KR20230163165A - Dust and gas hybrid collecting system of structure - Google Patents
Dust and gas hybrid collecting system of structure Download PDFInfo
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- KR20230163165A KR20230163165A KR1020220062920A KR20220062920A KR20230163165A KR 20230163165 A KR20230163165 A KR 20230163165A KR 1020220062920 A KR1020220062920 A KR 1020220062920A KR 20220062920 A KR20220062920 A KR 20220062920A KR 20230163165 A KR20230163165 A KR 20230163165A
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- 239000000428 dust Substances 0.000 title claims abstract description 52
- 239000003054 catalyst Substances 0.000 claims abstract description 96
- 239000000919 ceramic Substances 0.000 claims abstract description 62
- 239000007789 gas Substances 0.000 claims abstract description 34
- 239000002912 waste gas Substances 0.000 claims abstract description 34
- 238000004519 manufacturing process Methods 0.000 claims abstract description 20
- 230000003197 catalytic effect Effects 0.000 claims description 6
- 239000012855 volatile organic compound Substances 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims description 3
- 238000009833 condensation Methods 0.000 claims description 3
- 230000005494 condensation Effects 0.000 claims description 3
- 238000005516 engineering process Methods 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- 238000000746 purification Methods 0.000 claims 2
- 238000011001 backwashing Methods 0.000 claims 1
- 239000011261 inert gas Substances 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 238000005192 partition Methods 0.000 claims 1
- 238000009827 uniform distribution Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 16
- 238000012423 maintenance Methods 0.000 abstract description 9
- 239000000809 air pollutant Substances 0.000 abstract description 6
- 231100001243 air pollutant Toxicity 0.000 abstract description 6
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 238000011049 filling Methods 0.000 abstract description 5
- 238000001914 filtration Methods 0.000 abstract description 4
- 238000001816 cooling Methods 0.000 abstract description 3
- 238000001035 drying Methods 0.000 abstract description 3
- 238000009434 installation Methods 0.000 abstract description 3
- 238000010792 warming Methods 0.000 abstract description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 10
- 238000010586 diagram Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000004904 shortening Methods 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 229910052815 sulfur oxide Inorganic materials 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2068—Other inorganic materials, e.g. ceramics
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/4263—Means for active heating or cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/4272—Special valve constructions adapted to filters or filter elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/44—Auxiliary equipment or operation thereof controlling filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/48—Removing dust other than cleaning filters, e.g. by using collecting trays
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/71—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with pressurised gas, e.g. pulsed air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/72—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with backwash arms, shoes or nozzles
-
- 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
- B01D53/86—Catalytic processes
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Inorganic Chemistry (AREA)
- Ceramic Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
본 발명은 각 산업의 공정에서 대기 중으로 배출되는 분진과 폐가스를 동시저감하는 장치에 관한 것으로서 보다 상세하게는 세라믹필터에 선택 촉매를 담지하거나 폐가스와 반응하는 촉매를 선택해 충진 공간을 하나의 장치 내에 마련한 동시저감장치 시스템 구조에 관한 것이다.
각 산업 공정의 대기 오염 물질을 효과적으로 제거하기 위하여 오늘날 많은 대기 오염 물질 배출 시설물에서 고온 배기가스에 포함된 분진과 폐가스 처리의 필요가 증대되고 있다. 고온에서 사용이 가능한 세라믹필터를 이용한 고온 집진장치는 기존 여과 집진기에 비해 내열성이 우수하며 여과속도가 빠르고, 고온에서 촉매와 폐가스의 반응을 통해 분진과 함께 동시저감 함으로 별도의 냉각설비가 필요 없어, 제작비, 설치비, 유지보수 비용이 상대적으로 저렴한 장점이 있으며, 또한 고온의 청정가스를 건조, 보온 공정에 이용할 수 있는 장점이 있어서 전세계적으로 개발에 박차를 가하고 있다.
동시저감장치에 적용되는 세라믹필터 내지 세라믹촉매필터에 압축공기의 압력을 이용하여 필터 표면에 포집된 분진을 탈진절차를 반복 진행함에 따라 필터 차압을 유지하여 지속적인 운전이 가능하도록 펄스제트를 제공하고, 필터를 통과한 폐가스는 필터에 담지된 촉매와 반응을 통해 저감되거나 별도의 촉매 공간에서 저감되어 고온 공정에서 분진과 폐가스 동시저감장치 시스템에 관한 것이다.The present invention relates to a device that simultaneously reduces dust and waste gas discharged into the atmosphere in each industrial process. More specifically, it relates to a device that supports a selective catalyst in a ceramic filter or selects a catalyst that reacts with waste gas to provide a filling space in one device. It is about the structure of the simultaneous reduction device system.
In order to effectively remove air pollutants from each industrial process, the need to treat dust and waste gas contained in high-temperature exhaust gas is increasing in many air pollutant emission facilities today. A high-temperature dust collector using a ceramic filter that can be used at high temperatures has superior heat resistance and a fast filtration speed compared to existing filter dust collectors. It simultaneously reduces dust and dust through the reaction of catalyst and waste gas at high temperatures, eliminating the need for separate cooling facilities. It has the advantage of relatively low manufacturing, installation, and maintenance costs, and also has the advantage of being able to use high-temperature clean gas for drying and warming processes, so development is being accelerated around the world.
A pulse jet is provided to maintain the differential pressure of the filter to enable continuous operation by repeatedly dedusting the dust collected on the surface of the filter using the pressure of compressed air for the ceramic filter or ceramic catalyst filter applied to the simultaneous reduction device, The waste gas that has passed through the filter is reduced through reaction with the catalyst carried on the filter or reduced in a separate catalyst space, and relates to a simultaneous dust and waste gas reduction device system in a high temperature process.
Description
본 발명은 각 산업의 공정에서 대기 중으로 배출되는 분진과 폐가스를 동시저감하는 장치에 관한 것으로서 보다 상세하게는 세라믹필터에 선택 촉매를 담지하거나 폐가스와 반응하는 촉매를 선택해 충진 공간을 하나의 장치 내에 마련한 동시저감장치 시스템 구조에 관한 것이다.The present invention relates to a device that simultaneously reduces dust and waste gas discharged into the atmosphere in each industrial process. More specifically, it relates to a device that supports a selective catalyst in a ceramic filter or selects a catalyst that reacts with waste gas to provide a filling space in one device. It is about the structure of the simultaneous reduction device system.
각 산업 공정의 대기 오염 물질을 효과적으로 제거하기 위하여 오늘날 많은 대기 오염 물질 배출 시설물에서 고온 배기가스에 포함된 분진과 폐가스 처리의 필요가 증대되고 있다. 고온에서 사용이 가능한 세라믹필터를 이용한 고온 집진장치는 기존 여과 집진기에 비해 내열성이 우수하며 여과속도가 빠르고, 고온에서 촉매와 폐가스의 반응을 통해 분진과 함께 동시저감 함으로 별도의 냉각설비가 필요 없어, 제작비, 설치비, 유지보수 비용이 상대적으로 저렴한 장점이 있으며, 또한 고온의 청정가스를 건조, 보온 공정에 이용할 수 있는 장점이 있어서 전세계적으로 개발에 박차를 가하고 있다. In order to effectively remove air pollutants from each industrial process, the need to treat dust and waste gas contained in high-temperature exhaust gas is increasing in many air pollutant emission facilities today. A high-temperature dust collector using a ceramic filter that can be used at high temperatures has superior heat resistance and a fast filtration speed compared to existing filter dust collectors. It simultaneously reduces dust and dust through the reaction of catalyst and waste gas at high temperatures, eliminating the need for separate cooling facilities. It has the advantage of relatively low manufacturing, installation, and maintenance costs, and also has the advantage of being able to use high-temperature clean gas for drying and warming processes, so development is accelerating around the world.
동시저감장치에 적용되는 세라믹필터 내지 세라믹촉매필터에 압축공기의 압력을 이용하여 필터 표면에 포집된 분진을 탈진절차를 반복 진행함에 따라 필터 차압을 유지하여 지속적인 운전이 가능하도록 펄스제트를 제공하고, 필터를 통과한 폐가스는 필터에 담지된 촉매와 반응을 통해 저감되거나 별도의 촉매 공간에서 저감되어 고온 공정에서 분진과 폐가스 동시저감장치 시스템에 관한 것이다.A pulse jet is provided to maintain the differential pressure of the filter to enable continuous operation by repeatedly dedusting the dust collected on the surface of the filter using the pressure of compressed air for the ceramic filter or ceramic catalyst filter applied to the simultaneous reduction device, The waste gas that has passed through the filter is reduced through reaction with the catalyst carried on the filter or reduced in a separate catalyst space, and relates to a simultaneous dust and waste gas reduction device system in a high temperature process.
종래 기술에 따른 각 산업공정의 대기오염 방지시설의 배기가스 처리장치는 분진과 폐가스를 저감하는데 있어서 분진을 잡기위한 집진장치와 폐가스를 잡기위한 별도의 장치가 각각 있었다.In reducing dust and waste gas, the exhaust gas treatment device of air pollution prevention facilities for each industrial process according to the prior art had a dust collection device for catching dust and a separate device for catching waste gas.
종래 기술에 따른 집진장치는 분진 포집 내지 저감을 목적으로 하며, 섬유필터의 사용으로 운전온도가 낮고, 배기가스 중에 NOx 내지 VOCs와 같은 폐가스는 별도의 반응장치를 이용해 저감하였다. The dust collector according to the prior art aims to collect or reduce dust, has a low operating temperature by using a fiber filter, and waste gases such as NOx and VOCs in the exhaust gas are reduced by using a separate reaction device.
종래 기술에 따른 고온에서 분진 포집용으로 사용되는 세라믹필터의 경우 대부분 원형의 형상으로 고온 집진장치에서 분진포집용으로 사용되고 있으나 촉매를 담지한 경우 고가이며, 여과면적이 적어 각 산업공정에 적용하는데 어려움이 있었는데, 본 발명은 모듈화 세라믹필터를 1차 적으로 적층 장착하여 적정 여과면적을 확보하고, 촉매의 별도 공간을 확보해 하나의 장치로 만들어 분진과 폐가스를 동시에 저감하는 장치를 만들면 제작비용, 운전비용, 유지보수 비용 등의 절감 예상과 제한적인 공간에 설치할 수 있는 장점이 있다.In the case of ceramic filters used for dust collection at high temperatures according to the prior art, most of them have a circular shape and are used for dust collection in high-temperature dust collection devices. However, when carrying a catalyst, they are expensive and have a small filtration area, making it difficult to apply them to each industrial process. In the present invention, the modular ceramic filters are primarily stacked to secure an appropriate filtration area, and a separate space for the catalyst is secured to create a device that reduces dust and waste gas at the same time, thereby reducing production costs and operation. It has the advantage of expected savings in costs, maintenance costs, etc. and the ability to install in limited spaces.
이렇듯 각 산업공정의 대기 오염 물질을 효과적으로 제거하기 위하여 오늘날 많은 대기 오염 물질 배출 방지시설물에서 동시저감의 필요가 증대되고 있으며, 고온에서 사용이 가능한 세라믹필터 내지 세라믹촉매필터를 이용한 동시저감장치는 고온에서 분진과 폐가스를 동시 저감함으로 냉각설비가 별도로 필요 없어 공정을 단축할 수 있으며, 고온의 청정가스를 건조, 보온 공정에 이용할 수 있는 장점 또한 있어서 전세계적으로 개발에 박차를 가하고 있다,In order to effectively remove air pollutants from each industrial process, the need for simultaneous reduction is increasing in many air pollutant emission prevention facilities today, and simultaneous reduction devices using ceramic filters or ceramic catalyst filters that can be used at high temperatures are being used at high temperatures. By simultaneously reducing dust and waste gas, the process can be shortened by eliminating the need for separate cooling facilities. It also has the advantage of being able to use high-temperature clean gas for drying and warming processes, spurring development around the world.
또한, 이를 응용한 복합발전시설인 석탄가스화복합발전장치 (IGCC : Integrated Gasification Combined Cycle)나 가압유동층연소장치 (PFBC : Pressurized Fluidized Bed Combustion)와 각 산업 보일러 같은 공정에서 많은 개발이 이루어지고 있는 실정이다.In addition, much development is being carried out in processes such as integrated gasification combined cycle (IGCC), pressurized fluidized bed combustion (PFBC), and industrial boilers, which are combined cycle power plants that apply this. .
상기와 같은 종래기술의 문제점을 해결하고자, 본 발명은 세라믹필터 내지 세라믹촉매필터를 적층하여 장착하고 별도의 촉매 층이 있는 공간을 하나의 장치로 만들어 분진과 폐가스를 세라믹촉매필터와 촉매 층을 순차적으로 통과한 배기가스를 제거 내지 저감하는데 단순화한 동시저감장치를 제공하는 것을 목적으로 한다.In order to solve the problems of the prior art as described above, the present invention stacks and installs ceramic filters or ceramic catalyst filters, creates a space with a separate catalyst layer as one device, and removes dust and waste gas by sequentially using the ceramic catalyst filter and the catalyst layer. The purpose is to provide a simplified simultaneous reduction device for removing or reducing exhaust gas that has passed through.
또한 본 발명은 단순한 동시저감장치 시스템 구성을 통해 상대적으로 낮은 제조단가와 유지관리가 용이하여 유지비용을 최소화할 수 있으며, 공정을 단축하여 제한적인 공간에 설치 가능한 동시저감장치를 제공하는 것을 목적으로 한다.In addition, the present invention aims to provide a simultaneous reduction device that can be installed in a limited space by shortening the process and can minimize maintenance costs through relatively low manufacturing costs and easy maintenance through a simple simultaneous reduction device system configuration. do.
이외에 본 발명은 동시저감장치 시스템 관리나 정기점검 등의 미비로 취성에 약한 세라믹필터 내지 세라믹촉매필터의 파손과 촉매 기능저하가 올 경우를 최소화하는 동시저감장치를 제공하는 것을 목적으로 한다.In addition, the purpose of the present invention is to provide a simultaneous reduction device that minimizes the cases of damage to ceramic filters or ceramic catalyst filters that are vulnerable to brittleness and deterioration of catalyst function due to lack of simultaneous reduction device system management or regular inspection.
상기와 같은 종래기술의 문제점을 해결하고자, 본 발명은 세라믹필터 내지 세라믹촉매필터를 적층하여 장착하는데, 타공판과 필터 사이에 가스켓을 넣어 볼트와 너트로 고정하고 별도의 촉매 층이 있는 공간에 금속 재질의 박스를 만들어 폐가스 종류와 선택 반응한 팰렛 형태의 촉매를 채워 하나의 장치로 만들어 분진과 폐가스를 세라믹필터와 촉매 박스 층을 순차적으로 통과함으로 각 사업 공정의 배기가스를 제거 내지 저감하는데 단순화한 동시저감장치를 제공하는 것을 목적으로 한다.In order to solve the problems of the prior art as described above, the present invention stacks and mounts ceramic filters or ceramic catalyst filters. A gasket is placed between the perforated plate and the filter, fixed with bolts and nuts, and a metal material is placed in the space where the separate catalyst layer is located. By making a box and filling it with a pellet-shaped catalyst that selectively reacts with the type of waste gas, it is made into a single device, and dust and waste gas pass through the ceramic filter and catalyst box layers sequentially, simplifying the removal or reduction of exhaust gases in each business process. The purpose is to provide a reduction device.
또한 본 발명은 단순한 동시저감장치 시스템 구성을 통해 상대적으로 낮은 제조단가와 유지관리가 용이하여 유지비용을 최소화할 수 있으며, 공정을 단축하여 제한적인 공간에 설치 가능한 동시저감장치를 제공하는 것을 목적으로 한다.In addition, the present invention aims to provide a simultaneous reduction device that can be installed in a limited space by shortening the process and can minimize maintenance costs through relatively low manufacturing costs and easy maintenance through a simple simultaneous reduction device system configuration. do.
이외에 본 발명은 동시저감장치 시스템 관리나 정기점검 등의 미비로 취성이 높은 세라믹필터 내지 세라믹촉매필터의 파손과 촉매 기능저하가 올 경우를 최소화하는 동시저감장치를 제공하는 것을 목적으로 한다.In addition, the purpose of the present invention is to provide a simultaneous reduction device that minimizes the cases of damage to highly brittle ceramic filters or ceramic catalyst filters and deterioration of catalyst function due to lack of simultaneous reduction device system management or regular inspection.
본 발명은 세라믹필터 내지 세라믹촉매필터를 적층하여 장착하는데, 타공판과 필터 사이에 가스켓을 넣어 볼트와 너트로 고정하고 별도의 촉매 층이 있는 공간에 금속 재질의 박스를 만들어 폐가스 종류와 선택 반응한 팰렛 형태의 촉매를 채워 하나의 장치로 만들어 분진은 세라믹필터 표면에서 포집되고, 폐가스는 촉매 박스 층을 통과할 때 반응을 통해 깨끗한 공기로 바뀌어 각 사업 공정의 배기가스를 제거 내지 저감하는데 단순화한 동시저감장치를 제공하는 것을 목적으로 한다.In the present invention, ceramic filters or ceramic catalyst filters are stacked and mounted. A gasket is placed between the perforated plate and the filter, fixed with bolts and nuts, and a metal box is made in the space with a separate catalyst layer to create a pallet that selectively reacts with the type of waste gas. By filling it with a catalyst in the form of a single device, dust is collected on the surface of the ceramic filter, and when the waste gas passes through the catalyst box layer, it is converted into clean air through a reaction, simplifying the simultaneous reduction of exhaust gas from each business process. The purpose is to provide a device.
또한 본 발명은 단순한 동시저감장치 시스템 구성을 통해 상대적으로 낮은 제조단가와 유지관리가 용이하여 유지비용을 최소화할 수 있으며, 공정을 단축하여 제한적인 공간에 설치 가능한 동시저감장치를 제공하는 것을 목적으로 한다.In addition, the present invention aims to provide a simultaneous reduction device that can be installed in a limited space by shortening the process and can minimize maintenance costs through relatively low manufacturing costs and easy maintenance through a simple simultaneous reduction device system configuration. do.
이상에서 설명한 본 발명은 전술한 상세한 설명, 동작 예 및 도면에 의하여 한정되는 것은 아니고, 하기의 특허청구범위에 기재된 본 발명의 사상 및 영역으로부터 벗어나지 않는 범위 내에서 해당 기술분야의 당업자가 다양하게 수정 및 변경시킨 것 또한 본 발명의 범위 내에 포함됨은 물론이다.The present invention described above is not limited to the detailed description, operation examples, and drawings, and may be modified in various ways by those skilled in the art without departing from the spirit and scope of the present invention as set forth in the claims below. And changes thereof are also included within the scope of the present invention.
도 1은 본 발명의 동시저감장치의 실시 예에 대한 시스템 정면 구조의 개략도이다.
도 2는 본 발명의 동시저감장치의 실시 예에 대한 시스템 측면 구조의 개략도이다.
도 3은 본 발명의 동시저감장치의 실시 예에 대한 시스템 윗면 구조의 개략도이다.
도 4은 본 발명의 동시저감장치의 상부에 위치한 촉매 박스 지지틀과 촉매 박스를 실시 예로 나타낸 사시도이다.
도 5은 본 발명의 동시저감장치에 사용되는 촉매 박스를 실시 예로 나타낸 사시도이다.
도 6은 본 발명의 동시저감장치에 적용되는 세라믹필터 및 세라믹촉매필터의 실시 예를 나타낸 사시도이다.
도 7은 본 발명의 동시저감장치에 사용되는 촉매 박스 내에 충진되는 팰렛 형태의 질소산화물 저감촉매를 실시 예로 나타낸 사진이다.1 is a schematic diagram of the front structure of the system for an embodiment of the simultaneous reduction device of the present invention.
Figure 2 is a schematic diagram of the system side structure of an embodiment of the simultaneous reduction device of the present invention.
Figure 3 is a schematic diagram of the top structure of the system for an embodiment of the simultaneous reduction device of the present invention.
Figure 4 is a perspective view showing the catalyst box support frame and catalyst box located on the upper part of the simultaneous reduction device of the present invention as an example.
Figure 5 is a perspective view showing an example of a catalyst box used in the simultaneous reduction device of the present invention.
Figure 6 is a perspective view showing an example of a ceramic filter and a ceramic catalyst filter applied to the simultaneous reduction device of the present invention.
Figure 7 is a photograph showing an example of a nitrogen oxide reduction catalyst in the form of a pellet filled in a catalyst box used in the simultaneous reduction device of the present invention.
아래에서는 첨부한 도면을 참고로 하여 본 발명의 실시 예에 대하여 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자가 용이하게 실시할 수 있도록 상세히 설명한다. 그러나 본 발명은 여러 가지 상이한 형태로 구현 될 수 있으며, 여기에서 설명하는 실시 예에 한정되지 않는다. Below, with reference to the attached drawings, embodiments of the present invention will be described in detail so that those skilled in the art can easily implement the present invention. However, the present invention may be implemented in many different forms and is not limited to the embodiments described herein.
그리고 도면에서 본 발명을 명확하게 설명하기 위해서 설명과 관계없는 부분은 생략하였으며, 명세서 전체를 통하여 유사한 부분에 대해서는 유사한 도면 부호를 붙였다.In order to clearly explain the present invention in the drawings, parts that are not related to the description are omitted, and similar parts are given similar reference numerals throughout the specification.
명세서 전체에서, 어떤 부분이 어떤 구성요소를 "포함"한다고 할 때, 이는 특별히 반대되는 기재가 없는 한 다른 구성요소를 제외하는 것이 아니라 다른 구성요소를 더 포함할 수 있는 것을 의미한다.Throughout the specification, when a part is said to “include” a certain element, this means that it may further include other elements rather than excluding other elements, unless specifically stated to the contrary.
상기 목적을 달성하기 위하여 본 발명은 동시저감장치 본체에 있어서, 다수개의 모듈화 세라믹필터 내지 세라믹촉매필터의 적층 내지 배열과 촉매 박스에 다양한 형상의 촉매를 채워 넣은 구조물을 하나의 장치로 만들어 제작할 수 있다.In order to achieve the above object, the present invention is a simultaneous reduction device main body, and a structure in which a plurality of modular ceramic filters or ceramic catalyst filters are stacked or arranged and a catalyst box is filled with catalysts of various shapes can be manufactured as a single device. .
모듈화 세라믹필터(400) 내지 세라믹촉매필터(400)는 고온 약 500℃까지 별다른 문제없이 도 6의 도면과 같이 사용할 수 있는 구조로 제작되었으며, 필터의 기공조절과 표면의 코팅을 통해 분진 특성에 맞게 제작하여 효율을 높일 수 있으며, 세라믹촉매필터의 경우 발생하는 폐가스에 따라 촉매를 선택하여 담지함으로 공정 중에 발생하는 분진과 폐가스를 동시에 저감할 수 있도록 동시저감장치(100)의 기능을 제공한다.The modular ceramic filter 400 or ceramic catalyst filter 400 is manufactured in a structure that can be used as shown in the drawing in FIG. 6 without any problems up to a high temperature of about 500°C, and can be adjusted to suit the dust characteristics by adjusting the pores of the filter and coating the surface. Efficiency can be increased by manufacturing, and in the case of a ceramic catalyst filter, it provides the function of a simultaneous reduction device (100) to simultaneously reduce dust and waste gas generated during the process by selecting and supporting a catalyst according to the waste gas generated.
촉매 박스(330)와 촉매(300)는 별도의 촉매 층이 있는 공간에 금속 재질의 박스를 만들어 촉매 박스 지지틀(310)에 넣어 폐가스 종류와 선택 반응한 팰렛 형태의 도 7의 사진 형태의 촉매(300)를 채워 배기가스가 촉매 박스에 담긴 촉매 층을 250 ~ 350℃ 사이 통과할 때 촉매와 반응을 통해 깨끗한 공기(530)로 바뀌어 환경기준을 만족하고 각 산업 공정의 배기가스를 제거 내지 저감하는데 최적의 효율을 높이고 단순화한 동시저감장치(100)를 제공한다.The catalyst box 330 and the catalyst 300 are made of a metal box in a space with a separate catalyst layer, placed in the catalyst box support frame 310, and selectively reacted with the type of waste gas. The catalyst is in the form of a pellet in the photo of FIG. 7. When exhaust gas fills (300) and passes through the catalyst layer contained in the catalyst box between 250 and 350°C, it reacts with the catalyst and changes into clean air (530), satisfying environmental standards and eliminating or reducing exhaust gas from each industrial process. Provides a simultaneous reduction device (100) that increases optimal efficiency and simplifies the process.
도 1은 본 발명의 실시 예로 동시저감장치(100)의 정면 구조이며, 도 2는 측면 구조이고, 도 3은 위에서 바라본 구조의 구성 요소를 중심으로 설명한다.Figure 1 is the front structure of the simultaneous reduction device 100 as an embodiment of the present invention, Figure 2 is the side structure, and Figure 3 explains the components of the structure as seen from above.
본 발명의 실시 예에 따른 동시저감장치(100)는 각 산업 연소공정에서 발생하는 배기가스에 포함되어 있는 분진과 폐가스가 입구(510)로 들어오면 입구 호퍼(200)를 거쳐 세라믹필터(400)가 적층되어 있는 공간에 가이드 밴(115)에 의해 배기가스(520)가 일정한 분포로 확산되며, 세라믹필터(400)를 통과 하면서 분진은 필터 표면에 포집되고, 필터의 분진 포집으로 압력손실이 증가하면 컨트롤 판넬(210)에서 솔레노이드 밸브(150)를 작동하면 에어 탱크(140)에 압출되어 있던 공기가 솔레노이드 밸브(150)에서 제트 펄스로 압축 공기를 펄스 튜브(130)를 통해 세라믹필터에 역세정 분사하여 필터표면에 붙어 있는 분진을 털어 냄으로 일정한 차압을 유지해 지속적인 사용이 가능하도록 하는데, 같은 위치에 세라믹촉매필터(400)가 장착되었을 경우 선택 담지된 촉매에 의해 폐가스가 반응하면서 배기가스(525)로 정화되고, 좀 더 높은 폐가스의 저감효율이 요구될 때 촉매 박스(330)를 통과하면 정화된 배기가스(530)가 출구(540)로 나가 지속적인 분진 및 폐가스 동시저감으로 깨끗한 대기환경 유지하는 기술을 제공한다. In the simultaneous reduction device 100 according to an embodiment of the present invention, when dust and waste gas contained in exhaust gas generated from each industrial combustion process enters the inlet 510, it passes through the inlet hopper 200 and is filtered through the ceramic filter 400. The exhaust gas 520 is spread in a certain distribution by the guide van 115 in the space where the exhaust gas 520 is stacked, and as it passes through the ceramic filter 400, the dust is collected on the filter surface, and the pressure loss increases due to the dust collection of the filter. When the solenoid valve 150 is operated on the control panel 210, the air extruded from the air tank 140 is backwashed into the ceramic filter through the pulse tube 130 by using a jet pulse of compressed air from the solenoid valve 150. By spraying and shaking off the dust attached to the filter surface, a constant differential pressure is maintained to enable continuous use. When the ceramic catalytic filter (400) is installed in the same location, the waste gas reacts with the selected catalyst to produce exhaust gas (525). ), and when higher waste gas reduction efficiency is required, when it passes through the catalyst box (330), the purified exhaust gas (530) goes out to the outlet (540) to maintain a clean atmospheric environment by continuously reducing dust and waste gas simultaneously. Provides technology.
도 4는 본 발명의 실시 예로 동시저감장치(100)의 구조의 구성 요소에서 세라믹필터(400)를 통과 하면서 1차적으로 정화된 배기가스를 좀 더 높은 효율을 얻기 위해 촉매 박스(330)를 통과하게 하는데, 촉매 박스를 지지하는 틀(310)에 일정 간격으로 선택 촉매(300)을 촉매 박스(330)에 가득 넣어 고정하여 폐가스 저감효율을 증대시킬 수 있디.Figure 4 shows an embodiment of the present invention in which the exhaust gas that is primarily purified while passing through the ceramic filter 400 in a structural component of the simultaneous reduction device 100 passes through the catalyst box 330 to obtain higher efficiency. In this way, the waste gas reduction efficiency can be increased by filling the catalyst box 330 with the selected catalyst 300 and fixing it at regular intervals on the frame 310 supporting the catalyst box.
도 5는 본 발명의 실시 예로 동시저감장치(100)의 구조의 촉매 박스를 지지하는 틀(310)에 일정간격으로 선택 촉매(300)를 촉매 박스(330)에 가득 넣는데 있어, 촉매 박스(330)는 촉매 박스 후레임(340)을 ㄷ자로 절곡한 금속재질의 판재를 ㅁ자로 조립 성형하고, 양쪽 면에 매쉬 망(350)을 장착하여 용접함으로 공기의 흐름은 있으나 촉매의 크기보다 작아 통과 할 수 없는 매쉬 크기를 선정하여 압력손실을 최소화 하고 촉매의 손실 없이 유지할 수 있는 촉매 박스를 제공한다.Figure 5 is an embodiment of the present invention in which the catalyst box 330 is filled with the selective catalyst 300 at regular intervals in the frame 310 supporting the catalyst box of the simultaneous reduction device 100. ) is a catalyst box frame (340) formed by assembling and forming a metal plate bent into a U-shape, and attaching a mesh net (350) to both sides and welding it, so there is air flow, but it is smaller than the size of the catalyst, so it cannot pass through. We provide a catalyst box that minimizes pressure loss and maintains catalyst without loss by selecting a mesh size.
촉매 박스 지지틀(310)에 있어서, 동시저감장치(100)의 세로 구조뿐 아니가 가로 구조로 일정간격으로 촉매 박스(330)를 배열할 수 있으며, 공정 조건에 따라 위치 및 형태 또한 변경을 통해 최적의 효율을 얻을 수 있도록 하다.In the catalyst box support frame 310, the catalyst boxes 330 can be arranged at regular intervals not only in the vertical structure of the simultaneous reduction device 100 but also in the horizontal structure, and the position and shape can also be changed according to process conditions. To achieve optimal efficiency.
도 6는 본 발명의 실시 예로 동시저감장치(100)의 구조에 사용되는 세라믹필터 내지 세라믹촉매필터의 구조 내지 구성 요소로 상부캡과 하부캡 사이에 세라믹필터 내지 세라믹촉매필터를 두고 연결체를 이용해 조립하는데 있어, 사용 중에 열팽창과 수축에 의한 변화를 스프링으로 조립구조를 유지하도록 제공한다. Figure 6 shows the structure and components of a ceramic filter or a ceramic catalyst filter used in the structure of the simultaneous reduction device 100 as an embodiment of the present invention. A ceramic filter or a ceramic catalyst filter is placed between the upper cap and the lower cap using a connector. When assembling, springs are provided to maintain the assembled structure to prevent changes due to thermal expansion and contraction during use.
도 7는 본 발명의 실시 예로 동시저감장치(100)의 구조의 촉매 박스(330)에 촉매(300)가득 넣는데 있어, 촉매(300)의 형상은 구, 반구, 튜브, 로드 형상과 불규칙한 형상, 다 각형 등을 포함하며, 촉매(100)의 재질은 각 산업공정에서 발생하는 배기가스 중에 질소산화물(NOx), 휘발성유기화합물(VOCs), 황산화물(SOx), 기타 배가스 등을 포함해 저감을 목적으로 사용하는 상용촉매의 재료를 포함하며, 특히 이산화티타늄, 오산화바나듐, 알루미나, 소석회, 제올라이트, 규조토 등과 기타 촉매의 기능가진 무기재료 및 텅스텐, 구리, 망간과 기타 촉매의 기능가진 귀금속재료를 포함한다.Figure 7 shows an embodiment of the present invention, in which the catalyst box 330 of the simultaneous reduction device 100 is filled with catalyst 300, the shape of the catalyst 300 is sphere, hemisphere, tube, rod and irregular shape, It includes polygons, etc., and the material of the catalyst 100 reduces nitrogen oxides (NOx), volatile organic compounds (VOCs), sulfur oxides (SOx), and other exhaust gases from exhaust gases generated in each industrial process. It includes commercial catalyst materials used for this purpose, especially titanium dioxide, vanadium pentoxide, alumina, slaked lime, zeolite, diatomaceous earth, and other inorganic materials with catalytic functions, as well as tungsten, copper, manganese, and other precious metal materials with catalytic functions. do.
상기 본 발명의 동시저감장치(100)의 또 다른 실시 예로 구조의 구성 요소에서 각 사업공정의 적용하는 용량과 조건에 따라 세라믹필터 및 세라믹촉매필터(400)를 적용하는 수가 달라지며, 장착하는 구조에 있어서 가로 구조로 장착될 뿐만 아니라 세로 구조로 장착될 수 있으며, 세로로 장착될 경우 문(160), 에어탱크(140), 솔레노이드 밸브(150), 펄스튜브(130), 타공판(110), 촉매 박스 지지틀(310), 촉매 박스(310), 컨트롤 파넬(210), 분진호퍼(220), 분진 박스(240), 입구(510), 출구(540) 등을 포함하는 구조 및 구성이 각 산업공정의 현장 조건에 따라 적정 위치로 변경되어 설계되고 제작되는 것과 제작한 동시저감장치(100)를 보온(155)을 하는 것으로 결로현상을 방지하는 것을 포함한다.In another embodiment of the simultaneous reduction device 100 of the present invention, the number of ceramic filters and ceramic catalytic filters 400 applied varies depending on the applied capacity and conditions of each business process in the structural components, and the installation structure In addition to being mounted in a horizontal structure, it can be mounted in a vertical structure. When mounted vertically, the door 160, air tank 140, solenoid valve 150, pulse tube 130, perforated plate 110, Each structure and configuration includes the catalyst box support frame 310, catalyst box 310, control panel 210, dust hopper 220, dust box 240, inlet 510, outlet 540, etc. This includes preventing condensation by changing the design and manufacturing to an appropriate location according to the field conditions of the industrial process and keeping the manufactured simultaneous reduction device (100) warm (155).
이상에서 설명한 본 발명은 전술한 실시 예 및 첨부된 도면에 의하여 한정되는 것은 아니고, 하기의 특허청구범위에 기재된 본 발명의 사상 및 영역으로부터 벗어나지 않는 범위 내에서 해당 기술분야의 당업자가 다양하게 수정 및 변경시킨 것 또한 본 발명의 범위 내에 포함됨은 물론이다.The present invention described above is not limited to the above-described embodiments and the accompanying drawings, and may be modified and modified in various ways by those skilled in the art without departing from the spirit and scope of the present invention as set forth in the claims below. Of course, changes are also included within the scope of the present invention.
100 : 동시저감장치 본체
110 : 타공판
115 : 가이드 밴
120 : 필터 고정 볼트_너트
130 : 펄스튜브
140 : 에어 탱크
145 : 에어 탱크 고정대
150 : 솔레노이드 밸브
155 : 보온
160 : 문
165 : 위 문 잠금 고리
170 : 문 잠금 바
175 : 아래 문 잠금 고리
180 : 무 잠금 핸들
185 : 경첩
200 : 입구 호퍼
210 : 컨트롤 판넬
220 : 분진 호퍼
230 : 밸브
240 : 분진 박스
250 : 본체 지지대
300 : 촉매
310 : 촉매 박스 지지틀
330 : 촉매 박스
340 : 촉매 박스 후레임
350 : 매취 망
355 : 윗면 트임
360 : 측면 막힘
400 : 세라믹필터 내지 세라믹 촉매 필터
410 : 필터 지지대
510 : 고온 배기가스 입구
520 : 배가스 흐름 1
525 : 배가스 흐름 2
530 : 배가스 흐름 3
540 : 고온 배기가스 출구
100: Simultaneous reduction device main body 110: Perforated plate
115: Guide van 120: Filter fixing bolt_nut
130: pulse tube 140: air tank
145: Air tank fixture 150: Solenoid valve
155: Insulation 160: Door
165: upper door lock ring 170: door lock bar
175: Lower door lock ring 180: Lockless handle
185: hinge
200: Entrance hopper 210: Control panel
220: dust hopper 230: valve
240: Dust box 250: Body support
300: Catalyst 310: Catalyst box support frame
330: Catalyst box 340: Catalyst box frame
350: Matching net 355: Top opening
360: side blocking
400: Ceramic filter or ceramic catalyst filter
410: Filter support
510: High temperature exhaust gas inlet 520: Exhaust gas flow 1
525: exhaust gas flow 2 530: exhaust gas flow 3
540: High temperature exhaust gas outlet
Claims (7)
또 다른 실시 예로 동시저감장치(100)의 구조의 구성 요소에서 각 산업공정의 적용하는 용량과 조건에 따라 세라믹필터 및 세라믹촉매필터(400)를 적용하는 수가 달라지며, 장착하는 구조에 있어서 가로 구조로 장착될 뿐만 아니라 세로 구조로 장착될 수 있으며, 세로 구조로 장착될 경우 문(160), 에어탱크(140), 솔레노이드 밸브(150), 펄스튜브(130), 타공판(110), 촉매 박스 지지틀(310), 촉매 박스(310), 컨트롤 파넬(210), 분진호퍼(220), 분진 박스(240), 입구(510), 출구(540) 등을 포함하는 구조 및 구성이 현장 조건에 따라 적정 위치로 변경되어 설계되고 제작되는 것과 제작한 동시저감장치(100)를 보온(155)을 하는 것으로 결로현상을 방지하는 것을 특징으로 하는 동시저감장치.
In treating dust and waste gases (NOx, VOCs, HCl, SOx, etc.) contained in exhaust gas generated from each industrial combustion process with the simultaneous reduction device 100; When entering the inlet 510, the exhaust gas 520 is spread in a uniform distribution by the guide van 115 through the inlet hopper 200 and into the space where the ceramic filter 400 is stacked, and the ceramic filter 400 is As it passes, the dust is collected on the surface of the filter, and when the pressure loss increases due to the dust collection of the filter, the solenoid valve 150 is operated on the control panel 210, and the air extruded into the air tank 140 is released into the solenoid valve 150. By backwashing and spraying compressed air with a jet pulse onto the ceramic filter through the pulse tube (130) to shake off dust attached to the filter surface, a constant differential pressure is maintained to enable continuous use. A ceramic catalyst filter (400) is installed at the same location. ) is installed, the waste gas reacts with the selectively supported catalyst and is purified into exhaust gas 525, and when a higher waste gas reduction efficiency is required, when it passes through the catalyst box 330, the purified exhaust gas 530 It provides technology to maintain a clean air environment by continuously reducing dust and waste gases through exit 540.
In another embodiment, in the structural components of the simultaneous reduction device 100, the number of ceramic filters and ceramic catalyst filters 400 to be applied varies depending on the applied capacity and conditions of each industrial process, and the horizontal structure in the mounting structure It can be installed not only vertically, but also vertically. When mounted vertically, it supports the door 160, air tank 140, solenoid valve 150, pulse tube 130, perforated plate 110, and catalyst box. The structure and composition including the frame 310, catalyst box 310, control panel 210, dust hopper 220, dust box 240, inlet 510, outlet 540, etc. are determined according to site conditions. A simultaneous reduction device that is designed and manufactured by changing to an appropriate position and that prevents condensation by keeping the manufactured simultaneous reduction device (100) warm (155).
상기 동시저감장치는 세라믹필터(400)로 1차 분진을 필터표면에서 제거하고, 촉매 박스에서 2차로 발생 가스와 반응하는 촉매를 선택하여 다양한 형상과 크기로 만들어 넣어 정화하는 것을 특징으로 하는 동시저감장치.
According to paragraph 1,
The simultaneous reduction device is characterized in that it removes primary dust from the filter surface with a ceramic filter (400), selects a catalyst that reacts with the secondary gas generated in the catalyst box, and purifies it by making it in various shapes and sizes. Device.
상기 동시저감장치는 세라믹촉매필터(400)로 1차 분진을 필터표면에서 제거하고, 가스와 반응하는 촉매를 선택하여 세라믹필터에 담지하여 장착된 세라믹촉매필터(400)를 배기가스가 통과하면서 2차 정화하고, 촉매 박스(330)에는 발생 가스와 반응하는 촉매(300)를 선택하여 다양한 형상과 크기로 만들어 넣어 3차 정화로 효율을 높이는 것을 특징으로 하는 동시저감장치.
According to paragraph 1,
The simultaneous reduction device removes primary dust from the filter surface with a ceramic catalytic filter (400), selects a catalyst that reacts with gas, and supports it on the ceramic filter. As the exhaust gas passes through the installed ceramic catalytic filter (400), 2 A simultaneous reduction device that performs primary purification and increases efficiency through tertiary purification by selecting a catalyst (300) that reacts with the generated gas and putting it in various shapes and sizes in the catalyst box (330).
상기 동시저감장치(100)의 구조의 구성 요소에서 각 산업공정의 적용하는 용량과 조건에 따라 세라믹필터 및 세라믹촉매필터(400)를 적용하는 수가 달라지며, 장착하는 구조에 있어서 가로 구조로 장착될 뿐만 아니라 세로 구조로 장착될 수 있으며, 세로 구조로 장착될 경우 문(160), 에어탱크(140), 솔레노이드 밸브(150), 펄스튜브(130), 타공판(110), 촉매 박스 지지틀(310), 촉매 박스(310), 컨트롤 파넬(210), 분진호퍼(220), 분진 박스(240), 입구(510), 출구(540) 등을 포함하는 구조 및 구성이 현장 조건에 따라 적정 위치로 변경되어 설계되고 제작되는 것과 제작한 동시저감장치(100)를 보온(155)을 하는 것으로 결로현상을 방지하는 것을 특징으로 하는 동시저감장치.
According to paragraph 1,
In the structural components of the simultaneous reduction device 100, the number of ceramic filters and ceramic catalyst filters 400 to be applied varies depending on the applied capacity and conditions of each industrial process, and may be mounted horizontally in the mounting structure. In addition, it can be installed in a vertical structure, and when mounted in a vertical structure, the door (160), air tank (140), solenoid valve (150), pulse tube (130), perforated plate (110), catalyst box support frame (310) ), catalyst box (310), control panel (210), dust hopper (220), dust box (240), inlet (510), outlet (540), etc. are located at an appropriate location according to field conditions. A simultaneous reduction device that is designed and manufactured in a modified manner and is characterized in that it prevents condensation by keeping the manufactured simultaneous reduction device (100) warm (155).
상기 동시저감장치(100)에서 에어 탱크(140)에 압축 저장되어 솔레노이드 밸브(15), 펄스튜브(130)를 통해 세라믹필터에 역세정하는 압축가스는 공기, 질소 또는 불활성 가스인 것을 특징으로 하는 동시저감장치.
According to paragraph 1,
In the simultaneous reduction device 100, the compressed gas that is compressed and stored in the air tank 140 and backwashed in the ceramic filter through the solenoid valve 15 and pulse tube 130 is air, nitrogen, or an inert gas. Reduction device.
상기 동시저감장치(100)에서 세라믹필터 내지 세라믹촉매필터(400) 가 장착되는 타공판(110)의 뒤 부분의 1개 이상의 세라믹필터 내지 세라믹촉매필터(400)를 각각 격리하는 칸막이로 막는 것을 포함하는 것을 특징으로 하는 동시저감장치.
According to paragraph 1,
In the simultaneous reduction device 100, one or more ceramic filters or ceramic catalyst filters 400 at the rear of the perforated plate 110 on which the ceramic filters or ceramic catalyst filters 400 are mounted are blocked with a partition to isolate each. A simultaneous reduction device characterized by:
A simultaneous reduction device comprising the simultaneous reduction device according to any one of claims 1 to 6 and structural details for carrying out the invention, and each embodiment being designed and manufactured to suit field conditions.
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KR1020220062920A KR20230163165A (en) | 2022-05-23 | 2022-05-23 | Dust and gas hybrid collecting system of structure |
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