• Journal of Korean Society of Environmental Engineers
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• v.22 no.1
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• pp.91-101
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• 2000

The emission sources of volatile organic compounds (VOCs) are wastewater treatment plants. sanitary landfills, automobile industries, and so on. The VOCs are harmful to human beings because of their toxicity and carcinogenicity, and cause the serious air pollution problem producing ozone ($O_3$) as a result of photochemical reaction. To investigate the emission of VOCs from wastewater treatment plant, aeration basins at the City of Los Angeles' Hyperion Treatment Plant were selected and measured flux was compared with calculated flux. For compounds commonly associated with wastewater (DCM, TCM, PCE, UM, DCB, UND) and not expected in vehicle exhaust or ambient air coming off the ocean, concentrations immediately downwind of the aeration basins were a factor of ten or higher than those measured in the upwind air. The airborne flux of less degradable or non-biodegradable compounds, e.g., DCE, DCM, TCA, DCA, TCM, PCE, DCB, through an imaginary plane at the downwind side of the aeration basins was in agreement with the estimated flux from measured liquid phase concentrations. Henry's constant. aeration rate, and an assumption of bubble saturation. For several compounds (PCE, DCE, TCA), the ratio (measured flux/calculated flux) is almost unity.

• KSCE Journal of Civil and Environmental Engineering Research
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• v.11 no.3
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• pp.11-18
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• 1991

Volatile organic compounds(VOC) present in or generated by many sources, can be toxic, mutagenic or even carcinogenic, so that control of such emissions is significant. The 6 chlorinated organic chemicals as VOC were examined in this study. Prediction of the behavior of VOC on activated carbon beds is an important part of control system design. The objective of this study was to predict gas phase sorption isotherms from physical properties and liquid phase isotherms obtained with the same adsorbent and adsorbate. One of the techniques that was investigated was quantitative structure-activity relationships(QSAR) for the predicition procedures. It was possible to estimate sorption isotherms in the gas phase($a_g$) using either connectivity index, $^2{\chi}$, and the Henry's law coefficient ($H_a$) or the solubility and the equilibrium concentration in the gas phase. As a result of study, the predictive equation based on Freundlich model for $a_g$ was ${\log}\;a_g=0.238\;^2{\chi}+0.573\;{\log}\;H_a+4.330(r^2=0.94)$. Finally, this would provide a potentially useful tool to describe and predict sorption capacity without time-consuming tests.

• Clean Technology
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• v.18 no.4
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• pp.347-354
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• 2012

In this study, simulation works have been performed for the $CO_2$ removal process contained in the DME production process using NMP (N-methyl-2-pyrrolidone) as a solvent. PRO/II with PROVISION release 9.1 at Invensys was used as a chemical process simulator and NRTL activity coefficient model with Henry's law option and Soave-Redlich-Kwong equation of state were used for thermodynamic models. For the determination of the binary interaction parameters in NRTL model, regression works have been performed to match the experimental thermodynamic data. Optimal feed tray location which minimizes the reboiler heat duty was determined.

• 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.

• 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.

• 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.