Abstract:
The present invention relates to a redox flow battery, and more particularly, provides a redox flow battery including: a stack in which positive electrode cells, separators, and negative electrode cells are repeatedly stacked from bipolar plates, and a bipolar plate, a collector, and an end plate are sequentially disposed on an outer side of each of the outermost positive electrode cell and the outermost negative electrode cell; a positive electrode electrolyte tank that stores positive electrode electrolyte to be supplied to the positive electrode cells; and a negative electrode electrolyte tank that stores negative electrode electrolyte to be supplied to the negative electrode cells. The positive and negative electrode electrolyte tanks include: an outflow pipe arrangement for transferring electrolyte to the stack; an inflow pipe arrangement for receiving the electrolyte from the stack; and an electrolyte injection hole for injecting electrolyte, introduced into the positive and negative electrode electrolyte tanks, to the inside of the redox flow battery. Thus, electrolyte after redox is uniformly injected into an electrolyte tank is thus efficiently mixed with electrolyte remaining the electrolyte tank and is then returned to a stack, to prevent charging capacity and energy efficiency from being reduced by overvoltage, thereby improving a battery performance.
Abstract:
본 발명은 카바이드 유도 탄소 기반 음극 활물질 제조방법에 관한 것으로, 카바이드 유도 탄소를 제조하는 단계; 및 상기 카바이드 유도 탄소의 기공을 확장하는 단계를 포함한다. 이때, 기공을 확장하는 단계는 제조된 카바이드 유도 탄소를 공기 중에서 가열하는 활성화 공정으로 수행되는 것이 좋다. 본 발명은, 제조 단계에서 활성화 공정을 부가함으로써, 카바이드 유도 탄소 내에 형성된 기공을 확장할 수 있는 효과가 있다. 또한, 기공이 확장된 카바이드 유도 탄소를 음극활물질로 적용함으로써 충방전 효율이 향상된 리튬 이차전지를 제조할 수 있는 효과가 있다.
Abstract:
The present invention relates to a light oil recycling apparatus and a synthetic fuel manufacturing system including same in which light oil that is generated in a slurry bubble column reactor (SBCR) is recycled for stable supply to a reactor and is supplied while the flow rate of the light oil is controlled with precision. The synthetic fuel manufacturing system according to the present invention includes the slurry bubble column reactor and the light oil recycling apparatus. The slurry bubble column reactor generates a hydrocarbon compound through a Fischer-Tropsch synthesis reaction. The light oil recycling apparatus separates the light oil from a gas product that is discharged from the slurry bubble column reactor and evaporates the separated light oil for supply to the slurry bubble column reactor along with synthesis gas.
Abstract:
The present invention relates to a redox flow battery and an operating method, and according to the present invention, a catholyte tank and an anolyte tank are located higher than the position on which a stack is placed; a part of an electrolyte inside the stack is collected to be stored in an electrolyte tank, thereby preventing a countercurrent and self-discharge of the electrolyte during non-operation; and especially, nitrogen is flowed into the redox flow battery to prevent a drying phenomenon of a separation membrane induced by electrolyte insufficiency, thereby obtaining the effect of preventing a decrease in durability of the redox flow battery.
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 stack structure of an electrochemical flow cell and a redox flow battery including the same and, more specifically, to a a stack structure of an electrochemical flow cell and a redox flow battery including a frame which includes an instrument for both connecting and disconnecting and a manifold complex built up with a plurality of manifold unit modules which includes a felt electrode ensconced on the frame. Since adjusting the surface area of voltage and current according to the number of manifold unit module is possible, a user is able to secure the power output desired for the specifications and individual split and merge is easy so that a simple modification or replacement of partial unit modules is possible.
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.
Abstract:
PURPOSE: A method for preparing iron-cobalt composite catalyst and a method for implementing water-gas shift reaction activity in Fischer-Tropsch synthesis and producing highly selective liquid fuel using the same are provided to enhance the yield of liquid. CONSTITUTION: A method for preparing iron-cobalt composite catalyst comprises: a step of supporting 5-20 parts by weight of cobalt with respect to 100 parts by weight of an iron catalyst(S140); and drying the supported iron-cobalt at 100-150 deg.C. for 3-5 hours(S150). The method further comprises a step of plasticizing the iron-cobalt; and a step of reducing the iron-cobalt under a hydrogen atmosphere. [Reference numerals] (AA) Start; (BB) End; (S100) Precipitating iron(Fe), copper(Cu), and Na_2CO_3; (S110) Washing for removing sodium elements from precipitate; (S120) Mixing an SiO_2 solution and a K_2CO_3 solution with the precipitate; (S130) Spray-drying; (S140) Supporting the predetermined amount of cobalt; (S150) Drying the supported iron-cobalt