KR20030083115A - The de-sulfuration de-dioxins Equipment for Waste treatment system - Google Patents
The de-sulfuration de-dioxins Equipment for Waste treatment system Download PDFInfo
- Publication number
- KR20030083115A KR20030083115A KR1020020021529A KR20020021529A KR20030083115A KR 20030083115 A KR20030083115 A KR 20030083115A KR 1020020021529 A KR1020020021529 A KR 1020020021529A KR 20020021529 A KR20020021529 A KR 20020021529A KR 20030083115 A KR20030083115 A KR 20030083115A
- Authority
- KR
- South Korea
- Prior art keywords
- housing
- discharge electrodes
- dust collecting
- water
- dioxins
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/16—Plant or installations having external electricity supply wet type
-
- 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
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/10—Venturi scrubbers
-
- 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
- B01D47/14—Packed scrubbers
-
- 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
- B01D53/02—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 adsorption, e.g. preparative gas chromatography
- B01D53/04—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 adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- 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
- B01D53/32—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 electrical effects other than those provided for in group B01D61/00
-
- 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
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/41—Ionising-electrodes
Abstract
Description
본 발명은 도시쓰레기, 산업폐기물, 하수슬러지 등을 소각 처리하거나 용융, 고화 처리하기 위한 소각로, 용융로 등의 폐기물 처리시설에서 발생하는 배기가스를 처리하기 위한 집진장치에 관한 것으로, 특히 배기가스중에 포함된 분진과 설비의 부식을 촉진하고 호흡기를 통한 폐질환을 일으키는 스모그의 원인물질인 황산화물등의 가스상 오염물질과 인체에 치명적인 위해를 끼치는 발암물질로 알려진 다이옥신이나 퓨란 등의 환경오염물질을 동시에 처리할 수 있도록 한 것이다.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust collecting apparatus for treating exhaust gases generated in waste treatment facilities such as incinerators and melting furnaces for incineration, melting, and solidifying municipal waste, industrial waste, and sewage sludge. Simultaneous treatment of dust and gaseous pollutants such as sulfur oxides, which are the causes of smog that promotes corrosion of facilities and lung diseases through respiratory tracts, and environmental pollutants such as dioxins and furans, known as carcinogens, which cause fatal harm to the human body It is to be done.
일반적으로 사회 활동에 따라 부수적으로 발생하는 생활폐기물이나 산업폐기물 등을 2차적인 오염없이 처리함으로서 후대에 청정한 자연환경을 물려줄 수 있도록 하는 것은 인류의 숙원인 동시에 시급히 해결하여야 할 문제로 대두되어지고 있다.In general, it is a matter of humankind's desire and urgent problem to be solved by disposing of clean and natural environment by disposing secondary wastes and secondary wastes caused by social activities without secondary pollution. have.
통상 산업활동에 의해 발생하는 폐기물이나 일반적인 도시쓰레기 등을 처리하기 위해서는 재활용이 가능한 자원으로 분리하여 재활용을 하는 것이고, 재활용이 불가능한 폐기물중 썩는 것은 매립하여 처리하고 썩지 않는 것 중 연소가 가능한 유기물로 이루어진 폐기물은 소각 처리하거나 용융 고화시켜 해수면 매립 등에 활용토록 하고 있는 것이다.In order to dispose of wastes generated by industrial activities and general urban waste, it is usually separated into recyclable resources and recycled.In the non-recyclable wastes, the decayed waste is made up of landfilled organic matter that is combustible. Waste is incinerated or melted and used for landfilling.
근래에는 매립지의 부족으로 소각처리가 선호되고 있으며 많은 국가에서도폐기물 소각장 건립에 많은 예산을 투입하고 있는 실정이다.In recent years, incineration is preferred due to the lack of landfill, and many countries have invested a lot of money in constructing waste incinerators.
그러나, 이러한 폐기물을 소각 처리할 때에는 폐기물이 연소되면서 많은 먼지와 유해한 가스가 동시에 배출되어짐으로서 이러한 오염물질이 대기중으로 배출되지 않도록 하기 위한 적절한 오염방지시설의 설치가 요구되는 것이었다.However, incineration of these wastes required the installation of appropriate pollution prevention facilities to prevent the release of these pollutants into the atmosphere as the wastes were combusted, releasing many dusts and harmful gases at the same time.
특히, 이러한 배기가스 중에는 쓰레기에 함유되어진 황 성분이 연소용 공기와 결합하여 황산화물의 형태로 배출되어짐으로서 산업 설비와 교량 등 강재 구조물의 부식을 촉진하게되어 내구성을 떨어뜨림으로서 비용의 상승을 초래하고 특히, 스모그의 발생을 일으키는 원인물질로서 그 독성으로 인한 호흡기 자극과 폐질환을 일으키게 됨으로서 인류에게 폐해를 주게되는 것이다.Particularly, in these exhaust gases, sulfur components contained in the waste are discharged in the form of sulfur oxides in combination with combustion air, which promotes corrosion of steel structures such as industrial facilities and bridges, resulting in increased durability by lowering durability. In particular, as a substance that causes the occurrence of smog causes respiratory irritation and lung disease due to its toxicity is harmful to mankind.
또한, 베트남 전쟁에서 사용된 고엽제를 통해, 그 독성이 널리 인식된 다이옥신이 쓰레기 속에 본래부터 존재하던 것들의 일부가 소각시 분해되지 않거나, 염화벤젠(Chlorinated benzene)이나 염화페놀(Chlorinated phenol), 염화비닐(PVC) 등 다이옥신류와 관련된 화학구조를 갖는 화합물 등이 이미 쓰레기속에 존재하였거나 소각시 우선적으로 형성된 뒤 이들로부터 후속적인 반응을 통해 다이옥신류가 형성되거나, 다이옥신류와는 화학적으로 직접적인 관련이 없는 여러 물질들이 복잡한 반응을 통해서 발생되는 것이다.In addition, through the defoliant used in the Vietnam War, some of the toxic dioxin, which was widely recognized as toxic, did not decompose when incinerated, or chlorinated benzene, chlorinated phenol, Compounds having a chemical structure related to dioxins, such as vinyl (PVC), have already been present in the waste or formed preferentially upon incineration, and subsequent reactions therefrom form dioxins or have no chemical direct relationship with dioxins. Many substances occur through complex reactions.
이러한 다이옥신류는 소각시설의 로내 온도가 저온 영역에서 온도의 증가에 따라 발생수준이 급격히 감소하다가 다시 온도의 증가에 따라 증가되어지는 특성을 보인다.These dioxins have a characteristic that the temperature in the furnace of the incineration facility decreases rapidly as the temperature increases in the low temperature range, and then increases with the increase of the temperature.
따라서 이러한 다이옥신류의 발생을 억지하기 위해서는 소각시에 충분한 온도와 연소시간을 줌으로서 독성유기물질의 파괴를 유도하여야 하나 배출되어지는 쓰레기의 특성상 원소 조성의 균질화가 어렵고 완전한 혼합이 가능하지 못해 로내에서 부분적으로 저온구간이 생기고 이로 말미암아 불완전 연소의 원인이 되어 다이옥신류의 파괴가 제대로 일어나지 않게 되는 것이고, 동시에 다이옥신류로 변화되기 쉬운 염화벤젠(Chlorinated benzene)이나 염화페놀(Chlorinated phenol), 염화비닐(PVC) 등의 전구물질의 생성이 일어나게 되는 것이다.Therefore, in order to suppress the generation of dioxin, it is necessary to induce destruction of toxic organic substances by providing sufficient temperature and combustion time during incineration, but it is difficult to homogenize the composition of elements due to the characteristics of the wastes discharged and it is not possible to mix completely in the furnace. The low temperature zone is partially generated, which causes incomplete combustion, which prevents the destruction of dioxins, and at the same time, it is easily changed into dioxins such as chlorinated benzene, chlorinated phenol, and vinyl chloride (PVC). Will produce precursors, etc.).
특히, 쓰레기 연소가스중에 다이옥신류는 섭씨 250도 ~ 400도 사이에서 활발하게 재형성이 일어남으로서 배기가스의 처리를 위한 방지시설에 유입할 때 급격한 냉각을 필요로 하게 되는 것이다.In particular, dioxin in the waste combustion gas is actively reformed between 250 degrees Celsius and 400 degrees Celsius, which requires rapid cooling when entering the prevention facility for the treatment of exhaust gas.
종래에 소각시설에서 발생되는 먼지나 유해가스 등을 제거하기 위한 환경오염방지시설은 그 대다수가 다이옥신류의 독성물질을 제거하기 위한 목적이 아니라 산성가스나 중금속 등을 제거하기 위한 목적으로 설립된 것으로 불특정 다수인이 다이옥신류에 노출되어짐으로서 건강상 위해를 입을 수 있다는 문제점이 있었다.Conventionally, environmental pollution prevention facilities for removing dust and harmful gases generated in incineration facilities are established for the purpose of removing acid gases and heavy metals, but not for removing toxic substances of dioxins. There was a problem that many unspecified people could suffer health risks by being exposed to dioxins.
근래에는 다양한 방법으로 다이옥신류의 제거를 위한 환경오염방지시설이 제안되어지고 있으며 대표적인 방법으로는 흡착에 의해 제거하는 방법으로 세부적으로는 촉매의 반응을 이용하거나 산화반응을 이용하거나 흡착반응을 이용하는 방법 등이 이용되고 있는 것이다.Recently, environmental pollution prevention facilities for the removal of dioxins have been proposed in various ways. As a representative method, removal by adsorption is carried out by adsorption reaction in detail, using catalyst reaction, oxidation reaction or adsorption reaction. Etc. are used.
이러한 흡착에 의해 제거하는 방법은 다이옥신과 분사되는 물의 미용된 황산화물을 동시에 제거할 수 있는 것으로 활성탄이나 소석회 등의 흡착제를 방지시설의 전단에서 분무하여 배기가스와 혼합시킴으로서 흡착을 유도하고 다이옥신류가흡착된 흡착제를 후단부에서 여과포나 전기집진기 등을 이용해서 포집도록 하는 것으로 배기가스중에 불티가 포함되거나 온도가 비교적 높을 경우 화재의 위험이 있고, 배기 가스중에 다이옥신류의 함유 농도와 관계없이 항상 일정한 양의 흡착제를 분무시킴으로서 비용이 많이 소요되는 단점이 있었으며, 난류가 형성되거나 흡착제가 도달하지 못하는 사각지역으로는 미처리된 가스가 통과될 수 있다는 문제점이 있었다.The removal method by adsorption can simultaneously remove dioxins and undissolved sulfur oxides in the sprayed water. The adsorbents such as activated carbon and slaked lime are sprayed at the front of the prevention facility and mixed with the exhaust gas to induce adsorption. The absorbent adsorbent is collected at the rear end by using a filter cloth or an electrostatic precipitator.There is a risk of fire if the exhaust gas contains sparks or the temperature is relatively high. There was a disadvantage in that the cost is high by spraying the amount of the adsorbent, there was a problem that the untreated gas can pass through the blind area where turbulence is formed or the adsorbent does not reach.
한편, 전기집진기는 (+)전하가 대전되어진 다수개의 집진판 사이로 (-)전하를 띄는 방전극을 형성하여 집진판 사이로 이동하는 배기가스중에 포함된 분진 등의 입자상 오염물질에 (-)전하를 대전시켜 (+)전하를 띄는 집진판에 접착시켜 제거하는 것으로 고온 배기 가스의 처리와 고농도로 함진된 배기가스를 처리할 수 있다는 장점을 가지고 있으나 소각시설 등에서 발생하는 유해가스 등은 처리가 곤란하여 별도의 유해가스처리시설을 구비하여야 하며 집진기내 온도가 상승하여 고온에서 운전될 경우 다이옥신의 재생성이 우려되는 문제점이 있었다.On the other hand, the electrostatic precipitator forms a discharge electrode having a negative charge between a plurality of dust collecting plates in which positive charges are charged, thereby charging negative charges to particulate contaminants such as dust contained in exhaust gas moving between the dust collecting plates ( +) It has the advantage of treating high temperature exhaust gas and exhaust gas impregnated with high concentration by attaching to the dust collecting plate with charge, but it is difficult to process harmful gas generated from incineration facilities. It should be equipped with a treatment facility and there is a problem that the regeneration of dioxin is concerned when the temperature in the dust collector is operated at high temperatures.
본 발명은 상기한 종래의 문제점을 해결하기 위하여 안출한 것으로서, 집진판에 지속적으로 물의 분무를 행함으로서 유해가스와 분진을 동시에 처리할 수 있도록 된 습식전기집진기의 후단부에 (-)전하가 대전된 방전극과 활성탄이 충진되고 방전극으로 대전된 (-)전하에 대응토록 (+)전하가 대전되어진 고정상의 흡착층을 형성함으로서 방전극을 통과할 때 (-)전하가 대전된 오염물질의 흡착효율을 높임으로서 습식전기집진기를 통과하면서 미처리된 황산화물과 다이옥신류의 독성물질을쉽게 처리할 수 있도록 한 것이다.The present invention has been made in order to solve the above-described problems, the negative charge is charged to the rear end of the wet electrostatic precipitator which can simultaneously handle the harmful gas and dust by spraying water continuously on the dust collector. The adsorption efficiency of the contaminants charged with (-) charges as they pass through the discharge electrodes is formed by forming a fixed bed adsorption layer in which the (+) charges are charged to correspond to the (-) charges charged with the discharge electrodes and activated carbon. As it passes through the wet electrostatic precipitator, it can easily treat untreated sulfur oxides and toxic substances of dioxins.
도 1은 본 발명의 구성을 보이는 개략적인 종단면도.1 is a schematic longitudinal cross-sectional view showing a configuration of the present invention.
도 2는 본 발명의 제1실시 예에 따른 구성을 보이는 개략적인 종단면도.Figure 2 is a schematic longitudinal cross-sectional view showing a configuration according to a first embodiment of the present invention.
도 3은 본 발명의 제2실시 예에 따른 구성을 보이는 개략적인 종단면도.Figure 3 is a schematic longitudinal cross-sectional view showing a configuration according to a second embodiment of the present invention.
도 4는 본 발명의 제3실시 예에 따른 구성을 보이는 개략적인 종단면도.Figure 4 is a schematic longitudinal cross-sectional view showing a configuration according to a third embodiment of the present invention.
도 5는 본 발명에 따른 패킹의 사시도.5 is a perspective view of a packing according to the present invention;
<도면의주요부분에대한부호의설명>Explanation of symbols on the main parts of the drawing
1 : 가스입구관 3,3' : 분사기1: Gas inlet pipe 3,3 ': Injector
5 : 집진판 6,6` : 방전극5: dust collector 6,6`: discharge electrode
7,7` : 애자 8 : 세척밸브7,7`: insulator 8: washing valve
9 : 분사밸브 11 : 다공판9 injection valve 11 porous plate
14 : 배출구 15 : 고정추14 outlet 15: fixed weight
16 : 몸체 17 : 격자판16 body 17 grid
20 : 패킹층 21 : 물탱크20: packing layer 21: water tank
22 : 패킹 30 : 전기집진층22: packing 30: electrostatic precipitating layer
40 : 흡착층 42 : 활성탄40: adsorption layer 42: activated carbon
50 : 벤츄리 스크러버50: Venturi Scrubber
이하에서는 첨부 도면을 참조하여 본 발명의 가장 바람직한 일 실시 예를 상세히 설명하기로 한다. 우선, 각 도면을 설명함에 있어, 동일한 구성 요소들에 한해서는 비록 다른 도면상에 도시되더라도 가능한 한 동일한 참조부호를 갖는다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. First, in describing each of the drawings, the same components have the same reference numerals as much as possible even though they are shown in different drawings.
제1도에 도시된 바와 같이 본 발명의 구성은 몸체(16)의 일측으로 형성된 가스입구관(1)을 따라 유입되어지는 배기가스를 냉각하고 정화하기 위하여 물이 분무되어지는 분사기(3)가 몸체(16)의 사방으로 형성되어있고, 하부에는 분사된 물을 집수하여 순환사용하기 위한 배출구(14)가 형성되며, 상기 분사기(3)의 후단에는 유입되는 배기가스가 몸체(16)내에 골고루 분산되어질 수 다공판(11)이 형성되고, 일렬로 하방으로 길게 판상형의 집진판(5) 사이에 방전극(6)이 각각 직하방으로 형성되며 방전극(6)의 하부에는 방전극(6)의 고정추(15)의 자중에 의하여 펴지도록 고정추(15)가 형성되며, 상기 고정추(15)는 격자판(17)의 사이에 위치되어 다공판(11)을 통하여 유입되는 배기가스의 유속으로 인하여 방전극(6)이 흔들리는 것을 방지하고 방전극(6)은 집진판(5)의 상부에서 애자(7)를 통하여 전원이 공급되는 전기집진층(30) 및 애자(7`)를 통하여 전원을 공급받는 방전극(6`)과 입상의 활성탄(42)이 소정의 충진된 흡착층(40)으로 이루어지는 구성이다.As shown in FIG. 1, the configuration of the present invention includes an injector 3 in which water is sprayed to cool and purge the exhaust gas flowing along the gas inlet pipe 1 formed at one side of the body 16. It is formed in all directions of the body 16, the lower portion is formed with a discharge port 14 for collecting and circulating the sprayed water, the exhaust gas flowing into the rear end of the injector 3 evenly in the body 16 A porous plate 11 to be dispersed is formed, and discharge electrodes 6 are formed directly below each other between the plate-shaped dust collecting plates 5 extending in a row downward in a row, and a fixed weight of the discharge electrodes 6 is disposed below the discharge electrodes 6. A fixed weight 15 is formed to be unfolded by its own weight of 15, and the fixed weight 15 is positioned between the grid plates 17 and discharged due to the flow rate of the exhaust gas flowing through the porous plate 11. (6) is prevented from shaking and the discharge electrode (6) is the image of the dust collecting plate (5) The adsorption layer 40 in which the electrostatic precipitating layer 30 supplied with power through the insulator 7 and the discharge electrode 6 ′ and granular activated carbon 42 supplied with power through the insulator 7 ′ are filled with a predetermined amount. )
이때 전기집진층(30)의 집진판(5)에 물막을 형성하고 접착된 분진층을 제거하기 위한 위한 분사밸브(9) 및 세척밸브(8)가 형성되어지는 것이다.At this time, the injection valve 9 and the washing valve 8 for forming a water film on the dust collecting plate 5 of the electrostatic precipitating layer 30 and removing the adhered dust layer are formed.
본 발명의 다른 제1실시 예에 따르면, 가스입구관(1)의 전단에는 벤츄리스크러버(50)가 더 형성되어짐으로서 발생된 분진의 농도가 높은 배기가스로부터 분진을 제거함으로서 불티의 유입이나 흡착층(40)의 공극 폐쇄에 의한 활성탄 교체 주기가 감소되지 않도록 할 수 있는 구성이다.According to another first embodiment of the present invention, a venturi scrubber 50 is further formed at the front end of the gas inlet pipe 1 to remove the dust from the exhaust gas having a high concentration of dust, and thus, the inflow or adsorption layer of the bleeding layer. It is a structure which can prevent the activated carbon replacement cycle by the pore closure of 40 not being reduced.
본 발명의 다른 제2실시 예에 따르면, 가스입구관(1)의 후단 몸체(16)내로 구불구불한 면을 형성하여 표면적을 넓힌 다량의 패킹(22)을 충진시킨 1단 이상의 패킹층(20)을 직렬로 더 형성함으로서 분무되어지는 물과 배스가스의 접촉 면적을 증대시켜 유해가스의 흡수 처리 효율을 증대시킬 수 있도록 되는 구성이다.According to a second embodiment of the present invention, one or more packing layers 20 are formed by filling a large amount of packing 22 having a large surface area by forming a serpentine surface into the rear end body 16 of the gas inlet pipe 1. ) Is further formed in series to increase the contact area of water to be sprayed with the bath gas, thereby increasing the absorption efficiency of harmful gases.
본 발명의 다른 제3실시 예에 따르면, 상술한 벤츄리 스크러버(50)와 패킹층(20)이 복합적으로 더 형성되어지는 구성이다.According to another third embodiment of the present invention, the above-described venturi scrubber 50 and the packing layer 20 are further formed in combination.
이때, 소각시설 등으로부터 오염물질의 발생을 최소화하기 위해서 섭씨 850도 이상으로 연소된 쓰레기로부터 발생된 배기가스를 급냉시켜 방지시설로 유입되는 온도를 섭씨 130도 내지 200도 내외로 유지하기 위한 이코노마이저(미도시)를 형성함으로서 본 발명의 따른 방지시설 내에서는 온도에 의해 다이옥신류의 재생성이 일어나지 않도록 하는 것이고 몸체(16)의 후단에는 유인팬(미도시)을 형성하여 가스의 흐름이 원활하게 이루어지도록 할 수 있는 것이다.At this time, in order to minimize the generation of pollutants from incineration facilities, etc., an economizer for quenching the exhaust gas generated from garbage burned above 850 degrees Celsius to maintain the temperature flowing into the prevention facility within 130 degrees Celsius to 200 degrees Celsius ( (Not shown) to prevent the regeneration of dioxin by temperature in the prevention facility according to the present invention and to form a attracting fan (not shown) at the rear end of the body 16 so that the gas flows smoothly. You can do it.
상기 전기집진층(30)의 방전극(6) 및 흡착층(40)의 방전극(6`)으로는 (-)전원이 인가되고, 집진판(5)과 흡착층(40)으로는 (+)전원을 인가시켜 방전극(6)(6`)으로부터 대전되어진 유해가스가 쉽게 집진판(5)에 부착되거나 흡착층(40)에 흡착되어지도록 되는 것이다.The negative power is applied to the discharge electrode 6 of the electrostatic precipitating layer 30 and the discharge electrode 6 'of the adsorption layer 40, and the positive power is supplied to the dust collecting plate 5 and the adsorption layer 40. The harmful gas charged from the discharge electrodes 6, 6 'is easily attached to the dust collecting plate 5 or adsorbed to the adsorption layer 40.
이는 서로 같은 극끼리는 밀어내고 다른 극끼리는 당기는 성질을 이용하는것이다.This is because the same poles are pushed out and the other poles are pulled.
따라서 가스입구관(1)으로 유입되는 유해가스 및 분진의 대부분은 분무기(3)에서 1차로 흡수되거나 전기집진층(30)에 접착되어 정화되어지는 것이고 이러한 가스 중에 잔존하는 황산화물 등의 유해가스는 활성탄(42)이 충진되어진 흡착층(40)을 통과하면서 흡착되어짐으로서 청정한 가스로 배출되어지는 것이다.Therefore, most of the harmful gas and dust flowing into the gas inlet pipe 1 are first absorbed by the sprayer 3 or adhered to the electrostatic precipitating layer 30 to be purified, and the harmful gas such as sulfur oxides remaining in the gas. Is adsorbed while passing through the adsorption layer 40 in which the activated carbon 42 is filled, and is discharged as a clean gas.
특히, 다이옥신류의 재성성에 전구물질로 작용할 수 있는 염화페놀류와 소각재는 대부분이 분무되어지는 물과 집진판(5)에 접착 제거됨으로서 재생성에 의한 2차 오염을 방지할 수 있도록 되는 것이다.In particular, the phenol chlorides and incinerators, which can act as precursors for the regeneration of dioxins, are prevented from being secondaryly prevented by regeneration by being adhesively removed from the water to be sprayed and the dust collector 5.
한편, 1단 이상 직렬로 형성되어진 패킹층(20)에서는 유입되어진 배기가스가 충분한 시간 동안 분무되어진 물에 접촉되어짐으로서 배기가스중에 포함된 황산화물이 충분히 용해되어지도록 되는 것이고, 다이옥신의 재생성에 기인하는 전구물질로 작용할 수 있는 염화페놀류의 흡수와 미립화된 소각재 등을 제거하게 됨으로서 다이옥신의 재생성을 최대한 억제할 수 있는 것이고, 지속적인 살수에 따라 집진장치의 내부온도가 상승되지 않도록 함으로서 다이옥신의 제거와 재생성을 방지할 수 있도록 되는 것이다.On the other hand, in the packing layer 20 formed in one or more stages in series, the introduced exhaust gas is brought into contact with the sprayed water for a sufficient time so that the sulfur oxide contained in the exhaust gas is sufficiently dissolved, and is due to the regeneration of dioxin. By removing the absorption of phenolic chlorides and atomized incinerators that can act as precursors, the regeneration of dioxins can be suppressed as much as possible, and the internal temperature of the dust collector is not increased by continuous watering. Will be prevented.
미설명부호 21은 분무된 물을 집수하기 위한 물탱크이다.Reference numeral 21 is a water tank for collecting the sprayed water.
상술한 바와 같이 본 발명은 폐기물 처리시설에서 대기중으로 배출되는 배기가스중에 황산화물과 다이옥신류의 농도를 저감시킬 뿐만 아니라 다이옥신류의 전구물질인 염화페놀류의 유해가스와 비산재 등의 분진류를 동시에 처리함으로서 재생성에 의한 2차 오염을 방지하게 되는 효과가 있는 것이다.As described above, the present invention not only reduces the concentrations of sulfur oxides and dioxins in the exhaust gas discharged into the atmosphere from waste treatment facilities, but also simultaneously treats harmful gases such as phenol chlorides, which are precursors of dioxins, and dusts such as fly ash. By doing so, there is an effect of preventing secondary contamination by regeneration.
Claims (4)
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2002-0021529A KR100505125B1 (en) | 2002-04-19 | 2002-04-19 | The de-sulfuration de-dioxins Equipment for Waste treatment system |
| CN02122899A CN1451480A (en) | 2002-04-19 | 2002-06-18 | Wet desulfurization electrostatic dust-collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2002-0021529A KR100505125B1 (en) | 2002-04-19 | 2002-04-19 | The de-sulfuration de-dioxins Equipment for Waste treatment system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| KR20030083115A true KR20030083115A (en) | 2003-10-30 |
| KR100505125B1 KR100505125B1 (en) | 2005-07-29 |
Family
ID=29244754
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR10-2002-0021529A KR100505125B1 (en) | 2002-04-19 | 2002-04-19 | The de-sulfuration de-dioxins Equipment for Waste treatment system |
Country Status (2)
| Country | Link |
|---|---|
| KR (1) | KR100505125B1 (en) |
| CN (1) | CN1451480A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101141134B1 (en) * | 2010-02-05 | 2012-05-02 | 한국지질자원연구원 | Method for Removing Chloride in Municipal Solid Waste Incineration Bottom Ash via Washing and Carbonation Process |
| KR101314466B1 (en) * | 2012-05-29 | 2013-10-07 | 센텍(주) | Reactor for contact gas and liquid |
| KR20140126320A (en) * | 2012-03-29 | 2014-10-30 | 두산 렌트제스 게엠베하 | A flue gas purification device |
| KR102008880B1 (en) * | 2018-03-28 | 2019-08-08 | (주)엔노피아 | Complex pollutant treatment device from tire manufacturing process |
| CN116422097A (en) * | 2023-03-28 | 2023-07-14 | 北京华兴碳环境科技有限公司 | Industrial waste gas desulfurization and denitrification device |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101020258B1 (en) * | 2008-11-26 | 2011-03-08 | (주)플라즈마텍 | Acidic Exhaust Gas Treatment System |
| KR100939222B1 (en) * | 2009-08-20 | 2010-01-28 | (주)안성정기 | Device for simultaneous removal of nitrogen oxides and particulate using old and existing electrostatic precipitators |
| KR101239841B1 (en) | 2011-02-09 | 2013-03-11 | 현테크이엔지 주식회사 | White plume and odorous gas treatment module |
| CN102600973B (en) * | 2012-03-16 | 2014-07-02 | 山东大学 | Preposed flue for electrostatic precipitator |
| CN102671767A (en) * | 2012-05-16 | 2012-09-19 | 浙江菲达环保科技股份有限公司 | Wet-type electrical precipitator |
| CN103007681B (en) * | 2012-12-18 | 2015-03-18 | 中冶长天国际工程有限责任公司 | Activated carbon flue gas desulfurization and regeneration device and method |
| CN104492756B (en) * | 2014-12-08 | 2016-10-19 | 沈阳航空航天大学 | A kind of graphite dust processing means |
| KR102080942B1 (en) * | 2018-05-24 | 2020-02-24 | 이광수 | Polyurethane foam deodorization apparatus |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4344113A1 (en) * | 1993-12-23 | 1995-06-29 | Metallgesellschaft Ag | Process for cleaning waste gas from incineration |
| KR100241771B1 (en) * | 1997-06-24 | 2000-02-01 | 강재원 | Method and apparatus for treating harmful gas and dioxins |
| JP3545266B2 (en) * | 1999-07-08 | 2004-07-21 | 川崎重工業株式会社 | Dry exhaust gas treatment method and apparatus |
| JP2001347131A (en) * | 2000-06-05 | 2001-12-18 | Babcock Hitachi Kk | Method and device for removing hazardous material in waste combustion gas |
| KR100384781B1 (en) * | 2000-12-29 | 2003-05-22 | 주식회사 하이닉스반도체 | Duty cycle correction circuit |
-
2002
- 2002-04-19 KR KR10-2002-0021529A patent/KR100505125B1/en active IP Right Grant
- 2002-06-18 CN CN02122899A patent/CN1451480A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101141134B1 (en) * | 2010-02-05 | 2012-05-02 | 한국지질자원연구원 | Method for Removing Chloride in Municipal Solid Waste Incineration Bottom Ash via Washing and Carbonation Process |
| KR20140126320A (en) * | 2012-03-29 | 2014-10-30 | 두산 렌트제스 게엠베하 | A flue gas purification device |
| KR101314466B1 (en) * | 2012-05-29 | 2013-10-07 | 센텍(주) | Reactor for contact gas and liquid |
| KR102008880B1 (en) * | 2018-03-28 | 2019-08-08 | (주)엔노피아 | Complex pollutant treatment device from tire manufacturing process |
| CN116422097A (en) * | 2023-03-28 | 2023-07-14 | 北京华兴碳环境科技有限公司 | Industrial waste gas desulfurization and denitrification device |
Also Published As
| Publication number | Publication date |
|---|---|
| KR100505125B1 (en) | 2005-07-29 |
| CN1451480A (en) | 2003-10-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR100505125B1 (en) | The de-sulfuration de-dioxins Equipment for Waste treatment system | |
| CN105716092B (en) | A kind of system processing method of oil field ground sludge | |
| KR100875519B1 (en) | A plant for reducing hazardous articles of exhaust gas in a incinerator using activated carbon | |
| US11156358B2 (en) | Furnace apparatus | |
| JP2003251146A (en) | Method for removing dioxins and dust by using high temperature plasma and device therefor | |
| KR20060080998A (en) | Apparatus for wet-type electrostatic precipitator of waste gas abatement equipment | |
| CN213983577U (en) | Waste incinerator with flue gas recovery mechanism | |
| JP2018509581A (en) | Furnace equipment | |
| JP2000229217A (en) | Method and device for removing harmful material in waste gas or the like from incineration furnace or the like | |
| JP4270528B2 (en) | Equipment for removing harmful substances from exhaust gas in combustion furnaces | |
| JPH11165025A (en) | Method of removing noxious matter such as waste gas in combustion furnace or the like and removing device therefor | |
| JP3049527U (en) | Equipment for removing harmful substances such as exhaust gas in combustion furnaces | |
| JPH07204604A (en) | Treating device for fly ash in incinerator | |
| KR20030022752A (en) | Air Pollution Removal Device | |
| JPH10109011A (en) | Purifying method of waste gas at incinerator and device therefor | |
| KR101392643B1 (en) | Exhaust gas induce device using multi centrifugal for semi dry reactor | |
| JP3664941B2 (en) | Exhaust gas treatment method and system for ash melting furnace | |
| JP2004024979A (en) | Method and apparatus for treating exhaust gas | |
| Adu et al. | Design and construction of a gas filter system for hospital incinerators | |
| JP2008068192A (en) | Asbestos waste treatment apparatus and method | |
| JP2001149750A (en) | Method and device for treating waste gas containing dioxins and fly ash | |
| Male | Small Scale Plasma Gasification of Municipal Solid Waste | |
| JP3059686U (en) | Equipment for removing harmful substances such as exhaust gas in combustion furnaces | |
| KR20110030241A (en) | Air pollution material elimination apparatus | |
| KR20010083018A (en) | Purification device for waste incineration |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A201 | Request for examination | ||
| E701 | Decision to grant or registration of patent right | ||
| GRNT | Written decision to grant | ||
| FPAY | Annual fee payment |
Payment date: 20120723 Year of fee payment: 8 |
|
| FPAY | Annual fee payment |
Payment date: 20130719 Year of fee payment: 9 |
|
| FPAY | Annual fee payment |
Payment date: 20150622 Year of fee payment: 11 |
|
| FPAY | Annual fee payment |
Payment date: 20160722 Year of fee payment: 12 |
|
| FPAY | Annual fee payment |
Payment date: 20170720 Year of fee payment: 13 |
|
| FPAY | Annual fee payment |
Payment date: 20180723 Year of fee payment: 14 |
|
| FPAY | Annual fee payment |
Payment date: 20190722 Year of fee payment: 15 |