微波加热干燥毛细多孔介质的传热传质机理分析

本文在实验基础上系统分析了微波加热干燥湿物料的理论机理。提出了微波加热干燥毛细多孔湿物料是由初始加热阶段,压力泵水、泵汽(包括压力产生过程,压力泵汽水混合物主过程和压力驱动较难干燥水分蒸汽过程)阶段,干燥难干水分阶段组成。并结合反映每一阶段的主要特点建立了其特征物理模型。这些研究,比较全面的、抽象概括了微波加热干燥湿毛细多孔物料整个过程的物理特征。并初步分析了微波干燥过程驱动湿分的主动力——压力在无限长圆柱体内的分布规律。进而在分析的基础上提出了采用集总湿容法建立反映干燥规律较实用的物理模型。并根据电磁能吸收的特点,将干燥过程分为两段建立模型。这组模型能够比较好地反映实验规律。     

多孔介质传热传质分形理论初析

对分形理论在多孔介质传热传质过程中的应用进行了初步的分析,求出了基于分形理论的多孔介质固有渗透率和有效导热系数,建立了多孔介质渗流与导热的分形模型.     

含盐多孔材料传热传质研究

对含盐多孔材料内部温度、质度分布作了现场测定和数值模拟。建立了含盐多孔材料在一维温度质度场的耦合方程组,获得了其温度、质度动态分布规律,数值模拟结果与实测结果较为吻合,验证了数值模型的正确性,对促进含盐多孔材料热质迁移的研究,具有重要的意义     

液状制品真空冷冻干燥过程传热传质的研究

应用变时间步长有限差分法求解半球条件下冷冻升华干燥过程传热传质的非稳态数学模型，得到了冻干过程中制品内温度分布随时间变化的曲线,通过对牛奶的实验研究，检验了求解模型方法的可京隆和结果的直观性.     

模拟连续式振动流化床内传热传质的研究

在理论分析的基础上,将间歇模拟连续干燥的热质传递模型应用于振动流化床。测定了低气速(u＜u_(mf))下氧化铝大粒子在振动流化床干燥过程中的传质、传热系数,得出相应的关联式。为研究连续式振动流化床内传热提供了一种简便易行的方法。     

对撞流干燥的传热传质特性

对对撞流的传热传质过程进行了理论分析,论证了对撞流这一干燥形式强化传热传质过程的原理。设计了同轴对撞流干燥器,进行了对撞流强化传热传质过程的试验验证,总结了对撞流强化传热传质的特点和影响传热传质的因素。     

具有非均相化学反应的耦合传热传质熵产率方程

从质量、能量和熵平衡的基本原理出发,导出了具有非均相化学反应的耦合传热传质系统熵产率方程,得到了各种条件下熵产率方程的简化形式,为对具有非均相化学反应的耦合传热传质系统进行性能分析与改进提供了一种有力的工具。     

液状制品真空冷冻干燥过程传热传质的研究

应用变时间步长有限差分法求解半球条件下冷冻升华干燥过程传热质的非稳态数学模型，得到了冻干过程中制品内温度分布随时间变化的曲线。通过对牛奶的实验研究检验了求解模型方法的可靠性和结果的直观性。     

湿法脱硫塔一维传热传质性能模型理论与试验

为预测湿法脱硫系统(wet flue gas desulfurization, WFGD)浆液温度,提出湿烟气绝热饱和温度的概念,推导浆液温度与入口烟气温度及含湿量的函数关系。基于预测的浆液温度,建立脱硫塔内液滴运动、热质传递及压差分布一维耦合数学模型;分析脱硫系统三维不均匀性对于模型准确度的影响;用龙格-库塔法对模型进行迭代求解,探讨脱硫塔内主要运行变量(浆液颗粒直径、烟气入口温度及液气比)对传热传质的影响,获得相关参数的一维分布规律。为验证模型的正确性,分别进行现场测试和物模试验。结果表明,预测的浆液温度与现场实测温度有较好的一致性,最大相对误差为4.56%;浆液颗粒直径是影响传热传质的主要因素;颗粒在下降过程中速度迅速衰减,并趋向于最终不变值;烟气温度沿塔高呈指数规律分布。与模型预测温度及压力相比,物模试验温度分布与压力分布的最大相对误差分别为4.72%和6.46%。模型具有较高的准确度,对脱硫塔的设计、运行及SO₂的传质研究有指导意义。     

吸附式制冷吸附床内传热传质数学模型的数值求解

吸附床是吸附式制冷系统的核心部件,其传热传质性能的好坏直接影响到系统的制冷量.为了研究吸附床的传热传质特性,笔者建立了吸附式制冷系统中吸附床在非第一类边界条件时的一维传热传质的数学模型,并运用有限差分法对该数学模型进行了数值分析.该数学模型和计算结果有助于深入认识吸附床的传热传质特性,以期能为吸附床的具体设计提供理论依据     

长一维直通式辊底加热炉内传热数学模型研究

通过分析ＣＳＰ工艺中直通式辊底加热炉的热工及结构特性,采用地建立炉内辐射换热数学模型,与加热炉内连铸坯及炉衬的一维导热方程相耦合,建立长一维直通式辊底加热炉炉内传数学模型,通过对数注解,研究分析了不同的薄板坯移动速度及 种对加热炉炉内温度分布的影响。     

利用废轮胎热解炭制取活性炭的试验研究

热解炭是废轮胎热解的重要产物之一.以CO2气体作为活化剂对废轮胎热解炭制取活性炭的活化温度为820～950℃,活化时间为60～360 min.在试验条件下,活化温度越高,活化时间越长,活性炭烧失率越大,比表面积也越大.制得的活性炭具有与商业活性炭相似的中、大孔隙分布,而微孔则不发达,因此孔容积小于商业活性炭.在950℃,240 min条件下得到中等比表面积(306 m2/g)的活性炭.针对碘、苯酚和亚甲基蓝三种物质考察了活性炭的液相吸附特性.热解炭和活性炭对亚甲基蓝和苯酚具有良好的吸附性,而碘吸附值则与商业活性炭尚有较大差距.     

Heat mass transfer model of fouling process of calcium carbonate on heat transfer surface

A new heat mass transfer model was developed to predict the fouling process of calcium carbonate on heat transfer surface. The model took into account not only the crystallization fouling but also the particle fouling which was formed on the heat transfer surface by the suspension particles of calcium carbonate in the supersaturated solution. Based on experimental results of the fouling process, the deposition and removal rates of the mixing fouling were expressed. Furthermore, the coupling effect of temperature with the fouling process was considered in the physics model. As a result the fouling resistance varying with time was obtained to describe the fouling process and the prediction was compared with experimental data under same conditions. The results showed that the present model could give a good prediction of fouling process, and the deviation was less than 15% of the experimental data in most cases. The new model is credible to predict the fouling process. Supported by the National Basic Research Program of China (“973”Project) (Grant No. G2000026304) and the Beijing Municipal Elitist Cultivation Project (Grant No. 20061D0501500186)     

全氢罩式炉的发展与现状

从全氢罩式炉的结构、控制系统以及退火传热模型3个方面综述了全氢罩式炉的发展与现状.罩式炉的加热烧嘴由径向布置发展为切向布置;内罩的形式由光面发展为波纹型;冷却系统从单风冷发展为风冷-水冷系统和喷淋冷却系统.控制系统发展成为多级集散控制系统.传热模型研究范围很广泛,涉及到模型的建立、模型热工参数、热应力场、温度场模拟、控制模型等.指出了在传热模型方面还需要对热态流场问题和模型的普遍适用性进行进一步研究.     

Mathematical Model on heat transfer of water—cooling steel—stick bottom electrode of DC electric arc furnace

For predicting and controlling the melted depth of bottom electrode during the process of steelmaking,the water-cooling steel stick electrode is taken as an example.to analyze the process of heat transfer,then 3D mathematical model by control capacity method is built.At the same time,the measurement on the melted depth of bottom electrode is conducted which verified the correctness of the built mathematical model.On the base of verification,all kinds of key parameters are calculated through the application and a series of results are simulated.Finally,the optimum parameters are found and the service life of bottom electrode is prolonged.     

Modeling and numerical analysis of evaporative condensing regenerator

A two-dimensional steady state model was developed and solved numerically to predict the performance of evaporative condensing regenerator. Two-dimensional parameter distributions of air, solution and refrigerant were calculated by the mathematical model. The solution content first increases and then decreases along the solution flow direction. At y/H _r=0.98 (where H _r is the height of regenerator), air humidity increases from 1.99% to 2.348% firstly and then decreases. The experimental results were used to validate mathematical model. It is indicated that the simulation results agree with experimental data well. The results not only show that the mathematical model can be used to predict the performance of regenerator, but also has great value in the design and improvement of evaporative condensing regenerator.     

退火钢卷辐射换热及对流换热的讨论

主要研究罩式炉退火钢卷在退火过程中,对流热流及辐射热流的变化情况及其影响因素,由此得到退火过程的不同阶段对流热和辐射热的大小比较,以判断在计算过程中,忽略辐射热流是否合理。计算得出,到退火加热中期,钢卷通过对流获得总热量是通过辐射获得的总热量的35倍,到保温中期,这两个量仅相差9倍,且退火保温时间越长,二者差距越小。     

内热式多级连续蒸馏真空炉传热过程分析

在建立系统能量平衡公式的基础，对真空炉内的传热过程进行分析，由此，从传热学的角度上推理真空炉生产最优化控制的可能。     

钢坯加热仿真在实际系统中的应用

主要研究了钢铁企业中钢加热炉内钢坯的加热过程。使用VC 编程实时计算出炉内钢坯的温度分布。用MSSQL在钢坯温度计算过程中进行参数传递,在保证满足加工工艺的基础上对加热过程进行最优自动控制。     

Zonal method solution of radiative heat transfer in a one-dimensional long roller-hearth furnace in CSP

A radiative heat transfer mathematical model for a one-dimensional long furnace was set up in a through-type roller-hearth furnace （TTRHF） in compact strip production （CSP）. To accurately predict the heat exchange in the furnace, modeling of the complex gas energy-balance equation in volume zones was considered, and the heat transfer model of heating slabs and wall lines was coupled with the radiative heat transfer model to identify the surface zonal temperature. With numerical simulation, the temperature fields of gas, slabs, and wall lines in the furnace under one typical working condition were carefully accounted and analyzed. The fundamental theory for analyzing the thermal process in TI＇RI-IF was provided.