• Journal of Advanced Marine Engineering and Technology
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• 제27권7호
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• pp.906-913
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• 2003

The purpose of this 3-D numerical simulation is to evaluate the application of a commercial CFD code to predict 3-D flow and power characteristics of wind turbines. The experimental approach, which has been main method of investigation, appears to be its limits, the cost increasing with the size of the wind turbines, hence mostly limited to observing the phenomena on rotor blades. Therefore. the use of Computational Fluid Dynamics (CFD) techniques and Navier-Stokes solvers are considered a very serious contender. The flow solver CFX-TASCflow is employed in all computations in this paper. The 3-D flow separation and the wake distribution of 2 and 3 bladed Horizontal Axis Wind Turbines (HAWTs) are compared to Heuristic model and smoke-visualized experimental result by NREL(National Renewable Energy Laboratory). Simulated 3-D flow separation structure on the rotor blade is very similar to Heuristic model and the wake structure of the wind turbine is good consistent with smoke-visualized result. The calculated power of the 3 bladed rotor by CFD is compared with BEM results by TU-Delft. The CFD results of which is somewhat consist with BEM results. under an error less than 10%.

• KSBB Journal
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• 제29권4호
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• pp.250-262
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• 2014

A simulation study for finding purity changes of extract and raffinate as well as the best purity of (S)-ketoprofen in simulated moving bed (SMB) was performed with changing parameters of $m_2$ and $m_3$ from triangle theory. Aspen simulator allowed separation process simulation of (R)- and (S)-ketoprofen in SMB and compared 4-bed SMB and 8-bed SMB based on the same Henry constant and mass transfer coefficient. The 4-bed SMB consisted of 4 columns (200 mm of length, 10 mm of diameter) and the 8-bed SMB constructed by 8 columns (100 mm of length, 10 mm of diameter), and therefore total column length was made the same as 800 mm. Considering purities of both (R)-and (S)-ketoprofen, both 4-bed SMB and 8-bed SMB had the best purity when $m_2$ and $m_3$ were on 12.0 and 13.0 in the center of triangle. Taking only (S)-ketoprofen into account, 4-bed SMB as well as 8-bed SMB had the best purity when $m_2$ and $m_3$ were on 10.9 and 12.6 in the left outside triangle, and their purities were 93.3 % for 4-bed SMB and 96.9 % for 8-bed SMB.

• Korean Membrane Journal
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• 제6권1호
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• pp.55-60
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• 2004

In recent years, an increasing interest in membrane technology has been observed in chemical and environmental industry. Membrane technology has advantages of low cost, energy saving and environmental clean technology comparing to conventional separation processes. Pervaporation is one of new advanced membrane technology applied for separation of azeotropic mixtures, aqueous organic mixtures, organic solvent and petrochemical mixtures. Sodium alginate composite membranes were prepared for the enhancement of long-term stability of pervaporation performance of water-ethanol mixture using pervaporation. Sodium alginate membranes were crosslinked with CaCl$_2$ and coated with polyelectrolyte chitosan to protect washing out of calcium ions from the polymer. The surface structures of PAN and hydrolysed PAN membrane were confirmed by ATR Fourier transform infrared (FT-IR). A field emission scanning electron microscopy (FE-SEM; Jeol 6340F) operated at 15 kV. Concentration profiles for Ca in the membrane surface and membrane cross-section were taken by an energy dispersive X-ray (EDX) analyser (Jeol) attached to the field emission scanning electron microscopy (Jeol 6340F). Pervaporation experiments were done with several operation run times to investigate long-term stability of the membranes.

• Journal of Ginseng Research
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• 제12권2호
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• pp.164-172
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• 1988

인삼사포닌 정량분석의 상법 purification과정을 역상소형 $C_18$ 컬럼 전처리로 대체할 수 있었으며, 분석시간은 1/4로 단축되었다. 이 방법을 사용하면 total ginsenoside의 회수율은 높으나 protopanaxatriol계 ginsenoside들의 회수율은 약간 낮았으며, 근중 농도 정도의 당류는 ginsenoside 회수율에 영향을 미치지 않았다. Ginsenoside 회수율의 변이계수는 상법의 경우보다 작았으며 이 방법에 사용되는 ginsenoside의 적정량은 10~15mg이었다. 역상소형컬럼방법은 건삼과 홍삼시료처리시에도 상법과 고도의 유의성을 나타냈다. 신속 역상소형컬럼 방법을 실제로 이용하기 위하여 8점의 시료를 동시에 처리하는 소형아크릴 장치를 사용하였다.

• 한국해양공학회지
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• 제22권3호
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• pp.24-33
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• 2008

In this study, flow and creation and dissipation of vorticity around rectangular floating breakwater is investigated both experimentally and numerically. The PIV system(Particle image velocimetry) is employed to obtain the velocity field in the vorticity of rectangular structure. The numerical model, combined with ${\kappa}-{\varepsilon}$ turbulence model and the VOF method based on RANS equation, is used to analyze the turbulence structure. In the results of this study, the vorticity is found around conner of rectangular structure at all time domain, and creation and dissipation of vorticity are closely related to wave period. Separation points of phase of vortex due to flow separation for longer period waves are faster then for shorter period waves.

• Bulletin of the Korean Chemical Society
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• 제33권7호
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• pp.2224-2228
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• 2012

This study describes the ability of capillary electrochromatography (CEC) for the determination of imidacloprid and carbendazim in tomato samples. A novel liquid crystal crown ether modified hybrid silica monolithic column was synthesized, characterized and developed as separation column for the first time. Baseline separation of imidacloprid and carbendazim could be achieved using a mobile phase containing 90% (v/v) 20 mmol/L phosphate buffer (pH 7.0) and 10% (v/v) acetonitrile. The matrix matched calibration curves were linear with correlation coefficient $r^2$ > 0.9998 in the range of 0.20-10.00 mg/L. The limits of detection for imidacloprid and carbendazim were 0.061 and 0.15 mg/kg, respectively, which were below the maximum residue limits established by the European Union as well as Codex Alimentarius. Average recoveries for imidacloprid and carbendazim varied from 101.6-108.0% with relative standard deviations lower than 6.3%. This method was applied to the analysis of tomatoes collected from local markets.

• 한국막학회:학술대회논문집
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• 한국막학회 2005년도 추계 총회 및 학술발표회
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• pp.96-101
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• 2005

A theory for the material transports through ion exchange membrane has been developed on the basis of nonequilibrium thermodynamics by removing the assumption of solvent flow in the previous paper and applied to a detailed study of the ionic transport properties of new charged mosaic membrane(CMM) system. The CMM having two different fixed charges in the polymer membrane indicated unique selective transport behavior then ion-exchange membrane. The separation behavior of ion transport across the CMM with a parallel array of positive and negative functional charges were investigated. It was well-known the analysis of the volume flux and solute flux based on nonequilibrium thermodynamics. Our suggests preferential salt transport across the charged mosaic membranes. Transport properties of heavy metal ions, $Mg^{2+}$, $Mn^{2+}$and sucrose system across the charged mosaic membrane were estimated. As a result, we were known metal salts transport depended largely on the CMM. The reflection coefficient indicated the negative value that suggested preferential material transport and was independent of charged mosaic membrane thickness.

• 한국물환경학회지
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• 제20권3호
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• pp.296-300
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• 2004

The rejection properties of 6 aromatic pesticides were evaluated by a continuous flow system equipped with a hollow fiber NF membrane. Different from the separation experiment of batch cell, the rejection and the removal could be calculated exactly because the concentration of feed, permeate and retentate was separately obtained. The lowest and the highest rejection were found in carbaryl(54.8%) and methoxychlor(99.2%), respectively, and the removals were always shown higher than rejections. This may be caused by some reasons such as the solute adsorption on the membrane, the variation of feed concentration. Although molecular weight, molecular width regarded as solute characteristics and log P(n-octanol/water partition coefficient) as hydrophobicity could be applied to explain the rejection property, these factors should be considered together for better analysis. According to the higher relationship between log B(solute permeability) and molecular weight, it was revealed that the solute separation with this membrane was influenced more by molecular weight.

• 한국응용과학기술학회지
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• 제25권2호
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• pp.232-239
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• 2008

Separation of naphthalene from naphthalene and 2-methylnaphthalene mixture has been studied by layered melt and solution crystallization using ethylalcohol. Purity and yield of naphthalene depended mainly on the cooling rate: The effective distribution coefficient ($K_{eff}$) as the degree of impurity removal was observed to decrease with the decreasing in cooling rate. Purity of naphthalene can be enhanced to $5{\sim}7%$ by melt crystallization using 90% naphthalene and the purity of naphthalene can be obtained to be 99% up by solution crystallization.

• 자원리싸이클링
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• 제14권6호
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• pp.10-15
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• 2005

본 연구는 Karr column을 이용한 희토류원소의 분리에 대한 연구로서, 유량, 수상의 초기 pH, 유기상인 PC88A비누화도, 교반속도 등의 변수에 따른 Sm/ND이성분계의 분리특성을 조사하였다. 수상과 유기상의 유량이 16.5ml/min(체류시간 10분)에서 수상의 초기 pH가 높아짐에 따라 Sm/Nd의 추출율 및 분리계수가 증가하였으며, 비누화의 영향으로 반응 후 수상의 평형 pH가 약 1.5정도로 유지되었다 또한 PC88A 비누화도가 증가함에 따라 추출율 및 분리계수가 증가하였으며 적정 비누화도는 $40\%$였다. 그리고 교반 모터의 회전수 증가에 의해 추출율 및 분리계수가 크게 증가하는 결과를 보였다. 체류시간 10분, 초기 pH 1, PC88A비누화도 $40\%$,교반속도 120rpm에서 Nd $19.6\%$, Sm $72.5\%$가 추출되었다.