• 충청수학회지
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• 제5권1호
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• pp.151-157
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• 1992

The objective of this paper is to study two dimensional waves on the interface between two immiscible, invicid and incompressible fluid bounded by two rigid varing boundaries when gravity and surface tension appear. By using unfied asymptotic method, a K-dV equation with higher order terms from which many model equations for the fluid domain can be obtained, is derived.

• 한국의류산업학회지
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• 제9권1호
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• pp.113-118
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• 2007

It is well recognized that the wicking of liquids in a textile fabric takes place mainly through a capillary system composed of the individual fibers. Considering typical dyeing stages, it is thought that a high dye uptake on the fabric probably depends on the wickability. Three kinds of barely water soluble ketones, acetophenone(A), 2-pentanone(2P) and 3-pentanone(3P) were separately dissolved in methanol(M) and then each was mixed with aqueous solution of C. I. Red Acid 114. Wicking heights of dyeing solutions were measured under such conditions that the effect of gravity was negligible. The result could be graphed as a series of straight lines having the form s = $kt^{1/2}$, where s was distance traveled by the solutions, t was time, and k was slope of the line. The surface tension(${\gamma}$) of the ketones had more signifcant effect on the wickability compared to the viscosity(${\eta}$) of them. The greater wickability resulted in the higher dye uptake on the fabric and the order of wickabilty was equal to that of the surface tension(${\gamma}$) and dye uptake on the fabric, A>3P>2P>M.

• 대한기계학회논문집A
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• 제31권9호
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• pp.910-914
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• 2007

We present a simple and an inexpensive method for the fabrication of a nano-fluidic filter and a nano-pore micromixer using self-assembly of nano-spheres and surface tension. Colloid-plug was formed by surface tension of liquid in a microchannel to fabricate nanofluidic filter. When colloid is evaporated, nano-spheres in a colloid are orderly stacked by a capillary force. Orderly stacked nano-spheres form 3-D nano-mesh which can be used as a mesh structure of a fluidic filter. We used silica nano-sphere whose diameter is $567{\pm}85nm$, and silicon micro-channel of $50{\mu}m$-diameter. Fabricated nano-fluidic filter in a micro-channel has median pore diameter of 158nm which was in agreement with expected diameter of the nano-pore of $128{\pm}19nm$. A nano-pore micromixer consists of $200\;{\mu}m-wide,\;100\;{\mu}m-deep$ micro-channel and self-assembled nano-spheres. In the nano-pore micromixer, two different fluids had no sooner met together than two fluids begin to mix at wide region. From the experimental study, we completely apply self-assembly of nano-spheres to nano-fluidic devices.

• 수산해양기술연구
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• 제28권2호
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• pp.164-170
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• 1992

In order to understand and explain the spary combustion, it was necessary to understand the disintegration mechanisms of liquid jet. To understand the disintegration mechanisms of liquid jet, the disintegration phenomena and uniform droplet production regions of testing liquid jet was investigated by means of longitudinally vibration capillary nozzle, which was injected the testing liquids. The testing liquids were light oil and light oil and light oil blended with 25wt% fish oil (File fish oil, Sardine fish oil, Alaska pollac oil) The results can be summarized as follows: 1. The uniform droplet phenomena have been changed according to the frequency of capillary tube, the jet velocity and physical properties of testing oils. 2. Within the region of uniform droplet, Reynold number was increased as Weber number increases. 3. The lower limit of wave length in which uniform droplet was produced 0.8d which was lower than Rayleigh wave length 4. The light oil blended with file fish oil which has lower viscosity and surface tension had the widest uniform droplet production region on the frequency and velocity among testing oils. But light oil blended with sardine fish oil were similar with light oil in the uniform production region.

• 대한기계학회논문집B
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• 제28권12호
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• pp.1521-1527
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• 2004

Thermocapillary migration of a liquid slug is caused by temperature difference between the ends of a slug. The temperature difference induces the difference of the surface tension coefficient and consequently of capillary pressure between the ends of the slug. Presently available model to predict a velocity of thermocapillary migration adopts the Poiseuille equation which is valid only for a very long slug and neglects the shear stress near the contact line. In the present study, a new model has been developed to consider the shear stress near the contact line so that it can be applied to slugs or drops of general configuration. The experiments using mineral oil with the length to diameter ratio being 10 and a glass capillary were performed. It was found that the liquid slug began to move upon overcoming contact angle hysteresis when the temperature difference reached 35$^{\circ}C$. The results indicate that the new model well predicts the velocity of the liquid slug.

• Fibers and Polymers
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• 제6권2호
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• pp.131-138
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• 2005

A theoretical model is proposed in order to investigate rheological behavior of bubble suspension with large deformation. Theoretical constitutive equations for dilute bubble suspensions are derived by applying a deformation theory of ellipsoidal droplet [1] to a phenomenological suspension theory [2]. The rate of deformation tensor within the bubble and the time evolution of interface tensor are predicted by applying the proposed constitutive equations, which have two free fitting parameters. The transient and steady rheological properties of dilute bubble suspensions are studied for several capillary numbers (Ca) under simple shear flow and uniaxial elongational flow fields. The retraction force of the bubble caused by the interfacial tension increases as bubbles undergo deformation. The transient and steady relative viscosity decreases as Ca increases. The normal stress difference (NSD) under the simple shear has the largest value when Ca is around 1 and the ratio Of the first NSD to the second NSD has the value of 3/4 for large Ca but 2 for small Ca. In the uniaxial elongational flow, the elongational viscosity is three times as large as the shear viscosity like the Newtonian fluid.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2012년도 제38회 춘계학술대회논문집
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• pp.416-423
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• 2012

액체추진제 공급시스템의 액체포집장치는 추진기관으로 기포가 유입되는 것을 방지하는데 사용한다. 액체포집장치는 차단막의 미세 구멍의 모세관 효과를 이용하여 추진기관에 순수 액체만을 공급한다. 기포점은 액체포집장치의 설계에서 가장 중요한 설계변수이다. 본 논문에서는 문헌조사를 통해 액체포집장치의 성능에 영향을 미치는 변수들을 식별하고 기포점 측정 시험 장치를 구성하였다.

• 대한화학회지
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• 제16권6호
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• pp.341-348
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• 1972

질소의 흡착 등온곡선을 이용하여 흡착체의 동공부피 분포를 계산하는 과정에서 표면장력의 곡률 의존도 고려 효과를 조사하였다. 즉, 장세헌 등에 의한 표면장력의 곡률 의존도식과 캘빈 식으로부터 주어진 압력에서의 캘빈반경을 구하고, 이것으로부터 흡착체의 동공부피 분포를 계산하였다. 이와 같이하여 얻은 계산 결과를 표면장력의 곡률 의존도를 고려하지 아니한 종래방법에 의한 계산 결과와 비교하였다. 일반적으로 곡률 의존도를 고려해주면 동공부피 분포 곡선의 극대부분이 큰 동공 쪽으로 이동한다. 또한 모세관 응축이 일어나는 상대압력이 종래까지 생각했던 것보다 훨씬 낮아지고 있다. 이러한 효과들은 흡착체의 동공들이 미세해 질수록 더욱 현저하게 일어난다.

• 한국안광학회지
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• 제7권2호
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• pp.1-11
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• 2002

눈물 층을 사이에 두고 각막 위에 부착되어 있는 콘택트 렌즈(하드렌즈)에는 모세관 현상에 따른 장력이 렌즈 가장 자리에 균일하게 방사형으로 작용한다. 이러한 장력은 렌즈가 각막에 부착되는 힘의 근원이 된다. 렌즈착용 시 자체 무게에 의한 렌즈의 회전과 렌즈가 평형상태에 도달 한 후 각막에 부착되는 힘을 계산할 수 있는 방정식과 이의 수치 계산 컴퓨터 프로그램을 수립하였으며 이 컴퓨터 모델을 사용하여 렌즈 구경, 렌즈 B.C, 눈물의 점성, 눈물 층의 두께 등의 변수가 렌즈의 평형 위치 및 부착력에 미치는 영향을 모사(simulation)하였다. 일정 각막 B.C에서 렌즈 B.C 증가에 따라 눈물 충의 간격은 급격히 증가하는데 비해 렌즈의 직경 증가는 완만한 간격 증가를 수반한다. 렌즈의 B.C가 증가할수록, 즉 렌즈의 곡률이 완만할수록, 렌즈가 각막에 fitting되는 부착력은 급격하게 감소하며 직경 감소는 완만한 부착력 감소를 초래한다. 렌즈가 각막에 부착되는 순간 렌즈의 무게로 인하여 아래 방향으로의 회전 모멘트가 발생하게 되며 이와 동시에 렌즈 위 부분 눈물 층의 간격이 아래 부분보다 좁아지게 되어 위 방향으로 알짜 힘이 작용하게 되며 이에 따른 역방향 모멘트는 중력에 의한 모멘트를 상쇄하게 되어 렌즈는 일정 위치에서 평형 상태에 도달하게 된다. 렌즈 착용에 수반되는 초기 회전각 또는 회전 변위는 렌즈의 B.C가 증가할수록 급격히 증가하는데 비해 렌즈 구경 증가는 변위 증가율이 완만하다.

• 대한기계학회논문집A
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• 제27권5호
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• pp.657-665
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• 2003

Several interesting results were obtained from the flow visualization experiment in the accompanying paper, Part I. in the present study, Part II, a numerical study has been carried out to explain the detailed flow phenomena in micro-channel filling process. Hele-Shaw flow approximation was applied to the micro-channel geometry based on the small characteristic length. And surface tension effect has been introduced on the flow front as the boundary condition with the help of a dynamic contact angle concept between the melt front and the wall. A dimensional analysis for numerical results was carried out and a strong relationship between dimensionless pressure and Capillary number is obtained. The numerical analysis results are compared with the flow visualization experimental observations. And the numerical system developed in the present study seems to be able to predict the interesting micro-channel filling flow characteristics observed from experiments.