肋板式吸附床传热性能的数值模拟

设计了新型肋板式结构吸附床,建立了吸附床在非第一类边界条件的三维传热传质数学模型.应用计算流体动力学中有限控制体积方法对吸附床内传热特性进行了模拟计算,并通过研究吸附床内温度随时间的动态变化,分析了换热流体参数和吸附剂导热系数变化对床层传热特性的影响.计算结果表明,吸附剂的导热系数,换热流体流速、温度对床层传热特性影响显著且肋板式吸附床传热效率高,吸附床内温度分布均匀.     

太阳能固体吸附式制冷吸附床的设计及数值模拟分析

设计了管内填充吸附剂,管外走传热介质的新型吸附床结构,建立了相应的数学模型.以太阳能为驱动热源,分析了吸附床内温度在某时刻的静态分布以及温度、压力和脱附速率随时间的动态变化.通过对吸附床传热效果的分析指出该吸附床结构有较好的传热效果.     

固体吸附式制冷系统中吸附床传热强化及设计

吸附床是吸附式制冷系统的核心部件。分析吸附床的传热特性,总结归纳吸附床强化传热的方法,分别采用物化处理法、制冷循环改进法和结构法,认为吸附床的结构设计是整个吸附制冷系统性能改善重要方法。最后,在综合前人研究成果的基础上,提出和分析了一种新型的吸附床的结构设计方案。     

套管式吸附床传热性能的数值模拟

建立吸附床的传热数学模型,对套管式吸附床的传热性能进行数值模拟,并对影响吸附床传热性能的因素进行分析。结果表明:吸附剂导热系数是影响吸附床传热性能的关键因素,减小床层厚度和缩小套管的尺寸也能够明显改善吸附床的传热性能。     

化学吸附式制冷系统传热传质的数值模拟和实验研究

运用多孔介质理论分析了化学吸附式制冷系统中的吸附床,按多孔介质的质量、动量和能量传递过程建立了吸附床内流动、传热和传质耦合求解的数学模型,并根据吸附剂在吸附床内多孔介质中的流动特性,采用比经典的Darcy模型更精确的多孔介质流动模型-Ergun模型。所建立的数学模型较之现有的吸附床传热传质数学模型能更全面、准确的描述吸附床的传热传质特性。将所建立的模型对化学吸附制冷样机进行了模拟计算,计算结果和测试结果吻合得较好。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,并可进一步用于吸附床和系统的优化设计。     

煤矿锅炉房热交换器比较及选型

本文阐述了现用浮动盘管式热交换器、板式热交换器的使用情况及通过对板式热交换器、浮动盘管式热交换器和螺旋螺纹管热交换器从设备的结构、体积、传热效率、节能等几方面阐述了三者的特点,进行比较分析,为锅炉房热交换器的选型提供了参考依据。     

固体吸附式制冷系统中吸附床内的传热传质过程分析和强化

利用多孔性物质的吸附分离原理分析了固体吸附式制冷系统中吸附剂颗粒和整个吸附床的传热传质特性,并在此基础上介绍了目前国内外强化吸附床传热传质性能的主要措施。     

吸附式制冷系统传热传质的简化分析及吸附床的设计

近年来，围绕解决阻碍吸附式制冷系统走向市场的技术问题展开了许多研究，研究结果表明，采用经济实用又能改善传热传质的吸附床比较关键。本文对吸附床的传热传质做了简化分析，并对各种吸附床进行比较，在此基础上设计了一种新型的吸附床。     

固体吸附式制冷系统新型针刺板吸附床数值模拟研究

固体吸附式制冷系统中吸附床内填充的吸附剂是一种多孔材料,由于多孔结构的存在,床体与吸附剂颗粒及吸附剂颗粒之间存在较大的热阻,因而存在传热速率慢,传热不均匀的缺点;在已有的板翅式吸附床基础上提出了一种新型针刺板吸附床,利用针刺丰富的扩展表面作为传热面,解决吸附剂内传热速率慢、温度场不均匀的问题。     

非平衡吸附特征的吸附床传热传质特性

建立椰壳活性炭-甲醇吸附式制冷系统吸附床传热传质数学模型,应用该模型进行具有非平衡吸附特性的吸附床传热传质研究,利用数值方法对数学模型进行求解,讨论了吸附床在冷却过程中吸附剂温度、吸附速率、吸附量、制冷系数以及单位质量吸附剂制冷功率与时间的关系,吸附床在加热过程中吸附剂温度、脱附速率及脱附量与时间的关系.研究结果表明:吸附床在整个吸附过程中的吸附速率存在一个峰值0.001 2 ks/s,吸附床在整个脱附过程中的脱附速率存在一个峰值0.001 7ks/s,吸附剂温度变化率在换热阶段趋于平缓,制冷系数值在吸附阶段近似呈线性增长,而单位质量吸附荆制冷功率在吸附阶段存在一个峰值35 kW/kW.     

Application of an embossed plate heat exchanger to adsorption chiller

The present research conducted a parametric study on an embossed plate heat exchanger (plate HX) type adsorption chiller with SWS-1L and water pair, using a numerical method. The plate HX has a relatively high heat transfer capacity and compact size, and this study is a first attempt to apply the plate HX as a new type of adsorption chiller, as an improved alterative to the fin-tube type heat exchanger. A feasibility study was conducted on the base model and the result is comparable to the value for existing fin-tube type adsorption chillers. Furthermore, a parameter study was conducted for seven important design parameters, embossing diameter ratio, embossing height, embossing pitch, bed thickness, plate thickness, heating temperature and heat transfer fluid velocity. The results provided guidelines for the optimal designs of plate HX type adsorption chiller. The optimal values of COP and SCP were 0.5118 and 662.8 W kg⁻¹, respectively.     

太阳能吸附制冷空调吸附床温度场数值模拟与传热分析

建立了吸附床几何模型和数学模型,通过Fluent软件数值模拟得到床层温度分布的变化情况,并深入分析床层参数变化对床层温度分布的影响。结果表明,吸附剂的物性参数对床层温度分布影响显著;换热流体流速、温度对床层温度影响不大。在床层径向上存在着较大的温度梯度,但在轴向上温度分布比较均匀。在吸附剂的物性参数中,导热系数对床层温度变化影响最大。因此为了提高吸附床传热效率,应尽量增大吸附剂的导热系数,以及采取多种措施强化吸附床的传热效率。     

Forced convection adsorption cycle with packed bed heat regeneration: Cycle à adsorption à convection forcée avec régénération thermique du lit fixe

The convective thermal wave is part of a patented cycle which uses heat transfer intensification to achieve both high efficiency and small size from a solid adsorption cycle. Such cycles normally suffer from low power density because of poor heat transfer through the adsorbent bed. Rather than attempting to heat the bed directly, it is possible to heat the refrigerant gas outside the bed and to circulate it through the bed in order to heat the sorbent. The high surface area of the grains leads to very effective heat transfer with only low levels of parasitic power needed for pumping. The new cycle presented here also utilises a packed bed of inert material to store heat between the adsorption and desorption phases of the cycle. The high degree of regeneration possible leads to good coefficients of performance (COPs). Thermodynamic modelling, based on measured heat transfer data, predicts a COP (for a specific carbon) of 0.90 when evaporating at 5°C and condensing at 40°C, with a generating temperature of 200°C and a modest system regenerator effectiveness of 0.8. Further improvement is possible. Experimental heat transfer measurements and cycle simulations are presented which show the potential of the concept to provide the basis of a gas-fired air conditioner in the range 10–100 kW cooling. A research project to build a 10-kW water chiller is underway. The laboratory system, which should be operational by June 1997, is described.     

吸附式制冷循环的分析

以吸附式制冷循环的热力过程为依据，使用火用分析的方法对连续回热循环做了分析，对循环中各部分火用损进行了比较。指出了连续回热循环中火用损的主要部位，并探讨了回热率及吸附床的传热性能对循环火用效率的影响。     

单螺旋吹风式速冻装置料口改进的实验研究

从理论上分析了影响单螺旋吹风式速冻装置料口热质交换的主要因素是料口内外的热压压差和风压压差.在实验的典型工况下,热压和风压压差引起的冷量损失分别是3.90KW和1.48KW,均大于围护结构的热负荷(1KW).实验研究发现料口处风压和热压压差同时存在并相互叠加,提出了在进、出料口之间加装隔板的改进方案可以减小热压压差,料口平面与动压方向平行可以减小风压压差,料口处的热压与风压方向相反可以起到减小料口热质交换并减少冷量损失的作用.对比实验结果表明,料口处的冷量损失与料口处的风速成正比,风速度减小1/3左右,料口处的冷量损失减小为原来的1/3左右.     

A dynamic model of heat and mass transfer in a double-bed adsorption machine with internal heat recovery

This paper presents the results of a predictive two-dimensional mathematical model of an adsorption cooling machine consisting of a double consolidated adsorbent bed with internal heat recovery. The results of a base-case, taken as a reference, demonstrated that the COP of the double bed adsorption refrigeration cycle increases with respect to the single bed configuration. However, it was verified that, in order to maximize also the specific power of the machine, the adsorbent beds must have proper thermo-physical properties.Consequently, a sensitivity analysis was carried out, studying the influence of the main heat and mass transfer parameters on the performance of the machine. The results obtained allowed us to define the adsorbent bed design that maximizes its heat and mass transfer properties, as well as the most profitable heat recovery conditions.     

Heat transfer enhancement in magnetic cooling by means of magnetohydrodynamic convection

In this work, we analyze the potential of magnetohydrodynamic (MHD) convection to increase heat transfer during magnetic cooling. To do this, we consider a section of an active magnetic regenerator, namely a flat gadolinium plate, immersed in an initially stagnant heat transfer fluid (NaOH) which is placed in a cuboid glass cell. To create the MHD flow, a small electric current is injected by means of two electrodes and interacts with the already present magnetic field. As a result, a Lorentz force is generated, which drives a swirling flow in the present model configuration. By means of particle image velocimetry and Mach–Zehnder interferometry, the flow field and its impact on the heat transfer at the gadolinium plate are analyzed. For the magnetization stage, we show that a heat transfer enhancement by about 40% can be achieved even with low currents of 3 mA.