换热器课程中传热计算方法教学探究

通过在教学中采用比较的方法同步讲解换热器课程中平均温差法和效率传热单元法两种传热计算方法,并通过实际工程实例进一步说明两种方法在换热器设计计算和校核计算中的优缺点及试用场合,利于学生理解和开阔思路,取得较为满意的教学效果。

基于标准火灾曲线和热释放率的衬砌温度分布数值计算研究

为探明火灾下衬砌温度的分布特性,基于隧道火灾-衬砌辐射对流传热数学模型建立了衬砌温度数值计算方法,并对HC标准火灾曲线和30 MW火灾热释放率火灾工况进行计算分析。结果表明,标准火灾曲线最高温度普遍大于目前我国规范的要求。采用火灾温度作为衬砌壁面边界条件将显著增大衬砌温度荷载,2小时HC火灾曲线和30 MW火灾工况衬砌最高温度分别为778℃和351℃。标准火灾曲线工况衬砌内部的高温影响范围和高温值均显著大于30 MW火灾工况。

球团内保温管道传热计算方法研究

链箅机-回转窑-环冷机球团工程中设置热风循环系统对料层进行干燥、预热并加速氧化反应,该系统需要采用热风管道作为媒介,管道的管内介质温度比较高,管道材质要求及生产运行安全要求也相应比较高。为了实现安全生产,同时降低管道制造成本,需要研究一种准确的计算球团热风管道的方法,因此提出了一种球团工程内保温形式热风管道的传热计算方法。该方法对确定管皮温度、选择钢管材质等工作具有指导作用。

基于传热反问题方法的N2O/C2H4预混推进剂燃烧室热流测量研究

测量液体火箭发动机的热载荷是获取燃烧室内部信息的重要方法。为了获取N2O/C2H4预混推进剂燃烧室内壁的热载荷,建立了液体火箭发动机的热流计算的反问题方法,该方法基于对燃烧室壁面温度场的直接求解,通过对轴向多个位置测量温度的反演计算得到燃烧室内壁热流和温度。研究表明:应用文中建立的传热反问题方法能够较为准确地获得热流随时间及空间的分布;热电偶的位置对计算准确性有明显的影响,与理论深度偏差在0.2mm以内的随机深度偏差可导致超过4%热流反演误差;N2O/C2H4预混推进剂燃烧室热流及温度沿轴向逐渐降低,表明燃烧室内的反应释热过程主要在燃烧室头部附近发生。

触地围护结构传热问题的分析研究

目前关于触地围护结构传热问题的分析求解结果,其形式均比较复杂,实用性不强。国内现行的计算传热量的方法,过程亦较繁琐。本文通过深入分析,提出一种新形式的假设,使温度边界条件的模拟更接近实际,在复变域内求出了相应温度场的数学分析解,该解函数形式简单,实用性强,拓宽了研究范围,深化了讨论内容,为简化工程计算方法建立了基础。

双层模组动力电池包热管理设计与优化

某SUV动力电池包采用双层模组设计,双层模组的上层模组安装结构采用了冷却板与支撑结构一体化设计。测试结果表明,该设计在测试中出现模组温差过大问题(达8℃)。基于此,研究小组通过尺寸链与CAE分析,将尺寸链闭环中导热垫产生的形变、冷却板的形变与电芯底部承受力限值进行耦合计算,校核出最优尺寸边界(上层冷却板贴合面深度从1.2mm优化至1.05 mm),将电池包温差控制在5℃以内,满足了设计要求。仿真结果表明,该方法将尺寸链与CAE、Simulink多工具耦合,可以高效提供设计方案,减少验证费用,是经济有效的传热设计方法。

Analysis and modeling of alumina dissolution based on heat and mass transfer

A comprehensive heat and mass transfer model of dissolution process of non-agglomerated and agglomerated alumina particles was established in an aluminum reduction cell. An appropriate finite difference method was used to calculate the size dissolution rate, dissolution time and mass of alumina dissolved employing commercial software and custom algorithm based on the shrinking sphere assumption. The effects of some convection and thermal condition parameters on the dissolution process were studied. The calculated results show that the decrease of alumina content or the increase of alumina diffusion coefficient is beneficial for the increase of size dissolution rate and the decrease of dissolution time of non-agglomerated particles. The increase of bath superheat or alumina preheating temperature results in the increase of size dissolution rate and the decrease of dissolution time of agglomerated particles. The calculated dissolution curve of alumina（mass fraction of alumina dissolved） for a 300 k A aluminum reduction cell is in well accordance with the experimental results. The analysis shows that the dissolution process of alumina can be divided into two distinct stages： the fast dissolution stage of non-agglomerated particles and the slow dissolution stage of agglomerated particles, with the dissolution time in the order of 10 and 100 s, respectively. The agglomerated particles were identified to be the most important factor limiting the dissolution process.

A New Heat-conduction Logging Technique and its Application

The results of a heat-conduction experiment with a central point source in a sand barrel shows that the temperature of the heat source increase much faster in sand saturated with oil and air （dry sand） than in water sand. During cooling the temperature of the central heat source goes down slower in oil- or air-saturated sands than in water sands. Based on the theory of heat-conduction in porous media and the experimental results, we developed a new heat-conduction logging technique which utilizes an artificial heat source （dynamite charge or electric heater） to heat up target forma- tions in the borehole and then measure the change of temperature at a later time. Post-frac oil production is shown to be directly proportional to the size of the temperature anomaly when other reservoir parameters are fairly consistent. The method is used to evaluate potential oil production for marginal reservoirs in the FY formation in Song-Liao basin of China.

Developments in the understanding of gas–solid contact efficiency in the circulating fluidized bed riser reactor:A review

In the last several decades, circulating fluidized bed reactors have been studied in many aspects including hydrodynamics, heat and mass transfer and gas–solid two phase contacting. However, despite the abundance of review papers on hydrodynamics, there is no summary paper on gas–solid contact efficiency to date, especially on high density circulating fluidized beds(CFBs). This paper gives an introduction to, and a review of the measurement of contact efficiency in circulating fluidized bed riser. Firstly, the popular testing method of contact efficiency including the method of heating transfer experiment and hot model reaction are discussed, then previous published papers are reviewed based on the discussed methods. Some key results of the experimental work are described and discussed. Gas–solid contact efficiency is affected by the operating conditions as well as the particle size distribution. The result of the contact efficiency shows that the CFB riser is far away from an ideal plug flow reactor due to the characteristics of hydrodynamics in the riser. Lacunae in the available literature have been delineated and recommendations have been made for further work.

Transferring a Multi-atom Entangled State via Adiabatic Passage

We present a scheme for transferring atomic entangled states via adiabatic passage. In the scheme, we use photons to achieve efficient quantum transmission among spatially distant atoms. The probability of the successful transferring quantum state approaches 1. Meanwhile, the scheme is robust against the effects of atomic spontaneous emission.

Operator Fredholm Integration Equation in Intermediate Coordinate-Momentum Representation and Its Analogue to Thermo Conduction Equation

Using the technique of integration within an ordered product （IWOP） of operators we construct intermediate coordinate-momentum representation, with which we build a type of operator Fredholm integration equation that is an operator generalization of the solution of thermo conduction equation. Then we seach for the solution of operator Fredholm integration equations, which provides us with a new approach for deriving some operator identities.

An improvement to the simulation of phase-change heat-transfer during soil freezing and thawing

A new variable time step method,which is called the backwards calculating time step method,is presented in this paper.It allows numerical simulation of soil freezing and thawing while avoiding "phase change missing and overflowing".A sensitive heat capacity model is introduced through which the calculation errors are analyzed.Then the equation using the self-adjusted time step is presented and solved using finite differences.Through this equation,the time needed for a space cell to reach the phase change point temperature is calculated.Using this time allows the time step to be adjusted so that errors caused by "phase change missing and overflowing" are successfully eliminated.Above all,the obvious features of this method are an accelerated rate for adjusting the time step and simplifing the computations.An actual example proves that this method can accurately calculate the temperature fields during soil freezing and thawing.It is an improvement over traditional methods and can be widely used on complicated multi-dimensional phase change problems.

Discriminated Dimensional Analysis Versus Classical Dimensional Analysis and Applications to Heat Transfer and Fluid Dynamics

In contrast to classical dimensional analysis, discriminated dimensional analysis assumes that spatial coordinates are dimensionally independent of each other and allows other types of geometrical quantity to be used in the dimensional basis, such as surfaces and angles. As a consequence, discriminated dimensional analysis leads to a lower number of dimensional groups, which makes the solution more precise. Besides, these discriminated groups have a clear physical meaning in terms of force and energy balances. The paper introduces this technique and provides dimensional equations for the main quantities and physical parameters of the heat transfer and fluid flow fields. Two applications are presented to demonstrate the efficiency of this method.

Teleportation of an Unknown Atomic State via Adiabatic Passage

We propose a scheme for teleporting an unknown atomic state via adiabatic passage. Taking advantage of adiabatic passage, the atom has no probability of being excited and thus the atomic spontaneous emission is suppressed. We also show that the fidelity can reach 1 under certain condition.

Thermal Error Compensation for Telescopic Spindle of CNC Machine Tool Based on SIEMENS 840D System

In this paper, eddy current sensors and thermocouple sensors were employed to measure the thermal field and thermal deformation of a spindle of a telescopic CNC boring-milling machine tool, respectively. A linear regression method was proposed to establish the thermal error model. Furthermore, two compensation methods were implemented based on the SIEMENS 840D system by using the feed shaft of z direction and telescopic spindle respectively. Experimental results showed that the thermal error could be reduced by 73.79% when using the second compensation method, and the thermal error could be eliminated by using the two compensation methods effectively.

Theoretical and experimental research on heat transfer performance of the semi-open heat pipe

This paper focuses on the heat transfer performance of semi-open heat pipe which is a new type of heat pipe. After analyzing its condensation heat transfer mechanisms theoretically, several semi-open heat pipes in different length ratios and upper hole diameters are studied experimentally and compared with the same dimensions closed heat pipes. Experimental results show that the heat transfer performance of semi-open heat pipe becomes better by increasing heat transfer rate. At the first transitional point, the heat transfer performance of semi-open heat pipe approaches the level of the closed heat pipe. It is suitable to choose upper small hole about 1 mm in diameter and length ratio larger than 0.6 for the semi-open heat pipe.

Prediction of Fluid Velocity Distribution near a Rising Bubble

Flow and concentration fields of liquid phase in a gas-liquid contacting system are simulated to showthe Rayleigh convection by utilizing the finite-element method. The Schlieren images in CO2-ethanol system provided direct visual verification of the present simulation, and the simulated results were well consistent with theexperimental observation. The influence of the Rayleigh convection on mass transfer is analyzed qualitatively andquantitatively based on the simulated and the experimental results.