• Title/Summary/Keyword: 헨리상수

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Dimensionless Henry's Constant and Liquid-Vapour Equilibrium of Rosemary Aroma Compounds (로즈마리 향기성분의 기-액 평형과 무차원 헨리의 상수)

  • Yoon, Hyang-Sik;Jeong, Heon-Sang;Min, Young-Kyoo
    • Korean Journal of Food Science and Technology
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    • v.35 no.4
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    • pp.738-742
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    • 2003
  • In order to estimate the mass transfer characteristics of absorption into alcohol solution of aroma compounds such as cineol, myrecene and pinene which are major aroma compounds of rosemary, dimensionless Henry's constant in 70% ethyl alcohol concentration and aroma concentration with different ethyl alcohol concentration were analyzed. From the results of measurement of vapor phase concentration of aroma compounds with different ethyl alcohol concentration, headspace concentrations of all of three aroma compounds were decreased as ethyl alcohol concentration increased. But those patterns were slightly different. Dimensionless Henry's constant equation (Hi) of cineol compound with ethyl alcohol concentration (x) was as follows: $Hi=(-5.75+x)/(-7017.6+257.3{\times}x)$. Dimensionless Henry's constants of cineol, myrecene and pinene in 1 atm, $25^{\circ}C$ and 70% ethyl alcohol concentration were 0.0058, 0.0182 and 0.0365, respectively.

Optimal Condition of Photocatalytic Degradation of Benzene Using TiO$_2$ Coated on Support (TiO$_2$ 광촉매 졸 담체에 따른 가스상 벤젠 제거의 적정조건)

  • 양원호;손현석;김현용;박종래;조경덕
    • Proceedings of the Korea Air Pollution Research Association Conference
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    • 2002.04a
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    • pp.193-194
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    • 2002
  • 휘발성 유기화합물(VOCs)은 환경에 광범위하게 분포되어 있으며 특히 벤젠(benzene)은 발암물질로 규제가 강화되고 있다 또한 높은 증기압과 헨리상수를 가지고 있으므로 환경 중 이동이 용이하므로 대기, 수중, 토양 모두에 심각한 오염물질이 되고 있다. 이런 유기화합물 처리에 높은 효율을 나타내는 것이 자외선을 이용한 광분해(UV/Photodegradation)로 TiO$_2$를 촉매로 이용하는 것이다(Blystone et al., 1991). (중략)

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Characteristics of a Wet Air Cleaning System for Removal of Air Pollutants (습식 공기청정장치의 공기오염물질 제거 특성)

  • Bae, Gwi-Nam;Kim, Yong Pyo;Baik, Nam Jun
    • Journal of Korean Society of Environmental Engineers
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    • v.22 no.1
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    • pp.21-31
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    • 2000
  • Performance characteristics of a wet air cleaning system were investigated experimentally, and discussed in relation with physicochemical properties of the target pollutants. The system is composed of an air cleaner, a separator, and a medium filter. Removal efficiency of the system was measured for ambient particles and gaseous air pollutants: $SO_2$, NO, $NO_2$, HCHO, and $NH_3$. For particle removal test, particles were introduced into the system through a fan, and the particle size distribution was measured at three locations by using two laser particle counters. Particle removal efficiency for each system component was obtained from the particle size distribution. It was found that the separator primarily removed coarse particles greater than $5{\mu}m$ in diameter, and that the medium filter mainly removed fine particles less than $5{\mu}m$ in diameter. For gas removal test, air with gaseous air pollutant was injected into the outlet of the fan, and the concentration was measured both at the upstream of the air cleaner and at the downstream of the separator. It was found that the gaseous species with high Henry's law coefficients, such as $SO_2$, HCHO, and $NH_3$, showed high removal efficiency, but the gaseous species with low Henry's law coefficients, such as NO and $NO_2$, showed low removal efficiencies. It was also found that negative ions were generated from the air cleaner.

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An Experimental Study of Verification for PEMFC's 1-Dimensional Simulation (PEMFC 1차원 시뮬레이션 검증을 위한 실험적 연구)

  • Moon, Cheor-Eon;Ahn, Seong-Yool;Yang, Jang-Sik;Choi, Gyung-Min;Kim, Duck-Jool
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.06a
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    • pp.191-195
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    • 2007
  • In this study, we estimated the performance of PEMFC's unit cell as changing operating temperature in different inlet humidity condition at cathode side but anode dry, and tried to match experimental results with 1-dimensional simulation. We used $Nafion^{\circledR}112$ membrane and a self-manufactured PEMFC with active area of $25cm^{2}$ was used in this study. The range of operating temperature was $40{\sim}70^{\circ}C$ and oxygen through bubbled humidity chamber was supplied $0{\sim}80$% humidity condition as changing water temperature in humidity chamber. For figuring out governing equations, represent water contents in electrolyte membrane, the linear forward difference method was applied about time progress and quadratic central difference method was used about space progress. It was assumed that pressure terms were linearly changed due to thin electrolyte membrane. In low operating temperature condition, $40{\sim}60^{\circ}C$, increasing temperature rarely effected cell performance but we can see performance drop at $70^{\circ}C$. By modifying Henrry's constant and/or diffusion coefficient, the modified one-dimensional model was accomplished for calculation.

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A Simulated Prediction for Influences of Operating Condition in an Alkaline Fuel Cell

  • Jo Jang-Ho;Yi Sung-Chul
    • Journal of the Korean Electrochemical Society
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    • v.2 no.3
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    • pp.163-170
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    • 1999
  • The effects of the operating conditions in AFC single cells have not been studied in detail. In this study, by using a one-dimensional isothermal model a computational simulation was conducted to investigate the effects of the initial electrolyte concentration and the operating gas pressure. According to the result, the optimum electrolyte concentration at the base-case was found to be within $3.0\~3.5$ M. The variation of the cell performance according to the electrolyte concentration was found to be caused mainly by the charge transfer resistances of both electrodes, Henry's constant and the liquid phase diffusivity of the dissolved gases. It was also found that an increase in operating pressure increased the reaction rates and the solubilities of the gases, which led to a considerable enhancement of the cell performance.

Sensitivity Analysis for a Level-III Multimedia Environmental Model: A Case Study for 2, 3, 7, 8-TCDD in Seoul (다매체환경거동모형 (level-III)의 민감도분석기법: 서울지역의 2, 3, 7, 8-TCDD 사례연구)

  • Kwon, Jung-Hwan;Lee, Dong-Soo
    • Environmental Analysis Health and Toxicology
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    • v.17 no.3
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    • pp.225-238
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    • 2002
  • 유해물질의 거동에 대한 이해를 돕기 위해서 대도시지역을 대상으로 하여 fugacity를 이용한 level-III 다매체환경거동모형이 개발되었다. 이 모형에 의한 거동의 예측결과에 민감한 영향을 주는 입력과정과 변수들을 찾아내기 위하여 체계적으로 민감도분석을 수행할 수 있도록 하는 기법을 개발하고 사례연구로서 서울지역과 2, 3, 7, 8-TCDD을 대상으로 그 기법을 적용하였다. Sensitivity index에 의한 평가한 결과, 일정한 배출속도조건에서는 대기중의 바람속도, 그리고 대기에서 수체나 토양으로 전이되는 건식 및 습식 침적과정이 다매체거동에서 전체적으로 가장 중요한 과정인 것으로 나타났다. 또한 이들 거동과정 자체에 영향을 미치는 변수들에 대한 민감도 분석의 결과 건식침적의 경우 중력에 의한 입자들의 침강속도가, 습식침적의 경우 평균 강우속도가 대단히 중요한 변수임이 파악되었다. 물질의 물리화학적 특성 가운데에서는 z-값에 직접 영향을 주는 변수들, 즉, 헨리상수와 옥타놀-물 분배계수 등이 결과에 민감한 영향을 주는 것으로 나타났다. 이러한 사례연구는 본 연구에서 개발된 민감도분석기법이 유해물질의 다매체 거동모형을 개선하고 좀더 중요한 거동과정에 대한 이해를 넓히는데 효율적으로 사용될 수 있다는 것을 보여주고 있다.

Analysis of Amine Absorbents Volatility Based on the Chemical Structure (아민 흡수제의 화학구조에 따른 휘발 특성)

  • Lee, Kyung Ja;Lee, Ji Hyun;Kwak, No Sang;Lee, In Young;Kim, Jun Han;Eom, Yong Seok;Jang, Kyung Ryoung;Shim, Jae Goo;Lee, Yongtaek
    • Korean Chemical Engineering Research
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    • v.50 no.2
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    • pp.348-352
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    • 2012
  • Amine volatility occurring on the $CO_2$ capture process may result in significant economic losses and environmental impact. In this study, using an volatility measurement apparatus, we measured a amine volatility of various amines including MEA(Monoethanolamine), MDEA(N-Methyldiethanolamine), Pz(Piperazine), AMP(2-Amino-2-methyl-1-propanol), 2-MP(2-Methylpiperazine), DGA(Diglycolamine). For the quantitative analysis of volatility, we analyzed the effects of temperature and $CO_2$ loading using an gas chromatography analysis. The result shows that the amine volatility was increased by increasing Henry's constant(MDEA$-CH_3$)(for AMP).

Simulation of D-limonene Separation from Mandarine Extract in Simulated Moving Bed (SMB) (감귤 추출물로부터 D-리모넨 분리를 위한 유사 이동층 크로마토그래피(SMB) 전산모사)

  • Kim, Tae Ho;Ko, Kwan Young;Kim, In Ho
    • Korean Chemical Engineering Research
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    • v.54 no.1
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    • pp.81-88
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    • 2016
  • Limonene is orange flavored natural material that is mainly contained in mandarine and lemon peels. D-limonene was extracted from cold-storaged mandarine peel by using Soxhlet extractor at $120^{\circ}C$ for 2 hours with ethanol as solvent. Henry constants of d-limonene and impurity were calculated as $H_{Lim}=8.55$ and $H_{imp}=0.223$ from the result of HPLC analysis. 4-bed SMB of limonene simulation with $0.46{\times}25cm$ columns was conducted by using Aspen chromatography program. Then effective condition for purity was found by changing $m_2$ and $m_3$ values in triangle diagram. The highest purity was 98.59% at $m_2=2.57$, $m_3=9.55$. For this case, feed, desorbent, extract, and raffinate flow rates were 1 mL/min, 1.19 mL/min, 0.857 mL/min and 1.34 mL/min, respectively. Scale-up simulation was also conducted by increasing column diameter from 0.46 cm to 1.6 cm for getting the same efficiency. The increased flow rates were 12 mL/min, 14 mL/min, 10 mL/min, and 16 mL/min for feed, desorbent, extract, and raffinate. It was possible to scale-up with maintaining same limonene purity because linear isotherms of limonene and impurity were assumed.