• Journal of the Korean Wood Science and Technology
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• 제17권2호
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• pp.13-19
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• 1989

Two different quartz types of gasification reactor were used for pyrolysis and gasification of sawdust, ricestraw, ricehusk and municipal wastes which contain only cellulosics., operating at 1 atmospheric and vacuum pressure respectively. Also a stainless steel autoclave gasification reactor was used which is possible to use up to 100 atmospheric pressures and $800^{\circ}C$ of reaction temperature to complete pyrolysis and gasification reaction. The catalysts used in this reaction w- ere $K_2CO_3$, $Na_2CO_3$, Ni and Ni-$K_2CO_3$ as CO-Catalyst. The product gas mixtures were identified to be CO, $CO_2$, $C_3H_3$, $CH_4$ and $CH_3CHO$ etc. by Gas Chromatography and Mass Spectrometry. The pressurized gasification reaction shows significant increase in terms of methane composition and yield of product gases, comparing with those from unpressurized gasification reactions. The total volume of product gas mixtures amounts to 1600-1800ml per1gof waste of waste lignocellulosics or municipal waste, and the metane content of the gas mixtures reached to 40%, when $800^{\circ}C$ of reaction temperature and 100 atmospheric pressures with Ni-$K_2CO_3$ as CO-catalyst in the pressurized gasification reaction were used. This results show that the product gas mixtures containing 40% of methane call be used for alternative enegy source.

• 대한기계학회논문집B
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• 제38권9호
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• pp.781-787
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• 2014

PWMR(Pressurized wire mesh heating reactor)는 Intrinsic $CO_2$ 가스화 반응속도 해석에 필요한 활성화에너지와 빈도상수를 도줄하기 위해서 고안되었으며, 고압 및 고온(50atm, 1750K)조건 하에서 실험을 수행하였다. 본 연구에서는 고온조건에서의 실험을 위해 백금(Pt) 메쉬를 가열체로 사용하였고 직류전원공급기를 통해 백금메쉬로 전류를 인가하여 석탄 입자를 가열시킨다. 가열시 정확한 온도제어 및 반응시간 조절을 위해 직류전원공급기는 컴퓨터로 제어된다. 본 연구에서는, 인도네시아 아역청탄인 BERAU 를 사용하였으며 입자크기는 $90-150{\mu}m$, 압력과 온도조건은 각각 1-40atm 및 1373-1673K에서 실험을 진행하였다. 고압에서의 압력의 영향을 구분하기 위해 Internal/external effectiveness factor를 고려하였다. 최종적으로 BERAU 촤의 Intrinsic 가스화 반응속도론 을 $n^{th}$ order 반응식을 통해 도출하였으며 그 값은 203.8kJ/mol 의 값을 가졌다.

• 한국군사과학기술학회지
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• 제20권4호
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• pp.528-535
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• 2017

Fuel cells have been spotlighted in the world for being highly efficient and environmentally friendly. A hydrogen which is the fuel of fuel cell can be obtained from a number of sources. Hydrogen source for operating the polymer electrolyte membrane fuel cell(PEMFC) in the current underwater environment, such as a submarine and unmanned underwater vehicles are currently from the metal hydride cylinder. However, metal hydride has many limitations for using hydrogen carrier, such as large volume, long charging time, limited storage capacity. To solve these problems, we suggest diesel reformer for hydrogen supply source. Diesel fuel has many advantages, such as high hydrogen storage density, easy to transport and also well-infra structure. However, conventional diesel reforming system for PEMFC requires a large volume and complex CO removal system for lowering the CO level to less than 10 ppm. In addition, because the preferential oxidation(PROX) reaction is the strong exothermic reaction, cooling load is required. By changing this PROX reactor to hydrogen separation membrane, the problem from PROX reactor can be solved. This is because hydrogen separation membranes are small and permeable to pure hydrogen. In this study, we conducted the pressurized diesel reforming and water-gas shift reaction experiment for the hydrogen separation membrane application. Then, the hydrogen permeation experiments were performed using a Pd alloy membrane for the reformate gas.

• 한국환경과학회지
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• 제13권3호
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• pp.319-325
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• 2004

An experimental study on the preparation of monolithic porous polymers by environmentally friend process in supercritical carbon dioxide has been carried out. Polymerization mixture composed of a cross-linking monomer, initiator and functional co-polymer was charged in the reactor with sapphire window. After the system was purged with a flow of $CO_2$ for 15 min, the reactor was pressurized with liquid $CO_2$ up to 100 bars. The reactor was isolated from and placed back to the system via quick connector for shaking until the mixture had become fully homogeneous. The reactor was then heated and pressurized to the required reaction conditions and left overnight. After cooling and $CO_2$ evacuation, the polymer was removed from the reactor as dry, white, continuous monoliths. The effect of experimental conditions on the physical properties of porous polymer was systematically examined, and it was found that monomer content had a major effect on the physical properties of the polymers.

• 한국원자력학회:학술대회논문집
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• 한국원자력학회 1996년도 춘계학술발표회논문집(1)
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• pp.179-184
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• 1996

Power density distribution and criticality of a pressurized water reactor are calculated with a Monte Carlo calculation using the MCNP code. The MCNP model is based on one-eighth core symmetry. Individual fuel assemblies are modeled with fullscope three dimensional description except grid spacer. The fuel rod is divided into eight axial segments. Core internals above and below the active fuel region is represented as coolant. After 400 cycle calculations, the system converges to a k value of 1.09151$\pm$0.00066. Fission reaction rate in each rod is also calculated to use as the source term in pressure vessel fluence calculation.

• 한국지열·수열에너지학회논문집
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• 제18권4호
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• pp.12-21
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• 2022

Steam assisted gravity drainage(SAGD) is a process that drills well in the underground oil sands layer, injects hightemperature steam, lowers the viscosity of buried bitumen, and recovers it to the ground. Recently, direct contact steam generator(DCSG) is being developed to maximize steam efficiency for SAGD process. The DCSG requires high technology to achieve pressurized combustion and steam generation in accordance with underground pressurized conditions. Therefore, it is necessary to develop a combustion technology that can control the heat load and exhaust gas composition. In this study, process analysis of high-pressurized DCSG was conducted to apply oxygen enrichment technology in which nitrogen of the air was partially removed for increasing steam production and reducing fuel consumption. As the process analysis conditions, methane as the fuel and normal air or oxygen enriched air as the oxidizing agent were applied to high-pressurized DCSG process model. A simple combustion reaction program was used to calculate the property variations for combustion temperature, steam ratio and residual heat in exhaust gas. As a major results, the steam production efficiency of DCSG using the pure oxygen was about 6% higher than that of the normal air due to the reducing nitrogen in the air. The results of this study will be used as operating data to test the demonstration device.

• 한국전산유체공학회:학술대회논문집
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• 한국전산유체공학회 1998년도 추계 학술대회논문집
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• pp.211-219
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• 1998

Propellants pressurized and fed into the combustion chamber undergoes the mechanical, chemical combustion processes. Along with their distinctive physical characteristics, propellant combustion is typically divided into the processes; injection, atomization, mixing, vaporization and chemical reaction. These processes assumed to happen in a serial manner are strongly coupled, thereby involves formidable physical complexities. In this study a numerical experiment is attempted to simulate the burning sprays due to OFO, FOF triplet / FOOF split doublet injectors. Based on Eulerian-Lagrangian frame, Navier-Stokes equation system for compressible flows is preconditioned with low Reynolds number $k-{\varepsilon}$ turbulent model and time-integrated by LU-SGS, and the sprays are described by DSF model with the characteristics initialized by experimentally determined spray characteristics. Simplified single global reaction model approximates heptane-air reaction. It was observed that FOOF split doublet injector shows better atmization with shortest residence and the FOF triplet injector produces better combustion performance.

• 한국에너지공학회:학술대회논문집
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• 한국에너지공학회 2002년도 춘계 학술발표회 논문집
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• pp.173-177
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• 2002

두 개의 유동층 사이를 순환하는 금속매체(Metal or Metal oxide)를 이용하여 공기에 의한 금속매체의 산화와 기체연료(H$_2$, CO, CH$_4$등)에 의한 금속산화물의 환원반응이 별개의 반응기에서 일어나게 하는 새로운 개념의 연소기술인 매체순환식 가스연소기술은 공기와 기체연료를 직접 접촉시켜 반응하는 기존의 가스연소기에 비해 많은 장점을 가지고 있다.(중략)

• 한국수소및신에너지학회논문집
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• 제27권1호
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• pp.13-21
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• 2016

The Sulfur-Iodine thermochemical hydrogen production process (SI process) consists of the Bunsen reaction section, the $H_2SO_4$ decomposition section, and the HI decomposition section. The $HI_x$ solution ($I_2-HI-H_2O$) could be recycled to Bunsen reaction section from the HI decomposition section in the operation of the integrated SI process. The phase separation characteristic of the Bunsen reaction using the $HI_x$ solution was similar to that of $I_2-H_2O-SO_2$ system. On the other hands, the amount of produced $H_2SO_4$ phase was small. To investigate the effects of $SO_2$ solubility on Bunsen reaction, the continuous Bunsen reaction was performed at variation of the amounts of $SO_2$ gas. Also, it was carried out to make sure of the effects of partial pressure of $SO_2$ in the condition of 3bar of $SO_2-O_2$ atmosphere. As the results, the characteristic of Bunsen reaction was improved with increasing the amounts and solubility of $SO_2$ gas. The concentration of Bunsen products was changed by reverse Bunsen reaction and evaporation of HI after 12 h.

• 청정기술
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• 제27권1호
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• pp.93-103
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• 2021

기후변화 대응과 탄소배출 저감에 대한 심각성 및 필요성이 중요시 되면서 세계 각국은 온실가스를 감축하고자 하는 노력을 지속하고 있다. 다양한 노력들 중 탄소기반 연료 사용 시 발생되는 이산화탄소를 포집하여 활용하는 CCUS에 대한 연구가 활발히 진행되고 있으며, 이러한 관점에서 CCUS와 함께 활용될 수 있는 가압 순산소 연소에 대한 연구도 여러 연구자들에 의해 진행되고 있다. 본 연구는 가압 순산소 연소의 화염 구조와 오염물질 배출과 관련된 기초적인 정보를 분석하는데 목적이 있다. 이를 위해 대향류 확산 화염 모델을 이용하여 압력 및 산소분율에 따른 연소의 특성을 분석한 결과, 압력이 높을수록 화학 반응의 활성화로 인한 반응율의 증가로 연소 온도가 증가하고 화염두께는 감소한 반면, 산소분율이 높을수록 반응율 증가 및 산화제 운동량 변화에 따른 확산의 영향으로 연소 온도 및 화염두께 모두 증가하였다. 이와 관련된 열방출 반응을 3가지 구간으로 구분하여 분석한 결과, 특히 산소분율이 증가할수록 산화제 측면에서 나타나는 화학 반응이 혼합분율에 따라 크게 두 개의 영역으로 세분화되는 특성이 나타났다. 또한, NO의 생성 메커니즘에 따라 구분된 배출지수(EINO)를 분석하였고, 각 해석 조건에 따른 NO의 생성 경향을 제시하였다.