KR200150693Y1 - Dust collector - Google Patents
Dust collector Download PDFInfo
- Publication number
- KR200150693Y1 KR200150693Y1 KR2019950008209U KR19950008209U KR200150693Y1 KR 200150693 Y1 KR200150693 Y1 KR 200150693Y1 KR 2019950008209 U KR2019950008209 U KR 2019950008209U KR 19950008209 U KR19950008209 U KR 19950008209U KR 200150693 Y1 KR200150693 Y1 KR 200150693Y1
- Authority
- KR
- South Korea
- Prior art keywords
- water
- impeller
- chamber
- suction
- pipe
- 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.)
- Expired - Lifetime
Links
- 239000000428 dust Substances 0.000 title claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000007921 spray Substances 0.000 claims abstract description 3
- 238000005406 washing Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 13
- 239000002245 particle Substances 0.000 abstract description 5
- 239000004071 soot Substances 0.000 abstract description 5
- 238000004140 cleaning Methods 0.000 abstract description 4
- 239000010419 fine particle Substances 0.000 abstract description 4
- 238000002347 injection Methods 0.000 abstract 2
- 239000007924 injection Substances 0.000 abstract 2
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000000779 smoke Substances 0.000 abstract 1
- 238000010298 pulverizing process Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 2
- 239000003517 fume Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/40—Combinations of devices covered by groups B01D45/00 and B01D47/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/14—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
- B01D47/063—Spray cleaning with two or more jets impinging against each other
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/24—Separation 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/08—Centrifuges for separating predominantly gaseous mixtures
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/10—Centrifuges combined with other apparatus, e.g. electrostatic separators; Sets or systems of several centrifuges
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
본 고안은 유해가스 및 분진을 세정방식으로 분리 제거하는 세정집진기에 관한 것이다.The present invention relates to a cleaning dust collector for separating and removing harmful gases and dust in a cleaning manner.
종래의 세정집진기는 이의 규모가 크고, 구조가 복잡하며, 제작비가 고가일뿐만 아니라 많은 동력소모와 고장율이 높아 대중화되지 못하고 있는 결점이 있었던 것이다.Conventional scrubbers have a drawback that they are not popularized due to their large scale, complicated structure, high manufacturing cost, and high power consumption and high failure rate.
본 고안은 이상의 문제점을 해결하고자 안출한 것으로 이의 고안요지는 몸체(1)내에는 임팰러(5)가 축간(3)에 끼움 고정되어 모터(20)에 의해 회동되게 하고, 임팰러(5)의 주위에는 경사상으로된 다수의 분쇄판(6)이 설치되고, 그 외측에는 격판(7)을 개재시펴 와류실(8)과 원심분리실(9)을 형성하며 몸체(1)의 상부에 연설된 상부몸체(12)의 흡입구(16')에는 흡입관(16)이 연결되고, 그 내부에는 급수관(15)과 연결된 다수의 분사노즐(15")이 설치된 흡입혼합실(13)을 형성하므로서 펌프와 모토(20)을 가동시키면 급수관(15)에서는 물을 분사하고 임팰러(5)는 고속 회전하게 된다.The present invention has been devised to solve the above problems, and the subject matter of the present invention is that the impeller (5) is fitted in the shaft (3) in the body (1) to be rotated by the motor 20, impeller (5) In the periphery of the plurality of crushed plate 6 is provided, the outer side of the diaphragm (7) through the vortex chamber (8) and the centrifuge chamber (9) to form an upper portion of the body (1) A suction pipe 16 is connected to the suction port 16 ′ of the upper body 12, and a suction mixing chamber 13 is provided in which a plurality of injection nozzles 15 ″ are connected to the water supply pipe 15. Therefore, when the pump and the moto 20 are operated, the water pipe 15 sprays water and the impeller 5 rotates at high speed.
이때 임팰러(5)에서 생기는 구심력은 유해가스와 매연을 흡입하여 분사노즐(15")에서 분무되는 물에 강제 흡착시켜 미세한 물입자가된 후 임팰러(5)의 원심력에 의해 밖으로 비산되면서 경사상의 분쇄판(6)에 충돌되어 더욱 미세입자가 된 후 와류실(8)에 이르게 되면 청정된 공기와 유해가스 및 매연이 흡착된 물로 분리되고 이때 청정된 공기는 배기구(11)로 배출되고 유해가스와 매연을 흡착한 물은 배수구(11")로 배출된 후 종말처리되게 한 것이다.At this time, the centripetal force generated by the impeller 5 inhales harmful gas and soot and is forcibly adsorbed to the water sprayed from the injection nozzle 15 "to become fine water particles, and then inclined while being scattered out by the centrifugal force of the impeller 5. When it reaches the vortex chamber 8 by colliding with the crushing plate 6 of the upper phase and becoming more fine particles, the purified air and the harmful gas and the smoke are separated into the adsorbed water, and the clean air is discharged to the exhaust port 11 and harmful. The water adsorbed gas and soot is discharged into the drain 11 "and then terminated.
Description
본 고안은 공기속에 함유된 유해가스나 분진을 습식으로 분리 제거하는 세정 집진기에 관한 것이다.The present invention relates to a cleaning dust collector that wetly separates and removes harmful gases or dust contained in the air.
종래에도 여러 가지 종류의 분진제거 장치가 개발되고 있으나 이와 같은 장치들 중 건식분리 장치는 분리효율이 저조하고 습식으로 된 것은 시설규모가 크고, 구조가 복잡하여 고장의 빈도가 높고, 또한 많은 동력이 소요되기 때문에 이의 유지관리에 있어서도 많은 문제점이 있었던 것이다.Conventionally, various kinds of dust removal devices have been developed, but among these devices, the dry separation device has a low separation efficiency and a wet type, which has a large facility size, a complicated structure, a high frequency of failure, and a lot of power. There was a lot of problems in their maintenance because it takes.
본 고안은 이상의 문제점을 해결하고자 안출한 것으로 이의 고안요지는 유입구로 통해 흡입된 유해가스 및 분진이 급수관의 노즐에서 분무되는 분사수와 함께 임팰러실에 유입되면 고속회전의 임팰러 및 몸체에 부착된 분쇄판에 의해 강제흡입 및 미분쇄되어 와류실 및 원심분리실을 거치는 과정 청정공기와 유해가스 및 분진이 함침된 물입자로 분리되어 청정공기는 배기구로 배출되고 분진과 유해가스가 함침된 물입자는 배수구를 통해 배수되어 종말처리되게 한 것이다.The present invention was devised to solve the above problems, and the subject matter of the present invention is that when harmful gas and dust sucked through the inlet enter the impeller chamber together with the sprayed water sprayed from the nozzle of the water supply pipe, it is attached to the impeller and the body of the high speed rotation. Process of forced suction and pulverization by pulverizing plate and passing through vortex chamber and centrifugal chamber.Clean air is separated into clean air, harmful gas and dust impregnated water particles, and clean air is exhausted through the exhaust port, and dust and harmful gas impregnated water particles. Is to be drained through the drain and terminated.
제1도는 본 고안의 장치 표시 단면도.1 is a cross-sectional view of the device of the present invention.
제2도는 본 고안의 평면 표시 단면도.2 is a plan view cross-sectional view of the present invention.
* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings
1 : 몸체 1' : 공실1: Body 1 ': Vacancy
2 : 받침대 2' : 지지간2: base 2 ': support
3 : 축간 4 : 베아링3: Axle 4: Bearing
5 : 임팰러 5' : 고정구5: impeller 5 ': fixture
6 : 분쇄판 7 : 격판6: grinding plate 7: diaphragm
8 : 와류실 9 : 원심분리실8: vortex chamber 9: centrifuge chamber
10 : 배출관 11 : 배기구10 exhaust pipe 11 exhaust port
11' : 배수구 12 : 상부몸체11 ': drain hole 12: upper body
13 : 흡입혼합실 14 : 유입구13: suction mixing chamber 14: inlet
15 : 급수관 15' : 분배관15: water supply pipe 15 ': distribution pipe
15" : 노즐 16 : 흡입관15 ": Nozzle 16: Suction line
16' : 흡입구 17, 18 : 풀리16 ': inlet 17, 18: pulley
19 : 벨트 20 : 모터19: belt 20: motor
이를 도면에 의거 상세히 설명하면 다음과 같다.This will be described in detail based on the drawings.
몸체(1)의 하부에는 받침대(2) 및 지지간(2')를 개재시켜 축간(3)이 설치되고, 축간(3)의 하단에는 모터(20)의 축간에 끼움된 풀리(18)와 벨트(19)로 연결한 풀리(17)가 설치되며 축간(3)의 상단부에는 다수의 방사상 익편을 가진 흡기팬을 겸한 임팰러(5)가 설치되어 고정구(5')에 의해 고정되며 임팰러(5)의 주위인 몸체(1)의 주면에는 동심원상으로 다수의 경사 분쇄판(6)이 설치되고 그 외방에는 격판(7)을 개재시켜 와류실(8) 및 원심분리실(9)을 형성하고 원심분리실(9)의 일측에는 배출관(10)을 연결하되 이 배출관의 외측에는 배기구(11)가 연결되고 그 하방에는 배수구(11')가 연결되며 몸체(1)의 상부에 설치된 흡입구(16')에는 유입관(16)이 연결되고 이의 내주면에는 급수관(15)과 연결된 다수의 노즐(15")을 부착한 분배관(15')이 설치되고 그 하방에는 깔대기형 유입구(14)를 개재한 흡입혼합실(13)이 형성된 것이다.A shaft 3 is installed at a lower portion of the body 1 via a pedestal 2 and a support shaft 2 ', and at the lower end of the shaft 3, a pulley 18 fitted between the shaft of the motor 20 and A pulley 17 connected by a belt 19 is installed, and an impeller 5 serving as an intake fan having a plurality of radial blades is installed at the upper end of the shaft 3, and is fixed by a fixture 5 ′. On the main surface of the body 1, which is the periphery of 5), a plurality of inclined pulverizing plates 6 are installed concentrically, and the vortex chamber 8 and the centrifugal chamber 9 are formed through the diaphragm 7 on the outside thereof. And one side of the centrifugal chamber (9) is connected to the discharge pipe 10, the discharge port 11 is connected to the outside of the discharge pipe and the drain port 11 'is connected to the lower portion of the inlet (top) 16 ') is connected to the inlet pipe 16, and the inner peripheral surface thereof is provided with a distribution pipe (15') attached to a plurality of nozzles (15 ") connected to the water supply pipe (15) and the funnel type inlet below To 14 having a suction mixing chamber (13) through a.
이상과 같이 구성된 본 고안은 세정집진기인바 이를 사용할시는 모터(20)를 가동시키면 풀리(17)(18) 및 벨트(19)로 연결된 축간(3)이 회동됨에 따라 임팰러(5)는 고속회전을 하게 되고, 급수관(15)과 연결된 모터펌프가 가동됨에 따라 노즐(15")에서는 물을 분무하게 된다.According to the present invention configured as described above, when the motor 20 is used when the cleaning dust collector is used, the impeller 5 is rotated as the shaft 3 connected to the pulleys 17 and 18 and the belt 19 is rotated. As the motor pump is connected to the water supply pipe 15, the nozzle 15 "sprays water.
이때 임팰러(15)가 고속회전됨에 따라 생기는 구심력에 의해 흡입관(16)의 흡입구(16')을 통해 흡입혼합실(13)에 강제 유입된 매연 및 유해가스는 노즐(15")에서 분사되는 분무수에 의해 흡착되어 미세한 물입자가 된다.At this time, the fumes and harmful gases forced into the suction mixing chamber 13 through the suction port 16 'of the suction pipe 16 by the centripetal force generated by the high speed rotation of the impeller 15 are injected from the nozzle 15 ". Adsorbed by the sprayed water, it becomes fine water particles.
이와 같이 매연과 유해가스가 함유된 물미입자는 임팰러(5)의 흡인력에 의해 유입구(14)를 지나 임팰러실내에 유입된 후 고속회전되는 임팰러(5)의 원심력에 의해 몸체(1)에 설치된 경사분쇄판(6)에 부딪치면서 더욱 미세하게 파쇄되어 와류실(8) 및 원심분리실(9)로 유입되는 과정 공기와 물로 분리된 후 원심분리실(9)에 이르게 되면 청정된 공기는 배기구(11)를 통해 밖으로 배출되고 유해가스입자와 매연 등의 분진은 물속에 함침된 후 배수구(11')로 배출되어 종말처리조로 유입된다.As described above, the fine particles containing soot and harmful gas are introduced into the impeller chamber by the suction force of the impeller 5, and then the centrifugal force of the impeller 5 is rotated at high speed. When it hits the inclined crushing plate (6) installed in the finely divided into process air flowing into the vortex chamber (8) and the centrifuge chamber (9) and water is separated into the centrifuge chamber (9) Is discharged out through the exhaust port 11 and dust, such as harmful gas particles and soot is impregnated in the water and discharged into the drain 11 'and flows into the terminal treatment tank.
이상과 같이 본 고안은 임팰러(5)의 고속회전시 생기는 구심력은 유해가스와 매연을 강제 유입시켜 흡입혼합실(13)내에서 분무되는 분사수와 혼합시켜 물미입자가 되게 하고 고속회전되는 임팰러(5)의 원심력은 물미입자를 분쇄판(6)에 보내면 분쇄판(6)에서는 이를 더욱 미분쇄한 후 와류실(8)에 보내면 와류실(8)내에서는 물과 공기로 분리시켜 원심분리실(9)로 이송하게 되면 원심분리실(9)내에서는 청정된 공기는 배기구(11)로 배출되게 하고 유해가스 및 집진물이 흡착된 물은 배수구(11')로 통해 종말처리조로 배출되게 하였기 때문에 매우 실용적이다.As described above, the present invention is the centripetal force generated during the high speed rotation of the impeller (5) is forced to flow harmful gases and soot mixed with the sprayed water sprayed in the suction mixing chamber 13 to be fine particles of water and rotated at high speed The centrifugal force of the parlor 5 sends the fine particles of water to the pulverizing plate 6, and further pulverizes them in the pulverizing plate 6, and then sends them to the vortex chamber 8 to separate them into water and air in the vortex chamber 8. When transported to the separation chamber (9), in the centrifugal separation chamber (9), clean air is discharged to the exhaust port (11), and water adsorbed with harmful gases and dust is discharged to the terminal treatment tank through the drain port (11 '). It is very practical.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR2019950008209U KR200150693Y1 (en) | 1995-04-17 | 1995-04-17 | Dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR2019950008209U KR200150693Y1 (en) | 1995-04-17 | 1995-04-17 | Dust collector |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| KR960033647U KR960033647U (en) | 1996-11-19 |
| KR200150693Y1 true KR200150693Y1 (en) | 1999-07-01 |
Family
ID=19411806
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR2019950008209U Expired - Lifetime KR200150693Y1 (en) | 1995-04-17 | 1995-04-17 | Dust collector |
Country Status (1)
| Country | Link |
|---|---|
| KR (1) | KR200150693Y1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101074031B1 (en) * | 2009-06-12 | 2011-10-17 | 남진산업(주) | Fan and air-purification device |
| KR101187926B1 (en) * | 2010-08-16 | 2012-10-05 | (주)여진 | System for removing viscosity particle and stench |
| KR20160025366A (en) * | 2014-08-27 | 2016-03-08 | (주) 남진 | Wet Type Air Cleaner |
-
1995
- 1995-04-17 KR KR2019950008209U patent/KR200150693Y1/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101074031B1 (en) * | 2009-06-12 | 2011-10-17 | 남진산업(주) | Fan and air-purification device |
| KR101187926B1 (en) * | 2010-08-16 | 2012-10-05 | (주)여진 | System for removing viscosity particle and stench |
| KR20160025366A (en) * | 2014-08-27 | 2016-03-08 | (주) 남진 | Wet Type Air Cleaner |
| KR101691638B1 (en) | 2014-08-27 | 2017-01-02 | (주) 남진 | Wet Type Air Cleaner |
Also Published As
| Publication number | Publication date |
|---|---|
| KR960033647U (en) | 1996-11-19 |
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