Abstract:
본발명은슬러리기포탑반응기를이용한경유및 휘발유고함량합성연료의제조방법에관한것으로, 본발명에서는기존에저온 FT 반응에주로적용하는슬러리기포탑반응기(SBCR)를고온에서운전하여왁스의생산보다경유또는휘발유함량이증가된피셔트롭시합성반응생성물을생산할수 있는최적공정을제공할수 있다.
Abstract:
The present invention relates to a hydrocarbon compound using a fischer-tropsch synthesizing reaction and a manufacturing method thereof and, more specifically, to a hydrocarbon compound using a fischer-tropsch synthesizing reaction and a manufacturing method thereof capable of increasing the productivity of hydrocarbons with 5 or more carbons by optimizing the reducing state of an iron-based catalyst, and reducing the selectivity of CO_2 and the selectivity of CH_4 and C_2-C_4 hydrocarbons. The present invention comprises a reducing step of reducing the iron-based catalyst at 270-290°C for 18-22 h by injecting first gas containing CO_2, H_2, and CO in a first reactor charged with the iron-based catalyst; and a manufacturing step of manufacturing the hydrocarbon compound having the relatively lower selectivity of CO_2 in the whole of products than a case of being reduced by H_2 and CO as the first gas and the relatively higher selectivity of hydrocarbons with 19 or more carbons in the whole of the hydrocarbons than the case of being reduced by H_2 and CO as the first gas.
Abstract:
The present invention relates to a dynamic gas distributor and a bubble tower reactor using the same. The purpose of the present invention is to inhibit synthesis gas from leaking out of the dynamic gas distributor while promoting the reaction efficiency of a catalyst and the synthesis gas in the main body of a reactor. The dynamic gas distributor according to the present invention is installed on the main body of the bubble tower reactor to intercommunicate with the main body and includes a mixing box, a gas dispersing device, and a fixed dispersing disk. The mixing box has, on an upper part, an opening part formed to be able to be connected to the main body of the reactor and temporarily stores synthesis gas introduced through an inflow pipe. The gas dispersing device receives the synthesis gas from the outside of the mixing box, provides the synthesis gas into the mixing box, and sprays the synthesis gas to the fixed dispersing disk from the inside of the mixing box. Also, the fixed dispersing disk is installed to be combined with the opening part of the mixing box and converts the bubble particles of the synthesis gas dispersed by the gas dispersing device into uniform bubble particles by forming a plurality of opening holes on the surface thereof.
Abstract:
The present invention relates to a manufacturing method for an iron-carbide/carbon nanocomposite catalyst containing a potassium additive for high temperature fischer-tropsch synthesis reaction, the iron-carbide/carbon nanocomposite catalyst, a manufacturing method for liquid hydrocarbon using the iron-carbide/carbon nanocomposite catalyst and the liquid hydrocarbon. The purpose of the present invention is to provide the manufacturing method for the iron-carbide/carbon nanocomposite catalyst containing the potassium additive for high temperature fischer-tropsch synthesis reaction which uniformly dips potassium by using various methods such as a prior addition method which uniformly dips heptahydrate salt in an inner portion of a porous carbon support through a melt infiltration method while grinding and putting potassium salt, a middle addition method which infiltrates a potassium solution by a wet dip-coating method after the dip-coating of iron salt and a post addition method, the iron-carbide/carbon nanocomposite catalyst, the manufacturing method for liquid hydrocarbon using the iron-carbide/carbon nanocomposite catalyst and the liquid hydrocarbon. The present invention can produce a highly activated iron-carbide/potassium/carbon-based composite catalyst for a high temperature F-T reaction, wherein 5-30 wt% of activated iron-carbide particles are dipped in the porous carbon support and can manufacture liquid hydrocarbon in a high yield rate since the highly activated iron-carbide/potassium/carbon-based composite catalyst for a high temperature F-T reaction is thermostable in the high temperature F-T reaction of more than 300°C. [Reference numerals] (AA) Iron hydrate;(BB) Porous carbon supporter;(CC) K compound pre-addition method;(DD) Form amorphous Fe-C composites;(EE) K compound mid-addtion method;(FF) Iron-carbide/carbon composite formation;(GG) K compound late-addition method;(HH) Iron-carbide/calcium/carbon composite
Abstract:
본 발명은 수화된 금속염의 용융함침을 이용한 금속 또는 산화금속 촉매 담지체의 제조 방법 및 그 금속 또는 산화금속 촉매 담지체에 관한 것으로, 그 목적은 질산수화물 금속염이나 염화수화물 금속염의 낮은 용융점을 이용하여 금속 또는 산화금속 촉매 담지체를 대량으로 쉽고, 빠르게 제조하는 방법 및 그 금속 또는 산화금속 촉매 담지체를 제공하는 데 있다. 본 발명은 a) 금속 수화물 염을 다공 구조의 금속 지지체와 혼합하는 단계와; b) 혼합후 금속 수화물 염의 융점에서 용융 함침시켜 금속 수화물 염을 지지체에 담지하는 단계와; c) 지지체에 담지된 금속 수화물 염을 고온 소성시켜 분해하여 나노 입자화하는 단계;로 이루어진 수화된 금속염의 용융함침을 이용한 금속 또는 산화금속 촉매 담지체의 제조 방법 및 이로부터 제조된 금속 또는 산화금속 촉매 담지체를 발명의 특징으로 한다.
Abstract:
본 발명은 석탄액화(CTL) 및 천연가스 액화(GTL) 공정에서 피셔-트롭쉬(Fischer-Tropsch; FT) 반응에 사용되는 철-코발트 복합 촉매 및 그 제조 방법과 이를 촉매로 이용한 피셔-트롭쉬 합성 반응에서의 수성가스전환반응 활성구현과 고선택적 액체 연료 제조방법에 관한 것으로, 보다 상세하게는 피셔-트롭쉬 반응에서 합성가스의 H 2 /CO 조성 몰비가 2.0 근방의 범위에서 높은 활성을 보이지만 2.0 미만으로 낮아지게 되면 급격하게 활성이 떨어지는 기존의 코발트(Co) 촉매의 단점을 보완하고, 고온의 반응에서도 액체 오일(C 5+ ) 생산에 높은 선택성을 보이는 철 성분을 첨가한 철-코발트 복합 촉매 및 그 제조 방법을 이용하는데 있다.
Abstract:
PURPOSE: A dynamic gas distributor and a bubble column reactor applying the same are provided to improve a catalyst and a reaction efficiency in the reactor main body and to prevent a malfunction of the dynamic gas distributor and the loss of the catalyst by minimizing the back flow of the slurry in the reactor main body to the dynamic gas distributor during the reaction or at the completion of reaction. CONSTITUTION: A bubble column reactor comprises a reactor main body(10) and a dynamic gas distributor(20) arranged to be connected to the lower part of the reactor main body. The reactor main body stores the slurry containing the catalyst. The synthetic fuel is produced by the reaction of the slurry containing the catalyst with the synthesis gas introduced in the main body. The gas distributor disperses the synthesis gas supplied through the inlet tube(24) by rotation, converts the dispersed synthesis gas into the uniform bubble particle, and supplies this to the inside of the reactor main body.