• Journal of the Society of Naval Architects of Korea
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• v.39 no.2
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• pp.52-60
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• 2002

Line heating is a forming process which makes the curved surface with the residual strain created by applying heat source of high temperature to steel plate. in order to control the residual strain, it is necessary to understand not only conductive heat transfer between heat source and steel plate, but also temperature distribution of steel plate. In this paper we attempted to analyze is temperature distribution of steel plate by simplifying a line heating process to collision-effusive flux of high temperature and high velocity, and conductive heat transfer phenomenon. To analyze this, combustion in the torch is simplified to collision effusive phenomenon before analyzing turbulent heat flux. The distribution of temperature field between the torch and steel plate is computed through turbulent heat flux analysis, and the convective heat transfer coefficient between effusive flux and steel plate is calculated using approximate empirical Nusselt formula. The velocity of heat flux into steel plate is computed using the temperature distribution and convective heat transfer coefficient, and temperature field in the steel plate is obtained through conductive heat transfer analysis in which the traction is induced by velocity of heat flux. In this study, Finite Element Method is used to accomplish turbulent heat flux analysis and conductive heat transfer analysis. FEA results are compared with empirical data to verify results.

• Journal of Advanced Marine Engineering and Technology
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• v.39 no.7
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• pp.765-772
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• 2015

In this research, the characteristics of SOFC/GT (Solid Oxide Fuel Cell/Gas Turbine) system temperature, stack power and system efficiency for flow rates of air, CH4 and water supplied to SOFC stack have been investigated. The temperature of the gas supplied to cathode and anode of SOFC stack in the SOFC/GT system are maintained by utilizing exhaust gas without the addition of external heat source. As a result, within the scope of this study, temperatures of gas supplied to cathode and anode of SOFC stack were maintained at 1000 (K) by utilizing the exhaust gas of the SOFC/GT system without the addition of external heat source. The system efficiency is increased with increase of air flow rate supplied to the stack and with decrease of $CH_4$ flow rate supplied to the stack. In addition, it can be found that the flow rate of the exhaust gas supplied to the turbine had a significant effect on the system efficiency. And the efficiencies of SOFC stack and SOFC/GT system depending upon various operating conditions of the SOFC/GT system is 51~57% and 57~73%, respectively.

• Journal of the Korean Society of Food Science and Nutrition
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• v.26 no.1
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• pp.45-53
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• 1997

Salted mackerel(Scomber japonicus) is favorite diet in Korea from ancient times. The formation of N-nitrosamine and amines such as VBN, TMAO, TMA and DMA in salted mackerels were investigated when nitrite was added to salting water at the concentration of 0, 100, 500 and 1000mg/kg and influence of cooking method on the formation of N-nitrosamine was also analyzed. The content of VBN in mackerel during the salting increased contineously; after 50 days it was approximately more than 23.8 times as compared with that of raw sample. The TMAO nitrogen decreased while TMA increased in mackerel during the salting, the amounts of TMAO and TMA were 3.7~21.0mg/100g and 15.0~20.4mg/100g in salted mackerel, respectively. The content of DMA nitrogen increased remarkably in mackerel during the salting; DMA in sample salted for 50 days reached about 16.0 times more than that of raw sample. N-Nitrosodimethylamine (NDMA) content of control sample was detected less than 1.0$\mu\textrm{g}$/kg, but nitrite addition to salting water at 100, 500 and 1000ppm resulted in NDMA content of 8.1~14.6$\mu\textrm{g}$/kg, 24.5~45.5$\mu\textrm{g}$/kg and 53.8~77.2$\mu\textrm{g}$/kg, respectively. In contrast, cooked counterparts contained 3.3~12.6$\mu\textrm{g}$/kg of NDMA. In general, more NDMA were produced during cooking when samples cooked using direct heating methods such as a gas range and a briquet fire than when samples were cooked using indrect heating methods such as an electric range.

• Journal of Advanced Marine Engineering and Technology
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• v.40 no.6
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• pp.476-483
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• 2016

An organic Rankine cycle for ocean thermal energy conversion system is a generating cycle using the temperature difference between surface water and deep water of the ocean. The working fluid is an important factor in the thermodynamic performance of an organic Rankine cycle. There is pinch point analysis as thermodynamic analysis of an organic Rankine cycle. This study performed a thermodynamic performance analysis according to variation in the pinch point temperature difference in heat exchangers and variation of outlet temperature of heat source and heat sink. It analyzed the thermodynamic performance by applying seven types of simple working fluids in a simple Rankine cycle for ocean thermal energy conversion that was designed according to pinch point analysis. As a result of the performance analysis, cycle irreversibility and total exergy destruction factor more decreased, and second law efficiency more increased in the lower pinch point temperature difference and temperature variation of heat source and heat sink in heat exchangers. In addition, the irreversibility changed greatly at a point that occurred in the thermodynamic variation. Among the selected working fluids, RE245fa2 showed the best thermodynamic performance, and the performance of all working fluids was observed to be similar. It needs a strict theoretical basis about diverse factors with thermodynamic performances in selecting heat exchangers and working fluids.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.35 no.12
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• pp.1367-1373
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• 2011

This research concerns the development of a compression/absorption high-temperature hybrid heat pump that uses a natural refrigerant mixture. Heat pumps based on the compression/absorption cycle offer various advantages over conventional heat pumps based on the vapor compression cycle, such as large temperature glide, temperature lift, flexible operating range, and capacity control. In this study, a lab-scale prototype hybrid heat pump was constructed with a two-stage compressor, absorber, desorber, desuperheater, solution heat exchanger, solution pump, liquid/vapor separator, and rectifier as the main components. The hybrid heat pump system operated at 10-kW-class heating capacity producing hot water whose temperature was more than $90^{\circ}C$ when the heat source and sink temperatures were $50^{\circ}C$. Experiments with various $NH_3/H_2O$ mass fractions and compressor/pump circulation ratios were performed on the system. From the study, the system performance was optimized at a specific $NH_3$ concentration.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.38 no.9
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• pp.757-762
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• 2014

A solar heat and power hybrid system can simultaneously generate electricity and thermal energy. In this study, several experiments were carried out with a solar heat and power hybrid unit. Then, a method to increase the photovoltaic efficiency and amount of thermal energy was suggested based on a comparative analysis. The experiment was conducted using only the photovoltaic system as a reference case, with the photovoltaic-thermal air system as a hybrid case. A numerical increase in the photovoltaic efficiency per $1^{\circ}C$ was suggested based on a comparative data analysis of these two cases. In this experiment, the surface temperature on the air hybrid system was $13.52^{\circ}C$ lower than that in the reference case, and the photovoltaic efficiency was increased by 5.09. The amount of thermal energy produced was 15.69 Wt per $1^{\circ}C$ difference between the ambient and outlet temperatures. In this paper, therefore, a photovoltaic efficiency increase of 0.34 per $1^{\circ}C$ is proposed for the air hybrid system based on the analysis of the experimental data.

• Fire Science and Engineering
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• v.22 no.5
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• pp.72-78
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• 2008

The mass loss rate and heat release rate of EPS sandwich panel cores were analysed using variable external irradiation level. The experimental materials were exposed to incident heat fluxes form 20 to 50 kW/$m^2$. For the measurement of mass loss rate and heat release rate, the size of specimen was $100mm{\times}100mm{\times}50mm$ and the samples were 3 different kinds. The combustion heat were carried out from the Oxygen bomb calorimeter and the mass loss rate and heat release rate were carried out from the Mass loss calorimeter according to ISO 5660-1. As the results of this study, the mass loss rate of Type A, B, and C were 2.7 g/$m^2s$, 2.8 g/$m^2s$, and 2.3 g/$m^2s$ and the heat release rate of Type A, B, and C were 58.23 kW/$m^2$, 47.19 kW/$m^2$, and 50.06 kW/$m^2$ respectively at the heat flux of 50 kW/$m^2$. In conclusion, when the heat release characteristics applied to a classification system of Canada, Type A and C can be classified grade C-3, and Type C can be classified grade C-2 from all data of this study.

• Environmental and Resource Economics Review
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• v.15 no.3
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• pp.505-530
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• 2006

For the district heating and cooling business, it is required to install energy-saving facilities using energy from waste and land fill gases such as combined heat and power(CHP). The current issues that this business faces can be summarized as below: which facilities including CHP can be economically introduced and how much of their capacities should be. Most of such issues are clearly related to the optimal plant design of the district heating and cooling business, and the prices of energy services such as heating and cooling energy, and electricity. The purpose of this study is to establish linear program model of least cost function and to practice the empirical test on a assumed district heating and cooling business area. The model could choose the optimal type of energy-producing facilities among various kinds available such as CHP's, absorption chillers, the ice-storage system, etc. CHP with the flexible heat and power ratio is also in the set of available technologies. And the model show us the optimal ration of heat producing facilities between CHP and historical heat only boiler in the service area. Some implications of this study are summarized as below. Firms may utilize this model as a tool for the analysis of their optimal size of the facilities and operation. Also, the government may refer the results to regulate resonable size of business.

• Journal of Energy Engineering
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• v.10 no.3
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• pp.195-205
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• 2001

A great deal of energy is necessary with emission of lots of wastewater in dyeing and finishing process, but heat recovery from wastewater is not introduced since is technology is not developed yet. In order to obtain the method utilizing hot water produced by heat source, that is, dyeing wastewater it was investigated the characteristics of dyeing and finishing process and energy basic unit. Energy basic unit of polyester/cotton (T/C), polyester/rayon (T/R) and polyester dyeing process are higher than that of the other process. The average quantity of wastewater for each dyeing company is 20,470 ton/month, the average temperature of wastewater is about 41$^{\circ}C$. Because the SS solution of wastewater in polyester dyeing process is lower than that of the other process, the effect of corrosion in heat recovery system is low. Since the energy price for 1000 kcal produced by vapor compression heat pump is presumed to be 22.50 won, it is found to be very economic heat recovery system, and its payback is 2.09 years for the factory with LNG boiler.

• Proceedings of the Korea Water Resources Association Conference
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• 2010.05a
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• pp.1996-2000
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• 2010

국내 시설원예 면적은 2005년 기준 52,022ha에 달하고 있으며 약 23%에 해당하는 12,000ha는 겨울철에 난방기를 가동하여 원예작물을 생산하고 있다. 농업용 난방기의 보급은 가온재배 면적의 증가와 더불어 급신장하고 있어 농업용 면세유 중 경유 공급액 약 9,260억원 중 62%에 해당하는 1,350,000톤이 시설원예 난방에 사용된 것으로 추산되고 있다. 지속적인 유가 상승으로 시설재배 농가의 경영이 악화되고 있어 최근 히트펌프를 이용한 냉난방시스템에 대한 연구가 수행되고 있다. 시설원예 냉난방에 사용되는 히트펌프의 열원은 다양하게 적용할 수 있으나 강변에 위치하고 있는 시설원예단지의 경우 연 중 풍부한 유량과 안정적인 수온을 얻을 수 있는 강변여과수는 매우 매력적인 열원이다. 본 연구에서는 시범지역으로 남강댐 하류에 위치하고 있는 진주지역의 시설원예단지와 낙동강 유역의 구미지역 시설원예단지의 두 곳에 대하여 1일 $1,000m^3$의 강변여과수 개발에 대한 조사를 수행하였다. 육안 및 현장여건에 대한 조사를 수행하고 인근 지하수 사용현황에 대한 조사를 실시하였다. 진주지역의 경우 일부 농가에서 지하수를 사용하고 있었으나 1일 8~10시간 취수에 최대 취수량은 약 $120m^3$ 정도였다. 반면, 구미지역의 경우 1999년 구미첨단원예농단 조성사업의 일환으로 양액재배에 농업용수를 공급할 목적으로 지하수 개발이 실시되었으며 최근 인근 국화축제를 개최하는 지역에서 신규로 지하수를 개발하여 사용 중이었다. 전기비저항 탐사를 실시한 결과 진주지역은 지하 약 6~17m 지점에 대수층이 존재하는 것으로 판단되었고, 구미지역은 지하 약 10~20m 지점에 대수층이 존재할 가능성이 있지만 지하 20m 지점부터는 대수층의 가능성이 높은 것으로 판단되었다. 두 지역에 각각 두 공을 시추하여 조사한 결과, 구미지역의 경우 수면높이가 지하 약 10m이고 각각 2.5m와 4.6m의 모래자갈층을 형성하고 있어 $1,000m^3$/일의 취수량 개발이 원활하지 않을 것으로 판단되었다. 한편, 진주지역은 수면높이가 지하 약 3m이고 각각 3.5m와 6.5m의 모래자갈층을 형성하고 있어 $1,000m^3$/일의 취수량 개발이 가능할 것으로 판단되었다. 현장 시추조사 및 기존관정 조사결과, 구미지역에 비하여 진주지역이 지하수 물량 확보가 상대적으로 용이하고 신규 굴착 가능지점이 다수 분포하고 있어 연구지점으로 활용하는데 유리할 것으로 판단되었다. 따라서 진주지역에 여과수열원 확보를 위해 2곳의 양수관정을 설치하고 히트펌프를 이용하여 시설원예의 냉난방을 실시할 예정이다.