热漏对换热器(火积)耗散最小化的影响

建立了存在热漏的换热器的传热过程模型.假定热流体与冷流体间的传热以及冷流体与外界环境间的热漏均服从牛顿传热定律,在冷流体净传热量一定的条件下,应用最优控制理论导出了换热过程(火积)耗散最小时热流体温度和冷流体温度的最优构型,并将最优路径分别与热流体温度一定和热流率一定的传统传热策略进行了比较.研究结果对于实际换热器的优化设计和最优运行具有一定的理论指导意义.     

EAST 第一壁水冷结构类型传热能力的比较分析

为了能够更加直接地比较EAST 中第一壁水冷结构的传热能力，给出在未来设计中的选型参考，利用模拟分析的手段对现有的以及正在研制的水冷结构进行了在相同的工况下传热能力的对比分析。通过比较水冷结构中不同材料的温度，得到传热能力的优劣，同时考虑各种材料的许用温度，结合工艺难度及工程造价等因素对各结构进行了整体比较。计算结果显示，就传热能力而言，钨串结构最好，焊接结构次之，螺栓连接结构最差。结合造价及工艺难度等条件可以看出，钨串结构仍是目前最适用于高热负荷区域的结构，W/TZM/C 作为第一壁材料的焊接结构适用于较低热负荷的区域，螺栓连接结构在未来发展中将会逐渐被取代。     

Thermal—fluid modelling of an air—cooled condenser for refrigerants

A steady state thermodynamic model for an air—cooled finned—tube condenser, used in a typical deep freezer vapour compression system, operating with pure and refrigerant mixtures has been developed using finite difference method. The heat transfer aspects in the condenser are treated uniquely for superheated, two—phase and subcooled regimes and studied for various heat load, pressure, temperature, and mass flow rate. The condensation heat transfer coefficient, the tube length required for condensation, the degree of subcooling, and the temperature glide for different ambient temperatures are estimated. The simulation and the experimental results are in good agreement.     

Near-field heat transfer: A radiative interpretation of thermal conduction

It is shown in this article that the near-field radiative heat transfer can be interpreted as a conduction heat transfer due to the propagation of polaritons. We consider two situations. In the first one, two heated bodies at different temperatures are separated by a gap and in the second one a temperature gradient is imposed to a bulk material. In both situations, the radiative heat transfer is calculated by means of fluctuational electrodynamics. Asymptotic expressions of a thermal conductivity are obtained from the radiative heat transfer calculation. We interpret this conductivity as a consequence of the heat transfer by propagation and collisions of polaritons.     

Analysis of three-fluid separate type heat pipe exchanger

This paper puts forward an analytical model of heat transfer of a three-fluid separate type heat pipe exchanger. A universal basic temperature transfer matrix equation is obtained from the analysis of heat transfer. The equation is suitable for predicting performance of the parallel- or counter-flow type exchanger in that heat is transferred between one hot fluid and two cold fluids or between two hot fluids and one cold fluid. Finally, a calculated engineering example is taken, and the proposed model and result is proved to be reasonable.     

竖直微槽道内沸腾换热CHF实验研究

对于沸腾换热,一个主要的约束条件就是临界热流密度(Critical Heat Flux,简称CHF)。这个约束条件对沸腾换热量有一个最高值的限制。文中对矩形微槽道中的流动沸腾临界热流密度进行了实验研究。实验数据是在不同尺寸(0.15mm;0.4mm;1mm)微槽道中,在较大范围的面积质量流速和不同进口过冷度下,以去离子水为工质得到的。实验过程中发现,达到CHF时,靠近出口壁面温度会突然升高,此时传热效率迅速下降。实验数据分析结果表明:CHF随质量流量的增加而增加;进口过冷度对CHF没有明显影响;CHF随着出口干度的增加而降低。     

评估固体激光器对流换热系数的方法

 为提高固体激光器的热管理效果,提出了一种使用316L不锈钢片代替激光晶体评估固体激光器表面对流换热系数的方法。在低冷却水温的条件下,使用快响应热电偶对替代片和出口水流的动态温度进行测量,应用有限元方法计算不同对流换热系数下替代片的动态温度,讨论了对流换热系数对重频大能量激光器热效应的影响。通过寻找测量值和计算值的最小方差,得到该冷却结构下的激光器表面对流换热系数为3 500 W·m^-2·K^-1。     

Flow condensing heat transfer of R410A,R22, and R32 inside a micro-fin tube

An experimental study of condensation heat transfer characteristics of flow inside horizontal micro-fin tubes is carried out using R410A, R22, and R32 as the test fluids. This study especially focuses on the influence of heat transfer area upon the condensation heat transfer coefficients. The test sections were made of double tubes using the counter-flow type; the refrigerants condensation inside the test tube enabled heat to exchange with cooling water that flows from the annular side. The saturation temperature and pressure of the refrigerants were measured at the inlet and outlet of the test sections to defined state of refrigerants, and the surface temperatures of the tube were measured. A differential pressure transducer directly measured the pressure drops in the test section. The heat transfer coefficients and pressure drops were calculated using the experimental data. The condensation heat transfer coefficient was measured at the saturation temperature of 48°C with mass fluxes of 50–380 kg/(m²s) and heat fluxes of 3–12 kW/m². The values of experimental heat transfer coefficient results are compared with the predicted values from the existing correlations in the literature, and a new condensation heat transfer coefficient correlation is proposed.     

Self-rewetting carbon nanofluid as working fluid for space and terrestrial heat pipes

Thermal management is very important in modern electronic systems. Recent researches have been dedicated to the study of the heat transfer performances of binary heat transfer fluids with peculiar surface tension properties and in particular to that of “self-rewetting fluids”, i.e., liquids with a surface tension increasing with temperature and concentration. Since in the course of liquid/vapor-phase change, self-rewetting fluids behavior induces a rather strong liquid inflow (caused by both temperature and concentration gradients) from the cold region (where liquid condensates) to the hot evaporator region, this fluids have been proposed and investigated as new heat transfer fluids for advanced heat transfer devices, e.g., heat pipes or heat spreaders for terrestrial and space applications (Savino et al. in Space Technol 25(1):59–61, 2009). The present work is dedicated to the study of the thermophysical properties of a new class of heat transfer fluids based on water/alcohol solutions with suspended carbon nanostructures, in particular single-wall carbon nanohorns (SWNH), synthesized by a homemade apparatus with an AC arc discharge in open air (Mirabile Gattia et al. in Nanotechnology 18:255604, 2007). SWNHs are cone-shaped nanoparticles with diameters between 1 and 5 nm and lengths in the range of 20–100 nm. SWNHs could be found in the form of quite-spherical aggregates with diameters ranging from 20 to 100 nm. The paper also discusses the results of these investigations and laboratory characterization tests of different heat pipes, including reference ordinary heat pipes and innovative pipes filled with self-rewetting fluids and self-rewetting nanofluids. The potential interest of the proposed studies stems from the large number of possible industrial applications, including space technologies and terrestrial applications, such as cooling of electronic components.     

Working fluids for heat transformers

A large amount of thermal energy, in the temperature range of 50–90°C, released to the atmosphere by many commercial installations such as agrofeed, paper mills, dairies and process industries, can be upgraded making possible its use in various forms. Many attempts have benn made in most industrial sectors to recovery this energy by heat pumps, organic Rankine cycles and heat transformers. Among various possibilities, heat transformers present an attractive solution as low level heat can be transformed into a higher temperature with minimum consumption of external energy. Further transformers do not require high maintenance and operating cost.The theoretical performance characteristics of single stage heat transformers using various promising binary mixtures as working fluids have been discussed in this paper. The coefficient of performance, energy efficiencies and mass circulation ratio have been analysed as a function of heat delivery temperature. The comparison of working fluids has also been discussed.     

线性与非线性传热过程的Curzon-Ahlborn热机在任意功率时的效率

热机性能的优化是热力学领域的一个重要问题,而工质与热源之间的传热过程是热机工作时产生不可逆的主要来源.本文在引入功率增益和效率增益两个重要参数的基础上,基于一个简化的Curzon-Ahlborn热机模型并利用合比分比原理,给出了线性与非线性传热过程的热机在任意功率输出时的效率表达式,结合数值计算详细讨论了热机在任意功率输出时的特性.研究表明,参数ξ作为功率增益δP的函数存在两个分支:在第一分支上(不利情形),效率呈现出单调变化特征;在第二分支上(有利情形),效率随着的δP变化是非单调的且有最大值.随着传热指数的增加,热机的工作区域减小,这源于非线性传热过程包含热辐射所致.进一步发现功率-效率关系曲线存在权衡工作点,热机在该点附近工作能够实现最有效的热功转换.研究结果有助于深入理解具有不同传热过程热机的优化执行.     

Specific heat of electron gas of arbitrary dimensionality

The exchange contribution to the specific heat of an electron gas in d dimensions is calculated and is shown to lead to a logarithmic temperature dependence at low temperatures in all dimensions (d > 1).     

半干旱草原下垫面动量和感热总体输送系数参数化关系研究

本文利用锡林郭勒草原2008年春季近地层涡旋相关系统和铁塔的风、 温平均梯度观测资料, 分析了总体输送系数随梯度Richardson数的变化特征, 建立了动量总体输送系数随大气稳定度、近地层风速以及感热总体输送系数随大气稳定度和近地层气温的关系. 中性条件下, 半干旱草原植被下垫面动量总体输送系数与近地层大气动力状态之间存在明显的相互作用, 总体输送系数与近地面层风速之间满足二次曲线拟合关系; 风速较小时, 大气动力特征对地表粗糙度长度的改变不是很明显, 动量总体输送系数随气流增强而增大; 而当风速较大时, 强风速会使植被高度发生改变, 动量总体输送系数随气流增强而减小. 另外, 感热总体输送系数与近地层气温之间也存在二次曲线关系. 动量总体输送系数与近地层风速之间的关系、感热总体输送系数与近地层气温之间关系的建立为总体输送系数参数化提供了重要途径, 同时该方案避免了对动力学粗糙度长度和热力学粗糙度长度的求解. 关键词： 总体输送系数 参数化 湍流通量 相似性函数     

Optimal configuration of a class of endoreversible heat engines for maximum efficiency with radiative heat transfer law

Optimal configuration of a class of endoreversible heat engines with fixed duration, input energy and radiative heat transfer law (q ∝ Δ(T ⁴)) is determined. The optimal cycle that maximizes the efficiency of the heat engine is obtained by using optimal-control theory, and the differential equations are solved by the Taylor series expansion. It is shown that the optimal cycle has eight branches including two isothermal branches, four maximum-efficiency branches, and two adiabatic branches. The interval of each branch is obtained, as well as the solutions of the temperatures of the heat reservoirs and the working fluid. A numerical example is given. The obtained results are compared with those obtained with the Newton’s heat transfer law for the maximum efficiency objective, those with linear phenomenological heat transfer law for the maximum efficiency objective, and those with radiative heat transfer law for the maximum power output objective.     

Z箍缩驱动混合堆包层瞬态传热特性

Z箍缩驱动聚变-裂变混合能源堆(Z-FFR)以较长周期(10s)脉冲式运行,为实现3000 MW的热功率输出,单个脉冲需要产生的能量较大,包层和第一壁在强热冲击下的瞬态传热和温度特性是决定Z-FFR技术可行性的关键问题之一。通过理论计算,分析了在连续脉冲作用下包层和第一壁温度随时间的变化规律。同时以输出恒定的电功率为目标,提出了展平系统输出功率的简便方法,并分析了出口冷却剂温度的波动特性。结果表明材料最高温度均在安全限值内,第一壁表面瞬时高温层厚度约为0.5mm,系统输出功率波动幅度在-2.84%~+2.05%范围内。     

低温试验冷库传热系数的测量研究

简述了对于低温冷库传热系数测量所采用的一般方法,采用稳态法对一低温试验冷库进行了测量实验,然后通过非稳态积分法对试验数据进行验证。针对冷风机电机功率较大的特点,本实验采用变频器将电机功率调小,从而成功得出该低温试验冷库的传热系数。并与理论计算的数据进行对比,找出存在差别的原因。     

可调谐二极管激光吸收光谱测量真空环境下气体温度的理论与实验研究

真空环境不仅会导致热电偶等温度传感器表面材料解吸,而且其传热机理也与常压不同,因此采用常压下校准和溯源的温度传感器测量真空环境下气体温度存在诸多不确定性问题,为此,本文利用可调谐二极管激光吸收光谱技术(TDLAS)测量真空环境下气体温度,探索TDLAS温度测量技术在真空环境下的应用前景,在模拟热真空实验过程中,首先将真空气室浸没于恒温槽中,然后利用TDLAS测量真空气室中气体温度,同时利用一等标准铂电阻测量恒温槽的温度,试验结果表明:TDLAS和一等标准铂电阻测量得到的气体温度和恒温槽温度具有高度的一致性,两者之间的误差在恒温槽温度稳定时不超过±0.2℃。     

基于拟沸腾理论的超临界CO2管内传热恶化量纲分析

超临界流体广泛应用于工程技术领域,其流动传热特性对工程设计具有重要意义,但是,由于超临界流体的物理微观和宏观行为的机理尚不清晰,所以其异常的流动传热特性并未得到很好的解决.普遍认为超临界流体在分子尺度上可分为类气和类液两种不同的特性,直到最近通过实验在宏观上监测到超临界水类液和类气之间的转变,且这一过程与拟沸腾理论一致,使得问题逐渐变得清晰.本文基于拟沸腾理论对超临界CO2异常流动传热行为进行了研究,在假设类液和类气转换过程不均匀的情况下,从经典的量纲分析和亚临界过冷沸腾理论模型出发,提出了一个适用于超临界流体拟沸腾换热过程的分析方法.通过引入表征类气膜生长速度与流体主流平均流速之比π=(qw·ρ1)/(G·Δi·ρg)和表征近壁区类气膜温度梯度π13=(qw·βpc·di)/λg两个无量纲数,来表征拟沸腾如何导致传热恶化,解释了超临界CO2竖直向上加热流动过程中的异常换热特性,即较大的类气膜生长速度使近壁区快速聚集了较多的高温流体,而较大的类气膜温度梯度使类气膜覆盖在壁面.当核心的冷类液不能充分润湿热壁面时,传热恶化.新无量纲数较好的诠释了超临界流体拟沸腾诱导传热恶化机制,为超临界拟沸腾传热研究提供了理论依据.     

Circular radiation heat shields with temperature dependent emissivities: transient and steady-state analyses

Radiation heat loss is an important type of heat loss in thermal systems. In this work, a numerical study of the transient response of two circular radiation heat shields inserted between two parallel and circular surfaces of emissivities ε₁ and ε₂ is presented. The same dimensions have been assumed for the two main radiating surfaces and the two radiation shields. The radiation shields are assumed to have different emissivities on their top (ε₃ and ε₅) and bottom ( ε₄ and ε₆) surfaces, and both are assumed to be different but linear functions of temperature. A specific configuration is investigated in detail to highlight the transient temperature and heat transfer characteristics of the system. Some new results for the transient temperature and heat transfer characteristics of the system such as the effect of shield location, shield emissivities, the temperature dependence of shield emissivities, system dimensions, temperatures of the hot and cold surfaces and emissivities of the hot and cold surfaces are presented for future references. It has been observed that increasing the temperature of the first radiation shield by changing a parameter such as surface emissivity or distance between the radiation shield or the temperature of the hot surface, will not necessarily decrease the temperature of the second radiation shield.     

Feasibility and design studies for heat recovery from a refrigeration system with a canopus heat exchanger

This paper presents an investigation of the feasibility of heat recovery from the condenser of a vapour compression refrigeration (VCR) system through a Canopus heat exchanger (CHE) between the compressor and condenser components. The presence of the CHE makes it possible to recover the superheat of the discharged vapour and utilize it for increasing the temperature of the external fluid (water) removing heat from the condenser. The effects of the operating temperatures in the condenser and evaporator for different inlet water temperatures and mass flow rates on the heat recovery output and its distribution over the condenser and CHE (the fraction of the condenser heat available through the CHE), available outlet water temperature and heat recovery factor have all been studied and optimum operating parameters for feasible heat recovery have been ascertained. The parametric results obtained for different working fluids, such as R-22, R-12, R-717 and R-500, have been presented. It is found that, in general, a heat recovery factor of the order of 2.0 and 40% of condenser heat can be recovered through the Canopus heat exchanger for a typical set of operating conditions.