Abstract:
The present invention relates to a method for manufacturing an iron-carbide/silica nanocomposite catalyst for Fischer-Tropsch synthesis, to a catalyst thereof, to a method for synthesizing liquid hydrocarbon using the same, and to liquid hydrocarbon thereof. Provided are an iron-carbide/silica catalyst for Fischer-Tropsch synthesis, in which an iron-silicate structure having large specific surface area and having well developed pores is first formed by a hydrothermal reaction of silica particles with a nanostructure and an iron salt, and the same is activated in the presence of high temperature carbon monoxide to have high reactivity for Fischer-Tropsch synthesis, and a method for manufacturing the same. And provided are a method for effectively manufacturing liquid hydrocarbon based on high CO conversion ratio and selectivity by Fischer-Tropsch synthesis using the manufactured iron-carbide/silica composite catalyst, and liquid hydrocarbon thereof.
Abstract:
본 발명은 동시 용융함침에 의한 혼성 합금 촉매 담지체 제조 방법 및 그 합금 촉매 담지체에 관한 것으로, 그 목적은 담지 하고자 하는 금속염들을 기계적으로 동시 혼합 후, 혼합된 금속염을 녹여 다공성 지지체에 함침시켜 합금입자가 담지된 촉매 담지체들을 쉽고 빠르게 제조할 수 있는 동시 용융함침에 의한 혼성 합금 촉매 담지체 제조 방법 및 그 합금 촉매 담지체를 제공하는데 있다. 본 발명의 구성은 a) 둘 이상의 금속염들과 다공성 지지체 간의 혼합단계와; b) 공동 용융함침에 의한 금속염들 간의 융합단계와; c) 고온 소성과정을 통해 다공성 지지체 내 금속염들을 합금화 시키는 단계;를 포함하는 동시 용융함침에 의한 혼성 합금 촉매 담지체 제조 방법 및 그 합금촉매 담지체를 발명의 특징으로 한다.
Abstract:
본 발명은 동적 기체분배기 및 그를 적용한 기포탑 반응기에 관한 것으로, 합성가스의 기포입자를 균일하게 전환시킴은 물론, 기포입자의 후단에 생기는 웨이크(wake:교란된 공기의 흐름)에 의해 기포기둥이 발생되는 현상을 억제하여 반응기본체 내에서의 반응효율을 증진시키기 위한 것이다. 본 발명에 따른 기포탑 반응기는 반응기본체와 동적 기체분배기를 포함한다. 반응기본체는 촉매를 함유하는 슬러리가 저장되며, 촉매를 함유하는 슬러리가 유입되는 합성가스와 반응하여 합성연료를 생성한다. 그리고 동적 기체분배기는 반응기본체의 하부에 연통되게 배치되며, 유입관을 통해 공급되는 합성가스를 회전으로 분산시키고, 분산된 합성가스를 균일한 기포입자로 전환시켜 반응기본체의 내부로 공급한다.
Abstract:
The present invention relates to iron oxalate hydrate particles with controlled shapes and a manufacturing method thereof, iron oxide-carbon composites manufactured using the iron oxalate hydrate particles and a manufacturing method thereof, and the purpose thereof for manufacturing ferric oxalate particles with variously controlled shapes by conducting high temperature hydrolysis reaction of saccharides supplying carbon and the aqueous solution of a surfactant and water and providing oxidized iron/carbon composite therefrom. The present invention includes ferric hydroxide salt, a step of mixing the surfactant and saccharides with distilled water in a reactor; a step of forming iron oxalate particle with controlled shapes; a step of separating and washing it by putting distilled water or ethanol after reducing the temperature up to room temperature; a step of powderizing the iron oxalate particle; a step of high temperature sintering the iron oxalate particle under atmospheric condition or an inert gas atmosphere for hydrolysis to form oxidized iron particle among residual carbons. [Reference numerals] (S100) Step of mixing ferric hydroxide salt, a surfactant and saccharides with distilled water in a reactor; (S200) Step of forming iron oxalate particles with controlled shapes by decomposing ferric hydroxide salt through a hydrothermal reaction after temperature rising; (S300) Step of performing dispersing and washing by putting distilled water or ethanol after reducing the temperature up to room temperature; (S400) Step of performing centrifugation on the iron oxalate particles using a centrifuge; (S500) Step of powderizing the iron oxalate particles; (S600) Step of re-dispersing and washing using distilled water or ethanol after centrifugation; (S700) Step of high temperature sintering the iron oxalate particles with a controlled shape in a power condition under atmospheric condition or an inert gas atmosphere for hydrolysis to form oxidized iron particle among residual carbons
Abstract:
Disclosed are a production method of an Fe/carbon nanocomposite catalyst for the Fischer-tropsch synthesis which comprises the following steps: a mixing step of mixing an Fe metallic hydrate salt with porous carbon supporters; an impregnation step of melting and impregnating the mixture around a melting point of the Fe metallic hydrate salt, and impregnating the Fe metallic hydrate salt to the carbon supporters; a particle formation step of plasticizing the Fe metallic hydrate salt in the carbon supporters at high temperatures and under the carbon monoxide or hydrogen atmosphere, for forming metallic Fe carbide particles in the carbon supporters; and a drying step of passivating the Fe carbide particles with ethanol, and vacuum-drying the Fe carbide particles, the Fe/carbon nanocomposite catalyst produced by the same, and a production method of liquid hydrocarbon using the same. [Reference numerals] (AA) Iron hydrate salt;(BB) Porous carbon supporter;(CC) Low-temperature aging;(DD) Form amorphous Fe-C composites;(EE) High-temperature decomposition;(FF) Iron carbide / charcoal nanostructures;(S104) Fe-carbide catalyst activated outside reactor
Abstract:
PURPOSE: A synthetic fuel production apparatus using biomethane and a method thereof are provided to be used for vehicles and power generation plants. CONSTITUTION: A biogas reservoir(1) collects biogas from a biogas generation place and stores the biogas. A biogas purifier(2) separates biomethane with high purity from the biogas. A steam methane reforming device(3) is composed of a modular metal structure catalyst which generates synthetic gas by reforming the biomethane and a modular heat exchange reactor with multiple pipes. The Fisher-Tropsch synthesis reactor(5) is composed of a modular metal structure catalyst which liquefies the biogas to generate synthetic fuel and a modular heat exchange reactor with multiple pipes. An electricity generating device for a fuel cell(6) generates electricity using hydrogen with high purity as a raw material. [Reference numerals] (AA) H_2/CO rate 3:1; (BB) H_2/CO rate 2:1
Abstract:
PURPOSE: A metal and silica doped catalyst and a manufacturing method thereof are provided to uniformly dip metal particles with 20 wt% or higher concentration by developing pores and be thermally stable by not causing sintering between the metal particles at 700°C of high temperature heat treatment. CONSTITUTION: A manufacturing method of a metal and a silica doped catalyst comprises the following steps: manufacturing metal, metal oxide, or an alloy nano particles by decomposing organometallic compounds at high temperature by mixing with organic surfactant and organic solvent; coating the nano-particles with silica using micro emulsion; converting the metal and silica core-shell structure into the branched metal silicate structure using a high temperature hydrothermal reaction; and obtaining metal doped catalyst which is high deposited in silica by reducing and annealing the metal silicate structure under a high temperature hydrogen condition. The metal or metal oxide nano-particle and alloy nano-particle are manufactured in a non-aqueous system. [Reference numerals] (AA) Metal salt + organic surfactant; (BB) Thermal reduction or decomposition; (CC) Metal or metal oxide nanoparticles; (DD) Silica coating using microemulsion; (EE) Metal or metal oxide/silica core-shell nanoparticles; (FF) Hydrothermal reaction; (GG) Branch type metal silicate structure; (HH) High temperature plasticizing or reduction; (II) Metal/silica doped catalyst
Abstract:
PURPOSE: A trade bubble column reactor using a redistribution disc is provided to activate the reaction of a catalyst and synthetic gas inside the reactor by uniformly redistributing bubble particles of the synthetic gas. CONSTITUTION: A trade bubble column reactor using a redistribution disc comprises the following: a bubble column reactor body(10) for storing slurry containing a catalyst; a distributing unit(20) converting bubble particles of synthetic gas supplied through an inlet pipe(11) into uniform bubble particles, and supplying into the bubble column reactor body; a re-distributing unit(30) uniformly re-distributing the bubble particles; a filtering unit(40) discharging synthetic fuel after filtering and reacting with the catalyst; and an outlet pipe(12) discharging chemical fume generated from non-reacted synthesis gas.
Abstract:
PURPOSE: A multistage separation type cooling system for elimination of heat of reaction at a Fischer-Tropsch slurry bubble column reactor is provided to minimize the harmful elements for the bubbling in a reactor and enable the easy installation and maintenance of a cooling pipe. CONSTITUTION: A multistage separation type cooling system for elimination of heat of reaction at an FT(Fischer-Tropsch) slurry bubble column reactor comprises: a first cooling pipe(31) which is horizontally installed in an upper cover of a reactor; a second cooling pipe(32) which protrudes toward the outside and has a discharge hole at an end portion thereof; a third cooling pipe(33) which vertically connects the first and second cooling pipes; and an inner pipe(40) which absorbs the heat around the sprayed cooling water to enable the phase change into stream.
Abstract:
A cooling system for eliminating reaction heat at a fischer-tropsch slurry bubble column reactor is provided to control the heat-generating temperature inside the reactor by jetting the small amount of cooling water on a cooling pipe at cooling pipe through an injection pipe arranged inside the cooling pipe. A cooling system(100) for eliminating reaction heat at a FT(Fischer Tropsch) slurry bubble column reactor comprises: a first cooling pipe(10) which is arranged on the top of the FT slurry bubble column reactor(200) and is connected to the FT slurry bubble column reactor; a plurality of second cooling pipes(11) connected vertically downward to the bottom of the first cooling pipe; and a cooling water spray pipe(20) which has smaller inside diameter than the inside diameter of the second cooling pipe and the first cooling pipe and in which the end part is closed to form inside pressure; The first cooling pipe is arranged as in a concentric circle or a grid structure. The injection pipe is connected to a valve(22) to control the pressure of the cooling water and includes a plurality of nozzles(21) to spray the flowed water.