Abstract:
The present invention relates to a nickel (Ni) dispersion catalyst for reforming hydrocarbon including Ni dispersed in a hydrotalcite-like carrier wherein Ni occupies 50 wt% or more among the total of the catalyst and the specific surface area of the Ni is not less than 200 m^2/g. According to the present invention, a high content of the Ni dispersed in the carrier has a high dispersion, a large specific surface area, outstanding catalyst activity at low temperatures while having reaction stability, and excellent inside coking. Furthermore, the nickel dispersion catalyst is used for a diesel having aromatic compounds and a large range of boiling points for a long time.
Abstract translation:本发明涉及一种用于重整碳氢化合物的镍(Ni)分散催化剂,其包括分散在类水滑石载体中的Ni,其中Ni占催化剂总量的50重量%以上,Ni的比表面积不小于 200 m ^ 2 / g。 根据本发明,分散在载体中的高含量的Ni具有高的分散性,大的比表面积,在低温下具有突出的催化剂活性,同时具有反应稳定性和优异的内部焦化。 此外,镍分散催化剂长时间用于具有芳族化合物的柴油和大沸点范围。
Abstract:
본 발명에 따른 개질 촉매는 고표면적 스피넬 구조의 담체인 yMgO-(100-y)Al 2 O 3 상에 니켈-세륨 복합체, 니켈-코발트 복합체 또는 니켈-세륨-코발트 복합체를 담지시켜 제조된 것으로, 상기 개질 촉매의 존재 및 일정 반응 조건하에서 천연가스에 대한 수증기-이산화탄소 복합개질 반응을 수행함으로써, 니켈만을 단독으로 담지한 기존의 개질 촉매에 비해 코크(탄소) 침적에 대한 저항성, 촉매 안정성 및 촉매 활성을 향상시킬 수 있다. 또한, 본 발명의 합성가스 제조 방법에 의해 제조된 합성가스는 수소 대 일산화탄소의 몰비를 조절함으로써, 피셔-트롭쉬(Fischer-Tropsch) 공정 또는 메탄올 합성 공정에 적용할 수 있다.
Abstract:
본 발명은 열교환 장치를 내장한 일산화탄소 선택적 산화반응기 및 연료 개질 시스템에 관한 것으로, 일산화탄소의 선택적 산화반응이 일어나고, 가스의 유입구와 배출구를 갖는 반응기 본체; 반응기 본체의 내부에 설치되고, 냉각매체의 유입구와 배출구를 갖는 열교환부; 및 열교환부를 둘러싸도록 반응기 본체의 내부에 충진되는 다수의 일산화탄소 선택적 산화반응용 촉매로 이루어진 촉매층을 포함하는 일산화탄소 선택적 산화반응기를 제공하며, 또한 상기 선택적 산화반응기를 포함하는 연료 개질 시스템을 제공한다.
Abstract:
The present invention relates to a catalyst forming apparatus using a screw extruder. The present invention comprises: a screw extruder which makes the catalysts of a powder state into the catalyst of a dough state and then extrudes them; and a cutter which cuts the catalysts extruded in the screw extruder into a certain length and shape. The cutter comprises a pair of cutting drums which are rotatably arranged, and successively performs cutting while the catalysts pass between the cutting drums. The present invention enables the catalysts extruded in the screw extruder to be formed into the catalysts of a certain shape while directly passing through the cutter, thereby conveniently forming the catalysts into a pellet shape or a sphere shape.
Abstract:
PURPOSE: A fuel reformer is provided to enhance mixing characteristic of raw materials and to uniformly supply raw materials to a catalyst layer by uniformly distributing the mixed raw materials in the columnar direction. CONSTITUTION: A fuel reformer comprises a first cylindrical body (10), a second cylindrical body (20), a third cylindrical body (30), a steam reforming reaction part, and a raw material introduction portion. The first, second and third cylindrical body are concentrically arranges and the diameters are gradually enlarged. The first cylindrical body forms a combustion chamber. The steam reforming reaction part is formed in an intervening space between the second and third cylindrical bodies, and a reaction in which hydrocarbon is reformed to hydrogen by reacting with steam. The raw material introduction portion is connected from the side of the third cylindrical body to the third cylindrical body in the tangential direction. The raw material mixture which includes hydrocarbon is introduced to the raw material introduction portion.
Abstract:
PURPOSE: A multi-tube cylindrical steam reformer is provided to be able to reduce the diameter of the central line on which reaction tubes are arranged compared to a top-down burner, and therefore, to be able to design a compact furnace. CONSTITUTION: A multi-tube cylindrical steam reformer comprises a furnace (10); multiple reaction tubes (50) installed within the furnace, in which a reformation reaction that source natural gas and water vapor are transformed into modified gas including hydrogen; a central burner (20) which is installed in the center of the furnace, and heats reaction tubes by combusting the source natural gas while generating exhaust gas; and at least one side burner (30,40) which is installed on the side of the furnace, and heats reaction tubes by combusting the source natural gas while generating exhaust gas.
Abstract:
PURPOSE: A CO shift reactor with a steam generating part and a method for controlling an outlet temperature of the CO shift reactor are provided to contact a cooling medium with the outside of a reactor as a boundary of an external wall. CONSTITUTION: A Co shift reactor includes a steam generating unit(1). The steam generating unit generates stream by heat exchange between combustion flue gas waste heat and supply water. A CO shift reaction unit(2) is installed inside the steam generating unit. Heat exchange between generated heat of the CO shift reactor and high-temperature water stored in the steam generating unit is performed at a lower temperature than the generated heat. A temperature of an outlet is stably controlled by the heat exchange.