Heat and Mass Transfer Analogy Studies of Binary Liquid Mixture in Comparison with Eteanol-n-Heptane Evaporating to Air

ABSTRACT

An expenmental and theoretical study of heat and mass transfer analogy and a comparison of that to a binary liquid mixture evaporation is presented. Common organic solvents, ethanol and n-heptane, were used to form an alcohol - hydrocarbon mixture. Studies were carried out in a horizontal rectangular channel having air flow velocities of 0.2 – 0.9 m/s. Heat transfer coefficients were measured with a copper plate resistor and mass transfer coefficients with a square pool. The heat and mass transfer analogy is presented for a system having two evaporating compounds with a fixed value of air flow and verified by measuring and comparing mass transfer coefficients for distilled water with air flow velocities of 0.2 - 0.9 mls. An illustrative example of the use of the theory for industrial ventilation is presented.     

强制气流作用下溶液蒸发过程的传质规律

针对强制气流作用下溶液的蒸发过程,在分析气液相间力学特性的基础上,根据Levich涡流衰减理论和边界层理论,将气流流动状态与相间传质结合,研究了湍流气流横掠液面过程中气液相间的传质变化规律,分析了雷诺数、气流流道结构及普朗特混合长度对传质的影响,得到了气液相间的湍流质扩散系数的变化规律,湍流气流横掠液面条件下的对流传质准则数Sh=0.221Sc1/3Rex1/2. 结果表明,湍流扩散系数、传质系数与气流的流动状态密切相关,气流流道结构对气液相间的传质有重要影响.     

An Experimental Study of Porous Surface Tubes for Enhancement of Binary Liquid Mixture Pool Boiling Heat Transfer

Experiments have been conducted on the pool boiling of binary mixtures in JK tubeswith porous surface and ribbed channels,attempting to enhace the boiling heat transfer coefficientsinvolved.The binary mixtures used in this study are R113 and R11.The results show that the boilingfi1m heat transfer coefficients for the R113 and R11 binary mixtures in JK2 and JK1 tubes are 2—8tirnes and 2—5 times greater than those in smooth tubes respectively.Based on this experimentaldata and simple theoretical analysis,a correlation has been proposed to predict the boiling heattransfer coefficients for R113/R11 mixtures in a horizontal JK tube with a relative error of less than16%.     

Conditions of the Thermal Explosion under Forced Convection of a Reacting Mixture

Conditions of origination of the thermal explosion in a cylindrical chemical reactor equipped by a certain number of symmetrically located stirrers ensuring forced convection of the reacting mixture are considered in the approximation of an infinite Peclet number and under the assumption of laminar motion of the fluid. The critical value of the thermal explosion parameter (Frank-Kamenetskii parameter) is found as a function of the number of stirrers and the distance between the centerlines of the stirrers and reactor. As the number of stirrers increases, the calculations predict a lower probability of the thermal explosion, and the critical value of the parameter can severalfold exceed its classical value. It is found that the thermal explosion parameter substantially depends on the location of the stirrers, responsible for heat removal from the reactor. __________ Translated from Fizika Goreniya i Vzryva, Vol. 41, No. 5, pp. 49–54, September–October, 2005.     

Heat and Mass Transfer between Air and Liquid Desiccant in Cross‐flow Contact Systems

In this paper, an analytical solution of the coupled heat and mass transfer process in a cross‐flow liquid‐desiccant dehumidifier/regenerator is developed. By the use of reliable assumptions, the government equations for the system are solved by an analytical method. The results of the present analytical solution are compared with experimental data from the literature, and they show good agreement. The maximum error produced by the presented analytical solution is less than 12 %. The effect of the operating parameters is considered using the presented analytical solution. The results show that air inlet humidity, air flow rate, desiccant inlet temperature, and desiccant inlet concentration have more influence on the moisture removal rate in the cross‐flow dehumidifier. Also, air inlet humidity, desiccant inlet temperature, desiccant inlet concentration and desiccant flow rate have more effect on the moisture removal rate in the cross‐flow regenerator. The effect of the Lewis number on the performance of the dehumidifier/regenerator is investigated. As the results show, by the use of Le = 1.08 in the dehumidification process and Le = 0.96 in the regeneration process, instead of the value of unity, better results are obtained. The benefit of the present study is a simplified application for the evaluation of the outlet parameters of the cross‐flow air dehumidifier/regenerator.     

脂肪酸降膜蒸发传热研究

在垂直降膜管上进行脂肪酸混合物降膜蒸发传热的实验研究 ,分析了进料流量、热通量和操作压力等因素对传热性能的影响。建立了数学模型 ,并进行数值求解。实验结果表明 ,在层流情况下 ,流量的增加不利于传热 ,热通量和操作压力的增加对表面蒸发传热有利。将模型计算结果与实验结果比较 ,发现模型较好地预测了实验结果     

Effects of anisotropic scattering of radiation in laminar forced convection in a parallel-plate duct

Effects of anisotropic scattering to heat transfer in hydrodynamically-developed, thermally-developing steady laminar forced flow of a gray fluid between two infinite parallel plates are investigated for the case when the inlet temperature of the fluid is less than the wall temperature. An implicit finite difference scheme is applied to solve the energy equation, while the high order P_N method is used to solve the radiation part of this problem. The effects of the anisotropy, the conduction-to-radiation parameter, the optical thickness, the reflectivity of the plates and the inlet temperature on the local Nusselt number are studied.     

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。     

International Heat and Mass Transfer Forum

ABSTRACT

Results from three experimental studies are reviewed in order to examine the relationship between the heat and mass transfer coefficients in the combined infrared and convective drying process. These results demonstrared that the heat     

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。     

对流传热过程强化与能耗分析

为了强化对流传热,工程上普遍采用提高流体流速和改变管路流体力学特性的方法,但在强化传热的同时,增加了能耗.通过实验分析了流体流速对光滑直管和螺旋槽管传热效果的影响,得到了滞流区和湍流区的传热关系式和阻力与流速的函数关系式.通过对比相同流速下光滑直管和螺旋槽管强化比与阻力的情况,得到了两种流型下强化比以及阻力与流速的关系式,为工程设计和生产操作提供了理论参考.     

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。     

Simultaneous Momentum,Heat, and Mass Transfer with Color Change during Paddy Storage in Silo

Abstract:

A theoretical model has been developed to describe heat, mass, and momentum phenomena in cylinder-shaped silos where paddy is stored. Calculation based on the model predicts local temperature and moisture within the silo as a function of time and space. This information is then coupled with known kinetics of color change to predict yellowness or whiteness generated during storage. The model is evaluated using the published data. Natural air currents and the corresponding moisture migration are small for short storage periods and more extensive for long-term storage. The calculated result shows the similar trend to the published data in that moisture migrates from the central region, where the grains experience high temperature, to the outer regions, where the grains have lower temperatures. Paddy near the wall and on the top of the silo has relatively lower whiteness than at inner areas for storing it at 15% wet basis, this low luminosity is in part motivated by relative humidity, which is relatively high at such areas. At elevated initial moisture contents, paddy at the inner areas has lower whiteness due to large accumulation of heat from grain respiration, hence, it is a predominant effect on the color change, while the humidity plays a minor role.     

气隙式膜蒸馏传递过程的研究

本文用气隙式膜蒸馏装置测定了膜两侧流体的温度、流量及料液浓度对膜蒸馏通量的影响,并从理论上描述了传热、传质过程,建立了可以预测膜蒸馏过程渗透通量的数学模型.实验结果与模型预测吻合较好.     

管内进口段对流换热过程不可逆性的数值模拟

The irreversibility due to laminar forced convection in the entrance region of a duct was studied by means of numerical simulation. Local entropy generation distributions and total entropy generation were obtained based on the entropy generation equation. The effect of Reynolds number on the irreversibility was studied for constant wall temperature and heat flux. The results showed that the irreversibility in the entrance region was different from that in the fully developed region. Reynolds number had a strong effect on the irreversibility in the entrance region. The entropy generation caused by temperature difference was relatively dominant over that caused by viscous flow. The irreversibility at constant wall temperature was different from that at constant wall heat flux.     

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。     

Heat and Mass Transfer Relationship in Combined Infrared and Convective Drying

Results from three experimental studies are reviewed in order to examine the relationship between the heat and mass transfer coefficients in the combined infrared and convective drying process. These results demonstrared that the heat     

Analysis of laminar flow forced convection heat transfer with uniform heating in the entrance region of a circular tube

A new integral or boundary-layer solution for laminar flow heat transfer in the combined entrance region of a circular tube is presented for the case of constant wall heat flux. The solution is based on the hydrodynamic inlet-filled region concept originally proposed by Ishizawa (1966) and later adopted by Mohanty and Asthana (1978) to hydrodynamically developing flow through a circular tube. Unlike available boundary-layer solutions, the new analysis provides results which join smoothly and asymptotically to the fully developed values. Results for the Nusselt number were found to agree favorably with available numerical solutions.     

液滴在热液相介质中上升汽化时的传热与传质

本文分析了液滴在不互溶的液相介质中上升汽化时的传热和传质,导出了数模,进行了数值求解,获知在泡滴与液相接触的汽液边界处温度下降和浓度升高,存在着溶液的过冷(或过饱和)边界层。实验结果与数模计算结果表明,该模型能够较好地预測液滴汽化的整体特性。