Abstract:
본 발명은 산성가스, 중금속물질, 다이옥신, 먼지 동시제거용 복합기능여과시스템에 관한것으로, 그 목적은 연소배가스는 장치의 상부를 통해 선회류 형태로 유입되며, 산성가스는 장치의 상부에서 분사되는 흡수제와 반응하여 제거되고, 중금속물질 및 다이옥신류는 장치의 전단에서 분사되는 활성탄에 의해 흡착되어 제거되며, 일부 흡수제 및 활성탄은 배가스에 포함된 먼지와 함께 여과포에 부착되어 제거되며, 또한 미반응 산성가스 및 중금속물질 및 다이옥신류가 여과포에 부착된 흡수제 및 활성탄에 의해 제거될 수 있는 산성가스, 중금속물질, 다이옥신류 및 먼지 동시제거용 복합기능여과시스템을 제공하는데 있다. 본 발명의 구성은 연소배가스 유입관, 장치본체부, 흡수제분사노즐, 활성탄분사부, 청정배가스 배출부로 구성되고, 장치본체부는 배가스가 유입되어 흡수제와 반응하는 내통부와 여과집진이 이루어지는 외통부로 이루어진 것을 특징으로 한다.
Abstract:
PURPOSE: A combination type dust collecting apparatus is provided which maintains high dust collecting performance of the dust collecting apparatus and substantially extends performance and life time of dust collecting filter at the same time. CONSTITUTION: In a combination type dust collecting apparatus in which discharge electrodes(20), collecting electrodes(30) and dust collecting filters(40) are installed inside a main body(10) having inlet(11) and outlet(12), the combination type dust collecting apparatus comprises a splitting plate(50) installed inside the main body between the inlet and outlet; a plurality of mounting holes(51) formed on the splitting plate with being spaced apart from each other in a certain distance; cylindrical dust collecting filters one end of which is insertingly adhered to the mounting holes in a lower part of the splitting plate, and which are horizontally installed in a plurality of rows; a plurality of collecting electrodes which are adhered to the lower surface of the splitting plate at both sides of the dust collecting filters with being spaced apart from each other, and which are arranged slantly and horizontally in a row; a plurality of discharge electrodes which are spaced apart from each other at an outer side of the collecting electrodes and adhered to a mounting ring(60) vertically installed inside the main body in a plurality of rows; guiding portions(70) installed at the lower surface of the splitting plate in front of the collecting electrodes and dust collecting filters corresponding to the inlet; and an outlet installed at one side of the main body in an upper part of the splitting plate.
Abstract:
PURPOSE: A fabrication method of silicon carbide ceramics filters on the outer surface of which a coating layer is formed is provided to improve dust collection efficiency. CONSTITUTION: The fabrication method of silicon carbide ceramics filter includes the steps of mixing silicon carbide ceramics powder 100 vol.%, 0.1 to 30.0 vol.% of carbon powder (based on the 100 volume percent of silicon carbide ceramics powder), 1.0 to 15.0 wt.% of inorganic binder (based on the 100 weight percent of silicon carbide ceramics powder), 3.0 to 20.0 wt.% of organic binder, 0.1 to 5.0 wt.% of calcium carbonate, 0.1 to 15.0 wt.% of dispersant, 0.1 to 3.0 wt.% of releasing agent and 10.0 to 35.0 wt.% of water; aging the mixture; pressure extruding the mixture in the form of filter; coating the surface of the filter by spray coating a coating solution; and sintering the coated filter. The coating solution comprises, based on the 100 parts by weight of silicon carbide ceramics powder, 0.5 to 15.0 wt.% of clay, 0.1 to 5.0 wt.% of calcium carbonate, 0.1 to 5.0 wt.% of carboxymethylcellulose, 0.1 to 5.0 wt.% of dispersant, 0.1 to 3.0 wt.% of defoaming agent and 150 to 250 wt.% of water. The sintering process includes the steps of heating the coated ceramic filter up to 800°C at temperature elevation rate of 1 to 2 °C/min; holding it at 800°C for 1-6 hours; heating the coated ceramic filter in the temperature range of 1000 to 1800°C at temperature elevation rate of 4°C/min; holding it at 1000-1800°C for 1-10 hours; and cooling to ambient temperature at a cooling rate of 5°C/min.
Abstract:
The present invention relates to a spouted bed type reactor for dry flue gas desulfurization and a multi-stage desulfurization method using the same. The present invention aims to provide a spouted bed type reactor for dry flue gas desulfurization and a multi-stage desulfurization method using the same in which a pressure difference between a front end and a rear end of a spouted bed type is lowered to raise a catalysis rate of sulfur oxide included in exhaust gas and a powder absorbent for desulfurization introduced into a reactor and concurrently to collect in multiple stages the sulfur oxide (Sox) and the powder absorbent according to a density difference in the reactor, and thus to collect and react in multiple stages the sulfur oxide (Sox) and the powder absorbent, thereby raising a desulfurization ratio. A spouted bed type reactor for dry flue gas desulfurization comprises: a gravity sedimentation box (1); a venturi unit (2) increasing the velocity of exhaust gas; a reactor body (3) including a conical fluidization unit (31) in which a powder absorbent for desulfurization flows to remove sulfur oxide, a fluidization unit (32) in which water, the exhaust gas and the powder absorbent injected in an upper direction, circulate to remove the sulfur oxide, and an absorbent recirculation cyclone (33) precipitating and collecting the powder absorbent that is not to be reacted included in the exhaust gas; a powder absorbent supply device (4) supplying the powder absorbent for desulfurization in the conical fluidization unit; a re-circulation powder absorbent supply device (5) re-supplying the powder absorbent that is not to be reacted for desulfurization to the conical fluidization unit; a water injection supply device (6) injecting compressed air and water upward; and a filter dust collector (7).
Abstract:
PURPOSE: An integrated apparatus for removing fine dust and nitrogen oxides is provided to successively collect fine dust particles at a high efficiency and remove over 90% of nitrogen oxides by an SCR catalyst from exhaust gas in one apparatus, to suppress the increase of the pressure loss of a dust collecting filter, to remarkably improve the filtration rate, and to drastically increase the fine dust collection rate. CONSTITUTION: An integrated apparatus for removing fine dust and nitrogen oxides successively comprises a filtering and dust collecting part(A), a cleaning part(B), an exhaust gas mixing part(C), and an SCR reaction part(D). The filtering and dust collecting part comprises an outer container(1); an inlet and an outlet formed on the both ends of the outer container respectively; and an outer shape successively formed with a first standard hopper(2a), a second standard hopper(2b), a first modified hopper, and a second modified hopper in the lower part of the outer container. The internal space region of the outer shape is divided into first and second chamber space areas comprising an inner container using multiple partition walls and one partition plate, and third and fourth chamber space areas outside of the inner container. Fine dust is removed from each of the divided chamber space areas. The cleaning part removes the fine dust which is filtered by the filtration and dust collecting part. The exhaust gas mixing part injects a reducing agent into the exhaust gas passed the filtration and dust collecting part, and mixes. The SCR reaction part selectively reduces and removes nitrogen oxides from the exhaust gas passed the exhaust gas mixing part. [Reference numerals] (AA) Exhaust gas
Abstract:
PURPOSE: Provided are a dust collecting filter with a surface layer capable of preventing dust permeation thereinto, a method and an apparatus for fabricating the same. CONSTITUTION: The method for fabricating a dust collecting filter with a surface layer capable of preventing dust permeation comprises the steps of coating a mixture of ceramic particles(1) having a size of about 30 micrometers and fused adhesive(2), i.e. liquid ceramic, on the surface of a dust collecting filter, thereby forming a surface layer; making the surface layer absorb hot air at a high speed from the backside thereof, thereby forming pores(6) on the surface layer; and drying the dust collecting filter.
Abstract:
PURPOSE: A fabrication method of silicon carbide ceramics filters on the outer surface of which a coating layer is formed is provided to improve dust collection efficiency. CONSTITUTION: The fabrication method of silicon carbide ceramics filter includes the steps of mixing silicon carbide ceramics powder 100 vol.%, 0.1 to 30.0 vol.% of carbon powder (based on the 100 volume percent of silicon carbide ceramics powder), 1.0 to 15.0 wt.% of inorganic binder (based on the 100 weight percent of silicon carbide ceramics powder), 3.0 to 20.0 wt.% of organic binder, 0.1 to 5.0 wt.% of calcium carbonate, 0.1 to 15.0 wt.% of dispersant, 0.1 to 3.0 wt.% of releasing agent and 10.0 to 35.0 wt.% of water; aging the mixture; pressure extruding the mixture in the form of filter; coating the surface of the filter by spray coating a coating solution; and sintering the coated filter. The coating solution comprises, based on the 100 parts by weight of silicon carbide ceramics powder, 0.5 to 15.0 wt.% of clay, 0.1 to 5.0 wt.% of calcium carbonate, 0.1 to 5.0 wt.% of carboxymethylcellulose, 0.1 to 5.0 wt.% of dispersant, 0.1 to 3.0 wt.% of defoaming agent and 150 to 250 wt.% of water. The sintering process includes the steps of heating the coated ceramic filter up to 800°C at temperature elevation rate of 1 to 2 °C/min; holding it at 800°C for 1-6 hours; heating the coated ceramic filter in the temperature range of 1000 to 1800°C at temperature elevation rate of 4°C/min; holding it at 1000-1800°C for 1-10 hours; and cooling to ambient temperature at a cooling rate of 5°C/min.
Abstract:
PURPOSE: A silicon carbide ceramics filter for dust collection is provided, which has high strength with the addition of alkali metal and alkali earth metal. CONSTITUTION: The fabrication method of silicon carbide ceramics filter includes the steps of mixing silicon carbide ceramics powder 100 wt.%, 1.0 to 15.0 wt.% of sintering aid (clay), 1.0 to 5.0 wt.% of forming auxiliary agent, 0.1 to 5.0 wt.% of alkali metal compound, 0.5 to 5.0 wt.% of dispersant, and 5 to 15.0 wt.% of water; aging the mixture; pressure extruding the mixture in the form of filter at 100 to 800 kg/cm¬2; and sintering the filter. The sintering process includes the steps of heating the ceramic filter up to 800°C at temperature elevation rate of 1.5 °C/min; holding it at 800°C for 6 hours; heating the ceramic filter up to 1400°C at temperature elevation rate of 4°C/min; and holding it 1400°C for 10 hours. The alkali metal compound is selected from alkali element oxides, alkali element nitride, alkali element carbonate, alkali earth element oxides, alkali earth element nitride and alkali earth element.