• Prospectives of Industrial Chemistry
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• v.24 no.6
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• pp.3-18
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• 2021

가역적인 표면 젖음성의 제어가 가능한 스마트 표면은 첨단 센서, 기능성 멤브레인 등 여러 산업분야에 적용될 수 있는 계면제어 기술로써 많은 관심을 받을 것으로 기대된다. 표면의 젖음성은 표면의 화학적 구조와 기하학적 입체 구조에 의해 영향을 받는 데, 특히 외부자극에 의해 소재 물성을 가변시킬 수 있는 스마트 고분자 소재를 나노구조가 제어된 표면에 도입함으로써 표면의 젖음성을 초발수에서 초친수로 가역적으로 전환시킬 수 있는 스마트 표면을 효과적으로 구현할 수 있다. 자극 응답성 스마트 소재는 인가하는 외부자극에 따라 물리적 자극(빛, 온도, 전기, 자기)과 화학적 자극(pH, 용매, 이온)으로 구분할 수 있으며, 이를 복합적으로 적용한 이중/다중 유발 자극에 반응하는 소재가 있다. 본 기고문에서는 외부자극에 응답하는 자극응답성 고분자를 나노 구조 표면에 도입하여 초발수에서 초친수로의 가역적인 젖음성 변화가 가능한 고기능성 스마트 표면의 최근 연구 동향과 미래 전망에 대해 소개하고자 한다. 이런 다양한 외부자극을 이용한 표면 특성의 가역적 제어 기술을 통해 물-오일의 분리, 바이오센서, 약물 전달, 소프트로보틱스와 같은 스마트 소재의 잠재적 발전 가능성 또한 엿볼 수 있을 것으로 기대된다.

• Journal of Bio-Environment Control
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• v.10 no.2
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• pp.80-87
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• 2001

This study was conducted to provide basic data for the design of shading facility of greenhouse. The proper distance between external shading screen and roof surface, transmissivity of shading materials, and shading effects of external and internal shadings were analyzed. About a distance of 10 cm between inclined external shading screen and roof surface was enough to guarantee the external shading effect in the greenhouse without roof vent. The inside temperature of greenhouse installed with 85% internal shading screen was lower the maximum of 4$^{\circ}C$ and mean of 2$^{\circ}C$ than that with 55% internal shading screen in both natural ventilation and no ventilation condition. The difference of soil temperature between shading and no shading greenhouse was great, but the difference by shading rate or shading method was small. The performance of external shading for controlling inside temperature down was superior to that of the internal shading. The externally inclined shading screen parallel to the roof surface of greenhouse was more effective than the externally horizontal shading screen in controlling inside temperature of greenhouse without roof vent.

• Resources Recycling
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• v.31 no.3
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• pp.81-87
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• 2022

Energy consumption per unit weight of metal (kwh/kg of metal) is one of the most important economic indicators in the process of molten salt electrolysis. It is related to the heat loss of salt bath and the current efficiency of the process. The current efficiency is highly dependent on electrolysis temperature. On the other hand, the temperature of salt bath may increase significantly due to the difference (larger energy input than consumption) in heat balance at the beginning of electrolysis, which may cause different electrolysis temperature from an initially targeted value. This results in a bad effect on current efficiency. Therefore, it will be helpful to the reduction of energy consumption to compare the calculated and measured values of the temperature change of salt bath through the heat balance review at the early stage of electrolysis and to evaluate the energy loss to outside. In this study, based on the authors' experimental data, the heat balance was reviewed at the beginning of the electrolysis, and it was possible to evaluate the energy loss to the outside and the increase of the temperature of the salt bath quantitatively. Through such a method, heat loss reduction plan can be derived and current efficiency can be improved so that energy consumption can be reduced.

• Journal of Bio-Environment Control
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• v.15 no.4
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• pp.306-316
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• 2006

In this study, the effect of the shade level, water flow rate applied to the shades and the temperature of water on the greenhouse cooling was investigated depending on the shade level of 0, 35, 55, 75%, and water flow rate and water temperature by the test on the small wooden frames to find out the low cost cooling method. With increasing of the dry bulb temperature of outside air, the dry bulb temperature in the wooden frames increased. For the frames with the shade and water, inside temperatures of the frames were lower of -0.2$\sim$-1.2$^{\circ}C$ than the temperature of the outside air and higher than the water temperature. For the frames without water, inside temperatures of the frames were higher of 1.7$\sim$4$^{\circ}C$ than the outside and not affected by the shade level very much. The water flow rate and the temperature of the water were not the important factors to decrease the inside temperatures in the frames. The black globe temperature became lower with increasing of shade level. The shade frames with water curtain showed the best cooling effect because of reducing thermal radiation and cooling the plastic film cover. The surface temperatures of the plastic film cover for the water supplied modules became lower with increasing of the shade level. The relative humidity was decreased with the dry bulb temperature in the frame increasing and not affected by the dry bulb temperature of the outside air for the frames with the shade and water.

• Proceedings of the Materials Research Society of Korea Conference
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• 2011.10a
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• pp.34.1-34.1
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• 2011

태양전지 모듈의 25년 이상 보증을 위해 태양전지 모듈을 구성하는 부품 소재의 장기 열화메카니즘 연구가 중요시되고 있다. 그 중 봉지제(Encapsulation) 부품으로 적용되고 있는 태양전지 모듈용 에틸렌 비닐 아세테이트(Ethylene Vinyl Acetate, EVA)는 셀을 보호하는 폴리머 부품으로 장기 열화특성 연구가 중요하다. 따라서 EVA를 가속열화하여 25년 보증 내구성을 보유하고 있는지 연구가 필요하다. 본 연구에서는 태양전지 모듈을 구성하는 재료 중 외부환경에 민감한 폴리머 소재인 EVA의 Ultraviolet (UV), 온도 두 환경스트레스 조건을 적용한 가속수명시험을 수행하고 장기 열화메카니즘을 분석하였다. 시험에 앞서 UV/온도 가속수명시험을 설계하였다. UV/온도 가속조건을 설정하기 위해 실환경에서 변화하는 UV와 온도를 일정한 값으로 나타낼 수 있는 유효 UV (Effective UV)와 유효 온도(Effective temperature)를 도출하였다. 이를 통해 UV/온도 가속조건을 설정하였고 1년 및 25년 동안 EVA에 인가되는 stress와 동일한 양을 인가할 수 있는 시험시간을 결정하였다.

• Electrical & Electronic Materials
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• v.3 no.3
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• pp.187-194
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• 1990

광자기 메모리용 재료인 비정질 TbFe 박막을 대상으로 열자기 기록시 박막에 분포하는 온도와 이때 만들어지는 bit의 크기간에 상호관련성을 조사하였다. 레이저 조사에 의해 가열된 박막의 온도분포는 유한요소법을 이용한 열전달 해석에 의해 계산하였다. 레이저 가열종료 직전 박막 면에 분포하는 온도 contour로 부터 bit 크기를 예측하였다. 여기서 bit 크기는 온도 상승에 따라 보자력이 약화되어 외부자계와 박막반자장의 합력이 역자구를 만들어 준다고 가정하여 이 경계가 되는 온도(Tcrit)로 이루어지는 등온선의 크기로부터 정하였다. 열자기 기록 실험으로부터 기록 bit의 크기(Dmeas.)을 측정하여 레이저조사조건별로 예측한 bit크기(Dpred.)와 비교하였다. 특히, 레이저 pulse시간 변화에 따른 여러온도의 등온선 contour 직경변화를 조사하여 실측한 bit크기와 비교 검토함으로써 bit형성에 미치는 온도분포의 영향을 조사하였다. 이 결과 레이저 pulse시간이 길어지거나 레이저 power가 상대적으로 작을때 실측한 bit크기가 예측된 bit크기보다 커지는 것으로 나타났으며 이는 Tcrit 온도구배가 완만해질수록 bit경계가 되는 온도가 낮아지는 것으로 해석된다.

• Journal of Energy Engineering
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• v.24 no.2
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• pp.103-109
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• 2015

A heat recovery steam generator consists of inlet expansion duct and heat transfer tube bank modules. For the enhancement of heat transfer in the tube bank modules, the flow should be uniform before the 1st heat transfer tube bank module. The present study has been carried out to analyze the flow characteristics in the inlet expansion duct of a heat recovery steam generator by using numerical flow analysis. The aim of the present study is to establish the proper heat transfer mechanism in the heat transfer tube bank modules by the comparison of the heat transfer models, the case with the constant heat loss per unit volume and the case with heat loss by using inner and outer convective heat transfer coefficient of heat transfer tube. From the present research, it could be seen that the heat transfer mechanism with using inner and outer convective heat transfer coefficient derives more proper temperature distribution results and the acceptance criteria of the temperature distribution within ${\pm}10^{\circ}C$ before SCR is satisfied with using this heat transfer mechanism.

• Proceedings of the Optical Society of Korea Conference
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• 2009.02a
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• pp.515-516
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• 2009

• Journal of the Korean Institute of Gas
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• v.27 no.3
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• pp.123-133
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• 2023

Commercial hydrogen fuel cell vehicles are charged by compressing gaseous hydrogen to high pressure and storing it in a storage tank in the vehicle. This process causes the temperature of the gas to rise, to ensure the safety to storage tanks, the temperature is limited. Therefore, a heat transfer model is needed to explain this temperature rise. The heat transfer model includes the convective heat transfer phenomenon, and accurate estimation is required. In this study, the convective heat transfer coefficient in the hydrogen fueling process was calculated and compared using various correlation equations considering physical phenomena. The hydrogen fueling process was classified into the fueling line from the dispenser to the tank inlet and the storage tank in the vehicle, and the convective heat transfer coefficients were estimated according to process parameters such as mass flow rate, diameter, temperature and pressure. As a result, in the case of the inside of the filling line, the convective heat transfer coefficient was about 1000 times larger than that of the inside of the storage tank, and in the case of the outside of the filling line, the convective heat transfer coefficient was about 3 times larger than that of the outside of the storage tank. Finally, as a result of a comprehensive analysis of convective heat transfer coefficients in each process, it was found that outside the storage tank was lowest in the entire hydrogen fueling process, thus dominated the heat transfer phenomenon.

• Proceedings of the Korean Institute of Industrial Safety Conference
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• 2004.10a
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• pp.172-177
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• 2004