存在非均匀内热源的多孔介质内自然对流传热传质的数值研究

采用数值方法分析了具有非均匀分布内热源的竖直同心套管内多孔介质中的传热传质,浮力比N由1.5变为-1.5后,流体由顺时针流动变为逆时针流动且流体速度加快。｜N｜〈1时边界层的发展主要由热浮力控制。管隙中心处浓度分布在R=0.8处出现一个最小值。     

具有非均匀内热源的多孔介质中自然对流传热传质的数值研究

采用数值方法分析了具有非均匀分布内热源的竖直同心套管内多孔介质中的传热传质,内热源分布系数M较大时,造成流场中心的逆时针环流向中心挤压。浮力比N由1.5变为-1.5后,流体由顺时针流动变为逆时针流动且流体速度加快。Nusselt数在Z=0.7处出现转折。随M增大内壁面Nusselt数变化范围增大,并且转折点前移。上壁面Sherwood数也呈先增大后减小的趋势,并且在R=0.9处出现转折。     

Thermal Diffusion and MHD Effects on Combined Free‐Forced Convection and Mass Transfer of a Viscous Fluid Flow Through a Porous Medium with Heat Generation

The problem of thermal diffusion and magnetic field effects on combined free‐forced convection and mass transfer flow past a vertical porous flat plate, in the presence of heat generation is studied numerically. The governing momentum, energy and concentration equations are converted into a system of nonlinear ordinary differential equations by means of similarity transformations. The resulting system of coupled nonlinear ordinary differential equations is solved numerically by using the Shooting method. Numerical results are presented for velocity, temperature and concentration profiles within the boundary layer for different parameters of the problem including suction parameter, heat generation parameter, Soret number, Dufour number, magnetic parameter, etc. In addition, the effects of the pertinent parameters on the skin friction and the rates of heat and mass transfer are discussed numerically and illustrated graphically.     

多孔介质内复合对流传热传质的数值分析

采用数值方法分析了具有非均匀内热源的竖直套管中复合对流传热传质,考查内热源分布系数M和热质二浮力比N对速度、温度、浓度分布以及Nusselt数和Sherwood数的影响。结果表明：当N〉1时速度V为正,其值随N的增加而增大;当N〈-1.5时,V则先负后正。随着M增大,等温线和等浓度线分布更加密集,传热和传质过程更加明显。     

Unsteady MHD Free Convection Flow in the Presence of Inclined Magnetic Field with Suction and Heat Source

An analytical study is performed to examine the effects of a magnetic field on free convection flow when: (i) plate is moving impulsively with uniform velocity U; (ii) suction velocity normal to the plate is constant; (iii) fluid is subjected to a constant heat source of absorption type; (iv) magnetic lines of forces are assumed to be fixed relative to the porous plate; (v) magnetic field makes an angle α normal to the porous plate. The expressions for the velocity field and skin friction are obtained by the Laplace transform technique. The influences of the various parameters on flow field and skin friction are extensively discussed.     

Heat and Mass Transfer in Unsaturated Porous Cake with Heated Walls

The mineral granules in the industrial drying units such as rotary dryer or fluidized dryer or the membrane in the PEMFC experience transient multiphase heat and mass transfer with transient heating mode. In particular, the transport process within mineral granules in the dryer is difficult to model owing to effects of complicated granule-granule collision and granule-heated surface. This article presents a comprehensive model consisting of continuity and heat and mass balances of three phases in an unsteady state. Numerical results revealed the flow patterns and temperature distributions of gas and liquid phases in mineral granule over time. The thermal response of the heated medium will be very different under low and high mixing intensities. The development of a recirculation liquid zone to balance the yielded capillary suction gradient enhances local evaporation and vapor accumulation rates, thus determining the overall evaporation rate form medium.     

气泡在热液相介质中上升时的传热与传质

本文对气泡在热液相介质中上升时的传热与传质进行了分析,建立了数学模型,并进行了数值解,其结果可以说明气液相界面蒸发的特征。本文还通过实验对理论模型进行了验证。     

吸湿多孔介质冷冻干燥传质传热模型

本研究在作者提出的吸附—解吸平衡关系的基础上,建立了一个全新的考虑吸湿效应的多孔介质冷冻干燥数学模型。模型用有限差分法进行求解,并带有一个移动边界,以模拟介电材料辅助的微波冷冻干燥过程。介电材料选用碳化硅（SiC）,原料液为脱脂奶。模拟结果表明：介电材料能够有效强化微波冷冻干燥过程。在典型操作条件下,介电材料辅助的微波冷冻干燥所用的时间比普通微波冷冻干燥减少33.1%。当料液中固体含量较低或者固体产品的损耗因子较小时,介电材料对微波加热的效果不明显。基于冰饱和度、温度和水蒸气浓度的分布,本文分析了干燥过程中的传质传热机理,并对干燥速率控制因素进行了讨论。     

Free Heat and Mass Transfer in a Porous Enclosure with Side Vents

Free heat and mass transfer during drying in a porous enclosure with free vents has been investigated numerically. Enclosed moist air interacts with the surrounding air through freely vented ports situated on both sides perpendicular to the heated wall. Air, heat, and moisture transport structures are visualized respectively by streamlines, heat lines, and mass lines. Effects of thermal Rayleigh number, Darcy number, vent location, and enclosure inclination on the convective heat/moisture transfer rate and volume flow rate across this enclosure are discussed. For each case, partially enclosed fluid flow undergoes different phases, increasing with buoyancy ratio; that is, heat transfer–driven flow, heat- and moisture-aided flow, and moisture transfer–dominated flow. Numerical results demonstrate that the convective heat and moisture transport patterns and transport rates greatly depend on thermal Rayleigh number, properties of porous medium, and enclosure inclination. Practices for enhancing heat and moisture transfer have been suggested for drying processes.     

孔隙分布对多孔介质内流动和传热的影响

采用Sierpinski地毯分形技术建立多孔介质内流动和传热模型,通过改变固体基质位置研究了孔隙分布结构对多孔介质内流动特性和热效率的影响,3种孔隙分布为每分形一次固体基质分布在中心位置(A)、分布在中上方(B)和分布在右上方(C),当流体稳定流过多孔介质时,不同的孔隙分布表现出不同流动和传热特性. 结果表明,孔隙分布是影响多孔介质传输特性和传热效率的重要因素,无量纲渗透率k*C>k*B>k*A,多孔介质孔隙率大于0.8时更明显;流体流过不同孔隙分布的多孔介质时,相同孔隙率时与流体接触的固体基质面积A>B>C,传热效果A最佳、C最差. 孔隙分布影响了无量纲局部熵产率,在3种孔隙分布下用Be表示的热传导引起的熵产率占主导.     

新型多孔微热沉流动与传热的耦合数值分析

提出一种新型的多孔微热沉系统来实现高热流密度电子元器件封装散热的需求,分析了多孔微热沉系统的工作原理和特点,建立了微热沉金属壁面的传热以及多孔区域的流动与传热的耦合数学模型,并用SIMPLE算法对其进行整场求解,详细讨论了不同的热流、回流液入口速度以及进口位置对多孔微热沉传热性能的影响。数值计算结果表明,多孔微热沉在高热流密度情况下,加热表面能维持较低的温度水平。热流越大,加热表面的温度就越高;增加回流液体的入口速度可以明显的降低微热沉加热表面及底面的温度水平;多孔微热沉的下进口方式能够减小散热表面温度的不均匀性。多孔微热沉系统能有效解决高热流密度电子元器件的散热问题,提高器件可靠性与使用寿命。     

Two Dimensional Heat and Mass Transfer During Convective Drying of Porous Media

In this paper, we study numerically two-dimensional heat and mass transfer during convective drying in porous media. The set of macroscopic equations is very comprehensive and takes into account the effect of gaseous pressure. A numerical code has been established. This code has allowed us to determine t.he space-time evolution of the temperature, the total pressure and the moisture content.     

Gaseous Carbon Dioxide as the Heat and Mass Transfer Medium in Drying

Using available correlations for heat transfer, a comparative analysis of drying rates in CO₂ and in air was performed for several basic types of dryers. Higher heat transfer rates were found for dryers with active hydrodynamics, which translates into shorter drying time for materials dried in the first drying period. These results were validated by experiments on drying wheat kernels fluidized by air and by CO₂. Shorter drying times by about 20% were confirmed for CO₂, which offers energy savings of about 3% of the heat input to the dryer. Additional energy savings of 4% of the heat load can be expected for drying at temperatures below 100°C because of the lower wet-bulb temperature for CO₂ than that for air. The potential for CO₂ abatement was evaluated based on a case study for drying of distillers' spent grain.     

Gaseous Carbon Dioxide as the Heat and Mass Transfer Medium in Drying

Using available correlations for heat transfer, a comparative analysis of drying rates in CO₂ and in air was performed for several basic types of dryers. Higher heat transfer rates were found for dryers with active hydrodynamics, which translates into shorter drying time for materials dried in the first drying period. These results were validated by experiments on drying wheat kernels fluidized by air and by CO₂. Shorter drying times by about 20% were confirmed for CO₂, which offers energy savings of about 3% of the heat input to the dryer. Additional energy savings of 4% of the heat load can be expected for drying at temperatures below 100°C because of the lower wet-bulb temperature for CO₂ than that for air. The potential for CO₂ abatement was evaluated based on a case study for drying of distillers' spent grain.     

烧结型多孔管管内流动沸腾传热数值模拟

建立了烧结型表面多孔管多孔层的理论模型,应用Fluent软件对去离子水在烧结型表面多孔管和光滑管竖直管内的流动沸腾进行数值模拟,得到了不同流速下的气相体积分布云图和压力场云图,并利用场协同原理分析了管内的速度、温度场.结果表明,烧结型表面多孔管具有良好的强化沸腾传热性能.同时并未大幅度增加管内压力降.此外还分析了不同体...     

Influence of Chemical Reaction on Heat and Mass Transfer in MHD Radiative Flow due to Non-Coaxial Rotations of Disk and Fluid at Infinity

Theoretical Foundations of Chemical Engineering - An exact solution of the problem regarding influence of chemical reaction and buoyant force on the heat and mass transfer in a radiative flow due...     

磁性液滴在液体中的运动及接触传热

对磁性液滴在不互溶液体中的运动和接触传热特性进行了实验研究和理论分析，建立了磁性液滴在不互溶液体中运动的数学模型和传热关联式。实验结果表明，外加磁场对磁性液滴的流动和传热具有显著的强化作用。