• 한국지반공학회논문집
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• 제23권11호
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• pp.59-66
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• 2007

자갈혼합재료의 역학특성에 미치는 자갈혼합율의 영향을 분석하기 위하여 화강풍화토를 이용한 대형 일차원압축시험을 실시하였다. 본 연구에서는 일본 야마구치현(山口縣) 시모노세키시(下關市)에서 채취한 화강풍화토를 이용해 입도를 조절한 후 일정한 다짐에너지로 다짐한 공시체를 시험에 사용하였다. 시험결과, 동일한 함수비에서 동일한 다짐에너지로 다짐을 실시하여도 자갈혼합율에 따라 서로 다른 건조밀도를 보였고, 이로부터 최대건조밀도를 나타내는 자갈혼합율이 존재하는 것과 이 자갈혼합율에서 최소의 압축지수를 보이는 것을 확인하였다. 또한 본 연구에서는 이상혼합체이론(two-phase mixture theory)을 이용해 자갈혼합율의 영향을 정량적으로 평가할 수 있는 방법을 제안하였고, 제안한 방법을 통해 산정한 초기건조밀도와 재료정수는 실내시험으로부터 얻은 실측값을 정확히 추정하는 것으로 평가되었다.

• Bulletin of the Korean Chemical Society
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• 제15권1호
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• pp.45-52
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• 1994

We present a theoretical study of the non-symmetrical A/BC polymeric system. The polymer blends consist of two phases, a pure polymeric phase A on one side and a mixture of polymers B as a compatibilizer and C on the other. The adsorption of homopolymer B to the interface improves the interfacial adhesion between two phases. By employing the functional integral techniques, we derive the mean-field equations and solve them numerically to obtain the interfacial properties including the concentration profiles in the limit of infinite molecular weight for the polymers. Thecalculations of the interfacial properties are performed for typical values of the Flory X parameters and the volume fraction of polymer B in the asymptotic mixture phase. The interfacial adsorption of polymer B and the degrees of the specific interaction between the polymers play an important role in modification of the interfacial properties.

• 대한기계학회논문집
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• 제6권4호
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• pp.331-340
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• 1982

Numerical analysis is made on the turbulent heat transfer with suspension of solid particles in circular tube with constant heat flux. The mean motion of suspending particles in mixture is treated as the secondary gas flow with virtual density and viscosity. Our modeling of turbulent transport phenomena of suspension flow is based on this assumption and conventional mixing length theory. This paper gives the evidence that the mixing length models can be extended to close the governing equations for two phase turbulent flow with solid boundary at a first order level. Results on Nusselt numbers obtained by analytical treatments are compared with available experimental data and discussed. They suggest that the most important parameters of two phase turbulent heat transfer phenomena are relative particle diameter to pipe diameter, gas-solid loading ratio, and specific heat of suspending material.

• International Journal of Air-Conditioning and Refrigeration
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• 제13권1호
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• pp.51-60
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• 2005

This paper reviews the studies on the pressure drop and the heat transfer in microchannels. Although a lot of studies about the single-phase flow have been done until now, conflicting results are occasionally reported about flow transition from laminar flow to turbulent flow, friction factor, and Nusselt number. Some studies reported the early flow transition due to relatively greater wall effect like surface roughness, but the other studies showed that the flow transition occurred at the Reynolds number of about 2300 and the early flow transition might be due to less accurate measurement of the channel geometry. Also, there have been arguments whether the conventional relation based upon continuum theory can be applied to the fluid flow and the heat transfer in microchannels without modification or not. The studies about the two-phase flow in microchannels have been mostly about investigating the flow pattern and the pressure drop in rectangular channels using two-component, two-phase flow like air/water mixture. Some studies proposed correlations to predict two-phase flow pressure drop in microchannels. They were mostly based on Lockhart-Martinelli model with modification on C-coefficient, which was dependent on channel geometry, Reynolds number, surface tension, and so on. Others investigated the characteristics of flow boiling heat transfer in microchannels with respect to test parameters such as mass flux, heat flux, system pressure, and so on. The existing studies have not been fully satisfactory in providing consistent results about the pressure drop and the heat transfer in microchannels. Therefore, more in-depth studies should be done for understanding the fundamentals of the transport phenomena in the microchannels and giving the basic guidelines to design the micro devices.

• 공업화학
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• 제10권2호
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• pp.324-329
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• 1999

본 연구에서는 고압하에서 이산화탄소와 이소프로필 알코올과의 이성분계에 대한 상평형데이터를 얻기 위해 실험을 수행하였다. 실험장치는 정지형 (static type)을 사용하였으며, 정확도를 실험하기 위해 $80^{\circ}C$에서 이산화탄소-이소프로필 알코올계의 실험을 수행하여 Radosz의 실험결과와 비교하였다. 이산화탄소-이소프로필 알코올과의 이성분계 상거동 실험은 온도 40, 60, 80, 100, 그리고 $120^{\circ}C$에서 실험하였으며, 이때 압력은 41~133 bar 범위였다. 이산화탄소-이소프로필 알코올계에 대해 동일한 압력에서 용해도는 온도가 증가함에 따라 증가함을 알 수 있다. 또한 순성분 이산화탄소와 이소프로필 알코올의 증기압을 서로 연결하는 혼합물 임계곡선을 나타내었다. 본 연구에서 실험한 결과를 statistical associating fluid theory (SAFT)상태방정식에 의해 계산하였으며, 그 결과 온도에 독립적인 두 파라미터에 의해 곡선을 결정하였다.

• 대한기계학회논문집B
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• 제20권10호
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• pp.3361-3370
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• 1996

Micro-Macro approach is conducted for the mixture solidification to handle the closely linked phenomena of microscopic solute redistribution and macroscopic solidification behavior. For this purpose, present work combines the efficiency of mixture theory for macro part and the capability of microscopic analysis of two-phase model for micro part. The micro part of present study is verified by comparison with experiment of Al-4.9 mass% Cu alloy. The effect of back diffusion on the macroscopic variables such as temperature and liquid concentration, is appreciable. The effect, however, is considerable on the mixture concentration and eutectic fraction which are indices of macro and micro segregation, respectively. According to the diffusion time, the behavior near the cooling wall where relatively rapid solidification permits short solutal diffusion time, approaches Scheil equation limit and inner part approaches lever rule limit.

• Ocean Systems Engineering
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• 제12권1호
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• pp.63-86
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• 2022

A refined projection-based purely Lagrangian meshfree method is presented towards reliable numerical analysis of fluid flow interactions with saturated/unsaturated porous media of uniform/spatially-varying porosities. The governing equations are reformulated on the basis of two-phase mixture theory with incorporation of volume fraction. These principal equations of mixture are discretized in the context of Incompressible SPH (Smoothed Particle Hydrodynamics) method. Associated with the consideration of governing equations of mixture, a new term arises in the source term of PPE (Poisson Pressure Equation), resulting in modified source term. The linear and nonlinear force terms are included in momentum equation to represent the resistance from porous media. Volume increase of fluid particles are taken into consideration on account of the presence of porous media, and hence multi-resolution ISPH framework is also incorporated. The stability and accuracy of the proposed method are thoroughly examined by reproducing several numerical examples including the interactions between fluid flow and saturated/unsaturated porous media of uniform/spatially-varying porosities. The method shows continuous pressure field, smooth variations of particle volumes and regular distributions of particles at the interface between fluid and porous media.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2929-2934
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• 2007

Prediction methods for cavitation noise are presented. At first, direct numerical simulation of cavitating flow noise has been performed, and acoustic analogy equation based on the cavitation noise modeling is derived. For the direct numerical simulation, a density based homogenous equilibrium model is employed to simulate cavitating two-phase flow and the governing equations are solved with high-order numerical schemes to resolve cavitation noise. The compressible Navier-Stokes equations for mixture fluids are discretized with a sixth-order central compact scheme, and the steep gradient of flow variables and supersonic regions are treated with the selective spatial filtering technique. The direct simulation of cavitating flow noise is performed for a 2D circular cylinder at cavitation number 0.7 and 1. The far-field noise is also predicted with the derived analogy equation. Noise spectrum predicted with the equation is well compared with the result of direct numerical simulation and also agree well with the theory.

• 한국수자원학회:학술대회논문집
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• 한국수자원학회 2017년도 학술발표회
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• pp.292-292
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• 2017

하천에서 주로 부유사의 형태로 이송되는 유사는 크게 점착성 유사와 비점착성 유사로 구분된다. 입자의 크기가 약 $63{\mu}m$이하인 유사는 입자 표면의 전자기적 점착력의 영향이 우세하여 유사입자들은 지속적인 응집현상을 겪는다. 응집 현상을 통해 유사의 가장 단위인 일차입자(Primary Particle)들은 하나의 커다란 덩어리인 플럭(Floc)을 형성한다. 응집현상이 중요한 이유는 형성된 플럭의 크기 및 밀도가 끊임없이 변화하는 데 있다. 크기와 밀도의 지속적인 변화로 인하여 유사의 부유에 직접적으로 관계하는 침강속도가 변화한다. 우리나라의 금강 및 낙동강의 하구는 점착성 유사가 지배적인 환경으로, 하구에서의 유사 이동을 살펴보기 위해서는 흐름 방향 및 연직방향으로의 흐름 특성(Hydrodynamics)변화와 응집 모형을 통한 응집 현상의 고려가 필수적이다. 이에따라, 본 연구에서는 흐름 방향 및 연직방향으로의 2차원 점착성 유사 이동모형에 관한 개념적 틀(Framework)을 제시한다. 2차원 점착성 유사 이동 모형의 개념적 틀은 기존의 1차원 연직 점착성 유사 이동 모형을 근간으로 한다. 모형에서 흐름을 구성하는 지배 방정식은 오일러-오일러 이상방정식(Eulerian-Eulerian Two-Phase Equation)을 통해 얻는다. 유사상(Sediment Phase, Dispersed Phase)와 유체상(Fluid Phase, Continuous Phase)는 혼합물 이론(Mxiture Theory)를 통해 하나의 혼합물 상(Mixture Phase)의 지배방정식으로 대표된다. 난류의 계산은 와점성 모형 중 -${\varepsilon}$모형을 통해 수행되며, 부유사의 농도는 유사의 이송-확산 방정식을 통해 모의된다. 입력된 흐름 조건을 따라 초기 흐름이 모의되면, 유체 내에서 시간에 따른 플럭의 크기가 계산된다. 플럭의 크기가 계산되는 과정에서 밀도와 침강 속도가 계산되며, 그 이후에 유체 내 유사의 농도가 계산된다. 난류 모의가 수행되고 난 이후에, 유속이 재계산 된다. 이러한 과정을 통해 흐름 방향 및 연직 방향으로의 유사 이동 모의가 가능한 2차원 점착성 유사 이동 모형이 개발될 수 있을 것이라고 생각된다.

• 한국분말야금학회:학술대회논문집
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• 한국분말야금학회 1999년도 춘계학술대회 및 발표대회 강연 및 발표논문 초록집
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• pp.5-5
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• 1999

The Principal deficiency of the existing notion about the sintering-mixtures consists in the fact that almost no attention is focused on the Phenomenon of alloy formation during sintering, its connection with dimensional changes of powder bodies, and no correct ideas on the driving force for the sintering process in the stage of establishing chemical equilibrium in a system are available as well. Another disadvantage of the classical sintering theory is an erroneous conception on the dissolution mechanism of solid in liquid. The two-particle model widely used in the literature to describe the sintering phenomenon in solid state disregards the nature of the neighbouring surrounding particles, the presence of pores between them, and the rise of so called arch effect. In this presentation, new basic scientific principles of the driving forces for the sintering process of a two-component powder body, of a diffusion mechanism of the interaction between solid and liquid phases, of stresses and deformation arising in the diffusion zone have been developed. The major driving force for sintering the mixture from components capable of forming solid solutions and intermetallic compounds is attributed to the alloy formation rather than the reduction of the free surface area until the chemical equilibrium is achieved in a system. The lecture considers a multiparticle model of the mixed powder-body and the nature of its volume changes during solid-state and liquid-phase sintering. It explains the discovered S-and V-type concentration dependencies of the change in the compact volume during solid-state sintering. It is supposed in the literature that the dissolution of solid in liquid is realised due to the removal of atoms from the surface of the solid phase into the melt and then their diffusicn transfer from the solid-liquid interface into the bulk of liquid. It has been shown in our experimental studies that the mechanism of the interaction between two components, one of them being liquid, consist in diffusion of the solvent atoms from the liquid into the solid phase until the concentration of solid solutions or an intermetallic compound in the surface layer enables them to pass into the liquid by means of melting. The lecture discusses peculimities of liquid phase formation in systems with intermediate compounds and the role of the liquid phase in bringing about the exothermic effect. At the frist stage of liquid phase sintering the diffusion of atoms from the melt into the solid causes the powder body to grow. At the second stage the diminution of particles in size as a result of their dissolution in the liquid draws their centres closer to each other and makes the compact to shrink Analytical equations were derived to describe quantitatively the porosity and volume changes of compacts as a result of alloy formation during liquid phase sinteIing. Selection criteria for an additive, its concentration and the temperature regime of sintering to control the density the structure of sintered alloys are given.