Abstract:
PURPOSE: A vortex tube apparatus and a carbon dioxide absorption-separation system using thereof are provided to increase the contacting area of mixed gas and an absorbent by spraying the absorbent in a micro-droplet state. CONSTITUTION: A vortex tube apparatus includes a supplying pipe(110), an absorbent spray unit(120), a vortex producing unit(130), a first tube(140), a carbon dioxide separation unit(150), a second tube(160), a carbon dioxide analyzer, and a controller. The supplying pipe supplies mixed gas. The absorbent spray unit is installed on the supplying pipe. The vortex producing unit generates a vortex using the mixed gas supplied from the supplying pipe. The first tube is extended from the vortex producing unit, and forms a high temperature gas exhaust port. The carbon dioxide separation unit is installed on the high temperature gas exhaust port.
Abstract:
An apparatus for testing absorption equilibrium of an absorption solution is provided to absorb and separate a carbon dioxide included in a combustion gas generated after burning fossil fuel and to reduce an amount of the carbon dioxide emitted to airborne fundamentally. An apparatus for testing absorption equilibrium of an absorption solution for removing carbon dioxide from a combustion gas contains an air thermostat bath(1) maintaining a constant temperature using preheated air supplied from outside, a mixed gas storing tank(2) in which the carbon dioxide is supplied from outside and which is charged and an absorption reaction bath(3) in which a balancing test of the absorption-reaction of the carbon dioxide is performed by supplying the carbon dioxide from the mixing gas storing tank.
Abstract:
본 발명은 유동층 연소로에서 석탄, 하수슬러지, 목재 등과 같은 탄소원을 연소시킬 때 발생되는 질소산화물(NOx)과 아산화질소(N 2 O)를 저감하는 기술에 관한 것으로서, 유동층 연소로 내에서 질소산화물 및 아산화질소의 저감 반응에 활성을 가지는 물질로 구성된 다공성 유동매체와 함께, 무수 암모니아, 암모니아수, 우레아 수용액 등의 암모니아 계 환원제를 혼합하여 슬러리 형태로 제조하여 유동층 연소로 내에 분사하면, 유동층 연소로에서 고체 폐기물, 하수슬러지와 같은 질소함량이 높은 연료를 소각할 때 발생하는 질소산화물과 아산화질소를 동시에 제거하는 효과를 얻을 수 있다. 본 발명의 구성은 1단계에서는 다공성의 유동매체에 포함된 환원제가 표면에서부터 증발되면서 질소산화물(NOx)과 아산화질소(N 2 O)와 함께 반응하여 선택적비촉매환원반응이 일어나고, 환원제 일부가 증발되면서 가벼워진 유동매체는 분사된 영역보다 높은 상부로 이동하여, 2단계로 다공성 유동매체의 기공으로 확산하여 들어온 일부 질소산화물(NOx)과 아산화질소(N 2 O)가 기공 표면에서 환원제와 선택적촉매환원반응을 일으키며, 슬러리 상태에서 유동매체의 기공에 흡수되었던 환원제가 모두 증발되어 제거되면, 유동매체는 더욱 가벼워져 더 높은 상부로 이동하게 되어 미반응 N 2 O가 유동매체의 기공에서 분해되는 3단계 반응에 의한 질소산화물(NOx)과 아산화질소(N 2 O)의 동시 저감하는 방법을 특징으로 한다.
Abstract:
PURPOSE: A method for simultaneous removal of nitrogen oxide (NOx) and nitrous oxide (N2O) is provided to reduce costs to form apparatuses for removal of the respective NOx and N2O since the NOx and N2O are removed at the same time in the fluidized bed combustor. CONSTITUTION: A method for simultaneous removal of NOx and N2O is as follows. A reducing agent included in porous fluidization material is evaporated from the surface, and reacts to the NOx and N2O so that the selective non catalytic reduction (SNCR) occurs. The fluidization material, which is lighten by evaporation of a part of the reducing agent, removes to the upper part higher than the area the fluidization material is jetted. A part of NOx and N2O, which are diffused into the pore of the porous fluidization material, occur the selective catalytic reduction (SCR) with the reducing agent in the surface of the pore. The reducing agent, which is absorbed in the pore in slurry state, is evaporated and removed completely. The fluidization material becomes much lighter and moves much higher upper part, and unreacted N2O is degraded in the pore of the fluidization material. [Reference numerals] (a) Step 1: SNCR reaction of NOx by ammonia generated by urea decomposition (reaction area i); (b) Step 2: SCR reaction of NOx and N_2O by ammonia generated by urea decomposition (reaction area ii); (c) Step : decomposing reaction of N_2O (reaction area iii)
Abstract:
Disclosed is a flue gas absorbent composition which contains a compound and water. The compound has a ring structure and includes terminal primary amine groups and substituted alpha-carbon atoms neighboring the amine groups. Further, a use of a solution of a compound having a ring structure and terminal amine groups as a flue gas absorbent is disclosed. The absorbent composition includes a ring-structure compound having superior absorption ability when compared to conventional absorbents, thereby exhibiting excellent properties, i.e., flue gas absorption rate improved by 50 to 100% and flue gas absorption capacity improved by 200 to 400%, as compared with currently used absorbents such as monoethanolamine (MEA) and 2-amino-2-methyl-propanol (AMP).
Abstract:
An air distributing nozzle for the flowing of the fluid bed boiler and an installation method thereof are provided to prevent from the layer material being flowed in into the blast box along the nozzle by height between the air outlet and the air nozzle vertical hem are made two times of the air outlet size. An air distributing nozzle for the flowing of the fluid bed boiler comprises the air nozzle(2) is the air flowed in from the air supply hole installed in the upper side of the air distribution plate(1) flowed in the flowing layer burning route for supplying the air to the fluidized bed combustion to inside, and the air nozzle cap(3) punching a plurality of air hole(4) in the constant interval. The distance(D2) between the air outlet of one end of the air nozzle and the air nozzle cap are two times of the air nozzle diameter length(D1). Accordingly, the layer material does not flow reversely to the blast box of the air distribution plate lower part in which the air is collected.