• 한국연소학회:학술대회논문집
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• 한국연소학회 1999년도 제19회 KOSCO SYMPOSIUM 논문집
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• pp.155-163
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• 1999

A numerical study for simulating a swirling pulverized coal combustion in axisymmetric geometry is done here by applying the weighted sum of gray gases model (WSGGM) approach with the discrete ordinate method (DOM) to model the radiative heat transfer equation. In the radiative transfer equation, the same polynomial equation and coefficients for weighting factors as those for gas are adopted for the coal/char particles as a function of partial pressure and particle temperature. The Eulerian balance equations for mass, momentum, energy, and species mass fractions are adopted with the standard ${\kappa}-{\varepsilon}$ turbulence model, whereas the Lagrangian approach is used for the particulate phase for soot. The eddydissipation model is employed for the reaction rate for gaseous mixture, and the single-step first-order reaction model for the devolatilization process for coal. By comparing the numerical results with experimental ones, the models used here are confirmed and found to be one of good alternatives for simulating the combustion as well as radiative characteristics.

• Elastomers and Composites
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• 제33권2호
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• pp.103-109
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• 1998

The determination method of successful operation conditions to control the temperature and pressure in autoclave after non-taping vulcanization process was represented. Heat and mass balances were constructed to predict the mass flow rates of air, steam, and condensed water into or from autoclave when the temperature and pressure in the autoclave were to be controlled in the desired profiles. The balance equations were solved by appropriate mathematics, and the solution was applied to an autoclave system where the temperature and pressure were linearly decreased. The resulting solutions were illustrated in graphs.

• 한국기계가공학회지
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• 제11권6호
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• pp.189-194
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• 2012

The purpose of this study is to predict the performance of a cyclone drying machine and air ejector used in drying applications. This paper deals with optimization of the geometry of the ejector for sludge drying using computational fluid dynamics. To facilitate the design of a jet ejector for air drying machines, a numerical model of simultaneous mass and heat transfers between the liquid(sludge) and gas(air) phases in the jet ejector was developed. The steady-state model was based on unidimensional balance equations of mass, energy and momentum for the liquid and gas phases. It was shown that the optimum condition to minimize pressure and momentum loss of air in the ejector was d=220mm. It was found that sludge particles inside the cyclone was smoothly discharged by the conical wedge installed on the bottom of the cyclone.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2194-2199
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• 2007

An experimental study is performed to investigate the thermal and flow characteristics of subcooled liquid nitrogen in a natural circulation loop. Experimental apparatus is designed and constructed such that a closed loop is cooled at the top by a cryocooler and heated nearly at the bottom by cartridge heaters. Steady state is obtained by controlling the heating power to the cartridge heaters and a thin-film heater to reduce the cooling power of the cryocooler. Temperature is measured at several locations of the loop and the mass flow rate through the loop is estimated from the energy balance in terms of the measured temperatures. Experiment is repeated for various values of the vertical height between the cooling and heating parts. The results show that the heat transfer capability of the loop has a maximum at a certain value of height. The optimal height to maximize the heat transfer is in a good agreement with analytical prediction to take into account the buoyancy and viscous forces in the loop.

• 한국연소학회지
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• 제20권2호
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• pp.1-13
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• 2015

Drying, which is the oldest and most energy-intensive process, is an essential process for treatment of solid product. The specific procedure to design and evaluate the dryers, which are a rotary kiln dryer and a flash dryer, in case of drying the high-moisture coal was described. From determination of size to the heat and mass balance in one-dimensional model were conducted to evaluate the performance of dryers. Heat consumption, inlet gas temperature and size of the dryers were compared between a rotary kiln dryer and a flash dryer. Further considerations to evaluate the reactor elaborately were also discussed. Performance simulation of dryers along with the design procedure described here will provide helpful basis for understanding the concept of reactor design.

• 동력기계공학회지
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• 제10권2호
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• pp.36-40
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• 2006

In order to prevent the environmental pollution, the dryers are commonly used to treat sludge that one of sewages is polluting the quality of water. Generally, the drying method is various as to the property of material and use. Rotary dryer is a good apparatus to treat them. It is the way that is to make substance transmission and heat using hot air between sludge particle and heated gas. In this paper, we developed a 3-pass rotary dryer for a design program for the 3-pass rotary dryer with various conditions. The working conditions of dryer are a raw sludge feed rate, input & output water content and operation time etc.

• 열처리공학회지
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• 제14권5호
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• pp.282-285
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• 2001

Based on the mass balance of anion and cation fluxes, the parabolic rate constant ($K_p$) of oxide grown during the high-temperature oxidation of metal is theoretically calculated. It is assumed that the diffusion of oxygen anion and metal cation through oxide scale obeys the Fick's 1st law, the growth of oxide is controlled by the diffusion of ions, electrical potential gradient as driving force for diffusion of ions is ignored, and oxidation occurs within an existing oxide layer. Then, the parabolic rate constant can be expressed by $K_p=[2{\rho}_{MmOn}{M^2}_{MmOn}(mD_oC_o{^e}+nD_MC_M{^e})/nm]$.

• 한국태양에너지학회 논문집
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• 제24권3호
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• pp.39-46
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• 2004

In this paper, thermodynamic design data for heating of double-effect absorption system using LiCl-water for evaporator heating source of sofar energy are investigated for the water-LiCl pair and a comparative study of the water-LiCl pair with the water-LiBr pair is given used for the computer simulation. The computer simulation is based on mass, material and heat balance equations for each part of the system. Coefficients of performance and flow ratios for effects of different operating temperatures are investigated. It is found that the heating COP is higher for the water -LiCl pair than for the water-LiBr pair, and FR is lower for the water-LiCl pair than for the water LiBr pair.

• 한국가스학회지
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• 제5권2호
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• pp.22-29
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• 2001

체적거래제에 의하여 소규모 공동주택에 가스를 공급하기 위하여 적절한 용기설치수의 결정 및 용기교체시기에 대한 검토가 필요하다. 그러나 지금까지 국내에 축적된 자료가 없을 뿐만 아니라 용기 설치수의 결정과 용기수 및 가스사용 형태에 따라 용기교체시 남아 있는 액화석유가스 양에 대한 이론적 검토가 없었다. 따라서 본 연구에서는 자연기화능력, 잔량, 용기의 온도, 용기내부 압력 등을 시뮬레이션으로 살펴보았다. 용기표면으로부터 액화석유가스 용기의 총괄 열전달계수의 변화에 따른 자연기화량 변화는 크지 않으며, 실험으로부터 구한 값은 약 $9{\~}13 kcal/m^2{\cdot}hr{\cdot}^{\circ}C$이었다. 그리고 액화석유가스 용기내부의 압력이 압력조정기의 압력조정 하한계에 도달하였을 때 가스방출 유량은 공기로부터 전달되는 열량과 균형을 이루는 일정한 값으로 급격히 감소하였다. LP가스용기의 자연기화능력은 외기온도 및 프로판의 조성에 따라 증가하였고, 연속사용시간에 따라 초기 급격히 감소하여 일정한 값으로 수렴하였다. 한 가구당 용기수는 자동절체기 사용에 의하여 감소시킬 수 있는 것을 알 수 있다.

• 에너지공학
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• 제14권4호
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• pp.213-218
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• 2005

습공기 유동의 착상조건하에서의 열 및 물질 전달 특성을 이해하기 위해서, 미니 열풍동을 제작하고 열풍동의 시험부인 사각덕트 아랫면에 알루미늄 평판을 설치하고 평판의 중심력에 전기냉각모듈(Peltier device)을 부착하였다. 현미경(해상도 0.05mm)을 이용하여 습공기 유동 방향으로 알미늄 평판위의 7개점의 서리 두께를 측정하였으며, 전자저울(해상도 1mg)을 이용하여 각 운전시간대까지의 발생된 서리의 총괄 질량을 측정하였다. 여러 가지의 실험조건에서 서리두께와 서리질량 그리고 알미늄 평판상의 온도 분포 등을 구하고, 이로부터 습공기 유동의 습도 및 속도가 서리의 성장 특성에 미치는 영향을 분석하였다.