Abstract:
본 발명은 입체장애 아민(sterically hindered amine) 및 유기칼슘염(organic calcium salt)를 포함하는 이산화탄소의 흡수 및 탄산염 고정화를 위한 수용액 및 이를 이용한 이산화탄소의 흡수 및 탄산염 고정화 방법에 관한 것으로서, 본 발명에 따른 이산화탄소 흡수 및 탄산염 고정화를 위한 수용액은 이산화탄소 흡수제로서 높은 이산화탄소 흡수능, 낮은 이산화탄소 흡수 엔탈피 등을 가지는 입체장애 아민(sterically hindered amine)을 포함함으로써 수용액에 대한 이산화탄소 용해도를 현저히 향상시키고, 칼슘 이온 공급원으로서 유기칼슘염을 포함함으로써 칼사이트 및 바테라이트를 동시에 포함하여 산업상 활용도가 높은 탄산칼슘으로 이산화탄소를 고정화시킬 수 있다.
Abstract:
The present invention relates to a method for carbon dioxide capture and storage (CCS) and, more specifically, to a method to capture and store high-purity carbon dioxide while increasing energy efficiency by oxidizing (combusting) mixed gas containing hydrogen and carbon dioxide, from which part of the hydrogen has been separated; and transmitting thermal energy obtained therefrom to the mixed gas, from which hydrogen is to be separated, to preheat; and to a device for carbon dioxide capture and storage. According to the present invention, the method for carbon dioxide capture and storage can extend the lifetime of a hydrogen separation membrane and can increase the efficiency of a hydrogen separation process by removing hydrogen (H_2), carbon dioxide (CO_2), and aqueous vapor in the mixed gas containing aqueous vapor. Moreover, energy efficiency can be increased by recovering and oxidizing hydrogen not separated from a hydrogen separation membrane together with carbon dioxide, thereby heating mixed gas (H_2+CO_2), which has been cooled by removing the aqueous vapor, without an external energy supply. Also, high-purity carbon dioxide can be captured and stored.
Abstract:
The present invention relates to a carbon dioxide capture and storage (CCS) apparatus, in which a moisture separation process is performed prior to a hydrogen gas-carbon dioxide separation process through a hydrogen separation membrane so that the life of the hydrogen separation membrane can be extended and hydrogen separation process efficiency can be improved. The CCS apparatus according to the present invention includes a water gas shifter (WGS) reaction in which CO in synthetic gas containing H2 and the CO is allowed to react with vapor for discharge after conversion into carbon dioxide and hydrogen gas; a moisture separation membrane module that separates and discharges the vapor contained in mixed gas discharged from the WGS; and a hydrogen separation membrane module that has a plurality of palladium-based hydrogen separation membranes which separate the carbon dioxide and the hydrogen gas contained in the mixed gas passing through the moisture separation membrane module from each other.
Abstract:
The present invention provides a perovskite-type ion conductive oxygen membrane having a composition of Ba_1-xSr_xCo_1-yFe_yO_3-δ coated with barium chromium oxide, a producing method thereof, and an oxygen separation process using the membrane. The membrane coated with barium chromate based oxide of the present invention has a significantly improved oxygen permeability and thermal stability compared with an uncoated separation membrane, thereby being usefully applied in separating oxygen from air containing carbon dioxide and the like.
Abstract:
PURPOSE: A highly loadable and dispersive metal-oxide/carbon nano catalyst carrier and a production method thereof are provided to easily obtain catalysts in which metal-oxide particles are well dispersed along with carbon residues by removing excessive carbon substances which exists in a porous carbon molding frame. CONSTITUTION: A production method of highly loadable and dispersive metal-oxide/carbon nano catalyst carrier comprises the following steps; a mixing step which mixes metal-salt hydrate with a carbon molding frame in a porous structure; an impregnation step which impregnates the metal-salt hydrate in the carbon molding frame after melting and impregnating around the melting point of the metal-salt hydrate; a drying step which dehydrates the obtained mixed powder; and a removal step which forms metal oxide particles by sintering the carbon molding frame, in which the metal-salt hydrate is loaded, and removes carbons from the carbon molding frame leaving the partial amount of carbon. A sintering temperature above is ranged from 200 to 700 deg. C, and a sintering period is ranged from 30 to 48 hours. [Reference numerals] (AA) Melt-infiltration; (BB) High temperature sintering under the atmospheric condition; (CC) Removal of a carbon molding frame; (DD) Active oxidized metal particles; (EE) Remaining carbon(as a spacer)
Abstract:
본 발명은 석탄 합성가스를 슬러리에 함유된 촉매와 반응시켜 합성연료를 생성하는 재분산수단을 적용한 트레이 기포탑 반응기에 관한 것으로, 이를 위해 촉매를 함유하는 슬러리가 저장된 기포탑 반응기 본체;와, 유입관을 통해 공급되는 합성가스의 기포입자를 균일한 기포입자로 전환시켜 반응기 본체의 내부로 공급할 수 있도록 상기 반응기 본체의 저면에 배치되는 분산수단; 상기 반응기 본체의 내부를 트레이 형태로 구획되게 배치되며, 상기 분산수단으로부터 공급되는 합성가스의 기포 입자를 균일하게 재분산시키는 적어도 1개 이상의 재분산수단;과, 상기 반응기 본체의 내부 상측에 배치되어 촉매는 필터링하고 반응되어 생성된 합성연료만을 외부로 유출시키는 필터링수단; 및 상기 반응기 본체의 상단에 연결되어 미반응 합성가스 및 반응시 생성되는 화학가스를 외부로 배출시키는 유출관;을 포함하여 이루어지며, 상기 재분산수단은 내부 기공이 하단부에서 상단부로 연속적으로 불규칙하게 이어지는 다공성 금속 구조체와, 상기 다공성 금속 구조체의 상부에 결합되는 제 2분산디스크로 이루어지며, 여기에 상기 다공성 금속 구조체의 하부에 배치되는 다공성 촉매 금속 구조체를 더 포함하되, 상기 다공성 촉매 금속 구조체는 다공성 금속 구조체의 표면에 촉매층이 코팅되어 구성되는 것을 특징으로 한다.
Abstract:
PURPOSE: A catalyst for the Fischer-Tropsch process and a manufacturing method thereof are provided to accelerate the carbide forming reaction to increase the generation of hydrocarbon with a long chain like wax, and to be able to have the similar activity to the catalysts manufactured by co-precipitation by reducing the catalyst under the condition that synthetic gas (CO+H2) exists at a relatively low temperature of 350-400deg.C. CONSTITUTION: A catalyst for the Fischer-Tropsch process includes an iron compound as an active material, sodium and sodium hydroxide as co-catalyst, and a carrier. A manufacturing method of the catalyst for the Fischer-Tropsch process comprises the following steps: a step of removing moisture and foreign substances attached on the surface of the carrier by plasticizing the carrier; a step of stirring the plasticized carrier under the nitrogen atmosphere; a step of manufacturing a melted and dipped carrier by adding sodium and sodium hydroxide in the stirred carrier; a step of dipping an iron precursor and a copper precursor in the melted and dipped carrier; and a step of drying and plasticizing the carrier in which an iron precursor and a copper precursor are dipped.
Abstract:
PURPOSE: A manufacturing method for a metal- or metal oxide-supported catalyst using a melt-infiltration process with a metal hydrate salt and a metal- or metal oxide-supported catalyst thereof are provided to easily and quickly mass produce the metal- or metal oxide-supported catalyst by using a nitrate hydrate metal salt or a chloride hydrate metal salt with a low melting point. CONSTITUTION: A manufacturing method for a metal- or metal oxide-supported catalyst using a melt-infiltration process with a metal hydrate salt comprises the following steps: The metal hydrate salt is mixed with a metal substrate with a porous structure. After the mixing process, the mixture is melted at the melting point of the metal hydrate salt such that the metal hydrate salt infiltrates into the substrate. The metal hydrate salt infiltrated in the supporter is plasticized at a high temperature and chagrined to nanoparticles. The metal hydrate salt has a melting point within 35 - 120 deg. C. [Reference numerals] (a) Step of mixing metal hydrate salt and a support; (b) Step of carrying by melting impregnation; (c) Step of nanoparticulation by plasticizing
Abstract:
PURPOSE: An apparatus and a method for separating products from a Fischer-Tropsch process are provided to continuously product the products of the Fischer-Tropsch process containing wax by effectively discharging liquid products from the upper side of a reactor. CONSTITUTION: An apparatus for separating products from a Fischer-Tropsch process includes a temperature sensor(110), a porous inner filter(120), a collecting chamber(200), and a pressure sensor(300). The temperature sensor is arranged on the upper side of a reactor(100) and detects the temperature of gaseous products and liquid products. The inner filter is arranged in the reactor and adjusts the discharging amount of the products. The collecting chamber collects the liquid products from the reactor. The pressure sensor detects the pressure of the collecting chamber.