• 한국신재생에너지학회:학술대회논문집
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• 2007.11a
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• pp.118-121
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• 2007

수소 스테이션의 수소분리정제를 위한 Compact 형 PSA를 연구하였다. 수소 스테이션의 공정과정 중에서 수소 분리를 위한 PSA 장치는 에너지효율면에서 장점을 가지고 있지만 부피가 커서 많은 부지를 차지하는 단점이 있다. 수소 PSA의 이러한 단점을 줄이기 위하여 하나의 흡착탑 안에 다른 흡착탑을 넣는 Dual bed 형태의 Compact형 수소 PSA공정을 연구하였다. Compact형 수소 PSA는 하나의 bed안에 다른 하나의 bed를 넣음으로써 시스템이 차지하는 부피를 줄이는 한편, inner bed와 outer bed사이의 열교환 효과가 나타나기 때문에 그 효율을 높일 수가 있다. Compact형 Dual bed는 활성탄으로 충진하였고 공급 기체로는 4성분 수소 혼합물 ($H_2/CO/CH_4/CO_2$, 69:2:3:26 vol.%)를 사용하였다. 흡착탑의 동특성을 알아보기 위하여 공급유량 7LPM, 흡착압력 9atm의 조건으로 파괴 실험을 수행하였다. 또한, Compact형 흡착탑의 열교환 효과가 PSA공정에 미치는 영향을 보고자 한 쪽 탑에서 흡착을 할 때, 다른 탑에서 탈착이 일어나는 실험을 하였다. 그리고 P/F ratio에 따라 Compact형 PSA 공정 실험을 하고 Compact형 흡착탑과 같은 부피의 일반 두 탑 PSA 공정을 시뮬레이션 값과 비교함으로써 Compact형 PSA의 성능을 알아 보았다. 그 결과 Dual bed PSA는 작은 부피를 차지하는 장점뿐만 아니라 열적 효과로 인하여 기존의 단일 흡착탑 PSA에 비하여 보다 높은 효율을 나타내면서 우수한 수소 분리 성능을 보여주었다.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.17 no.12
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• pp.723-729
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• 2016

This study compared fin-tube and parallel-flow heat pipes for their sensible heat exchange rate, heat recovery amount, and air-side pressure drop. Tests were done with different refrigerant charging rates of 40-60% vol. and air flow rates of 300-1,400. The sensible heat exchange rate was highest for both types of heat pipes at a working fluid charge of 40% vol. and low flow rate. For the parallel-flow heat pipe, the 60% vol. charge is too high and results in a low sensible heat exchange rate. The reason is that the thicker liquid film of the tube wall deteriorates the heat transfer effect. Hence, the optimal charging rate is 40 to 50% vol. The evaporator heat pipe has a larger air-side pressure drop than the condenser section heat pipe. The reason is considered to be condensation water arising from the evaporator surface. Compared to the fin-tube heat pipe, the parallel-flow heat pipe showed better performance with a working fluid charging rate of 48%, volume of 41%, and an air-side pressure drop about 37%.

• Applied Chemistry for Engineering
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• v.8 no.1
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• pp.67-75
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• 1997

Heterogeneous cation exchange membrane consisting of cation exchange resin particles (diameter of less than $149{\mu}$) which are finely dispersed in a polyethylene matrix, were produced as forms of sheet. The characteristics were measured after treating hot water or saturated sodium chloride. When membranes were treated with hot water or saturated sodium chloride, cation exchange resin particles swell and expand pushing away the polyethylene matrix of membranes. The above treatment results the formation of narrow cavities between a cation exchange resin particles and polyethylene matrix, and the formation of fine micro-cracks on the polyethylene matrix. Thus, we were obtained good physical and electrochemical properties. On the treatment with hot water or saturated sodium chloride, the optimum conditions for good heterogeneous cation exchange membrane were treatment time of 30min and treatment temperature of $90^{\circ}C$.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.35 no.1
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• pp.61-66
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• 2011

The performance of microchannel PCHE (Printed Circuit Heat Exchanger) is superior to that of other existing commercial heat exchangers. Further, it is also more efficient than other heat exchangers. Various microchannels, whose shapes are straight (I), Wavy, Beehive, Surf, I-Wavy, I-Beehive, or I-Surf, are computationally modeled in this study. The counter-flow arrangement is used, and the flow characteristics, heat transfer, and pressure drop in the microchannels under various mass flow rate conditions are investigated. The results for I microchannel is chosen as the benchmarks and is compared with those of newly proposed microchannels. It is found that the surf-shaped microchannel is most efficient in improving the overall performance of a PCHE.

• Proceedings of the Korea Water Resources Association Conference
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• 2023.05a
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• pp.127-127
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• 2023

지표수와 하상 경계층에서 발생하는 흐름 교환은 하천, 호소, 연안, 해안 등 자연계에 존재하는 수환경시스템에서 일반적으로 나타나는 수리학적 특성으로서, 흐름 교환이 발생하는 경계층 아래 하상층 영역을 혼합대(hyporheic zone)라 부른다. 수질오염사고 등에 의해 외부의 오염물질이 하천 내 유입될 경우, 혼합대 흐름에 의해 하상층으로 침투되고 지표수 대비 유속이 느린 하상 내 공극 흐름에 의해 거동함에 따라 이들의 하천 내 체류시간이 증가하게 된다. 따라서, 본 연구에서는 지표수와 하상 흐름을 연계한 수치해석 방법을 적용하여 혼합대가 지표수 내 용질 체류시간에 미치는 영향을 분석하였다. 먼저 연직 2차원 Reynolds 평균 Navier-Stokes(RANS) 방정식과 Darcy 방정식을 연계하여 지표수와 하상 내 흐름을 해석하였다. 지표수 영역은 RANS 방정식을 이용하여 모의하였고, 지표수 흐름해석에서 얻어진 하상의 압력장을 경계조건으로 하여 Darcy 방정식과 함께 하상 내 흐름을 모의하였다. 여기서 하상의 형태는 자연계 하천에서 일반적으로 관찰되는 사련하상(Ripple bed)으로 모사하였다. 이후, 지표수-하상 연계모의를 통해 얻어진 흐름 결과를 바탕으로 지표수-하상 경계층에서 용질거동을 모의하였다. 흐름 모의결과를 과거 실험자료와 비교한 결과, 지표수 영역 내연직흐름 분포를 정확하게 재현하였고, 동시에 혼합대 흐름 구조에 큰 영향을 미치는 지표수-하상 경계층 압력 분포 역시 관측값과 유사하게 나타났다. 용질거동 해석을 통해 얻어진 용질의 체류시간을 분석한 결과, 혼합대 흐름이 고려된 경우(투수성 하상)와 고려되지 않은 경우(불투수성 하상)를 비교했을 때 전자에서 체류시간 분포의 감수곡선이 길어지고 첨두농도가 감소하는 것으로 나타났다. 아울러, 지표수 영역의 유입부 경계의 평균 유속이 증가함에 따라 최대 체류시간이 감소하는 것으로 나타났는데, 이는 지표수-하상 경계층에서의 압력 경사가 커져 혼합대 내 유속이 증가함에 기인하는 것으로 분석되었다.

• Journal of the Korean Society of Marine Environment & Safety
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• v.15 no.1
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• pp.63-69
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• 2009

Gas volumetric fractions and pressure loss are very important parameters in understanding and predicting gas-liquid two-phase flows. They are also essential to design large heat exchanging system in many industries, boiler and refrigerating systems mounted at ships. This paper therefore presents a theoretical method of predicting the pressure loss and gas volumetric fractions in gas-liquid two-phase flows for the whole range of pipe inclinations. The theoretical analysis is based on the two-fluid stratified flow model. It also provides the results of the comparisons between this theoretical analysis results and previous experimental results.

• Journal of Energy Engineering
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• v.7 no.1
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• pp.44-56
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• 1998

Separate heat pipe exchanger is considered as the high thermal transportation equipment, because evaporator and condenser are separately positioned in the long distance. Its characteristics are that the working fluid is circulated naturally by the position height of two exchangers. But the operating characteristics are restricted by the temperature of hot and cold fluid, flow pattern and diameter of vapor line, etc. in this study, the vapor pressure and the minimum height of two exchangers are studied about the factors restricting the operating characteristics.

• Transactions of the Korean Society of Mechanical Engineers
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• v.14 no.1
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• pp.179-188
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• 1990

The characteristic of volumetric efficiency considering gas exchange process in a reciprocating engine is presented in this paper. The characteristic method is used for solving gas exchange problems of engine system in theoretical studies. The validity of the simulation is investigated by a comparison with the results obtained by the experiment which have been performed on the practical 4-cycle, 4-cylinder gasoline engine. The relationship between the volumetric efficiency and the intake pressure variation according to configuration of intake pipe, position of branch point, valve timing, compression ratio is clarified through simulation and experiment. The results predicted by the simulation are found to be in approximate agreement with those obtained by the experiment.

• The Journal of the Petrological Society of Korea
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• v.3 no.3
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• pp.185-195
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• 1994

An experimental study of iron-aluminium partitioning between synthetic garnet and synthetic epidote was carried out, as equilibrium was maintained in the exchange reaction expressed as follows : $Ca_3Fe_2Si_3O_12\+\2\Ca_2Al_2AlSi_3O_12$(0H) = $Ca_3Al_2Si_3O_12\+\Ca_2Al_2FeSi_3O_12$(0H) Temperature has a pronounced effect on the distribution of Fe and A1 between the minerals. However, the pressure effect is not so drastic as in the exchange reaction. With increasing temperature, $Fe^{+3}$ becomes redistributed from garnet into epidote, whereas A1 becomes redistributed from epidote into garnet. This is in line with the general principle of phase correspondence, as the temperature increases the more electropositive metal aluminium redistributes from epidote into garnet. The agreement between the experimental results of this study and the natural samples suggests that $K_D=X^{Ep}_{Fe}/X^{Gr}_{Fe}$ may be a useful geothermometer for metamorphic rocks containing garnet and epidote that are close to binary Fe-A1 compounds.

• Journal of Energy Engineering
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• v.10 no.4
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• pp.357-362
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• 2001

A bench type ammonia-water absorber heat exchange cycle was tested by varying the system charging concentration, refrigerating valve opening and weak solution flow rate. It was observed that the cooling capacity was increased as the system charging concentration was increased. Optimum system charging concentration was found for the coolong capacity of the system. The opening rate of refrigerant expansion valve had a direct influence on the refrigerant sub-cooling at the condenser outlet. Optimum sub-cooling was found to be 0~4$^{\circ}C$. As the weak solution flow rate increased the concentration of strong solution and the evaporating pressure decreased. There existed a optimum weak solution flow rate which maximized the cooling capacity and COP.