Abstract:
본 발명은 본 발명은 원유정제공정에서 발생하는 상압잔사유와 같은 중질유를 유동층접촉분해하여 가솔린, 프로필렌 등을 생산하는 설비의 배가스로부터 에틸렌을 농축하여 회수하기 위한 방법과 장치에 관한 것이다. 본 발명은 유동층접촉분해 배가스(FCC) 중의 에틸렌 순도를 높이고 약흡착성분들의 농도를 낮추어 줌으로써 후단의 에틸렌 치환탈착 공정에서 에틸렌 세정양을 줄이고, 약흡착성분과 탈착제의 증류 분리 조작 시 손실되는 탈착제의 양을 줄일 수 있는 압력변동흡착공정을 이용한 유동층접촉분해 배가스로부터의 에틸렌 회수방법 및 장치를 제공함으로써 중질유의 유동층접촉분해 배가스로부터 에틸렌은 높은 순도 및 저비용으로 회수할 수 있다.
Abstract:
PURPOSE: A desorption material for a continuous sulfur oxide adsorption removal process and a method consecutively removing a sulfur oxide from a hydrocarbon stream using the same are provided to efficiently remove a sulfide from a hydrocarbon stream by maintaining the sulfur oxide adsorption quantity of an adsorption material highly in a continuous process repeating the adsorption and desorption of the sulfur oxide. CONSTITUTION: A desorption material for a continuous sulfur oxide adsorption removal process includes any one selected from a DME (dimethyl ether), a DMC (dimethyl carbonate), and a MTBE (methyl tertiary butyl ether), and a mixture thereof. The desorption material additionally includes hexane or benzene. The desorption is performed at 40~90>=, 1~20barg. The vaporization latent heat of the desorption material is below 500 kJ/kg. The boiling point is 120>= or less which is a sulfide oxidation temperature. A method consecutively removing a sulfur oxide from a hydrocarbon stream includes following steps. A step for absorbing the sulfur oxide from a hydrocarbon stream by using an adsorption material selectively adsorbing the sulfur oxide; a step for reproducing the adsorption material by detaching the adsorbed sulfur oxide with the desorption material; and a step for reusing by separating a desorption material from the detached sulfur oxide and the mixture of the desorption material.
Abstract:
PURPOSE: A manufacturing method of an anisotropy element and a method thereof are provided to implement fine pitch connection by forming a nanostructure or a microstructure with the anisotropy element. CONSTITUTION: After a plate-shaped substrate is annealed, an electro polishing process of the plate-shaped substrate is executed(a-1). The pre-processed substrate is firstly anodized(a-2). An oxide layer of the substrate which is firstly anodized is eliminated in an etching process(a-3). The plate-shaped substrate is secondly anodized(a-4). A plurality of minute through holes is extended by acid treatment(a-5). [Reference numerals] (AA) Surface; (BB) Lateral cross section; (CC) Start; (DD) Pre-treatment; (EE) Firstly anodizing; (FF) Oxide etching; (GG) Secondly anodizing; (HH) Through hole extension; (II) End; (JJ) Step a-1; (KK) Step a-2; (LL) Step a-3; (MM) Step a-4; (NN) Step a-5;
Abstract:
본 발명은 공기 중의 산소를 선택적으로 흡착하는 산소 선택성 흡착제의 제조방법으로서, BaMg(CO 3 ) 2 입자 또는 BaMg(CO 3 ) 2 의 외부에 MgCO 3 또는 Mg(OH) 2 가 부착된 입자를 제조하는 단계 및 상기 입자를 고온 소성하는 단계를 포함하는 것을 특징으로 하는 산소 선택성 흡착제의 제조방법 및 이에 따라 제조된 산소 선택성 흡착제를 제공한다. 본 발명에 따른 산소 선택성 흡착제는 종래의 산소 선택성 흡착제보다 공기 중의 산소를 빠른 속도로 흡착시키면서도 높은 열적 안정성 및 우수한 산소 흡착능을 나타낸다.
Abstract:
본 발명은 온도변동 흡착공정에 의해서 연소배가스로부터 이산화탄소를 농축 회수하는 장치 및 방법에 대한 것이다. 본 발명은 이산화탄소 선택성 흡착제가 충진된 흡착탑에서 흡착-가열탈착-세정-냉각의 공정으로 이루어진 한 주기 운전을 수행함으로써 흡착-가열탈착-냉각단계로 운전이 되는 기존의 온도변동흡착공정에 비해 높은 흡착제 활용과 이산화탄소 제거율을 제공한다. 또한 가열탈착 및 냉각 공정은 탑 내의 가스를 연속적으로 재순환하여 운전함으로써 충분한 가열 및 냉각이 이루어지게 하는 것을 특징으로 한다. 이산화탄소 (Carbon dioxide), 온도변동흡착공정(Temperature swing adsorption), 연소배가스 (Combustion flue gas)
Abstract:
PURPOSE: An oxygen selective absorber and a method for preparing the same are provided to uniformly form a protective film on the surface of barium-contained compound using magnesium oxide. CONSTITUTION: Magnesium alkoxide is dissolved in alcohol in order to obtain magnesium oxide precursor solution. A barium-contained compound is dispersed in the magnesium oxide precursor solution in order to solate the dispersion solution. Distilled water is added to the solated dispersion solution in order to be gelated. The gelated dispersion solution is undergone a drying process and a sintering process.
Abstract:
PURPOSE: A catalyst for acid components in high TAN crude oil and a manufacturing method thereof are provided to especially remove naphthenic acid among the acid components, and to improve activity and stability under acidic atmosphere. CONSTITUTION: A catalyst used for removing acid components in high TAN crude oil includes alkaline earth metal silicate or alkaline earth metal aluminate which is gained by reacting silicate or aluminate anions with alkaline earth metal cations. A molar ratio of alkaline earth metal/Si or Al is 10 or less. The catalyst is manufactured by a high-temperature plasticity method, a sedimentation method or a sol-gel method. The catalyst is used at a temperature of 150 °C ~ 500 °C. The catalyst for removing the acid components is a natural mineral of forsterite, talc or enstatite.
Abstract:
A slurry composition for preparing a carbon dioxide adsorptive paper, which has a ceramic fiber and an adsorbent with excellent adsorption properties of carbon dioxide as principal raw materials, a honeycomb type adsorption element using a carbon dioxide adsorptive paper prepared from the composition, and a manufacturing method of the honeycomb type adsorption element are provided. A manufacturing method of a carbon dioxide adsorption element comprises: a paper making step of forming a carbon dioxide adsorptive paper using a carbon dioxide adsorptive paper making slurry comprising a carbon dioxide adsorbent and a ceramic fiber; and a honeycomb forming step of forming the carbon dioxide adsorptive paper formed in the paper making step into a single side corrugated body, and laminating or winding the single side corrugated body. The manufacturing method further comprises: a surface coating step of impregnating a honeycomb structured carbon dioxide adsorption element with an inorganic binder and drying the inorganic binder impregnated in the honeycomb structured carbon dioxide adsorption element after performing the honeycomb forming step; and a heat treatment step of decomposing organic matters in the honeycomb structured carbon dioxide adsorption element.
Abstract:
PURPOSE: Provided are a method for producing stable solid granular adsorbent with cylinder or sphere feature used for C4 olefin separation from mixtures and an application of the same adsorbent. CONSTITUTION: The method comprises the steps of dissolving silver compound such as caustic silver, lipid silver oxide, halogenation silver, silver oxide and a mixture thereof, into a solvent; mixing the silver compound solution with clay supports; drying the mixture at temperature between 100-200°C for 3 hours or more; and heat treating the dried mixture at 30-350°C for 3 hours or more, wherein feature of the clay support may be powder, granular, cylinder, or sphere, and contains 60-85 wt% of SiO2, 4-25 wt% of Al2O3, 2-10 wt% of Fe2O3, 3wt% of CaO, 7wt% of MgO, 3wt% of Na2O and 3wt% of K2O.