一个多孔有机织物热湿传递过程的数学模型

利用多孔介质中的Darcy定律建立了一个多孔有机织物中热湿传递过程的数学模型，并提出了一个描述多孔有机织物中液相水重力与表面张力的对比关系的数H=5gρldcLτlεl1/3/2σcosФε1/3采用Crank—Nicolson方法数值求解了该模型，得到了在相同初始和边界条件下，不同有机材料织物中的热湿传递过程，并给出了多孔有机织物中的水蒸汽的浓度场分布、温度场分布以及纤维中的含水量的分布。计算结果与实验结果是吻合的。     

一种着装人体动态热湿传递模拟方法

针对服装热湿功能设计问题,结合改进的人体热调节模型和微元织物热湿耦合模型,实现了着装人体动态热湿传递过程的模拟。水分的蒸发凝结、纤维对湿的吸附解吸、液态水的毛细传递、人体汗水在体表积聚等现象,及其对服装热性能的作用在模型中都给予了考虑。并给出了计算流程。算例表明了模拟方法的有效性。     

混凝土中化学-热-湿-力耦合过程的数值方法

提出了一个火灾下混凝土中化学-热-湿-力耦合过程分析的两级数学模型. 混凝 土模型化为充满两种非混溶孔隙流体的非饱和变形多孔多相介质. 数学模型基于控制干空 气、湿份及基质溶解物的质量守恒、混凝土介质混合体的动量守恒和焓(能量)守恒的耦合 偏微分方程组. 模型中特别考虑到了高温下的脱盐过程. 构造了一个用于数值模拟 化学-热-湿-力耦合行为的有限元求解过程的混合弱形式. 并且针对其中具有非自伴随算子特性的 双曲线控制方程的空间离散进行了特殊考虑. 数值结果例题显示所发展的数学模型和数值方 法在重现火灾条件下的混凝土中化学-热-湿-力耦合行为的有效性.     

多孔介质在压力梯度作用下的热质耦合数值模拟

多孔介质干燥导致热质耦合传输过程。本文基于连续介质力学的宏观尺度,对多孔介质的热、湿和气三者耦合迁移进行数值模拟,研究压力梯度对热质传输的影响。多孔介质传质机理主要为水汽和空气的对流和扩散传输、吸附水在含湿量梯度作用下的自由扩散和其在温度梯度即Soret效应驱动下的流动。采用Galerkin加权余量的有限元方法,提出了...     

谷粒的热——湿应力分析

针对谷物烘干问题,本文研究弹性及粘弹性圆球和椭球的热,湿应力。对圆球分析表明,热应力峰值远比湿应力峰值出现时间早,在假定材料为热,湿流变简单的Maxwell粘弹性体条件下,本文导出了圆球的热,湿应力分布公式,并应用有限元法研究了椭球的热,湿应力,文中以无量纲形成给出了圆球中心和表面应力随时间的 变化情况,以及椭球中心轴向应力峰值随椭球长,短半轴之比的变化情况。     

预张力纤维织物超高速碰撞热-力学特性分析

高性能纤维织物承力层承担充气舱的内压载荷,并为充气舱提供空间碎片防护。充气舱内压载荷将导致纤维织物承力层产生预张力,并对纤维织物的空间碎片超高速碰撞特性产生显著影响,从而影响其空间碎片防护性能。为分析预张力对纤维织物超高速碰撞过程中热-力学特性的影响,采用Johnson-Cook强度模型和Mie-Grüneisen状态方程建立了纤维材料热-力耦合材料模型,利用有限元法-光滑粒子流体动力学耦合算法对纤维织物的纱线编织结构进行离散建模,并通过施加张力载荷实现纤维织物靶板的预拉伸,进而建立了预张力纤维织物超高速碰撞数值模型,分析并得到了预张力作用下纤维织物超高速碰撞热-力学特性及空间碎片防护性能。结果表明:在弹丸超高速碰撞下,随着预张力的提高,纤维织物穿孔面积增大,碎片云扩散角减小,弹丸动能吸收率降低,碰撞区域温度降低。预张力的存在显著降低了纤维织物的空间碎片防护性能。     

Cu-Al-Be形状记忆合金湿磨粒磨损性能研究

采用销-盘式二体磨损试验研究了CuAlBe形状记忆合金的湿磨粒磨损行为．结果表明，CuAlBe形状记忆合金的磨损性能不完全取决于材料硬度，具有热弹性马氏体组织的A合金的抗磨性优于高硬度B合金．在湿磨粒磨损条件下，A合金具有β′1 β双相组织，在磨粒的交变应力作用下，由于β相应力诱发马氏体相变、β′1相马氏体变体择优取向并产生形状记忆效应，使应变弹性回复，并钝化裂纹尖端，使得A合金具有优良的抗磨粒磨损性能．     

Maxwell粘弹性球体的湿应力

谷物烘干时，谷粒内部的热－湿应力太大，可能使谷粒出现裂纹．基于这一实际问题，本文研究了当初始湿度和平衡湿度给定时，Ｍａｘｗｅｌ粘弹性圆球内的湿应力分布，及其随时间的变化情况．     

迷彩服织物与人体肘部皮肤摩擦特性研究

在往复摩擦模式下模拟迷彩服穿着环境,研究了5种不同迷彩服织物的表面结构、亲疏水性、接触力值以及干湿状态对皮肤摩擦特性的影响.结果表明:在法向载荷为1 N时,湿态下的环境增强了织物与皮肤间的黏着力,织物与皮肤在湿态下的摩擦系数均高于干态;当法向载荷增加到5 N时,界面间的干湿状态对织物与皮肤的摩擦系数无明显影响.在干态时,不同迷彩服织物与皮肤的摩擦性能与织物的材质和针织结构有关,纯棉材质和斜纹结构的织物与皮肤的摩擦系数较小;在湿态时,不同迷彩服织物与皮肤的摩擦性能与织物的亲疏水性有关,疏水性强的织物由于增强了皮肤的水合作用以及界面间的粘附力,因此增加了织物与皮肤的摩擦系数.质地较硬的平纹结构织物易造成摩擦后的皮肤表面粗糙,造成皮肤不同程度的角质层分离及表皮撕裂,增加了皮肤表面损伤的风险.     

坡形加热下的二维广义磁热黏弹性问题研究

运用具有一个热松弛时间的广义热黏弹性理论，研究了处于均布磁场中的二维磁热黏弹 性问题. 运用Laplace变换(对时间变量)和Fourier变换(对于一个空间变量)，得到了变 换域内场量的精确表达式，并把结果应用到表面受到坡形加热的半空间问题. 应用 数值逆变换得到了时间-空间域内场量的解，对丙烯酸塑料 给出场量的响应图. 并把运用广义热黏弹性理论所得的结果与传统热黏弹性理 论及热弹性理论下的结果进行了比较.     

Experimental determination of transient wall temperature distributions close to growing vapor bubbles

Experiments were performed to study the spatio-temporal temperature variation underneath growing bubbles on a thin platinum heating foil in saturated and subcooled nucleate pool boiling of water at atmospheric pressure. The transient wall temperature distributions were recorded with spatial resolution of 40 μm by a high-speed infrared camera at intervals of 1 ms, synchronised with a high-speed video camera to record bubble motion. Examples are presented of the transient distributions of wall temperature, heat flux and heat transfer coefficient underneath bubbles growing with the fast and slow bubble detachment mechanisms in saturated and subcooled pool boiling. Comments are made on the evidence for and against particular mechanisms of heat transfer.     

Boiling heat transfer characteristics of nanofluids in a flat heat pipe evaporator with micro-grooved heating surface

An experimental study was performed to understand the nucleate boiling heat transfer of water–CuO nanoparticles suspension (nanofluids) at different operating pressures and different nanoparticle mass concentrations. The experimental apparatus is a miniature flat heat pipe (MFHP) with micro-grooved heat transfer surface of its evaporator. The experimental results indicate that the operating pressure has great influence on the nucleate boiling characteristics in the MFHP evaporator. The heat transfer coefficient and the critical heat flux (CHF) of nanofluids increase greatly with decreasing pressure as compared with those of water. The heat transfer coefficient and the CHF of nanofluids can increase about 25% and 50%, respectively, at atmospheric pressure whereas about 100% and 150%, respectively, at the pressure of 7.4 kPa. Nanoparticle mass concentration also has significant influence on the boiling heat transfer and the CHF of nanofluids. The heat transfer coefficient and the CHF increase slowly with the increase of the nanoparticle mass concentration at low concentration conditions. However, when the nanoparticle mass concentration is over 1.0 wt%, the CHF enhancement is close to a constant number and the heat transfer coefficient deteriorates. There exists an optimum mass concentration for nanofluids which corresponds to the maximum heat transfer enhancement and this optimum mass concentration is 1.0 wt% at all test pressures. The experiment confirmed that the boiling heat transfer characteristics of the MFHP evaporator can evidently be strengthened by using water/CuO nanofluids.     

Artificial boiling heat transfer in the free convection to carbonic acid solution

Free convection phenomenon has been experimentally investigated around a horizontal rod heater in carbonic acid solution. Because of the tendency of the solution to desorb carbon dioxide gas when temperature is increased, bubbles appear when cylinder surface is heated. The bubbles consists mainly carbon dioxide and also a negligible amount of water vapor. The results present that dissolved carbon dioxide in water significantly enhances the heat transfer coefficient in compare to pure free convection regime. This is mainly due to the microscale mixing on the heat transfer surface, which is induced by bubble formation. In this investigation, experiments are performed at different bulk temperatures between 288 and 333 K and heat fluxes up to 400 kW m⁻² at atmospheric pressure. Bubble departure diameter, nucleation site density and heat transfer coefficient have been experimentally measured. A model has been proposed to predict the heat transfer coefficient.     

Heat transfer in bubble layers at high pressures

An original experimental investigation of heat transfer with steam condensation on a surface of a horizontal cooled tube immersed in a bubbling layer was carried out. A copper test section 16 mm in diameter and 285 mm in length was placed in a bubbling column 295 mm in diameter. Experiments were made under a pressure of 0.72-3.8 MPa with volume steam content 0-0.18, steam superficial velocities 0-0.18 m/s, and liquid-wall temperature difference 38–106 K. The heat transfer process in a bubbling layer under high pressures is shown to be of considerably intensity; with moderate values of steam content heat transfer coefficients reach 10–12 kW/(m²·K). The use of the known correlations assumed for the case of air bubbling under atmospheric pressure results in systematically underestimating heat transfer by 30–80%. Data were obtained on heat transfer with film condensation of steam and natural convection of subcooled water at high temperature differences outside the range investigated earlier. Experimental data table is appended.     

Comparison of the heat transfer characteristics of supercritical pressure water to that of subcritical pressure water in vertically-upward tubes

A systematic comparison was made between the forced convection heat transfer characteristics of the supercritical pressure water and that of the subcritical pressure water in vertically-upward tubes. It was found that, severe heat transfer deterioration did not occur in the vertically-upward internally-ribbed tube at supercritical pressures, and the variations in the inside wall temperature with the bulk fluid enthalpy experienced three stages, namely, the continuously increasing stage, the smoothly changing stage and another continuously increasing stage at the supercritical pressures; however, at subcritical pressures, there existed at least four stages for the variation of the inside tube wall temperature, i.e., the continuously increasing stage, the basically unchanging stage, the sharply rising stage and another continuously increasing stage. The heat transfer coefficients in the subcritical two-phase region, in which the heat transfer deterioration did not occur, were much greater than those in the heat transfer enhancement region of supercritical pressure water. In the large specific heat region of supercritical pressure water, the enhanced heat transfer was impaired by increasing the heat flux; however, in the subcritical two-phase region, the higher the heat flux, the greater the heat transfer coefficient would be. It was also found that the heat transfer deterioration of supercritical pressure water was similar in mechanism to the DNB (departure from nucleate boiling) at subcritical pressures.     

Condensation of binary immiscible systems on a vertical tube

A careful experimental investigation is described to determine condensation heat transfer coefficients for the pure systems carbon tetrachloride, trichloroethylene, benzene and cyclohexane and their aqueous heteroazeotropes on a vertical oxidised copper tube at atmospheric pressure. The values are compared whenever possible with those reported in the literature and discrepancies in the results are attributed to the presence of non-condensible gases, the wetting behaviour of the condensates on the oxidised copper surface and the compositions of the vapour mixtures.     

Multiphysics Simulation Combining Large-Eddy Simulation,Wall Heat Conduction and Radiative Energy Transfer to Predict Wall Temperature Induced by a Confined Premixed Swirling Flame

A multi-physics simulation combining large-eddy simulation, conjugate heat transfer and radiative heat transfer is used to predict the wall temperature field of a confined premixed swirling flame operating under atmospheric pressure. The combustion model accounts for the effect of enthalpy defect on the flame structure whose stabilization is here sensitive to the wall heat losses. The conjugate heat transfer is accounted for by solving the heat conduction within the combustor walls and with the Hybrid-Cell Neumann-Dirichlet coupling method, enabling to dynamically adapt the coupling period. The latter coupling procedure is enhanced to determine statistics (mean, RMS, \(\ldots \)) in a permanent regime accurately and efficiently thanks to an acceleration technique which is derived and validated. The exact radiative heat transfer equation is solved with an advanced Monte Carlo method with a local control of the statistical error. The coupled simulation is carried out with or without accounting for radiation. Excellent results for the wall temperature are achieved by the fully coupled simulation which are then further analyzed in terms of radiative effects, global energy budget and fluctuations of wall heat flux and temperature.     

Investigation of heat transfer by means of pool film boiling on vertical cylinders in gravity

In this study, the heat transfer by means of pool film boiling on immersed vertical cylindrical rods was investigated. For this purpose, the rods with various dimensions, which have been heated up to 600°C, were immersed in a pure water pool in the different temperatures. The centre temperature and water temperature versus operation time were measured by K type thermocouples at the atmospheric pressure. After experimental studies, the surface temperatures of rods and heat transfer coefficients were calculated by means of Lumped method from the measured temperatures. Consequently, an empirical equation was developed between the Nusselt, Grashof, Prandtl and Jakob numbers. The experimental results showed that the specimens having the same characteristic lengths exhibited the same heat transfers performance although the specimen’s diameters and lengths differed considerably.     

Nucleate pool boiling of aqueous solution of citric acid on a smoothed horizontal cylinder

Nucleate pool boiling heat transfer coefficients were measured during pool boiling of the mixtures of Citric acid/water on a horizontal heated Cylinder. The experiment was done at atmospheric pressure and heat fluxes up to 113 kW m⁻² and mass fraction range 0.1496–0.613 over all ranges of mass fraction, the heat transfer coefficients of the mixtures are markedly less than those in single component substances and, in particular, are dramatically deteriorated in the vicinity of both single component substances. An applicability of existing correlations to the present experimental data is discussed. As a result, it is difficult for any existing correlation to predict the true values of pool boiling heat transfer coefficients over all ranges of mass fraction in mixtures of citric acid/water. Available correlation results were not exactly adapted to experimental data and for the best estimation, a new modified model based on Stephan-Kroner has been achieved with reasonable accuracy. Also the status of bubble generation showed that nucleation site density is strictly functioning of heat flux.     

Study on laminar film condensation of saturated steam on a vertical flat plate for consideration of various physical factors including variable thermophysical properties

The extended theory of the steady state laminar film condensation process of pure saturated vapour at atmospheric pressure on an isothermal vertical flat plate is established. Its equations provide a complete account of the physical process for consideration of various physical factors including variable thermophysical properties, except for surface tension at the liquid-vapour film interface. First, similarity considerations are proposed to transform the governing system of partial differential equations and its boundary conditions into the corresponding dimensionless system. Then, the dimensionless new system is computed numerically in two steps: First neglecting shear force at the interface, so that the initial values of the boundary conditionsW _{xl, s} andW _{yl, s} are obtained. Then, the calculations of a problem of the three-point boundary-value for coupling the equations of liquid film with those of vapour film are carried out. Furthermore, the correlations for heat transfer coefficient and mass flow rate are proposed by analysis of heat and mass transfer and it is found that the heat transfer coefficient is function of dimensionless temperature gradient $\dot L$ , and that the condensate mass flow rate is function of the mass flow rate parameter (η _lδ W _{xl, s} ? 4W _{yl, s} )of liquid. In addition, the corresponding heat and mass transfer correlations expressed by subcooled temperature Δt are developed. According to Nusselt's theory four different assumptions are set up for an investigation of the effects of the film condensation of saturated vapour, so that the validity of Nusselt's theory can be further clarified. Quantitative comparisons from the results of the heat transfer coefficient and mass flow rate of the condensate indicate that the effect of variable thermophysical properties on the heat and mass transfer is appreciable. The effect of thermal convection in the condensate film is obviously larger than those of shear force at liquid-vapour interface, and the effect of the inertia in the condensate film is very small. Finally, it is also shown that Nusselt's theory, in using Drew reference temperature, will decrease the heat transfer coefficient by at most 5.11%, and will increase the mass flow rate of the condensate by at most 2.45%, provided that the effect of the surface tension is not taken into account.