• The KSFM Journal of Fluid Machinery
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• v.12 no.4
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• pp.7-13
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• 2009

The purposes of present work are to analyze the convective heat transfer with three-dimensional Reynolds-averaged Navier-Stokes analysis, and to optimize shape of the mixing vane using the analysis results. Response surface method is employed as an optimization technique. The objective function is defined as a combination of inverse of heat transfer rate and friction loss. Two bend angles of mixing vane are selected as design variables. Thermal-hydraulic performances have been discussed and optimum shape has been obtained as a function of weighting factor in the objective function. The results show that the optimized geometry improves the heat transfer performance far downstream of the mixing vane.

• 한국전산유체공학회:학술대회논문집
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• 2002.05a
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• pp.79-87
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• 2002

The present work analyzed the effect of mixing vane shape on the flow structure and heat transfer downstream of mixing vane in a subchannel of fuel assembly, by obtaining velocity and pressure fields, turbulent intensity, flow-mixing factors, heat transfer coefficient and friction factor using three-dimensional RANS analysis. NJl5, NJ25, NJ35, NJ45, which were designed by the authors, were tested to evaluate the performances in enhancing the heat transfer. Standard $\kappa-\epsilon$ model is used as a turbulence closure model, and, periodic and symmetry conditions are set as boundary conditions. The flow blockage ratio is kept constant, but the twist angle of mixing vane is changed. The results with three turbulence models( $\kappa-\epsilon$, $\kappa-\omega$, RSM) were compared with experimental data.

• Journal of computational fluids engineering
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• v.14 no.2
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• pp.1-8
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• 2009

The purposes of present work are to analyze the convective heat transfer with three-dimensional Reynolds-averaged Navier-Stokes analysis, and to optimize shape of the mixing vane taken tolerance into consideration by using the analysis results. Response surface method is employed as an optimization technique. The objective function is defined as a combination of heat transfer rate and inverse of pressure drop. Two bend angles of mixing vane are selected as design variables. Thermal-hydraulic performances have been discussed and optimum shape has been obtained as a function of weighting factor in the objective function. The results show that the optimized geometry improves the heat transfer performance far downstream of the mixing vane.

• Journal of the Korean Chemical Society
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• v.17 no.4
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• pp.235-239
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• 1973

Kinetic studies of benzoyl chlorides solvolysis have been carried out in acetone-water mixtures. Results show that bimolecular process predominates in the low water content region but SN1 process becomes increasingly important in the high water content solvent composition.

• Proceedings of the KIEE Conference
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• 2006.07c
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• pp.1574-1575
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• 2006

보통의 AC PDP에서는 Ne, Xe 혼합가스를 사용한다. Xe %가 높아짐에 따라 PDP의 효율은 올라가지만 그와 함께 최초의 방전을 일으키는 방전 개시 전압 또한 올라간다. 이러한 이유로 실제 PDP에서 무한정 Xe %를 올릴 수는 없다. 그래서 우리는 Xe gas보다 원자번호가 낮은 불활성기체인 Kr gas를 첨가시킴으로써 동일한 효율에서 방전개시전압이 낮은 최적의 3원 가스 조성비를 찾아보았다.

• Journal of the Korean Chemical Society
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• v.18 no.5
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• pp.329-340
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• 1974

Sulfadiazine, $C_{10}H_{10}N_4O_2S$, forms monoclinic crystals of space group $P21}c$ from a mixture of acetone and ethanol with $a=13.71{\pm}0.04,\;b=5.84{\pm}0.03,\;c=15.11{\pm}0.05{\AA},\;{\beta}=115.0{\pm}0.3^{\circ}$, and four molecules per cell. Three dimensional photographic data were collected with $CuK\alpha$ radiation. The structure was determined using Patterson and Fourier synthesis methods and refined by block diagonal least-squares methods with isotropic thermal parameter for all non-hydrogen atoms. The final R value was 0.15 for the 1517 observed independent reflections. The dihedral angle between the planes through the benzene ring and the pyrimidine ring is $76^{\circ}$. The conformational angle formed by the projection of the S-C(5) bond with that of N(1)-C(1) where the projection is taken along the S-N(1) bond is $77^{\circ}$. The imino nitrogen atom, N(1), and pyrimidine nitrogen atom, N(3), form intermolecular $N-H{\cdots}N$ hydrogen bond between the molecules related by center of symmetry. Amino nitrogen atom, N(4), forms two intermolecular $N-H{\cdots}O$ hydrogen bonds, with O(1) and O(2) atoms of different molecules separated by b. A two dimensional network of hydrogen bonds form infinite molecular sheets parallel to the (100) plane. Adjacent sheets are bound together by van der Waals forces.

• Proceedings of the Korean Vacuum Society Conference
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• 1999.07a
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• pp.133-133
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• 1999

비정질 탄소막 제조에 있어서 수소가 포함된 반응성 가스를 사용할 경우 제작된 탄소막 내부에는 수소가 포함되게 되며, 이러한 수소원자들은 막의 특성에 중요한 영향을 주는 것으로 알려져 있다. 따라서, 본 연구에서는 비정질 탄소막(a-C:H) 내부에 존재하는 수소가 탄소막의 특성에 미치는 영향을 알아보고, 막 내부에 포함된 수소의 함량과 공정조건 사이의 함수계를 조사함으로써 수소의 함량을 인위적으로 통제할 수 있는 가능성을 제시하고자 한다. 수소가 포함된 비정질 탄소막은 2.45 GHz의 전자기파를 사용하는 electron cyclotron resonance plasma enhanced chemical vapor deposition (ECR-PECVD) 방법과 DC magnetron sputtering 법을 사용하여 제작하였다. 기판으로는 Si(001) wafer를 사용하였으며, 아세톤과 에탄올을 사용하여 표면의 유기성분을 제거하고, 진공챔버속에서 Ar 플라즈마를 발생시켜 sputter etching 방법으로 표면을 세척하였다. ECR-PECVD 방법에서는 반응가스로 메탄(CH4)과 수소(H2)의 혼합가스를 사용하였으며, 혼합가스의 비는 5~50% 범위내에서 변화를 주었다. 수소가스의 유량은 100SCCM으로 고정하였으며, 마이크로웨이브의 power는 360~900W였고, 기판에 가해준 negative DC bias 전압은 0~-500V이었다. DC magnetron sputtering 방법에서는 반응가스로 아세틸린(C2H2) 가스를 사용하였으며, 플라즈마 발생을 용이하게 하기 위해서 Ar 가스와 혼합하여 사용하였다. Ar 가스의 유량은 10SCCM으로 고정하였으며, 아세틸렌 가스의 유량은 5~20SCCM 범위내에서 주입하였다. 이때, 기판에 가해준 negative DC bias 전압은 0~-100V이었다. 제작된 탄소막의 수소 함량을 조사하기 위하여 Fourier Transform Infrared (FTIR) 분광법과 Elastic Recoil Detection Analysis (EFDA) 법을 사용하였으며, 증착율은 SEM 단면촬영과 a-step을 이용하여 측정하였고, 막의 경도는 Micro-Hardness Testing 법을 사용하여 측정하였다.

• Journal of the Korean Vacuum Society
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• v.9 no.4
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• pp.382-388
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• 2000

Hydrogenated amorphous carbon (a-C:H) films were fabricated by electron cyclotron resonance plasma-enhanced chemical vapor deposition. The bonding structure of carbon and hydrogen in the a-C:H films has been investigated by varying the deposition conditions such as ECR power, gas composition of methane and hydrogen, deposition time, and negative DC self bias voltage. The bonding characteristics of the a-C:H thin film were analyzed using FTIR spectroscopy. The IR absorption peaks of the film were observed in the range of $2800\sim3000 \textrm{cm}^{-1}$. The atomic bonding structure of a-C:H film consisted of $sp^3$ and $sp^2$ bonding, most of which is composed of $sp^3$ bonding. The structure of the a-C:H films changed from $CH_3$ bonding to $CH_2$ or CH bonding as deposition time increased. We also found that the amount of dehydrogenation in a-C:H films was increased as the bias voltage increased.

• Journal of the Korean Chemical Society
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• v.43 no.4
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• pp.418-422
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• 1999

A method is described for the selective determination of Cr(III) and Cr(VI) in aqueous solutios by flame atomic absorption spectrometry. Selective extraction of $Cr_2O_7^{2-}$ was performed by Aliquat 336/NIBK from the mixtures of $Cr^{3+}$ and $Cr_2O_7^{2-}$, and the extraction of $Cr^{3+}$ was followed after complex formation with citrate by using the same extractant. The concentraction of each analyte in the extract was determined by $N_2O-C_2H_2$ flame atomic absorption spectrometry. The recoveries of $Cr^{3+}$ and $Cr_2O_7^{2-}$ from 50mL of aqueous solution ranging 0.1~1.0 ${\mu}g/mL$ as Cr respectively by single extractions with 5 mL of 1%(V/V) Aliquat 336/MIBK were resulted as 98.8∼101.7%.

• Korean Journal of Materials Research
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• v.7 no.3
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• pp.234-243
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• 1997

The crystal structure of arc melted $ZrV_{x}Mn_{1-x}Ni_{1.0},\;ZrV_{x}Mn_{0.8-x}Ni_{1.2},\;ZrV_{x}Mn_{0.6-x}Ni_{1.4}$ alloys which are known to have AB2 type Laves structure was investigated. They had mixed phases of C14 and C15. The radius ratio ($r_{A}/r_{B}$) of atoms in A site to that of B site was found to be an important parameter in explaining the omposition dependence of the crystal structure The C15 structure showed a linear increase with the ratio in as-cast conditions. However, the annealed alloys revealed a definite ratio at which the stability of both phases are divided distinctly. The composition of the alloys could be closely controlled by maintaining the argon pressure in the chamber over 1 arm during arc melting. In contrast, the alloy ingot melted in VIM showed a significant loss of hln.