• 대한기계학회논문집B
• /
• 제37권1호
• /
• pp.9-18
• /
• 2013

이상 횡 유동은 응축기, 증발기와 원자로 증기발생기와 같은 쉘과 튜브의 열 교환기에서 볼 수 있다. 이상 유동장에 놓인 구조물에 작용하는 수동력을 이해하기 위해서는 이상유동의 특성을 이해하는 것이 중요하다. 이상 유동의 유동특성과 유동변수를 소개하고 관군에서의 압력손실과 실린더에 작용하는 압력분포에 의한 수동력을 평가하기 위한 실험을 수행하였다, 실험부 입구에서 이상유동은 혼합되었으며 실험은 횡 방향 이상 유동장에 놓인 정규 삼각형 배열을 갖는 관군을 사용하여 수행하였다. 관군에서의 흐름방향 압력손실을 측정하여 이상유동의 마찰승수를 계산하고 이론적 결과와 비교하였다. 또한 특정 실린더에 작용하는 원주 방향 압력 분포의 측정결과와 이상유동의 기초이론에 근거하여 압력손실계수의 분포 및 항력계수에 미치는 체적건도와 단위면적당 질량유량의 효과를 평가하였다. 튜브 표면에 작용하는 측정된 압력을 수치해석방법으로 적분하여 항력계수를 계산하였다. 작은 질량 유량의 경우에 측정된 마찰 승수는 기존의 이론 결과와 잘 일치하며 압력분포에 의한 항력계수에 작용하는 기공률의 영향은 기존의 실험결과와 정성적으로 유사한 경향을 보이고 있다.

• 대한설비공학회:학술대회논문집
• /
• 대한설비공학회 2003년도 하계학술대회 논문집
• /
• pp.115-115
• /
• 2003

• 설비공학논문집
• /
• 제17권11호
• /
• pp.1014-1021
• /
• 2005

Flow channels with non-circular cross-sections are encountered in a wide variety of heat exchangers. Accurate friction factor and Colburn j factor data are essential for the design and viable applications of such heat exchangers. In this study, an analysis is con ducted on heat transfer and pressure drop characteristics for tube-bundle heat exchanger with various arrangements of tubes, of which their geometry could easily be modified from a circular one in a harsh environment. The parameters investigated are aspect ratio, pitch, and inclined angle of tubes. The results obtained are: (1) Aspect ratio has larger influence on the j and f factor than pitch; (2) As aspect ratio increases, both j and f factors decrease; (3) The high performance is achieved when the pitch and aspect ratio are in the range of 1.5${\~}$2.5 and 1.25${\~}$2.0, respectively; and (4) the inclined arrangements of tubes show unfavorable results for both heat transfer and pressure drop characteristics in spite of the positive possibility of condensate removals in a latent heat recovery system.

• Journal of Advanced Marine Engineering and Technology
• /
• 제33권1호
• /
• pp.44-51
• /
• 2009

The Characteristics of the flowfield through tube banks with in-line and staggered arrangements were investigated by PIV. Strouhal numbers, velocity vectors and velocity profiles around the cylinders with in-line and staggered arrangements were observed at the pitch ratio Pt/D=2.0 and Reynolds number of Re=$Re=4.0{\times}10^3$. As the results The flow patterns through tube banks were almost a straight line in case of the in-line arrangement while it was almost 八 type in case of the staggered arrangement in the direction of the wake. The average velocity in the rear region of the tube banks with the staggered arrangement was far smaller than that with the in-line arrangement. The Strouhal number in the last rank was far smaller than that in the front ranks in both of the in-line and staggered arrangements. The wake of each cylinder changed with time and with the position of the cylinder.

• 대한기계학회논문집B
• /
• 제24권11호
• /
• pp.1478-1485
• /
• 2000

An experimental study has been performed to investigated the forced convection heat transfer characteristics of 6 circular cylinders in staggered arrangement in a cross flow of air. The water scale deposited on condenser wall of power plant was used to investigate the effect of roughness of scaled surfaces. The relative roughness*average diameter of scale/cylinder diameter) was in a range of k/d=0.0066, 0.0111, 0.0167, 0.0222 and 0.0278. The cylinder spacings(L/d) varies from 1.5 to 4.0 where L denote the cylinder spacings along and normal to the upstream uniform flow direction. The Reynolds number was varied in a range of 10, 000$\leq$ Re $\leq$ 50,000. The local and mean Nusselt numbers were investigated as a function of scale roughness, the cylinder spacing and Reynolds number. The results are compared with those of clean cylinder and inline tube bank, subsequently the mean fouling resistance over the entire circumference was estimated from those results as a function of scale roughness, the cylinder spacing and Reynolds number.

• 한국전산유체공학회지
• /
• 제17권3호
• /
• pp.39-44
• /
• 2012

In this study, a longitudinal pitch effect on in-line tube bank heat transfer has been analyzed numerically. To verify the accuracy of the solver model and boundary conditions, global Nusselt number(Nu) and pressure drop across the 2 row tube bank are compared with the existing experimental correlations under 500 ~ 2,000 Reynolds number(Re) range. By changing transverse pitch($S_T$) or longitudinal pitch($S_L$) separately in tube bank, we're trying to identify the each effect on heat transfer. We found that the effect of transverse pitch can be accounted for Reynolds number evaluated with maximum velocity($V_{max}$) at the smallest flow area similar to most existing correlations. Variation of the longitudinal pitch($S_L$) has a greater impact on the heat transfer compared to the transverse pitch($S_T$). Overall Nusselt number increases with larger longitudinal pitch($S_L$), however individual Nusselt number of the tube row has significant difference after the first row.

• 대한기계학회:학술대회논문집
• /
• 대한기계학회 2008년도 추계학술대회B
• /
• pp.2530-2535
• /
• 2008

The Visualizations of the flowfield through tube banks with in-line and staggered arrangements were investigated by PIV. Strouhal numbers, velocity vectors and velocity profiles around the cylinders with in-line and staggered arrangements were observed at the pitch ratio $P_t/D=2.0$ and Reynolds number of $Re=4.0{\times}10^3$. As the results The flow patterns through tube banks were almost a straight line in case of the in-line arrangement while it was almost 八 type in case of the staggered arrangement in the direction of the wake. The average velocity in the rear region of the tube banks with the staggered arrangement was far smaller than that with the in-line arrangement. The Strouhal number in the last rank was far smaller than that in the front ranks in both of the in-line and staggered arrangements. The wake of each cylinder changed with time and with the position of the cylinder.

• 한국산학기술학회논문지
• /
• 제17권6호
• /
• pp.18-25
• /
• 2016

대형 압축식 냉동기의 증발기 전열관으로는 그간 평활관이 주로 사용되어 왔으나 최근들어 비등 성능이 우수한 성형 가공관을 많이 사용하고 있다. 증발기는 관군으로 구성되고 따라서 증발기 내 위치에 따라 냉매 상태가 다르다. 특히 R-11, R-123과 같은 저압 냉매는 압력변화에 따른 포화온도 변화가 크므로 위치에 따라 포화온도가 다르게 된다. 따라서 증발기를 적절히 설계하려면 증발기 내 각 위치에서의 냉매의 상태를 적절히 예측하여야 한다. 본 연구에서는 대형 냉동기의 만액식 증발기를 모사할 수 있는 컴퓨터 프로그램을 개발하였다. 이 프로그램은 증발기를 미소 체적으로 구분하고 각 미소 체적에 적절한 관 내외측 열전달 및 압력손실 상관식을 적용하여 해석을 수행하였다. 본 프로그램을 R-123을 사용하는 T사의 만액식 증발기 해석에 적용한 결과 만족할 만한 결과를 얻었다. 이 프로그램을 이용하여 신 냉매인 R-123, R-134a를 사용하는 만액식 증발기의 해석을 수행하였고 특히 관군 세장비의 영향을 검토하였다.

• 한국작물학회지
• /
• 제29권2호
• /
• pp.128-135
• /
• 1984

Nepal에서 도입된 수도 'Gamadi' 품종은 Gamadiness 특성(구내성숙성)의 유전분석을 시도하였다. 그 결과를 요약하면 다음과 같다. 1. 본연구에 공시된 표식인자들 즉 제 I 연관군의Cl, nx, Pla, 제III연관군의 Pn, Rd, Pub, 제II, IV, V, VI, VII, VIII, IX, X, XI, XII 연관군의 각각 lg, g, Ps, gh, Hla, la, nl, bl, bc, 및 gl은 과거의 보고와 일치되는 분리비를 나타내어 이 실험에서의 유전분리가 정상적인 것이었음을 입증한다. 2. 'Gamadiness'는 2개의 우성유전자에 의하여 보족적인 작용으로 표현되어 Gamadi 9: 정상7의 분리비를 보였다. 이 2개유전자를 G-a와 G-b로 명명하였다. 3. G-a 유전자는 제Ⅸ연관군의 nl 유전자와 0.37$\pm$0.027의 조환가로 연관되어 있음을 확인하였다. 4. G-b 유전자는 제XI연관군의 bc 유전자와 0.27$\pm$0.061의 절환가로 연관되어 있음을 확인하였다.절환가로 연관되어 있음을 확인하였다.

• 대한기계학회논문집B
• /
• 제25권12호
• /
• pp.1831-1843
• /
• 2001

In this study, convective boiling tests were conducted for enhanced tube bundles. The surface geometry consists of pores and connecting gaps. Tubes with three different pore sizes (d$_{p}$ = 0.20, 0.23 and 0.27 mm) were tested using R-123 and R-l34a for the following range: 8 kg/m$^2$s G 26 kg/m$^2$s, 10 kW/m$^2$ q0 40 kW/m$^2$and 0.1 $\chi$ 0.9. The convective boiling heat transfer coefficients were strongly dependent on heat flux with negligible dependency on mass flux or quality. For the present enhanced geometry (pores and gaps), the convective effect was apparent. The gaps of the present tubes may have served routes for the passage of two-phase mixtures, and enhanced the boiling heat transfer. The convective effect was more pronounced at a higher saturation temperature. More bubbles will be generated at a higher saturation temperature, which will lead to enhanced convective contribution. The pore size where the maximum heat transfer coefficient was obtained was larger for R-l34a (d$_{p}$ = 0.27 mm) compared with that for R-123 (d$_{p}$ = 0.23 mm). This trend was consistent with the previous pool boiling results. For the enhanced tube bundles, the convective effect was more pronounced for R-134a than for R-123. This trend was reversed for the smooth tube bundle. Possible reasoning is provided based on the bubble behavior on the tube wall. Both the modified Chen and the asymptotic model predicted the present data reasonably well. The RMSEs were 14.3% for the modified Chen model and 12.7% for the asymptotic model.model.