• 공업화학
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• 제9권6호
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• pp.829-834
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• 1998

환경문제와 관련하여 오존층 파괴의 주요 원인으로 알려진 CFC를 열플라즈마를 이용하여 완전하게 분해하였다. CFC113($C_2Cl_3F_3$)을 선정하여 열플라즈마 분해에서의 적절한 공정 조건을 검토하였다. 실험에 앞서, 상압에서 300 K~5000 K범위에서 CFC113, $H_2$, $O_2$간의 열역학적 화학평형조성을 고찰함으로써 CFC113의 분해 생성의 경향을 알 수 있었다. 실험은 상압, 상온에서 CFC113과 $H_2$, $O_2$혼합가스의 주입량, 그리고 냉각관 직경의 변화에 따른 분해생성물을 조사하였고 이를 기체크로마토그래피로 분석하였다. 그 결과, 각각 99.99%이상의 분해율을 보였다. CFC113/$H_2$=1/3에서 $O_2$비가 증가할수록 CO로의 전화율은 감소하였다. CFC113/$O_2$=1/1, 1/1.5, 1/2에서 $H_2$비가 3이상 증가될수록 CO로의 전화율이 증가하였다. 그 이유는 $H_2$첨가가 증가할수록 환원분위기에서 $H_2O$가 생성되고 $CO_2$생성량이 감소하기 때문이다. DC power가 증가하여도 CO로의 전화율 변화는 차이가 없었으며, 총유량이 증가할 경우 CO전화율이 약간 감소하는 경향을 보였다. 냉각관의 직경을 8 mm에서 4 mm로 작게 할 경우 빠른 냉각속도로 인하여 CO로의 전화율이 증가하였다.

• 한국태양에너지학회 논문집
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• 제34권2호
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• pp.73-81
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• 2014

Ocean thermal energy conversion(OTEC) is a power generation method that utilizes temperature difference between the warm surface seawater and cold deep sea water of ocean. As potential sources of clean-energy supply, Ocean thermal energy conversion(OTEC) power plants' viability has been investigated. Therefore, this paper evaluated the thermodynamic performance of solar-OTEC convergence system for the production with electric power and desalinated water. The comparison analysis of solar-OTEC convergence system performance was carried out as the fluid temperature, saturated temperature difference and pressure of flash evaporator under equivalent conditions. As a results, maximum system efficiency, electric power and fresh water output show at 40, 10, 2.5 kPa of the flash evaporator pressure, respectively. And their respective enhancement ratios were approximately 6.1, 18, 8.6 times higher than that of the base open OTEC system. Also, performance of solar-OTEC system is the highest in the flash evaporator pressure of 10 kPa.

• 방사성폐기물학회지
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• 제16권1호
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• pp.59-64
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• 2018

사용후핵연료을 건식처리하는 파이로프로세싱 중 전해정련 및 제련공정 후 발생되는 우라늄과 초우라늄 및 희토류 등의 염화물을 함유한 LiCl-KCl 공융염에는 특히 희토류 함량이 높기 때문에 유효자원으로 활용이 가능한 형태의 우라늄과 초우라늄의 분리/회수가 쉽지 않다. 이러한 문제점을 해결하기 위해 본 연구에서는 $LiCl-KCl-UCl_3-NdCl_3$ 시스템에서 산화제($K_2CO_3$)를 이용하여 $UCl_3$를 산화물 형태로 전환한 후 전기화학적 방법을 이용하여 $NdCl_3$를 금속형태로 분리하는 실험을 실시하였다. 실험에 앞서, 이론적 평형계산을 수행하여 우라늄 염화물을 산화물로 전환하기 위한 실험조건을 결정하였다. 상기의 실험에서 LiCl-KCl 내 $UCl_3$는 첨가제의 주입량이 이론적 반응당량에 근접하였을 때 거의 대부분이 염내에서 염화물 형태로 존재하지 않는 것으로 나타났다. 이후 액체금속음극을 이용하여 $NdCl_3$를 금속형태로 전착시켰으며, 전착실험 후 투명한 용융상의 LiCl-KCl 공융염과 갈색의 우라늄 산화침전물이 존재함이 확인되었다. 이러한 결과들을 통해 $LiCl-KCl-UCl_3-NdCl_3$ 시스템에서 우라늄 및 희토류를 각각 분리할 수 있는 방안을 수립할 수 있을 것으로 판단된다.

• 한국태양에너지학회 논문집
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• 제27권3호
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• pp.37-44
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• 2007

For the past few years, the concern for clean energy has been greatly increased. Ocean Thermal Energy Conversion(OTEC) power plants are studied as a viable option for the supply of clean energy. In this paper, the thermodynamic performance of OTEC cycle was examined. Computer simulation programs were developed under the same condition and various working fluids for closed Rankine cycle, regeneration cycle, Kalina cycle, open cycle and hybrid cycle. The results show that the regeneration cycle using R125 showed a 0.17 to 1.56% increase in energy efficiency, and simple Rankine cycle can generate electricity when the difference in warm and cold sea water inlet temperatures are greater than $15^{\circ}C$. Also, the cycle efficiency of OTEC power plant using the condenser effluent from nuclear power plant instead of the surface water increased about 2%.

• 한국태양에너지학회 논문집
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• 제30권3호
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• pp.124-130
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• 2010

Ocean Thermal Energy Conversion(OTEC) power plants have been examined as a viable option for supplying clean energy. This paper evaluated the thermodynamic performance of the OTEC Power system for the production of electric power and desalinated water. The results show that newly developed fluids such as R32, R125, R143a, and R410A that do not cause stratospheric ozone layer depletion perform as well as R22 and ammonia. Overall cycle efficiency of open cycle is the lowest value of 3.01% because about 10% of the gross power is used for pumping out non-condensable gas. Also, the hybrid cycle is an attempt to combine the best features and avoid the worst features of the open and closed cycles. The overall cycle efficiency of hybrid cycle is 3.44% and the amount of desalinated water is 0.0619 kg/s.

• BMB Reports
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• 제40권2호
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• pp.205-211
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• 2007

The stability curve - a plot of the Gibbs free energy of unfolding versus temperature - is calculated for bovine erythrocyte carbonic anhydrase in 150 mM sodium phosphate (pH = 7.0) from a combination of reversible differential scanning calorimetry measurements and isothermal guanidine hydrochloride titrations. The enzyme possesses two stable folded conformers with the conformational transition occurring at ~30$^{\circ}C$. The methodology yields a stability curve for the complete unfolding of the enzyme below this temperature but only the partial unfolding, to the molten globule state, above it. The transition state thermodynamics for the low- to physiological-temperature conformational change are calculated from slow-scan-rate differential scanning calorimetry measurements where it is found that the free energy barrier for the conversion is 90 kJ/mole and the transition state possesses a substantial unfolding quality. The data therefore suggest that the x-ray structure may differ considerably from the physiological structure and that the two conformers are not readily interconverted.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2008년도 춘계학술대회 논문집
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• pp.169-173
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• 2008

Stirling engine is a promising heat engine with a high efficiency, muti-fuel capability, low emission, quiet operation, very low maintenance and long life. As one of the promising applications, solar power system based on the Stirling dish, providing net solar-to-electric conversion efficiencies reaching 30%, can operate as stand-alone units in remote locations or can be linked together in groups to provide utility-scale power. This paper introduced a new Scroll-type Stirling engine, being developed for solar power, superior to conventional Stirling engines. The Scroll-type Stirling engine is characterized as traits of continuous and wholly separated compression and expansion; one-way flow system; direct cooling and heating the fluid in the working spaces through the extensive inner surfaces of scroll wraps. All theses traits contribute to achieving thermodynamic cycle closer to the ideal Stirling cycle (exactly speaking, Ericsson cycle).

• Journal of Pharmaceutical Investigation
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• 제40권spc호
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• pp.9-17
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• 2010

Polymorphism has been recognized to be a critical issue throughout the drug product development process. Most of solid phase drugs have polymorphism, which has generated a great deal of interest and the field has been evolving rapidly. Preferably, thermodynamically most stable form of a drug substance is selected to obtain consistent bioavailability over its shelf life and various storage conditions. Moreover, it has the lowest potential for conversion from one polymorphic form to another. However, metastable or amorphous forms may be used intentionally to induce faster dissolution rate for rapid drug absorption and higher efficacy. For pharmaceutical industry, polymorphism is one of the key activities in form selection process together with salt selection. This article introduces the main features in the investigation of solid form selection especially polymorphic behavior with thermodynamic backgrounds, physicochemical properties with solubility, dissolution, and mechanical properties, and characterization techniques for proper analysis. The final form can be recommended based on the physicochemical and biopharmaceutical properties and by the processability, scalability and safety considerations. Pharmaceutical scientists especially in charge of formulation need to be well aware of the above issues to assure product quality.

• 한국농공학회논문집
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• 제57권1호
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• pp.79-87
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• 2015

A thermochemical equilibrium model was constructed for predicting composition of synthesis gas in biomass gasification. The model included estimation of equilibrium constants using Gibbs free energy. After constructing the model, the results were compared with the experimental values and predictions from a previous model. Gas compositions were reasonably well agreed with them and showed effects of operational and fuel condition. When the reaction temperature increased, the lower heating values decreased due to the decrease in CH4 concentrations. The methane concentrations were lower than those observed in experimental results. The model was used to predict the gas composition and heating values for the cases of mixed fuel of charcoal and un-dry woodchips. Although downdraft gasifiers require fuels less than 15% of moisture contents, the model results indicated that the mixed fuel with charcoal and woodchips which had over 25% of moisture contents could be used in the downdraft gasifiers. It might be explained by increase in energy density resulting from mixing charcoal. The results imply that the efforts and costs for drying biomass fuels could be reduced by mixing charcoal or fuels with higher calorific values.

• Bulletin of the Korean Chemical Society
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• 제30권1호
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• pp.153-156
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• 2009

Low temperature methane steam reforming to produce $H_2$ for fuel cells has been calculated thermodynamically considering both heat loss of the reformer and unreacted $H_2$ in fuel cell stack. According to the thermodynamic equilibrium analysis, it is possible to operate methane steam reforming at low temperatures. A scheme for the low temperature methane steam reforming to produce $H_2$ for fuel cells by burning both unconverted $CH_4$ and $H_2$ to supply the heat for steam methane reforming has been proposed. The calculated value of the heat balance temperature is strongly dependent upon the amount of unreacted $H_2$ and heat loss of the reformer. If unreacted $H_2$ increases, less methane is required because unreacted $H_2$ can be burned to supply the heat. As a consequence, it is suitable to increase the reaction temperature for getting higher $CH_4$ conversion and more $H_2$ for fuel cell stack. If heat loss increases from the reformer, it is necessary to supply more heat for the endothermic methane steam reforming reaction from burning unconverted $CH_4$, resulting in decreasing the reforming temperature. Experimentally, it has been confirmed that low temperature methane steam reforming is possible with stable activity.