Abstract:
본 발명은 피셔-트롭쉬 합성반응용 고체촉매와 생성물의 연속 분리배출장치 및 방법에 관한 것으로서, 더욱 상세하게는 합성가스로부터 합성유를 제조하는 피셔-트롭쉬 합성반응에 있어서, 고체 촉매입자와 생성물의 혼합 슬러리를 원료가스의 주기적인 펄스(pulse)에 의해 연속적으로 분리할 수 있을 뿐만 아니라, 생성물을 효과적으로 반응기 하부로 배출시켜 고품질의 장쇄 탄화수소(long-chain hydrocarbon)인 왁스(wax)를 포함하는 피셔-트롭쉬 생성물을 안정된 조업하에 연속적으로 생산할 수 있도록 한 피셔-트롭쉬 합성반응용 고체촉매와 생성물의 연속 분리배출장치 및 방법에 관한 것이다. 이를 위해, 본 발명은 반응기 상부에 설치되어 반응물의 수위를 감지하는 수위감지수단; 상기 반응기 하부에 설치되어 반응기 내부에 혼합된 고체촉매 및 생성물을 분리하여 배출시켜주는 고체촉매/생성물 분리수단 및 배출수단; 및 상기 수위감지수단으로부터 감지신호를 입력받아 상기 배출수단의 개폐동작을 제어하는 제어부를 포함하고, 상기 분리수단은 고체촉매를 걸러주고 상기 배출수단은 반응물로부터 분리된 생성물을 반응기 하부로 생성량만큼 연속적으로 배출시키는 것을 특징으로 하는 피셔-트롭쉬 합성반응용 고체촉매와 생성물의 연속 분리배출장치를 제공한다. 피셔-트롭쉬 반응, 슬러리 기포탑 반응기, 가스펄스, 촉매, 원료가스, 합성유, 왁스
Abstract:
PURPOSE: A composite reaction system for Fisher-Tropsch synthesis is provided to improve the total reaction efficiency by transferring a catalyst which is suitable to hydrogenation into a secondary reactor, and to improve conversion rate of the reaction. CONSTITUTION: A composite reaction system for Fisher-Tropsch synthesis includes a slurry bubble tower main reactor(20) and a fixing layer secondary reactor(21) in which an iron-based catalyst is fixed. The slurry bubble tower main reactor has a distributor(14) and a sintered metal filter(15). The distributor disperses the synthetic gas into uniform bubbles(1). A plurality of pores of which diameter is 7μm or less is formed on the sintered metal filter. The main reactor and the secondary reactor include a thermocouple(26) and a plurality of flow control valves(16,25). A solid catalyst(2) of reactant slurry is filtered by the sintered metal filter.
Abstract:
A cobalt/phosphorus-alumina catalyst for reacting Fischer-Tropsch is provided to manufacture liquid hydrocarbon from synthetic gas by an F-T reaction, to increase hydrothermal stability and to reduce non-activation speed. A cobalt/phosphorus-alumina catalyst for reacting Fischer-Tropsch is manufactured by containing cobalt(Co) at a phosphorus-alumina support made by dipping phosphorus(P) at an alumina surface of which a specific surface area is 300 ~ 800 m^2/g. The cobalt/phosphorus-alumina catalyst is double pore structure that a small pore size and macro-pore(PS2) exist at the same time. The phosphorus of 0.05 ~ 20 weight% is dipped based on alumina 100 weight%. The cobalt(Co) 5~ 40 weight% is contained based on the phosphorus-alumina 100 weight%.
Abstract:
PURPOSE: A cobalt/aluminum phosphate catalyst capable of manufacturing carbon fiber under low temperature region and a manufacturing method thereof are provided to manufacture the carbon fiber efficiently while using a Fisher-Tropsh catalyst. CONSTITUTION: A manufacturing method of a cobalt/aluminum phosphate catalyst includes the following steps: forming hydrogel by acidifying a compound after mixing precursors of which the P/Al molar ratio is adjusted; synthesizing an amorphous aluminium phosphate supporter having the specific surface area 150 ~ 300 m^2/g after drying the hydrogen under the temperature of 100 ~ 200 °C; and manufacturing the cobalt/aluminum phosphate catalyst by sintering the dried support under the temperature of 200 ~ 700 °C.
Abstract:
Cobalt/zirconium-phosphorus/silica catalysts for Fischer-Tropsch synthesis and a preparation method thereof are provided to offer improved dispersibility and reducing property of cobalt and active components stably. A preparation method of a cobalt/zirconium-phosphorus/silica catalyst includes the following steps of: dipping a zirconium precursor and a phosphorus precursor in porous silica of which specific surface area is in a range of 200 ~ 800 m^2 / g; drying the porous silica in which a precursor is dipped in temperature of 100 ~200 °C; producing a zirconium - phosphorus/silica by firing the dried phosphorus silica; drying the dipped zirconium - phosphorus / silica support in 100 ~ 200 °C; and producing the cobalt/zirconium-phosphorus/silica catalyst by plasticizing the dried zirconium - phosphorus/silica support.
Abstract:
An indicator for detecting a sulfide compound, and a method for determining the lifetime of an adsorbent by using the indicator are provided to allow it to be prepared simply, to have a uniform color and to allow the color of an indicator to be changed rapidly and clearly by a sulfide compound. An indicator for detecting a sulfide compound comprises a silica or alumina support; and a transition metal which is supported in the silica or alumina support. The transition metal is a single metal or a mixture of at least two metals selected from copper, zinc, nickel and iron. The ratio of the transition metal is 0.5~10 by weight to the support. The sulfide compound is at least one selected from dimethyl sulfide, tetrahydrothiophene] and t-butylmercaptane.
Abstract:
A manufacturing method of cobalt/phosphorus-alumina catalyst for Fischer-Tropsch synthesis is provided to secure stable selectivity to a liquid hydrocarbon more than C5 and to develop a competitive GTL process. A manufacturing method of cobalt/phosphorus-alumina catalyst for Fischer-Tropsch synthesis comprises steps of: mixing aluminium alcoholate with alcoholometer organic solvent and manufacturing aluminium alcoxide solution; mixing organic carboxylic acid 0.01 ~ 1 molar ratio and the water 2 ~ 12 molar ratio into the aluminium alcoxide solution, including a precursor and manufacturing boehmite sol in which the phosphorus is comprised; distilling and drying the boehmite sol in which the phosphorus is comprised and separating and collecting alcohol and manufacturing the boehmite in which powdered phosphorus is comprised; plasticizing the powdered boehmite and manufacturing a phosphorus-alumina support; dipping a cobalt precursor into the phosphorus-alumina support; and manufacturing the cobalt/phosphorus-alumina catalyst.
Abstract:
A cobalt/zirconia-alumina catalyst in which small pores and large pores coexist by supporting cobalt as an active component on a zirconia-alumina support which comprises ZrO2 and Al2O3 and has a specific surface area by a coprecipitation process, thereby containing the cobalt in the support is provided, and a method for producing liquid hydrocarbons from syngas using the catalyst is provided. In a catalyst for Fischer-Tropsch reaction in which cobalt as an active component is supported on a support, the catalyst for Fischer-Tropsch reaction is characterized in that the catalyst is a catalyst in which cobalt as an active component is supported on a mixed support of zirconia and alumina containing Al2O3 and ZrO2, bimodal structures in which small pores(PS1) with a relatively small pore size and large pores(PS2) with a relatively large pore size coexist are formed in the catalyst, the small pores(PS1) ranges from 2 to 10 nm and the large pores(PS2) ranges from 10 to 200 nm, the ZrO2 is contained in the amount of 1 to 30 wt.% relative to the Al2O3, and the cobalt is contained in the amount of 5 to 40 wt.% relative to the total support. A method for producing liquid hydrocarbons from syngas comprises subjecting syngas to Fischer-Tropsch reaction in the presence of the catalyst for Fischer-Tropsch reaction to produce liquid hydrocarbons. Further, a specific surface of the carrier is 150 to 400 m^2/g and a specific surface of the catalyst is 100 to 300 m^2/g.
Abstract:
본 발명은 황 화합물 검지용 지시제 및 이를 이용한 황 화합물 흡착제에 관한 것으로서, 더욱 상세하게는 LNG(액화천연가스)나 LPG(액화석유가스) 등의 연료가스 중에 함유된 황 화합물로 이루어진 부취제를 제거하기 위해 사용되는 황 흡착제의 수명 및 교체 시기를 소정의 가스 분석 장비를 사용하지 않고, 쉽고 간편하게 육안으로 확인이 가능하도록 하기 위하여, 실리카, 알루미나 또는 제올라이트 지지체 표면에 특정의 전이금속을 담지시킨 후 이를 황 화합물과 반응하면 제3의 색으로 변색되는 황 화합물 검지용 지시제 및 상기 지시제를 일반적으로 사용되는 활성탄에 적층하여 탈황 성능을 획기적으로 증가시킴과 동시에 지시 성능을 갖는 황 화합물 흡착제에 관한 것이다. 황 화합물 검지용 지시제, 황 화합물 흡착제, 지지체, 활성탄
Abstract:
PURPOSE: An indicating agent for detecting sulfur compounds and a sulfur compounds absorbing agent using the same are provided to rapidly change the color of the indicating agent by easily reacting the sulfur compounds. CONSTITUTION: An indicating agent for detecting sulfur compounds is obtained by carrying a molybdenum compound on the surface of a silica, alumina, or zeolite carrier. A transition metal aqueous solution is prepared by dissolving the transition metal precursor of molybdenum. A support is prepared by carrying the transition metal aqueous solution in a silica, alumina, or zeolite carrier. Moisture is eliminated from the carrier.