의 혼합배출구(47a)로 배출되게 구성한 것을 특징으로 하는 연도가스 처리장치.The liquefying collector tube according to claim 1, wherein the liquefying collector pipe is a lid collector (41a) having an outer cover (41a) surrounding the funnel mold (42a) covered with the upper plate (42b) and capable of proportionally opening and closing the exhaust pipe The gas introduced into the outer tube 41a is guided by the dispersion hole 44a and the inclined guide vane 44b distributed on the upper plate 42a at the upper portion of the inner tube, A tip 46a in the direction of two to eight equidistant screw threads is provided at the bottom of the annular nozzle 45a and compressed air is supplied through the tip 46a to the inner tube 42a so as to cause strong whirling in the direction of the screw thread in the inner tube 42a so that the powerful liquid in the inner tube 42a liquefies the pollution gas flowing in the threaded direction of the inner tube wall surface into the particulate matter, (42a) so as to be absorbed by the particles falling down on the inner wall surface of the inner tube is discharged to the mixing outlet (47a) of the flue gas treating apparatus (a). 청구범위 제1항에 있어서, 입자수집관(6d)은 내부에 이송스크류(62)을 설치하여 구동수단(63)으로 구동하며, 배출구(64)는 공해가스의 유출이 없도록 기밀되어(65)로 개폐할 수 있게 한 것을 특징으로 하는 연도가스 처리장치.The particle collecting pipe (6d) according to claim 1, wherein the particle collecting pipe (6d) is provided with a conveying screw (62) and driven by a driving means (63), and the outlet (64) is airtightly sealed (65) So as to be able to open and close the flue gas. 청구범위 제1항에 있어서, 회전공급기는 실린더(71)내의 공급익판(72)을 저속모터(73)로 구동하여 상부에 수집되는 입자를 반복하여 입자수집관에 공급하고 입자수집관내의 풍압이 역류되지 않게 한 것을 특징으로 하는 연도가스 처리장치.The rotating feeder according to claim 1, wherein the rotating feeder drives the feed blade (72) in the cylinder (71) with a low-speed motor (73) to repeatedly feed the collected particles to the particle collecting tube So as not to flow backward. 연도가스발생원; 사이클론관; 다중사이클관; 유해가스 액화수집관; 공기 압축기 및 입자수집관을 구비하여 연도가스 처리장치를 구성하되, 냉각된 연도가스를 공급받는 일차수기(100)와; 일차수집기 배출가스를 공급받는 단위수집기로(200)로 구성하고; 하나 이상의 단위수집기(200)를 중첩하여 설치하며; 일차수집기(100)를 구성하는 다중사이클론관, 사이클론관 및 액화수집관의 입자배출구 및 혼합배출구를 밀폐 입자수집관(6a)에 연결하고, 입자수집관(6a)에 가스배출구(61a)를 설치하며; 단위수집기(200)를 구성하는 사이클론관 및 액화수집관의 입자배출구 및 혼합배출구를 입자수집관(6ef)에 연결하고 입자수집관(6ef)에 가스배출구(61ef)를 설치하며, 최종 단위수집기의 액화수집관의 배기관(43) 배출가스를 이송관(b2)을 통해 송풍기(11)에서 일차수집기(100)에 공급되는 연도가스에 합류시킨 것을 특징으로 하는 연도가스 처리장치.A flue gas source; Cyclone tube; Multi cycle tube; Hazardous gas liquefaction collector; (100) having an air compressor and a particle collecting pipe to constitute a flue gas treating apparatus, the flue gas being supplied with cooled flue gas; Comprising a unit collector (200) which receives a primary collector discharge gas; One or more unit collectors (200) are stacked and installed; The particle discharge port and the mixed discharge port of the multiple cyclone pipe, the cyclone pipe and the liquefaction collection pipe constituting the primary collector 100 are connected to the closed particle collection pipe 6a and the gas discharge port 61a is installed in the particle collection pipe 6a ; The particle outlet and the mixed outlet of the cyclone tube and the liquefying collector tube constituting the unit collector 200 are connected to the particle collecting tube 6ef and the gas outlet 61ef is installed in the particle collecting tube 6ef, Wherein the flue gas discharged from the exhaust pipe (43) of the liquefaction collection pipe is joined to the flue gas supplied from the blower (11) to the primary collector (100) through the transfer pipe (b2). 연도가스발생원; 사이클론관; 다중사이클관; 유해가스 액화수집관; 공기 압축기 및 입자수집관을 연도가스 처리장치를 구성하되, 냉각된 연도가스를 공급받는 일차수기(100)와; 일차수집기 배출가스를 공급받는 단위수집기로(200)로 공급하고; 하나 이상의 단위수집기(200)를 중첩하여 설치하며; 일차수집기(100)를 구성하는 다중사이클론관, 사이클론관 및 액화수집관의 입자배출구 및 혼합배출구를 밀폐 입자수집관(6ef)에 연결하고, 입자수집관(6ef)에 가스배출구(61ef)를 설치하며; 단위수집기(200)를 구성하는 사이클론관 및 액화수집관의 입자배출구 및 혼합배출구를 입자수집관(6ef)에 연결하고 입자수집관에 가스배출구(61ef)를 설치하며,최종 단위수집기의 가스배출구(61ef)배출공기를 이송관(b2)을 통해 송풍기(11)에서 일차수집기(100)에 공급되는 연도가스에 합류시킨 것을 특징으로 하는 연도가스 처리장치.A flue gas source; Cyclone tube; Multi cycle tube; Hazardous gas liquefaction collector; An air compressor and a particle collecting tube constituting a flue gas treating apparatus, the flue gas treating apparatus comprising: a primary processing unit (100) for supplying a cooled flue gas; Supplying the primary collector exhaust gas to the supplied unit collector 200; One or more unit collectors (200) are stacked and installed; The particle discharge port and the mixed discharge port of the multiple cyclone pipe, the cyclone pipe and the liquefaction collection pipe constituting the primary collector 100 are connected to the closed particle collection pipe 6ef and the gas discharge port 61ef is installed in the particle collection pipe 6ef ; The particle outlet and the mixed outlet of the cyclone tube and the liquefying collector tube constituting the unit collector 200 are connected to the particle collecting tube 6ef, the gas outlet 61ef is installed in the particle collecting tube, and the gas outlet 61ef) discharge air is merged with the flue gas supplied to the primary collector (100) from the blower (11) through the transfer pipe (b2). ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: It is disclosed by the contents of the first application.
KR1019960000753A 1996-01-16 1996-01-16 Flue gas treatment apparatus KR0178256B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019960000753A KR0178256B1 (en) 1996-01-16 1996-01-16 Flue gas treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019960000753A KR0178256B1 (en) 1996-01-16 1996-01-16 Flue gas treatment apparatus

Publications (2)

Publication Number Publication Date
KR970058760A true KR970058760A (en) 1997-08-12
KR0178256B1 KR0178256B1 (en) 1999-03-20

Family

ID=19449494

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019960000753A KR0178256B1 (en) 1996-01-16 1996-01-16 Flue gas treatment apparatus

Country Status (1)

Country Link
KR (1) KR0178256B1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100754532B1 (en) * 2005-12-29 2007-09-03 신잔토개발 주식회사 Dust collector for construction waste
KR101527389B1 (en) * 2013-03-14 2015-06-09 함형춘 Dust collecting device using centrifugal force for dust disposal of agricultural products

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102203139B1 (en) * 2020-03-19 2021-01-21 남숭호 Apparatus for purifying exhaust gas using rotational force

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100754532B1 (en) * 2005-12-29 2007-09-03 신잔토개발 주식회사 Dust collector for construction waste
KR101527389B1 (en) * 2013-03-14 2015-06-09 함형춘 Dust collecting device using centrifugal force for dust disposal of agricultural products

Also Published As

Publication number Publication date
KR0178256B1 (en) 1999-03-20

Similar Documents

Publication Publication Date Title
US6270544B1 (en) Cyclone separator having a tubular member with slit-like openings surrounding a central outlet pipe
RU2006129323A (en) CLASSIFIER FOR GRANULATED MATERIAL
US2687780A (en) Gas cleaning apparatus
US4357152A (en) Fluid borne particulate separator
KR970058760A (en) Flue gas treatment device
US5215553A (en) Apparatus for separating particles from a gaseous medium
RU2365432C1 (en) Installation for recycling of luminescent lamps and method for their recycling
US3620370A (en) Ore concentrator
RU2260470C1 (en) Vortex-type dust collector
JP2004098404A (en) Label taking-off machine and recycling recovery treatment system for waste plastic container
RU2344868C1 (en) Vertical dust catcher
CN216150076U (en) Cyclone dust collector
CN215141020U (en) Improved cyclone dust collector
SU1036401A1 (en) Separator for powdered materials
CN212870823U (en) Air-flow type cooling machine for gypsum processing
CN2767848Y (en) Multifunctional low-resistance cooling cartridge
JPH11235573A (en) Pneumatic crushing and screening device
CN214021971U (en) Improved generation winnowing equipment
RU2132750C1 (en) Vortex dust catching method and apparatus
CN215027327U (en) Adjustable sintering machine flue gas internal circulation device
RU2056143C1 (en) Apparatus for gasses clearance from impurities
RU2014111C1 (en) Gas purifier
SU1166847A1 (en) Separator for pulverulent materials
JPH08159415A (en) Pressurized fluidized bed boiler
CN2408361Y (en) Gas/solid separator

Legal Events

Date Code Title Description
A201 Request for examination
N231 Notification of change of applicant
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
LAPS Lapse due to unpaid annual fee