• 한국전산유체공학회:학술대회논문집
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• 한국전산유체공학회 2010년 춘계학술대회논문집
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• pp.473-478
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• 2010

In this study, the Ergun's equation has been verified in order to calculate pressure drop of the two phase flow. The equation had been used in the high Reynolds number region for interior ballistic analysis in spite of being verified in the low Reynolds number region. Therefore additional verification seems to be inevitable. Thus, the validity of the equation has been verified using CFD in the high Reynolds number cases of the diameter-particle ratio 10, 13 and 16.

• 한국전산유체공학회지
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• 제16권2호
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• pp.62-65
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• 2011

Characteristics of the pressure drop in an expanded bed have been compared to those in a packed bed for numerical study of the interphase drag in gas-particle flows. A numerical analysis of the pressure drop by the particle drag has been conducted according to the tube-to-particle diameter ratios and Reynolds numbers for comparison. As the tube-to-particle diameter ratios increase at the same Reynolds number, the pressure drop tends to converge. It has been confirmed that characteristics of the pressure drop in the expanded bed are similar to those in the packed bed.

• 대한설비공학회지:설비저널
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• 제13권3호
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• pp.168-182
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• 1984

For the purpose of drying high moisture rough rice effectively, from the view point of pre-drying, some basic experiments of fluidized bed drying of rough rice were carried out. The minimum fluidization velocities $(U_{mf})$ for both rough rice and glass bead were analyzed to find out fluidizing characteristics. The main results obtained were as follows ; 1) Minimum fluidization velocity of rough rice and glass bead were 2.01m/s and 4.07m/s, respectively, when using the distributor with $16\%$ opening ratio. 2) $U_{mf}$ calculated by Shirai's empirical equation and that calculated by Wen's modified equation were inconsistent with experimental data, while $U_{mf}$ calculated by Ergun's equation was consistent with the experimental data. 3) The following equations, on the basis of Leva's equation, were obtained. $$C_{mf}=1.19\times10^{-4}(Re_p)^{-0.0318)\;(rough rice)$$ $$C_{mf}=1.02imes10^{-4}(Re_p)^{-0.0047)\;(glass bead)$$

• 태양에너지
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• 제12권2호
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• pp.43-50
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• 1992

공기(空氣)가 통과(通過)하는 소결금속(燒結金屬)에서의 압력손실(壓力損失)에 대한 기초(基礎) 지식(知識)을 얻기 위하여 실험적(實驗的)으로 연구(硏究)를 수행(遂行)하여, 소결금속(燒結金屬)의 공극율(空隙率)과 소결금속(燒結金屬)을 통과(通過)하는 공기(空氣)의 유속(流速)이 압력손실(壓力損失)에 미치는 영향(影響)을 고찰(考察)하고, 또 본(本) 실험(實驗) 결과(結果)를 비소결금속(非燒結金屬)에서의 압력손실(壓力損失)에 대한 대표적(代表的)인 Ergun의 식(式)과 마찰계수(摩擦係數)의 관점(觀點)에서 비교(比較)하였다. 본(本) 연구결과(硏究結果), 소결금속(燒結金屬)에서의 압력손실(壓力損失)은 유속(流速)이 증가(增加)할 수록 증대(增大)하며, 또 동일 유속(流速)에서는 공극율(空隙率)이 감소(減少)(입자직경(粒子直徑)이 감소(減少))할 수록 증대(增大)한다. 특히 본(本) 실험(實驗) 결과(結果)를 소결금속(燒結金屬)의 두께와 직경(直徑) 및 입자직경(粒子直徑)의 무차원수(無次元數)들로 표현되는 무차원(無次元) 실험식(實驗式)으로 유도(誘導)하였으며, 이 실험식(實驗式)은 본(本) 연구결과(硏究結果)와 ${\pm}15%$ 범위에서 일치하고 있다.

• 한국전산유체공학회:학술대회논문집
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• 한국전산유체공학회 2011년 춘계학술대회논문집
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• pp.41-45
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• 2011

Pressure drops of two-phase flow in a pipe according to particle shapes have been calculated and analyzed. The numerical analysis for 3 cases of Reynolds number has been conducted for each particle shape. In case of the cylinder shape, the particles had been assumed to be randomly distributed for each Reynolds number. The results have been averaged and compared to those of the case of the ball shape. Additionally, pressure drops of ball and cylinder shapes has been compared to the result of Ergun's equation.

• 한국전산유체공학회:학술대회논문집
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• 한국전산유체공학회 2009년 춘계학술대회논문집
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• pp.310-314
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• 2009

A numerical code for the interior ballistics has been investigated. The method of the ghost cell extrapolation has been used for the moving boundary with the projectile movement. The porosity effect and the Ergun's Equation have been used in the numerical calculation for the grain combustion. The calculation results of the numerical code have been compared and verified through those of the lumped parameter method. Computerization techniques of the numerical analysis for the interior ballistics have been developed.

• 한국산업융합학회 논문집
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• 제24권5호
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• pp.573-579
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• 2021

In this study, flow analysis was performed on three types of strainers for ships with different flow rates to predict the pressure drop of the strainer due to the filter of strainer. In the case of flow analysis, the flow analysis was performed by applying the porous media method by applying the resistance value derived by Ergun's equation to the filter position. As a result of the analysis, it was found that when the dimensions of the strainer body were small, the influence of the flow rate on the pressure drop was large. In addition, the amount of pressure drop and the flow rate are almost linearly proportional, and an analysis formula that can predict the amount of pressure drop was derived. In order to predict the amount of pressure drop of the strainer when blockage exist in the strainer filter, the analysis was performed by introducing the resistance ratio to derive the prediction equation. Using this equation, it is thought that it will be possible to predict the performance of the strainer due to blockage in the future strainer design and field application.

• 태양에너지
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• 제6권1호
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• pp.3-11
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• 1986

Minimum fludizing velocities and voidages were investigated for closely sized sand and magnesia particles with mean diameters in the range of $297-841\;{\mu}m$ over the temperature between 15 and $1.000^{\circ}C$. Boundaries between changing behaviour at $Re_{mf}=14$ and Ar=17,000 were observed. In beds of fine particles in Geldart's group "B", the minimum fluidizing velocity ($U_{mf}$) decreased as temperature increased, but not as much as expected on account of the gas viscosity increase, furthermore the increase in the minimum fluidizing voidage (${\in}_{mf}$). With larger particles in group "D", $U_{mf}$ increased, first, with temperature increase because of reduced gas density, and depending on the particle size, $U_{mf}$ reduced as flow conditions moved from turbulent to laminar. Among the correlations predicting $U_{mf}$, Ergun equation agreed best with the experimental data providing that the change in ${\in}_{mf}$ according to temperature is allowed for.

• 한국기계가공학회지
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• 제18권8호
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• pp.82-90
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• 2019

We propose an equivalent model of a sintered metal mesh filter calculated by Ergun's equation and polynomial regression for the CFD analysis of breakaway devices at a hydrogen fueling station. CFD analysis of filters that cause high pressure loss is essential because breakaway devices in high-pressure hydrogen conditions require low pressure loss. A differential pressure experiment with a filter was performed in a low-pressure air condition considering similarities. An equivalent model was developed by deriving the resistance value by the polynomial regression using the experimental results. The results of CFD analysis using the equivalent model show that there was almost no error in the operating condition of the breakaway device compared to the experimental results. Through this work, we believe that the proposed equivalent model of a filter can be applied to the analysis of breakaway devices in hydrogen fueling stations. We will study how to optimize the shape and position of the filter in breakaway devices using the developed equivalent model.

• 대한토목학회논문집
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• 제13권3호
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• pp.93-105
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• 1993

본(本) 연구(硏究)에서 24개의 국부세굴공식(局部洗掘公式)을 이용(利用)하여 금강수계내(錦江水系內) 보청천(報靑川)에서의 교각설치(橋脚設置)에 따른 국부(局部) 세굴심도(洗掘深度)를 산정(算定)하여 서로 비교(比較) 하였는 바, 이때 24개의 국부세굴공식(局部洗掘公式)들은 무차원화(無次元化)된 공식(公式) 형태(形態)에 따라 6개의 그룹으로 구분(區分)되었다. 국부(局部) 세굴공식(洗掘公式) 적용자료(適用資料)로는 금강수계내(錦江水系內) IHP 대표측정지점(代表測定地點)인 산성, 이평, 산계 지점(地點)에 설치(設置)된 교량자료(橋梁資料)들과 실측(實測)된 하상자료(河床資料)들을 이용하였다. 하상자료(河床資料)들은 교량설치지점(橋梁設置地點)의 유향방향(流向方向)으로 좌안, 중앙부, 우안의 대표지점(代表地點)으로부터 시료(試料)를 채취(採取)하여 체가름 분석(分析)을 실시(實施)한 결과(結果)를 사용(使用)하였으며, 수리학적(水理學的) 자료(資料)로는 1982년(年)부터 1991년(年)까지 IHP 자료(資料)로 관측(觀測)된 최대(最大) 홍수위(洪水位) 및 최대(最大) 홍수위(洪水位)일때의 유속(流速)을 이용(利用)하였으며 교각자료(橋脚資料)들은 현장(現場)에서 실측(實測)된 자료(資料)를 이용(利用)하였다. 또한, 추후 보청천내(報靑川內) 교각(橋脚) 설치(設置)에 따른 국부(局部) 세굴(洗掘)을 검토(檢討)하기 위한 적절(適切)한 세굴공식(洗掘公式)을 제안(提案)하기 위하여 보청천(報靑川)과 흐름조건(條件)이 유사(類似)한 하천(河川)에서 실측(實測)된 129개의 국부세굴자료(局部洗掘資料)와 비교(比較)하였으며, 이를 통하여 Arunachalam 공식(公式), Shen-Karaki III 공식(公式), Jain-Fischer 공식(公式)이 보청천내(報靑川內) 세굴심도(洗掘深度) 산정(算定)을 위하여 비교적(比較的) 적절(適切)한 공식(公式)으로 판단(判斷)되었다. 또한 Inglis-Lacey 공식(公式)과 Shen-Karaki II 공식(公式)은 Fr의 수(數)가 0.3 이상인 비교적(比較的) 빠른 흐름에서 적용(適用)이 가능(可能)하며, Froehlich 공식(公式), Laursen I 공식(公式), Laursen II 공식(公式), Neill 공식(公式), Melville 공식등(公式等)은 Fr의 수(數)가 0.3 이하의 비교적(比較的) 느린 흐름에서 적용(適用)이 가능(可能)하고, Blench 공식(公式)이나 Inglis-Poona 공식(公式)은 Froude 수(數)에 따라 변화(變化)가 상당히 커서 적용(適用)하지 않는 것이 바람직한 것으로 판단(判斷)되었다. 또한 Sarma-Krishnamurthy 공식(公式), Ahmad 공식(公式), Coleman 공식(公式), Varzeliotis 공식(公式), Larras 공식(公式), Bata 공식(公式), Chitale 공식(公式), Venkatadri 공식(公式), Basik-Basamily-Ergun 공식(公式), U.S.G.S. 공식(公式), Shen I 공식(公式)들은 실측(實測)된 국부(局部) 세굴심도(洗掘深度)에 비하여 지나치게 적게 세굴심도(洗掘深度)를 산출(算出)하는 것으로 나타났다.