• 대한전기학회:학술대회논문집
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• 대한전기학회 2002년도 하계학술대회 논문집 C
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• pp.1518-1520
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• 2002

Purpose of this research compares best transfer speed about applied frequency and voltage using characteristic of $L_1-B_4$ mode and $L_1-B_8$ mode linear ultrasonic motor that use piezoelectric effect. By method of study, analyzed best transfer speed measuring and comparison load status that use actuality telephone card in $L_1-B_4$ mode linear ultrasonic motor and no-load status of $L_1-B_8$ mode linear ultrasonic motor. Experiment result is applied frequency(58.4Hz) in $L_1-B_4$ mode linear ultrasonic motor (load state) and the best transfer speed by 19.8[cm/s] at applied voltage(56V) point. Also, $L_1-B_8$ mode linear ultrasonic motor (no-load state) is best transfer speed by applied frequency(27.9kHz) and 32.96[cm/s] at applied voltage (50V) point.

• 한국안광학회지
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• 제8권1호
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• pp.53-57
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• 2003

5분 간격으로 착색시간을 증가시켜 R, G, Y, B칼라렌즈를 제작하였다. 색 좌표 분석은 분광측색계와 CIE $L^*a^*b^*$ color system를 사용하였다. 착색 시간에 따른 색좌표 이동 형태는 $b^*(Y-B)={\beta}a^*+{\alpha}$이며, 거의 선형적으로 변하였다. 적색의 경우 착색시간이 길수록 $G{\rightarrow}R$, $B{\rightarrow}Y$ 형태로 이동하고, Parameter ${\alpha}$, ${\beta}$ 값은 각각 -3.49, 0.90을 얻었다. 녹색의 경우 색좌표 이동은 $R{\rightarrow}G$, $B{\rightarrow}Y$ 형태이다. 10분의 착색 시간에서 가장 순수한 녹색 칼라를 얻었다. Parameter ${\alpha}$, ${\beta}$값은 각각 -0.72, -0.55을 얻었다. 황색과 청색의 경우 모두 착색 시간이 길수록 순수한 색이 된다. 황색에서 Parameter ${\alpha}$, ${\beta}$값은 각각 14.11, 1.58이고, 청색에서 Parameter ${\alpha}$, ${\beta}$값은 각각 -11.62, 1.30을 얻었다.

• 건축사
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• 7호통권435호
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• pp.16-17
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• 2005

• Environmental Engineering Research
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• 제19권4호
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• pp.345-354
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• 2014

In this paper, effects of physical configurations and operating conditions on bubble column performance were analyzed in terms of bubble hydrodynamic and mass transfer parameters. Bubble column with 3 different dimensions and 7 gas diffusers (single / multiple orifice and rigid / flexible orifice) were applied. High speed camera and image analysis program were used for analyzing the bubble hydrodynamic parameters. The local liquid-side mass transfer coefficient ($k_L$) was estimated from the volumetric mass transfer coefficient ($k_La$) and the interfacial area (a), which was deduced from the bubble diameter ($D_B$) and the terminal bubble rising velocity ($U_B$). The result showed that the values of kLa and a increased with the superficial gas velocity (Vg) and the size of bubble column. Influences of gas diffuser physical property (orifice size, thickness and orifice number) can be proven on the generated bubble size and the mass transfer performance in bubble column. Concerning the variation of $k_L$ coefficients with bubble size, 3 zones (Zone A, B and C) can be observed. For Zone A and Zone C, a good agreement between the experimental and the predicted $K_L$ coefficients was obtained (average difference of ${\pm}15%$), whereas the inaccuracy result (of ${\pm}40%$) was found in Zone B. To enhance the high $k_La$ coefficient and absorption efficiency in bubble column, it was unnecessary to generate numerous fine bubbles at high superficial gas velocity since it causes high power consumption with the great decrease of $k_L$ coefficients.

• Journal of Biosystems Engineering
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• 제37권3호
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• pp.155-165
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• 2012

This study was performed to offer the data for design of the seedling bed transfer equipment to make the automation of working process in a plant factory. The seedling bed transfer equipment pushing the seedling bed with bearing wheels on the rail for interconnecting each working process by a pneumatic cylinder was made and examined. The examined transfer force to push the seedling bed with a weight of 178.9 N by the pneumatic cylinder with length of 60 cm and section area of 5 $cm^2$ was measured by experiments. The examined transfer forces was compared with theoretical ones calculated by the theoretical formula derived from dynamic system analysis according to the number of the seedling bed and pushing speed of the pneumatic cylinder head at no load. The transfer function of the equipment with the input variable as the pushing speed $V_{h0}$(m/s) and the output variable as the transfer force f(t)(N) was represented as $F(s)=(V_{h0}/k)(s+B/M)/(s(s^2+Bs/M+1/(kM))$ where M(kg), k(m/N) and B(Ns/m) are the mass of the bed, the compression coefficient of the pneumatic cylinder and the dynamic friction coefficient between the seedling bed and the rail, respectively. The examined transfer force curves and the theoretical ones were represented similar wave forms as to use the theoretical formular to design the device for the seedling bed transfer. The condition of no vibration of the transfer force curve was $kB^2>4M$. The condition of transferring the bed by the repeatable impact and vibration force according to difference of transfer distance of the pneumatic cylinder head from that of the bed was as $Ce^{-\frac{3{\pi}D}{2\omega}}<-1$, where ${\omega}=\sqrt{\frac{1}{kM}-\frac{B^2}{4M^2}}$, $C=\{\frac{\frac{B}{2M}-\frac{1}{kB}}{\omega}\}$, $D=\frac{B}{2M}$. The examined mean peak transfer force represented 4 times of the stead state transfer force. Therefore it seemed that the transfer force of the pneumatic cylinder required for design of the push device was 4Bv where v is the pushing speed.

• 대한기계학회논문집
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• 제16권4호
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• pp.765-774
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• 1992

본 연구에서는 수직 등온 평행평판의 혼합대류 열전달에 대하여 두 평판의 길 이가 다른 경우를 고찰하고자 Reynolds수, Grashof수, 평판간격을 변수로 하여 수치해 석 하였다.

• 대한설비공학회지:설비저널
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• 제13권2호
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• pp.10-15
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• 1984

The aims of this study are to obtain a suitable method and a proper mesh for investigation of the temperature distribution and heat transfer. The relative errors of temperature distribution and heat transfer for each mesh are acquired in accordance with linear finite element (FEM 3), square finite element (FEM 6), cubic finite element (FEM 10), and finite difference method (FDM). It has been found that FEM 10 is the most accurate measure to obtain the temperature distribution and heat transfer. However, no significant results have been obtained successfully, because when higher order finite element methods are used the more computational efforts are necessary due to the distribution of elements. The results of this study are as follows ; 1 . In case of a=b=L, meshes for less than $1\%$ relative errors (temperature distribution) acquired in various methods to exact solution are $2\times2,\;4\times4,\;8\times8\;and\;8\tiems8$ for each FEM 10, FEM 6, FEM 3 and FDM and a=L, b=1/2L are $10\times5$ for each FEM 3 and FDM. And the tendency of results acquired of heat transfer is similar to those above. 2 . In computational efforts (a=b=L), FEM 6 has taken 21 times. and FEM 10 154times FEM 3 and FDM and FEM 3 is the sane as FDM.

• 대한기계학회논문집B
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• 제28권10호
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• pp.1139-1146
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• 2004

The effect of triangular tabs attached at the perimeter of jet nozzle on heat transfer enhancement was investigated experimentally. The modified flow structure was visualized using a smoke-wire method. Four different types of jet nozzle having 0, 4, 6 and 8 tabs were tested at jet Reynolds number Re=15,000 to investigate the effect of tabs on the variation of heat transfer rate. The local and average Nusselt numbers are increased with increasing the number of tabs. At nozzle-to-plate distance of L/D=4, the average Nusselt number was increased about 9.9% at Re=15,000 in the impingement region for the case of 8 tabs attachment. As the nozzle-to-plate distance increases, however, the heat transfer enhancement effect of triangular tabs is reduced. For the case of 4 tabs, the heat transfer enhancement is not so distinctive at L/D=8. As the protrusion depth of tabs into the jet flow increases, the heat transfer rate is also enhanced when the nozzle-to-plate distance is smaller than L/D=6.

• 대한기계학회논문집B
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• 제29권2호
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• pp.287-293
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• 2005

In the present study, to determine the flow rate of droplets supplied to heat transfer surface after (j-1)th rebound, $D_X[j{\ge}2]^{\ast}$, it was assumed that the rebound droplets are distributed according to the Gaussian distribution from 0 to L, in which the flight distance L is determined by maximum flight distance $L_{max}$. We also assumed that $L_{max}$ is dependent on the air flow velocity and mean size of droplets. The local heat flux of a dilute spray in high temperature region was predicted using the newly evaluated $D_X[j{\ge}2]^{\ast}$. In addition, the predicted results by the present model were compared with the existing experimental data.

• Applied Biological Chemistry
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• 제17권2호
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• pp.143-148
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• 1974

Aflatoxin $B_1$은 전자수용성(電子受容性)을 높여주는 염화아연(鹽化亞鉛) 존재하(存在下)에서 전자공여성분자(電子供與性分子)인 Benzene과 Charge-transfer Complex를 만들며, 그 생성기구(生成機構)는 Aflatoxin $B_1$이 염화아연(鹽化亞鉛)과 일차적(一次的)으로 배위결합(配位結合)된 화합물(化合物)을 거쳐, 이것이 Benzene과 결합(結合)하여 착물(錯物)을 형성(形成)한다. 이 착물(錯物)의 안정도상수(安定度常數) 즉(卽) 평형상수(平衡常數) 0.198 l/mole이었다. 따라서 Aflatoxin $B_1$은 약(弱)한 전자수용체(電子受容體)이나, Benzene 보다 강(强)한 전자공여체(電子供與體)와는 염화아연(鹽化亞鉛)이 존재(存在)하지 않아도 Charge-transfer Complex를 만들 수 있다는 가능성(可能性)을 제시(提示)해 주는 것이며, Tryptophane, Histidine과 같은 강(强)한 전자공여체(電子供與體)를 함유(含有)한 단백질(蛋白質) 또는 Guanine, Adenine과 같은 전자공여체(電子供與體)를 함유(含有)한 DNA등(等)과의 Aflatoxin $B_1$의 결합(結合)은 그 결합(結合) Mechanism으로서 Charge-transfer Complex 형성(形成)으로 이루어진다는 추정(推定)을 할 수 있다.