包层氚增殖球床不同装载方案的有效热导率研究

针对聚变堆固态包层的产氚载体中锂陶瓷颗粒组成的氚增殖球床,建立了基于离散元-计算流体力学(DEM-CFD)方法的球床传热分析模型,进行了离散元(DEM)几何模型有效性验证、网格敏感性分析和计算流体力学(CFD)传热模型有效性验证.用该模型模拟计算了粒径分布球床、不同粒径的一元球床、二元球床的有效热导率,研究了相同填充率...     

Influence of Streamwise Pitch on Local Heat Transfer Distribution for In-Line Arrays of Circular Jets with Spent Air Flow in Two Opposite Directions

Abstract

The effect of streamwise jet-to-jet spacing on local heat transfer distribution due to an in-line rectangular array of confined multiple circular air jets impinging on a surface parallel to the jet plate are experimentally studied. The length-to-diameter ratio of nozzles of the jet plate is 1.0. The flow, after impingement, is constrained to exit in two opposite directions from the confined passage formed between the jet plate and target plate. Mean jet Reynolds numbers based on the nozzle exit diameter (d) covered are 3,000, 5,000, 7,500, and 10,000; jet-to-plate distances studied are d, 2d, and 3d. Streamwise jet-to-jet distances of 3d, 4d, and 5d, and a constant spanwise pitch of 4d, are considered. The jet plates have ten spanwise rows in the streamwise direction and six jets in each spanwise row. The flat heat transfer surface is made of thin stainless-steel metal foil. Local temperature distribution on a target plate is measured using a thermal infrared camera. Wall static pressures in the streamwise direction are measured midway between the spanwise jets to estimate cross-flow velocities and individual jet velocities. The streamwise distribution of the jet flow and the cross flow is found to be least influenced by the streamwise pitch variation for the range of parameters considered during the present study. Heat transfer characteristics are explained partially on the basis of flow distribution. The cooling performance, based on the strip-averaged Nusselt number per unit mass flow rate of coolant per unit area of cooled surface, indicates deterioration for lower streamwise pitch and higher jet-to-plate distance.     

非能动传热球床堆有效导热系数的壁面效应分析

本文针对非能动传热机制下简单立方球床堆有效导热系数进行了数值研究,根据有效导热系数的空间分布特性,对球床堆的近壁面区域和主体区域作了划分;分析了不同非能动传热机制下的有效导热系数的壁面效应;最后分析了导热、辐射和自然对流对近壁面和主体区域有效导热系数的贡献.结果发现,近壁面区域是在壁面附近一个球径范围内的区域;由于辐射...     

INFLUENCE OF FLUID FLOW ON NUCLEATE BOILING FROM A TUBE

Abstract

The mechanisms of nucleate boiling on the outside of a horizontal tube differ fundamentally from those on a flat plate. In this experimental work the variation of heat transfer coefficient around the periphery of a tube is measured with the aim of clarifying these mechanisms. A specially designed tube is used in which local variations are not masked by conduction through the metal surface. The tube diameter is 27 mm, and the working fluid is R113 under saturated conditions at 1 atm.

When there is no imposed velocity the peripheral variations are typically 10–20% with the maximum heat transfer coefficient at the base of the tube. At very low velocity of upward flow ( ? 0.1 m/s) there is a marked change in the variation, with the maximum coefficient occurring at a point about 70° from the base. At higher velocities there is a slight increase in angle to the maximum point with maximum peripheral variations in heat transfer coefficient of around 25%.

The variations are explained in terms of nucleate boiling at the base and top and flow boiling at the sides. The thin layer of two-phase bubbly flow at the sides leads to the predominance of heat transfer caused by sliding bubbles aver other mechanisms in this region. The complex mix of mechanisms involved in boiling on tubes implies an inherent limit to the accuracy of predictive correlations.     

Rotating flexible disk under shaft temperature increment

A rotating flexible annular thin disk subjected to the temperature increment of the shaft clamping the disk was modeled in this paper. At disk top and bottom surfaces and free outer edge, the heat convection boundaries were assumed. Disk transverse deflection was considered as a function of both disk radial and circumferential coordinates, and temperature distribution was solved along disk thickness and radial directions simultaneously. As a result, the shaft temperature increment causes thermo-elastic instability of some disk modes. Effects of the shaft temperature increment, ratio of disk convective heat transfer coefficient to thermal conductivity, disk thickness, nodal circle and diameter numbers of disk mode on the natural frequencies, thermo-elastic instability and critical angular speed of the disk were discussed.     

Experimental Investigation of Heat Transfer in Two-phase Flow Boiling

In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m², vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m²s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number.     

HCCB-TBM����Li4SiO4�򴲶ѻ��ṹ����ֵģ��

通过离散元法初步模拟了微球在重力作用下的堆积行为,并分析了氚增殖区Li4SiO4球床的局部堆积结构.研究结果表明,摩擦系数和恢复系数对球床最终堆积结构有很大的影响.当摩擦系数较小时,摩擦系数对球床堆积结构的影响起主要作用;当摩擦系数较大时,恢复系数对球床堆积结构的影响起主要作用.球形颗粒从靠近壁面处的规则分布逐渐过渡到内部区域的均匀随机分布.球床局部堆积因子表现出了明显的壁面效应,其分布随着微球到壁面距离的增加而呈现出振幅逐渐减小的振荡趋势.所得到的球床堆积结构信息可用于研究球床传热特性和提氚气体流动特性的随机堆积球床模型的建立.     

有液滴卷吸时的环状流换热系数的预测模型

本文对垂直上升光管中环状流流动沸腾的理论模型进行了分析,以液膜紊流的动量方程和能量方程为基础,推导了环状流的数学模型,通过求解动量方程和能量方程,获得了流动沸腾换热系数的预测模型,并对该预测模型进行了数值求解,将预测的换热系数同实验值作了比较。     

氚增殖剂球床内氦气流动特性的数值模拟

通过计算流体力学(CFD)数值模拟方法,对氚增殖剂球床内部的氦气流动特性进行了初步研究。分析了球床流通长度和流通截面对提氚气体压降的影响,获得了不同入口流速下规则堆积球床和随机堆积球床的压降和阻力系数。      

A study of the heat transfer characteristics of a laser rod in a concentric circular tube

An analytical solution was derived from a two-dimensional heat conduction model with non-uniform boundary conditions for a side-pumped, side-cooled cylindrical laser rod. The convective heat transfer coefficient and the spatially varying fluid temperature were determined from the theoretical solutions or experimental correlations of convective heat transfer in an annular passage with prescribed heat fluxes. The first term of the analytical solution coincides with the result of the one-dimensional model. The other terms indicate that the axial temperature-rise in a laser rod has positive correlations with the axial coolant temperature-rise, the radial Biot number and the length-to-radius ratio of the laser rod. Subsequently, a conjugate numerical simulation that couples up the fluid convection and the solid conduction was performed. Compared with the analytical solution, the conjugate numerical simulation better exhibits the entrance effects of flow and heat transfer; therefore, it may provide more accurate solution in specific cases. PACS 44.10.+i; 44.90.+c     

一种新型两相流动中环状流液膜换热模型的研究

本文从汽液界面紊流脉动受到抑制的物理基础出发,提出对近界面缓冲层的混合长理论应进行修正,通过试验得到了相应的数学表达式及速度分布,并据此发展了一个新的环状流液膜换热模型。通过与试验值的比较,本文模型的计算结果与现有模型的计算结果相比较更趋于合理。     

竖直环形通道内液氮流动沸腾的MUSIG模型分析 第二部分:径向气泡直径和界面面积浓度的预测

由于考虑了气泡的破裂和聚合,同两流体模型相比,MUSIG模型(多尺寸组模型)能更准确地描述流场内气泡直径。采用MUSIG模型详细分析了不同壁面热流量,液体入口速度,过冷度以及不同管道高度时通道内气泡相界面面积、当地气泡直径、空泡系数等参数沿径向的分布。分析结果表明,MUSIG模型可用来预测泡弹状流型转变区的流动参数,也即该模型拓展了两流体模型的使用范围。     

Numerical Investigation of Heat Transfer Characteristics of scCO2 Flowing in a Vertically-Upward Tube with High Mass Flux

In this work, the heat transfer characteristics of supercritical pressure CO₂ in vertical heating tube with 10 mm inner diameter under high mass flux were investigated by using an SST k-ω turbulent model. The influences of inlet temperature, heat flux, mass flux, buoyancy and flow acceleration on the heat transfer of supercritical pressure CO₂ were discussed. Our results show that the buoyancy and flow acceleration effect based on single phase fluid assumption fail to explain the current simulation results. Here, supercritical pseudo-boiling theory is introduced to deal with heat transfer of scCO₂. scCO₂ is treated to have a heterogeneous structure consisting of vapor-like fluid and liquid-like fluid. A physical model of scCO₂ heat transfer in vertical heating tube was established containing a gas-like layer near the wall and a liquid-like fluid layer. Detailed distribution of thermophysical properties and turbulence in radial direction show that scCO₂ heat transfer is greatly affected by the thickness of gas-like film, thermal properties of gas-like film and turbulent kinetic energy in the near-wall region. Buoyancy parameters Bu < 10⁻⁵, Bu* < 5.6 × 10⁻⁷ and flow acceleration parameter K_v < 3 × 10⁻⁶ in this paper, which indicate that buoyancy effect and flow acceleration effect has no influence on heat transfer of scCO₂ under high mass fluxes. This work successfully explains the heat transfer mechanism of supercritical fluid under high mass flux.     

Experimental Investigation of Local Heat Transfer in a Square Duct With Continuous and Truncated Ribs

In the present study, the turbulent heat transfer and fiction in a square duct roughened by continuous and truncated ribs on one wall has been investigated experimentally. The ribs are oriented transversely to the main stream in a periodic arrangement. For both cases, the rib height-to-hydraulic diameter ratio is 0.15, the rib pitch-to-height ratio is fixed at 12, and the Reynolds number varies from 8,000–20,000. Liquid crystal thermography is applied to demonstrate detailed distribution of heat transfer coefficient between a pair of ribs. The results show that the horseshoe vortices produced by truncated ribs are quite different from the flow structures altered by continuous ribs. It is noted that continuous ribs give higher heat transfer augmentation and pressure drop than truncated ribs. Moreover, the truncated ribs cannot be employed to eliminate hot spots which occur in the corresponding continuous types.     

基于流动沸腾传热机理的分段式微通道结构优化研究

列车牵引变流器功率模块IGBT的散热问题近年来备受关注.本文以微通道内流动沸腾换热的"M"型曲线峰值点传热强化理论为依据,通过实验研究微通道长度和结构对冷板表面温度的影响,发现短通道能够有效控制通道内蒸汽干度水平,使得微通道冷板内以弹状流或薄膜环状流为主流流型,从而获得较高传热系数.在一定面积的冷板内设置短通道组合的分...     

随机填充增殖剂球床内载气流动特性数值模拟

固态氚增殖包层是聚变堆及聚变-裂变混合堆产氚包层的重要候选结构之一,其球床通道内载气流动特性将影响氚提取效率。利用离散元方法(DEM)生成随机填充增殖剂球床,通过径向孔隙率分布验证其合理性,计算流体力学(CFD)模拟计算其通道内气体流场特征。模拟得到:球床内吹扫氦气流速随孔隙率波动并随入口流速增大而均匀增大,通道内氦气流向及流速变化显著,Blake-Kozeny方程可良好预测该随机填充球床通道压降。     

中国 HCCB-TBM 氚增殖球床热工水力学特性数值模拟

基于 CFD 软件平台,针对中国 HCCB-TBM 氚增殖区球床热工水力学特性开展 3 维数值模拟研究。 依据 ITER 实际运行工况给出吹氚氦气和结构冷却剂氦气在硅酸锂球床内的流动与传热特性,获取球床内详细的 速度分布、温度分布和压力降。计算结果表明：圆球的排列方式影响球床内氦气流场和球床的最高温度;ITER 运行工况下 HCCB-TBM 增殖区硅酸锂小球及其壁面的最高温度不会超过设计温度。研究结果为增殖区热工水力 学方案的设计验证和下一步开展实验提供参考。     

�й� HCCB-TBM ���ֳ���ȹ�ˮ��ѧ������ֵģ��

Based on the CFD software platform FLUENT, three-dimensional numerical simulation was carried out for thermal hydraulics characteristics of the breeder zone pebble bed for China helium cooled ceramic breeder-test blanket module (HCCB-TBM). According the actual operating conditions of ITER, such as the nuclear heat distributions in the breeder zone and structure wall, the inlet velocities and temperatures of purge gas helium and coolant helium, the flow field and heat transfer characteristics of the purge gas helium carrying the tritium flowing over the lithium silicate pebble bed were obtained, and the temperature distribution and pressure drop were presented as well. The calculation results show that the permutation mode of the lithium silicate spheres in the pebble bed have an influence on the flow field and the maximum temperature of the pebble-bed. The maximum temperature of the pebble-bed and the structure wall does not exceed the designed temperature under the ITER operating conditions. The results will be benefit for the design verification of the breeder zone thermal hydraulics scheme and improving the following experiments of the purge gas.     

Assessment of thermal performance of the functionally graded materials in annular fins

Heat transfer enhancement in the annular fins with uniform profile is investigated in the present study. Conventional fin materials are replaced with the functionally graded materials in order to increase the rate of heat transfer and corresponding fin efficiency. Here, the fin material properties, such as conductivity, are assumed to be graded along the annular fin radius, R, as a linear function. The governing equation of the annular fin is computed with an approximate analytical method using the mean value theorem. It is revealed that the in-homogeneity index, β, of the fin material plays an important role on the thermal characteristics of the annular fins. Alternatively, heat dissipation between the fin surface and surrounding fluid in the annular fins increases with increasing the inhomogeneity indices, β. Finally, it is stated that application of the functionally graded material in the annular fins enhances the fin efficiency in comparison to the annular fins with homogeneous material. It is hoped that the results obtained from this study arouse interest among thermal designers and heat exchanger industries.     

三维微肋螺旋管内流动沸腾流型与传热性能

采用三维微肋螺旋管进行了制冷剂R134a在管内的流动沸腾传热与流型可视化实验。随着流量和干度的变化,流型可划分为泡状流、塞状流、分层波状流、间歇流以及环状流。在Taitel-Dukler流型图上给出了流型的分区及其转变曲线,讨论了螺旋管内两相流动流型转变的特性。传热实验揭示了质量流量、热流密度及蒸汽干度对传热性能的影响,三维微肋螺旋管的强化因子为1.5-2.1。