• 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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• 제22권2호
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• pp.27-35
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• 2017

This paper reviews the previous industrial solid bed process simulations to provide a better understanding of the modeling approaches to the particle reactions in the bed. Previous modeling studies on waste incinerator, iron ore sintering bed, blast furnace, iron ore pellet indurator, and biomass combustor can be seen on the common ground of unsteady 1-D modeling scheme. Approaches to the particle reaction modeling have been discussed in terms of the status of solid particles in the bed, types of reaction progression in a particle, and the consideration of the intra-particle temperature gradient.

• 에너지공학
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• 제21권1호
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• pp.43-46
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• 2012

A fluidized bed drying approach was utilized to the synthesis of water glass based silica aerogel powders. The effects of the fluidized bed drying conditions such as the superficial velocity and temperature of hot air and bead size as well as bead/wet-gel ratio, on the physical properties such as tapping density and productivity of the aerogel powders were systematically investigated. The experimental results showed that the amount of beads mixed with wet-gels in the fluidized bed column has the most profound impact on the fluidization efficiency, greatly enhancing the yield of the aerogel powders up to 98% with a proper bead/wet-gel weight ratio as compared to 72% without using beads. No significant change was observed in the tapping density over a wide range of the fluidized drying condition. Consequently the fluidized bed drying approach shows a good promise as an alternative route for the large-scale production of the aerogel powders.

• 한국연소학회:학술대회논문집
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• 한국연소학회 1998년도 제17회 KOSCI SYMPOSIUM 논문집
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• pp.1-8
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• 1998

Waste combustion above a grate is the core process of incineration systems, stability of which should be guaranteed for emission minimization. However, complicated reactions and heat and mass transfer phenomena make understanding the process difficult. One dimensional bed combustor with a numerical combustion model is utilized to investigate the combustion process of the bed, using cubic wood particles as a simulated fuel. Bed combustion behavior is characterized with apparent flame propagation speed, which has close relationship with air supply rate and chemical and physical characteristics of the fuel. Base on the availability of oxygen, two distinct reaction zone is identified; the oxygen-limited and the reaction-limited zone leading to the extinction by excessive convection cooling. The numerical modeling shows good agreement with the experimental results. The transient bed combustion behavior of local temperature and oxygen consumption rate is adequately reproduced. The numerical model is extended to model the waste bed combustion of a commercial incineration plant, which shows meaningful results as well.

• 한국수소및신에너지학회논문집
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• 제25권4호
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• pp.355-363
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• 2014

Thermal shock or overheating of WGS catalyst for SEWGS system during hydrogen pre-treatment can cause reactivity decay of the catalyst. To select appropriate pre-treatment condition, temperature profiles of catalyst bed (or outside fluidized particle bed of bed insert) during pre-treatment were measured and then CO conversions of those catalysts during WGS reaction were also measured and compared. Drastic overheating of catalyst took place when we reduce catalyst at fixed bed condition and these catalysts showed low CO conversion during WGS reaction. On the contrary, there was no overheating of catalyst at fluidized bed condition not only physical mixing case but also bed insert case. Spring type bed insert showed acceptable CO conversion even at low WGS content. Consequently, feasibility of high CO conversion without decay of reactivity of catalyst and holding the WGS catalyst inside the SEWGS reactor as tablet shape were confirmed using spring type bed insert.

• 청정기술
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• 제25권2호
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• pp.161-167
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• 2019

바이오매스의 급속열분해를 위하여 지난 수십 년간 다양한 형태의 반응기가 개발되었다. 급속열분해 공정의 반응기는 유동층 반응기가 많이 사용되어 왔으며, 최근에는 분사층 반응기를 이용한 바이오매스의 급속열분해 특성에 대한 연구가 다수의 연구자들에 의해 수행되고 있다. 분사층 반응기의 유동화 특성은 입자의 물리적 특성, 유체 제트의 속도, core와 annulus의 구조에 영향을 받으며, 반응기의 기하학적 구조는 분사층 내부의 core와 annulus 구조를 결정하는 주요 인자이다. 따라서 분사층 반응기의 최적설계를 위해서는 열분해 반응에 영향을 주는 인자에 대한 바이오매스의 급속열분해 특성에 대한 연구가 수행되어야 한다. 하지만 분사층 반응기의 기하학적 구조에 의한 바이오매스의 급속열분해 특성은 자세히 연구되지 않았다. 본 연구에서는 분사층 반응기의 원뿔각과 반응 온도 변화에 따른 Jatropha curcas L. seed shell cake의 급속열분해 실험을 수행하여 분사층 반응기의 최적 형상과 반응 온도를 도출하였다. 실험결과, 열분해 오일의 에너지 수율은 반응 온도 $450^{\circ}C$, 분사층 반응기의 원뿔각 $44^{\circ}$에서 63.9%로 가장 높게 나타났다. 그리고 분사층 반응기 내 고체입자의 열전달과 기체상 열분해 생성물의 체류시간은 원뿔각의 영향을 받아 열분해 생성물의 수율 및 열분해 오일의 품질에 영향을 주는 것으로 나타났다.

• Elastomers and Composites
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• 제52권3호
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• pp.216-223
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• 2017

The additive manufacturing technology, also called 3D printing, is growing fast. There are several methods for 3D printing. Fused deposition modeling (FDM) type 3D printing is the most popular method because it is simple and inexpensive. Moreover, it can be used for printing various thermoplastic materials. However, it contains the cooling of layered road and causes thermal shrinkage. Thermal shrinkage should be controlled to obtain high-quality products. In this study, temperature distribution and cooling behavior of a layered road with cooling are studied through computer simulation. The thermal shrinkage of the layered road was simulated using the calculated temperature distribution with time. Shape variation of the layered road was predicted as cooling proceeded. Stress between the bed and the layered road was also predicted.This stress was considered as the detaching stress of the layered road from the bed. The simulations were performed for various thermal conductivities and temperatures of the layered road, bed temperature, and chamber temperature of a 3D printer. The simulation results provide detailed information about the layered road for FDM type 3D printing under operational conditions.

• 한국응용과학기술학회지
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• 제21권3호
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• pp.225-230
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• 2004

Synthesis gas is a high valued compound as a basic chemicals at various chemical processes. Synthesis gas is mainly produced commercially by a steam reforming process. However, the process is highly endothermic so that the process is very energy-consuming process. Thus, this study was carried out to produce synthesis gas by the partial oxidation of methane to decrease the energy cost. The effects of reaction temperature and flow rate of reactants on the methane conversion, product selectivity, product ratio, and carbon deposition were investigated with 13wt% Ni/MgO catalyst in a fluidized bed reactor. With the fluidized bed reactor, $CH_4$ conversion was 91%, and Hz and CO selectivities were both 98% at 850$^{\circ}C$ and total flow rate of 100 mL/min. These values were higher than those of fixed bed reactor. From this result, we found that with the use of the fluidized bed reactor it was possible to avoid the disadvantage of fixed bed reactor (explosion) and increase the productivity of synthesis gas.

• 한국화재소방학회논문지
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• 제28권6호
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• pp.22-27
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• 2014

본 연구에서는 Fuel bed를 이용한 실험을 통하여 지표화 확산에 의한 온도 분포, 화염 높이, 복사열, 확산속도 등을 측정하였다. 실험 변수로는 수종, 풍속 및 경사도 등을 사용하였다. 수종으로는 침엽수종인 소나무 낙엽과 활엽수종인 굴참나무 낙엽을 사용하였다. 풍속은 터널식 방 구조에서 간이풍속 장치를 이용하여 1 m/s, 3 m/s, 5 m/s 풍속을 조절하여 실험하였다. 경사도는 Fuel bed의 기울기를 $0^{\circ}$, $10^{\circ}$, $20^{\circ}$, $30^{\circ}$로 변화시켜 가며 조절하였다. 온도 분포 및 확산속도를 측정하기 위하여 K-type 1.6 mm 열전대를 35개를 격자모양으로 배치하였다. 측정을 위하여 복사열량계를 사용하였으며 이외에도 비디오 카메라 및 열화상 카메라를 사용하였다.

• 생명과학회지
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• 제21권1호
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• pp.127-133
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• 2011

${\beta}$-galactosidase를 공유결합으로 키토산 담체에 고정화하여 고정화 효소의 특성을 조사하였다. 또한 충진층 반응기에서 연속 조업을 실시하여 공정 최적화를 실시하였다. 키토산 담체에 대한 효소 고정화 효율은 최대 75%을 나타내었다. 고정화 효소에 대한 최적의 pH는 7.0이었고 최적의 온도는 $50^{\circ}C$였다. pH와 온도의 실험 범위에서 고정화 효소가 자유 효소에 비해 넓은 분포를 보여 pH와 온도에 덜 민감하게 작용하였다. 충진층 반응기에서 고정화 효소의 운전에 대한 수학적 모델을 세우고 수치적으로 해를 구하였다. 투입되는 유당의 농도와 유량에 대해서 충진층 반응기의 출구에서 유당의 전환율을 측정하였다. 실험 결과를 경쟁적 저해 효소 반응식과 물질전달 저항을 고려한 수학적 모델의 결과와 비교하였다. 모델의 결과는 실험 결과를 5% 이내의 오차로 잘 예측하였다. 그리고 충진층 반응기의 길이에 따른 유당 전환율과 연속운전 시간에 따른 효소의 비활성화를 고려한 전환율을 모델로부터 예측하였다.