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《Chemical Engineering Communications》2007,194(7):975-993
This article presents the modeling of heat transfer of upward annular flow in a smooth tube and a spirally internally ribbed tube. First, analytical models of two-phase flow dynamics and heat transfer of annular flow in flow boiling were derived from the liquid film momentum and energy equations for smooth tubes. Combined with empirical correlations for liquid droplet entrainment and deposition rates in annular flow, modeling of heat transfer of upward annular flow in the smooth tube was conducted. The predicted heat transfer coefficients of annular flow agree with the experimental results very well for the smooth tube. Based on the heat transfer model for smooth tubes, a simplified annular flow heat transfer model for the spirally internally ribbed tube was proposed by modifying the interfacial friction factor. The predicted heat transfer coefficients by the modified heat transfer model for the spirally internally ribbed tube agree with the experimental results to some extent. It is suggested that the heat transfer model for the spirally ribbed tube be further improved by modifying the correlations for liquid droplet entrainment and deposition rates in annular flow, which should describe the feature of annular flow in the spirally internally ribbed tube. Extensive experimental data are needed for this purpose. 相似文献
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Entrapment, E, in vertical gas-liquid annular flows may be pictured as a balance between the rate of atomization, RA, of the liquid layer and the rate of deposition of drops, R D. Laboratory measurements of RA, RD and E are reviewed. Theoretical analyses are discussed which picture RA as related to the growth of wavelets through a Kelvin-Helmholtz instability and RB as being directly proportional to the root-mean-square of the turbulent velocity fluctuations of the drops. An equation for E can be developed, which assumes that the deposition constant is independent of drop concentration and that the rate of atomization varies linearly with the flow rale of the liquid in the film. Limitations of this approach, suggested by measurements of RA and RD at large liquid flows, are discussed. 相似文献
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<正>1引言 传热恶化有不同的类型,就工程换热设备设计和运行的实际需要来说,人们最关心的是以下几点:(1)传热恶化发生的位置(壁温飞升起始点),一般用。cr来表示;(2)传热恶化发生后壁温飞升的最大值,一般用A儿。。来表示;(3)壁温飞升最大值的位置,一般用K。。。来表示;(4)传热恶化发生后的。mi。。本文着重分析讨论后3个问题。 相似文献
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水平微肋管内流动蒸发换热特性的实验研究 总被引:8,自引:0,他引:8
为了研究微肋管结构尺寸及工况等对管内流动蒸发性能的影响,对4种微肋管和1根9.52 mm光管进行了实验,4根微肋管中管外径为9.52 mm和7 mm的各2根,所用工质为R22.实验中质量流速变化范围为90~400kg8226;m-28226;s-1,所选工况为:蒸发温度7℃,入口干度15%~20%,出口过热度5~6℃.获得了蒸发换热性能随质量流速的变化,讨论了微肋结构尺寸和管径等对蒸发换热性能的影响.两根9.52mm微肋管的传热系数比光管分别分别提高了130%和180%,而其内表面积只比光管分别增加了40%和70%. 相似文献
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The effect of solids concentration on the bubble to bubble-slug, bubble-slug to slug, and slug to churn flow transitions in gas-liquid-solid vertical flow has been studied using air, water, and glass beads in a 5 cm ID plexiglass column. Several simple models to predict the transitions were developed utilizing criteria proposed for gas-liquid vertical flow. These criteria are shown to apply equally well in the absence or presence of the solid phase
With solids present in the flow, the bubble to bubble-slug and bubble-slug to slug flow transitions both occurred at lower superficial gas velocities because of increased bubble coalescence. However, the slug to churn flow transition was unaffected by solids in the range of flow conditions studied. 相似文献
With solids present in the flow, the bubble to bubble-slug and bubble-slug to slug flow transitions both occurred at lower superficial gas velocities because of increased bubble coalescence. However, the slug to churn flow transition was unaffected by solids in the range of flow conditions studied. 相似文献
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建立了带有气液分离器的高沸点有机工质流动沸腾换热实验台,对垂直上升多孔表面管内高沸点有机工质异丙苯的强化流动沸腾换热与阻力特性进行了实验研究,获得了传热系数与压降随干度的变化情况,并与光管内的实验结果进行了比较.另外,还通过实验得到了三个质量流速下的流动沸腾曲线.实验过程中质量流速范围为391~790kg8226;m-28226;s-1,实验工况干度范围为0.09~0.58,压力范围为0.16~0.31MPa.通过对实验数据的回归分析,获得了传热系数与摩擦压降的计算关联式.实验结果表明,多孔表面管在强化换热的同时,并没有使阻力增加很多,具有良好的应用前景. 相似文献
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This paper presents an experimental study of dispersed flow heat transfer in 90-degree circular bends. From extensive measurements, two different heat transfer patterns are identified, i.e. heat transfer without and with rewetting. Their intrinsic mechanisms are analysed, based on the present experimental evidence and our previous theoretical studies. Effects of mass flow rate, wall heat flux, system pressure and curvature ratio on heat transfer are also investigated. An empirical criterion is developed to identify the heat transfer pattern in the bend. 相似文献
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This paper presents an experimental study of dispersed flow heat transfer in 90-degree circular bends. From extensive measurements, two different heat transfer patterns are identified, i.e. heat transfer without and with rewetting. Their intrinsic mechanisms are analysed, based on the present experimental evidence and our previous theoretical studies. Effects of mass flow rate, wall heat flux, system pressure and curvature ratio on heat transfer are also investigated. An empirical criterion is developed to identify the heat transfer pattern in the bend. 相似文献
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A steady heat transfer problem has been analyzed as a conjugate problem with turbulent flow in a circular tube. The three kinds of thermal boundary conditions considered here are specified as constant temperature, constant heat flux and constant heat transfer coefficient at the outer surface of the wall.
From the results of numerical calculation for Prandtl numbers in the range 0.01 ≤ Pr ≤ 10 and for Reynolds numbers in the range 104 ≤ Re ≤ 105, it was confirmed that the dimensionless parameter Rc could have significant effects on the heat transfer and the temperature field in the fluid adjacent to the wall. 相似文献
From the results of numerical calculation for Prandtl numbers in the range 0.01 ≤ Pr ≤ 10 and for Reynolds numbers in the range 104 ≤ Re ≤ 105, it was confirmed that the dimensionless parameter Rc could have significant effects on the heat transfer and the temperature field in the fluid adjacent to the wall. 相似文献
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引 言流动沸腾传热广泛存在于石油、化工、轻工、动力及能源等各个领域 ,但三相流动沸腾传热的研究极少 .李修伦等[1]在流动沸腾系统中加入惰性固体粒子 ,进行了汽 -液 -固三相流沸腾传热的初步研究 .李修伦、闻建平[2 ,3]进一步将三相流和沸腾换热相结合 ,较好地解决了沸腾传热强化和防垢、除垢问题 .李修伦、张利斌等[4 ]又采用循环流化床技术 ,结合粒子在沸腾系统中的强化特性 ,开发了汽 -液 -固三相循环流化床蒸发器 ,它具有良好的强化传热和防、除垢性能 .上述研究均属于单组分三相流动沸腾传热 ,而关于二元物系三相流动沸腾传热的研… 相似文献
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This article addresses the squeezing flow and heat transfer between parallel disks when one disk is impermeable and the other is porous. Appropriate similarity transformations are invoked to convert the partial differential equations into ordinary ones. Expressions for velocity and temperature fields have been obtained by homotopy analysis method (HAM). The effects of embedding parameters such as squeeze number (S), Hartman number (M), Prandtl number (Pr), and Eckert number (Ec) are analyzed through graphs for the velocity and temperature profiles and tables for skin friction coefficient and local Nusselt number. It is observed that the series solutions are convergent only at third-order of approximation. The obtained results for velocity are also compared with the homotopy perturbation method (Domairry and Aziz, 2009). 相似文献