Abstract:
PURPOSE: A dry type carbon dioxide collecting apparatus is provided to improve the collecting efficiency of carbon dioxide by preventing the reverse flow of gas to a vertical transferring pipe using a bubbling fluidized-bed collector. CONSTITUTION: A dry type carbon dioxide collecting apparatus includes a collecting reactor(101), a vertical transferring pipe(108), a regenerating reactor(124), a first separator(112), and a second separator(120). The collecting reactor includes a collecting buffering chamber(102) and a collecting diffusing plate(104). A part of a space formed on the upper side of the collecting diffusing plate is filled with absorbent particles(138). One end part of the vertical transferring pipe is in connection with the collecting reactor. Another end part of the vertical transferring pipe is in connection with the first separator. The first separator collects carbon dioxide based on the absorbent particles and separates and discharges remaining gas. The regenerating reactor includes a regenerating buffering chamber(126) and a regenerating diffusing plate(128). A part of a spaced formed on the regenerating diffusing plate is filled with absorbent particles. Absorbent particles separated from the first separator are supplied to the regenerating reactor. The second separator separates and discharges carbon dioxide separated from the regenerating reactor.
Abstract:
PURPOSE: A fluidized bed drying apparatus is provided to improve the drying efficiency by flowing backward particles dried more with particles dried less because gas of different flow velocity is supplied. CONSTITUTION: A fluidized bed drying apparatus comprises a particle pouring unit(100), a dryer unit(200), a hot air supplying unit(300), a dust collection unit(400), a filter unit(500), a heat exchanging unit(600), and a pressing unit(700). Wet particles are inserted into the particle pouring unit. The inner space of the dryer unit is partitioned by a perforated plate(202) into upper and lower parts(206,208). The hot air supplying unit supplies gas to the dryer unit. The dust collection unit separates power of gas particles discharged from the dryer unit. The filter unit filters fine dust discharged from the dust collection unit. The heat exchanging unit supplies external gas to the hot air supplying unit. The pressing unit presses the power and particles discharged through the dryer unit, the dust collection unit, and the filter unit into a pellet form.
Abstract:
PURPOSE: A fluidized bed reaction apparatus using a solid spraying nozzle with a bent part is provided to bend the solid spraying nozzle and to install the solid spraying nozzle in the second region of fluidized bed reactors. CONSTITUTION: A fluidized bed reaction apparatus includes distributing plates(112a, 112b), solid spraying nozzles(115a, 115b), bent parts(116a, 116b), and solid circulating pipes(130a, 130b). The distributing plates separate a first region(111a) and a second region(113a). Reaction gas is contained in the first region. Solid particles are contained in the second region. The distributing plates form a plurality of holes to transfer reaction gas to the second region. The solid spraying nozzles introduce and emit gas for solid spraying gas. The bent parts are formed between one end part and another end part of the solid spraying nozzles. The solid circulating pipes are in connection with another end part of the solid spraying nozzles.
Abstract:
PURPOSE: A CLC(Chemical-Looping Combustor) and a chemical-looping combustion method using the same are provided to improve the reaction efficiency by distributing the fuel, which is injected into a reduction reactor, to a lower fuel inlet and side gas inlets. CONSTITUTION: A CLC(100) comprises an oxidation reactor(110), a reduction reactor(120), a lower fuel inlet(121), and one or more side gas inlets(123,124). The lower fuel inlet is located in the lower part of the reduction reactor. The side gas inlets are located on one side of the reduction reactor.
Abstract:
PURPOSE: The solid particle amount circulating can be controlled easily. Provided is the liquid layer system capable of the solid circulation between two reactors selective. CONSTITUTION: A liquid layer system comprises the internal space is divided with the spreader plate(21) into the top reaction chamber(22) and lower part introduction area(23). The solid particle of two types having the different diameter is charged in the reaction chamber and the reaction is proceed. With the first fluid bed reactor in which the exhausting part projected to outside is formed on the reaction chamber sidewall and discharging the solid particle charged in inside.
Abstract:
PURPOSE: To provide a system for separating and recovering CO2, the system capable of easily performing temperature control and continuous operation of the reactor by using a conveyance reactor or fluidized bed reactor having a high flow rate as a reactor for recovering CO2. CONSTITUTION: The system for separating and recovering CO2 comprises: a recovery reactor(1) for recovering CO2 by contacting CO2-contained gas(11) supplied from the outside with a dry type solid absorbent; a cyclone number 1(3a) connected to the recovery reactor to exhaust gas and separate solid containing CO2 only; a fluidized bed reactor(2) for separating the solid into CO2 and a dry type solid absorbent using a fluidization gas(8) by receiving solid containing CO2 through a solid transfer pipe(7) comprising a loop chamber(5) connected to the cyclone number 1, and sending the separated dry type solid absorbent to the recovery reactor again through a transfer means; and a cyclone number 2(3b) for releasing CO2 separated from the fluidized bed reactor to the outside so that the separated CO2 is used.
Abstract:
PURPOSE: A flange insulator and a method for insulating a flange are provided to facilitate the insulating process and to allow the insulator to be completely restored even when the insulator is disassembled caused by the leakage of fluid. CONSTITUTION: A pipe(1) and a flange(2) are coupled to each other through a butt welding process. A flange insulator formed with an insulator(4) surrounding the end of the pipe(1) and the flange(2) is installed at an outer portion of the flange. Then, the flange insulator is fixed by a bolt. The flange insulator has a pipe insertion space and a flange insertion space at an inner portion thereof. The outer portion of the flange insulator is covered by the insulator(4). Then, a thin metal plate(6) is formed on the outer portion of the insulator(4). Two flange insulators are assembled with a pipe insulator(3) so as to insulate the flange.
Abstract:
PURPOSE: A pressurized and fluidized layer combustion system is provided to prevent the green house effect by preventing nitrogen oxide form being generated during the combustion process through continuously supplying pressurized oxygen. CONSTITUTION: Oxygen(3) is supplied into a pressurized and fluidized layer combustion furnace(4), thereby raising pressure in a pressurized and fluidized layer combustion system with moving material consisting a fluidized layer. Then, oxygen(3) is burned by supplying a solid fuel(2). At this time, limestone is added to prevent sulfur contained in the solid fuel(2) from being discharged as sulfuric oxide. While the combustion process is being carried out, combustion gas is generated. Impurities contained in combustion gas are filtered while combustion gas is passing through an impurity collecting device(5). In addition, a compressor(6) supplies pressure to combustion air. Then, combustion gas is again supplied to the pressurized and fluidized layer combustion furnace(4) through a CO2 route.
Abstract:
PURPOSE: A pressurized and fluidized layer combustion system is provided to prevent the green house effect by preventing nitrogen oxide form being generated during the combustion process through continuously supplying pressurized oxygen. CONSTITUTION: Oxygen(3) is supplied into a pressurized and fluidized layer combustion furnace(4), thereby raising pressure in a pressurized and fluidized layer combustion system with moving material consisting a fluidized layer. Then, oxygen(3) is burned by supplying a solid fuel(2). At this time, limestone is added to prevent sulfur contained in the solid fuel(2) from being discharged as sulfuric oxide. While the combustion process is being carried out, combustion gas is generated. Impurities contained in combustion gas are filtered while combustion gas is passing through an impurity collecting device(5). In addition, a compressor(6) supplies pressure to combustion air. Then, combustion gas is again supplied to the pressurized and fluidized layer combustion furnace(4) through a CO2 route.
Abstract:
본 발명은 유동층을 이용한 슬러지 소각 방법 및 장치에 관한 것으로, 다량의 수분(40%-80%)을 함유한 하수슬러지 또는 제지슬러지를 소각시키기 위한 유동층 소각장치로서 슬러지를 소각로에 투입시키고 소각로의 하부에서 공기를 불어넣어 슬러지가 부유상태에서 소각하며, 소각시 발생되는 배가스는 사이클론에서 분진을 포집하고 고온의 배가스를 건조시스템에 유입시켜 고수분함유의 슬러지를 건조하고 배가스를 정제하는 세정기나 미세분진을 포집하는 여과포 집진기를 거쳐 대기 오염 물질을 제거하고 배출하도록 하는 것에 관한 것이다.