• Korean Chemical Engineering Research
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• 제54권4호
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• pp.527-532
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• 2016

감압상태(1torr)의 순환유동층 플라즈마 반응기(내경 10 mm, 높이 800 mm)에서 기상 유속과 고체순환속도가 축방향 고체체류량 분포에 미치는 영향을 연구하였다. 폴리스타이렌 고분자 입자와 질소가스를 고체 및 기상 물질로 각각 사용하였다. 감압상태 순환유동층의 고체 순환량 변화는 상승관의 많은 기체 유량(40~80 sccm)에 의한 변화만큼 고체재순환부의 작은 유량 변화(6.6~9.9 sccm)에 의해서도 가능하였다. 감압상태 순환유동층의 고체 순환속도는 재순환부 기체 유속에 따라 증가하였다. 상승관내의 축방향 고체 체류량 분포는 하부의 농후상 영역에서 상부의 희박상 영역까지 높이에 따라 감소하는 형태를 나타내었다. 상승관 내 각 높이에서 고체순환속도의 증가에 따라 직선적으로 고체 체류량이 증가하였다. 이로써 플라즈마 형성과 유지 그리고 플라즈마 반응을 위해 적절한 플라즈마 로드 위치를 결정할 수 있다.

• 한국세라믹학회지
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• 제43권6호
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• pp.376-382
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• 2006

In the $Al(OH)_3-SiO_2-AlF_3$ system, leaf-shaped fluorotopaz was first formed at $800^{\circ}C$ and mullite whisker was formed at $1,100^{\circ}C$. The mass transportation of Al and Si as gas phase, the fast reaction and growth, and the absence of liquid phase existence in mullite whisker showed that the formation and growth of mullite was from the solid-vapor reaction.

• Journal of Electrochemical Science and Technology
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• 제10권3호
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• pp.294-301
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• 2019

The quasi-solid-state hybrid electrolytes were synthesized by chemical cross-linking reaction of methacrylate-functionalized $SiO_2$ ($MA-SiO_2$) and tetra (ethylene glycol) diacrylate in aqueous electrolyte. A quasi-solid-state electrolyte synthesized by 6 wt.% $MA-SiO_2$ exhibited a high ionic conductivity of $177mS\;cm^{-1}$ at room temperature. The electrochemical $H_2$ sensor assembled with quasi-solid-state electrolyte showed relatively fast response and high sensitivity for hydrogen gas at ambient temperature, and exhibited better durability and stability than the liquid electrolyte-based sensor. The simple construction of the sensor and its sensing characteristics make the quasi-solid-state hydrogen sensor promising for practical application.

• 한국수소및신에너지학회논문집
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• 제27권5호
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• pp.494-502
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• 2016

A 1-dimensional heterogeneous reactor model with the gas-solid interfacial phase gradients was developed for the simulation of the packed bed reactor where the exothermic reversible water gas shift reaction for the natural gas steam reformed gas was proceeding in adiabatic mode. Experimental results obtained over the WGS catalyst, C18-HA, were best simulated when the frequency factor of the reaction rate constant was adjusted to a half the value reported over another WGS catalyst, EX-2248, having the same kinds of active components as the C18-HA. For the reactor of the inside diameter 158.4 mm and the bed length 650 mm, the optimum feeding temperature of the reformed gas was simulated to be $194^{\circ}C$, giving the lowest CO content in the product gas by 1.68 mol% on the basis of dried gas. For reactors more extended in the bed length, the possible lowest CO content in the product gas with the optimum feeding temperature of the reformed gas were suggested.

• 한국연소학회지
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• 제13권2호
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• pp.23-32
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• 2008

Gasification characteristics in the fluidized bed reactor are essential for the design of a gasification furnace to optimize the operation condition. Moisture content of the solid fuel is one of the important factors to influence directly the gasification characteristics. So it is necessary to investigate the effect of moisture content of solid fuel in partial oxidation condition. Gasification characteristics are investigated with results from thermogravimetric analyzer and lab-scale fluidized bed reactor for wood and RDF samples along with changing moisture contents. Additionally lab-scale fluidized bed reactor was run continuously and gas concentrations at the exit were measured. It is observed that the rate of reaction in partial oxidation condition is between the results from the combustion environment and from the inert condition. Moisture content in a particle slows down the heating rate of a particle. So, reaction is delayed by the moisture content. However, RDF samples those are easy to break-up don't show the effect of moisture content. The result of continuous operation condition shows that proper moisture content promotes gasification because steam from the particles helps gasification of the solid fuel. A simulation to predict the syn-gas composition was conducted by the Aspen Plus process simulator. The cold gas efficiency of the experiment was compared with results from the simulation.

• 한국수소및신에너지학회논문집
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• 제35권2호
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• pp.162-167
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• 2024

Fossil fuels have been main energy source to people. However, enormous amount of CO₂ was emitted over the world , resulting in global climate crisis today. Recently, solid oxide electrolyzer cell (SOEC) is getting attention as an effective way for producing H₂, a clean energy resource for the future. Also, SOEC could be applicable to reverse water-gas shift reaction process due to its high-temperature operating condition. Here, SOEC system was utilized for both H₂ production and CO₂ reduction process, allowing product gas composition change by controlling operating conditions.

• Journal of Mechanical Science and Technology
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• 제15권4호
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• pp.473-481
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• 2001

By depicting the transfer of heat and combustion reaction to take place within thin gas layers close to the propellant surface burning in a steady-state fashion, a mathematical equation has been deduced to describe the burning rate of solid propellant as a function of initial grain temperature and chamber pressure. It has been also assumed that chemical reaction could take place in premixing-diffusing zone but were carried out mainly in the reaction-flame zone. All these phenomena taken place in each zone of combustion have been assumed to be steady-state. In the present investigation, the equation, γ=$\kappa$$.$(1/R(T(sub)i+C))(sup)n$.$exp(-E(sub)a/R(T(sub)i+C))(P/z) is being presented and it is compared with experimental data. The proposed model has been tested and evaluated vis-a-vis strand burner data for three different propellants based on CTPB, and it has been found that the deviation of the computed burning rates from the measured rates ranged up to 2%.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2014년도 제49회 KOSCO SYMPOSIUM 초록집
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• pp.135-137
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• 2014

Excess enthalpy flame propagating an porous inert medium, which recirculate exhaust heat to the upstream cold mixture, is theoretically analyzed. Using the activation-energy asymptotics, the flame structure is divided into the thin reaction and the gas-phase preheat zone, as is traditionally done. Ahead and behind of the two, there exist an outer preheat zone, where heat is convectively transferred from solid to gas, and a downstream re-equilibrium zone, where thermal equilibrium between phases is established. Asymptotic solutions of species and energy equations in each zone are obtained and then matched to each other, and finally the mass burning rate is obtained as a function of the flame propagation velocity with respect to the solid phase and physical properties of gas and solid.

• 한국농공학회논문집
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• 제54권3호
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• pp.75-80
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• 2012

Gasification is a therm-chemical conversion process to convert various solid fuels into gaseous fuels under limited supply of oxygen in high temperature environment. Considering current availability of biomass resources in this country, the gasification is more attractive than any other technologies in that the process can accept various combustible solid fuels including plastic wastes. Mixed fuels of biomass and polyethylene pellets were used in gasification experiments in this study in order to assess their potential for synthesis gas production. The results showed that higher reaction temperatures were observed in mixed fuel compared to woodchip experiments. In addition, carbon monoxide, hydrogen, and methane concentrations were increased in the synthesis gas. Heating values of the synthesis gas were also higher than those from woodchip gasification. There are hundred thousand tons of agricultural plastic wastes generated in Korea every year. Co-gasification of biomass and agricultural plastic waste would provide affordable gaseous fuels in rural society.

• 자원리싸이클링
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• 제24권6호
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• pp.3-8
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• 2015

일정 온도에서 중량 변화를 통하여 가스화 반응 특성을 살펴볼 수 있는 열중량 분석기(thermobalance)를 이용하여 하수슬러지의 수증기 가스화 특성 및 발생 가스의 농도 분석을 실시하였다. 반응 온도 및 수증기의 분압이 증가할수록 가스화 반응이 촉진되어 반응 속도가 증가하는 것으로 나타났다. 반응 kinetics 해석은 기체-고체 화학반응의 세 가지 모델이 이용되었다. 이 중 하수슬러지 촤의 수증기 가스화는 modified volumetric reaction model이 반응 kinetics를 가장 잘 나타내었으며, 이 때 activation energy와 빈도 인자는 각각 155.5 kJ/mol, $14,087s^{-1}atm^{-1}$로 분석되었다. 또한, 수증기의 분압에 따른 반응 차수는 0.68이었다. 합성가스의 발생 특성을 살펴보고자 $900^{\circ}C$에서 생성 합성가스를 분석한 결과 수소의 농도가 가장 높았으며 수증기 분압이 증가할수록 생성기체의 농도 특히 수소 농도가 급격히 증가하였다. 가스화와 동시에 수성가스화 변환반응이 진행되어 생성기체의 수소 생성 농도가 일산화탄소에 비하여 2-4배 높은 값을 나타내었다.