KR20000018211A - The method of a minute dust collecting - Google Patents
The method of a minute dust collecting Download PDFInfo
- Publication number
- KR20000018211A KR20000018211A KR1020000002761A KR20000002761A KR20000018211A KR 20000018211 A KR20000018211 A KR 20000018211A KR 1020000002761 A KR1020000002761 A KR 1020000002761A KR 20000002761 A KR20000002761 A KR 20000002761A KR 20000018211 A KR20000018211 A KR 20000018211A
- Authority
- KR
- South Korea
- Prior art keywords
- dust
- aggregating agent
- fine dust
- blower
- polymer aggregating
- Prior art date
Links
- 239000000428 dust Substances 0.000 title claims abstract description 52
- 238000000034 method Methods 0.000 title claims abstract description 5
- 229920000642 polymer Polymers 0.000 claims abstract description 16
- 239000007921 spray Substances 0.000 claims abstract description 3
- 239000000701 coagulant Substances 0.000 claims description 13
- 239000000809 air pollutant Substances 0.000 claims description 4
- 231100001243 air pollutant Toxicity 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 4
- 238000005406 washing Methods 0.000 claims description 3
- 239000013618 particulate matter Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 10
- 239000007788 liquid Substances 0.000 abstract description 8
- 230000005484 gravity Effects 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 4
- 230000004931 aggregating effect Effects 0.000 abstract 4
- 239000003795 chemical substances by application Substances 0.000 abstract 4
- 239000003344 environmental pollutant Substances 0.000 description 6
- 231100000719 pollutant Toxicity 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 238000003915 air pollution Methods 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- G—PHYSICS
- G07—CHECKING-DEVICES
- G07D—HANDLING OF COINS OR VALUABLE PAPERS, e.g. TESTING, SORTING BY DENOMINATIONS, COUNTING, DISPENSING, CHANGING OR DEPOSITING
- G07D7/00—Testing specially adapted to determine the identity or genuineness of valuable papers or for segregating those which are unacceptable, e.g. banknotes that are alien to a currency
- G07D7/06—Testing specially adapted to determine the identity or genuineness of valuable papers or for segregating those which are unacceptable, e.g. banknotes that are alien to a currency using wave or particle radiation
- G07D7/12—Visible light, infrared or ultraviolet radiation
-
- G—PHYSICS
- G07—CHECKING-DEVICES
- G07D—HANDLING OF COINS OR VALUABLE PAPERS, e.g. TESTING, SORTING BY DENOMINATIONS, COUNTING, DISPENSING, CHANGING OR DEPOSITING
- G07D11/00—Devices accepting coins; Devices accepting, dispensing, sorting or counting valuable papers
- G07D11/20—Controlling or monitoring the operation of devices; Data handling
Landscapes
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
본 발명은 각종 산업시설에서 발생되는 대기오염물질중 미세먼지의 집진처리방법에 관한 것이며 원심력 집진시설과 세정식 집진시설을 이용하여 미세먼지의 비중과 입경을 크게하여 효과적으로 집진처리할 수 있도록 한 것이다.The present invention relates to a method for collecting fine dust among air pollutants generated in various industrial facilities and to effectively collect dust by increasing the specific gravity and particle size of the fine dust using a centrifugal force dust collector and a cleaning dust collector. .
일반적으로 대기오염의 집진처리는 전기집진시설, 여과집진시설, 원심력집진시설, 관성력 집진시설, 세정식 집진시설이 있고 대기오염의 발생상태에 따라 경제성과 집진시설의 특징을 고려하여 선택적으로 사용하게 된다.Generally, air pollution dust collection treatment includes electric dust collection facilities, filter dust collection facilities, centrifugal dust collection facilities, inertial dust collection facilities, and cleaning dust collection facilities. do.
그러나 대기오염량이 많은 전기로, 용광로 등지의 경우에는 3㎛이하의 미세먼지(분진)가 많이 발생되며 이를 집진하는 시설로는 전시집진시설이나 여과집진시설이 입경이 적은 미세먼지의 집진처리가 효과적이기는 하나 이는 설치와 유지관리에 많은 비용이 소요되는 문제점이 발생되고 원심력 집진시설이나 세정식 집진시설의 경우에는 시설비용과 유지관리 비용은 절감되나 3μ이하의 미세먼지는 비중이 극히 적고 입경이 적어 이를 집진처리하기에는 처리효율이 다른 처리시설보다 떨어져 이들 시설은 사용되지 못하고 있다.However, in the case of electric furnaces, blast furnaces, etc., which have a large amount of air pollution, a lot of fine dust (dust) of less than 3 ㎛ is generated. This is a costly problem for installation and maintenance. In the case of centrifugal dust collectors or cleaning dust collectors, the cost of facilities and maintenance is reduced, but the fine dust of less than 3μ is extremely small and the particle size is small. In order to collect this, the treatment efficiency is lower than that of other treatment facilities, and these facilities are not used.
이에 본 발명은 종래의 위와 같은 제반결점을 해소하고 원심력 집진시설과 세정식 집진시설을 이용하여 3μ이하인 미세먼지의 집진효율을 극대히 높일 수 있도록 함에 그 목적을 두고 있다.Accordingly, the present invention aims to solve the above-mentioned general defects and to increase the dust collection efficiency of fine dust which is 3μ or less by using a centrifugal force dust collector and a cleaning dust collector.
도은 본 발명의 블럭도Is a block diagram of the present invention.
도2는 종래의 집진처리상태를 보인 블럭도Figure 2 is a block diagram showing a conventional dust collecting state
※ 도면의 주요부분에 대한 부호설명※ Explanation of Codes on Major Parts of Drawings
1 : 대기오염 발생원 2 : 송풍기1: air pollution source 2: blower
3 : 집진시설 4 : 배기관3: dust collection facility 4: exhaust pipe
5 : 고분자응집제고압분무장치 6 : 이송관5: polymer coagulant high pressure spraying device 6: feed pipe
7 : 와류판7: vortex plate
오염물질발생원(1)의 대기오염물질을 송풍기(2)를 통하여 원심력 또는 세정식 집진시설(3)로 유입시켜 집진처리후 배기관(4)을 통하여 배기함에 있어서, 오염물질발생원(1)과 송풍기(2) 사이의 이송관(6)에 와류판(7)과 고분자응집제고압분무장치(5)를 설치하여서 된 구성이다.In the air pollutant of the pollutant source (1) is introduced into the centrifugal force or washing dust collector (3) through the blower (2), and the dust is treated and exhausted through the exhaust pipe (4), the pollutant source (1) and the blower It is the structure which provided the vortex board 7 and the high molecular | density coagulant high pressure spraying apparatus 5 in the transfer pipe 6 between (2).
이와 같은 본 발명은 산업시설에 오염물질발생원(1)에서 오염물질을 송풍기(2)를 통하여 이송관(6) 내로 유입하게되면 유입되는 대기오염물질은 와류판 (6)에서 와류가 형성되고 이와 동시에 동 와류판(6)과 근접위치에 설치된 고분자응집제고압분무장치(5)에서 액상의 고분자응집제가 액상의 분자상태로 분무되어 미세먼지와 고분자응집제의 액상분자가 결합되면서 자체 가스온도에 의해 건조되어 3μ이하의 미세먼지 입자는 비중과 입경이 큰 오염물질로 변화시켜서 입경과 비중이 커진 상태에서 송풍기(2)를 통하여 집진시설(원심력 또는 세정식)(3)로 유입되어 집진처리가 이루어지고 집진처리된 공기는 배기관(4)으로 통하여 배기가 이루어지게 된다.In the present invention as described above, when the pollutant is introduced into the transfer pipe 6 through the blower 2 from the pollutant source 1 in an industrial facility, the air pollutant introduced therein forms a vortex in the vortex plate 6. At the same time, in the polymer coagulant high pressure spraying device (5) installed in close proximity to the copper vortex plate (6), the liquid polymer coagulant is sprayed in the liquid molecular state, and the fine dust and the liquid molecule of the polymer coagulant are combined and dried by their own gas temperature. The fine dust particles of 3μ or less are converted into pollutants having a large specific gravity and particle diameter, and the dust is treated by being introduced into the dust collecting facility (centrifugal force or washing type) 3 through the blower (2) while the particle diameter and specific gravity are increased. The collected air is exhausted through the exhaust pipe (4).
이 때 고분자응집제의 고압분무장치(5)에서 분사되는 액상의 고분자응집제는 오염물질이 이송관(6)으로 유입되는 양과 오염물질의 입경에 따라 분사량이 달라지게 되므로 고압분무장치(5)의 노즐수를 여러개로 설치하여 분사량을 조절하면 되고, 또 고분자응집제는 점성을 가진 액상이고 미세먼지는 고체이므로 결합이 잘 되므로 집진처리에 효과적인 상태의 비중과 입경이 되도록 고분자응집제의 분사량을 조절하면 된다.In this case, the liquid polymer coagulant sprayed from the high pressure spray device 5 of the polymer coagulant may vary depending on the amount of contaminants introduced into the transfer pipe 6 and the particle size of the pollutant. The number of injections may be adjusted by installing a plurality of water, and the polymer coagulant may be a viscous liquid and fine dust solid, so that the cohesion may be well controlled.
이와 같은 본 발명은 이송관(6)으로 유입되는 오염된 기체는 150~200℃ 상태이고 오염된 기체 속에 3μ이하인 미세먼지와 이송관(6) 내에 10Kg/㎤ 이상으로 분사되는 고분자응집제의 액상분자가 결합되어져 비중과 입경이 큰 물질로 바뀌어져 집진시설(3)로 유입되고 집진처리 되므로 집진효율은 전기집진시설이나 여과 집진시설의 효율이상으로 높아지게 되고 고분자응집제의 분사비용이 추가되나 전기집진시설이나 여과집진시설의 운영비용보다는 경제적이 된다.In the present invention, the contaminated gas flowing into the conveying tube 6 is in a state of 150 to 200 ° C., and the fine dust having 3 μm or less in the contaminated gas and the liquid molecules of the polymer coagulant sprayed at 10 Kg / cm 3 or more in the conveying tube 6. Is combined, and the specific gravity and particle size are changed into materials, which are introduced into the dust collecting facility (3) and are collected and treated. Therefore, the dust collecting efficiency becomes higher than the efficiency of the electric dust collecting facility or the filter dust collecting facility, and the injection cost of the polymer coagulant is added. However, it is more economical than the operating cost of the bag filter.
따라서 이상과 같은 본 발명은 원심력 집진시설 또는 세정식 집진시설에서 오염물질발생원에 설치하는 이송관에 와류판과 고분자응집제 분사장치를 설치하여 액상의 고분자응집제 분자를 미세먼지와 결합하여 비중과 입경을 크게 형성하여 집진처리하므로서 미세먼지의 집진처리 효율을 높일수 있고 전기집진시설이나 여과집진 시설에 비하여 집진처리 비용을 절감할 수 있는 매우 유용한 발명이다.Therefore, the present invention as described above, by installing a vortex plate and a polymer coagulant injector in the transfer pipe installed in the source of contaminants in a centrifugal dust collector or a cleaning dust collector to combine the liquid polymer coagulant molecules with fine dust to increase the specific gravity and particle size It is a very useful invention that can increase the dust collection efficiency of the fine dust by forming a large dust collecting treatment, and reduce the dust collection cost compared to the electric dust collector or filter dust collector.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020000002761A KR20000018211A (en) | 2000-01-21 | 2000-01-21 | The method of a minute dust collecting |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020000002761A KR20000018211A (en) | 2000-01-21 | 2000-01-21 | The method of a minute dust collecting |
Publications (1)
Publication Number | Publication Date |
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KR20000018211A true KR20000018211A (en) | 2000-04-06 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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KR1020000002761A KR20000018211A (en) | 2000-01-21 | 2000-01-21 | The method of a minute dust collecting |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100883536B1 (en) * | 2008-05-14 | 2009-02-17 | 대지정공주식회사 | Dust process device of a workshop |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62106819A (en) * | 1985-11-01 | 1987-05-18 | Tokyo Copal Kagaku Kk | Method and apparatus for cleaning air |
JPS62114625A (en) * | 1985-11-13 | 1987-05-26 | Ishikawajima Harima Heavy Ind Co Ltd | Method and apparatus for purifying dust-containing high-temperature gas |
JPH03217212A (en) * | 1990-01-19 | 1991-09-25 | Ken Tanaka | Wet type dust removing device with outer air introducing hole |
JPH06292842A (en) * | 1993-04-09 | 1994-10-21 | Hitachi Ltd | Dust removing device |
JPH1066818A (en) * | 1996-08-26 | 1998-03-10 | Nico Tec:Kk | Dust collecting apparatus |
JPH10151373A (en) * | 1996-11-22 | 1998-06-09 | Tsutomu Nozaki | Setting-type liquid cyclone separator provided with rapid exhauster |
KR19990010029A (en) * | 1997-07-14 | 1999-02-05 | 박현수 | Filter dust collector for gaseous and particulate contaminants |
-
2000
- 2000-01-21 KR KR1020000002761A patent/KR20000018211A/en not_active Application Discontinuation
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62106819A (en) * | 1985-11-01 | 1987-05-18 | Tokyo Copal Kagaku Kk | Method and apparatus for cleaning air |
JPS62114625A (en) * | 1985-11-13 | 1987-05-26 | Ishikawajima Harima Heavy Ind Co Ltd | Method and apparatus for purifying dust-containing high-temperature gas |
JPH03217212A (en) * | 1990-01-19 | 1991-09-25 | Ken Tanaka | Wet type dust removing device with outer air introducing hole |
JPH06292842A (en) * | 1993-04-09 | 1994-10-21 | Hitachi Ltd | Dust removing device |
JPH1066818A (en) * | 1996-08-26 | 1998-03-10 | Nico Tec:Kk | Dust collecting apparatus |
JPH10151373A (en) * | 1996-11-22 | 1998-06-09 | Tsutomu Nozaki | Setting-type liquid cyclone separator provided with rapid exhauster |
KR19990010029A (en) * | 1997-07-14 | 1999-02-05 | 박현수 | Filter dust collector for gaseous and particulate contaminants |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100883536B1 (en) * | 2008-05-14 | 2009-02-17 | 대지정공주식회사 | Dust process device of a workshop |
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