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讨论在填充层水泥砂浆的导热系数发生改变时,地板辐射采暖的各种参数的变化情况,以及节能效果比较。 相似文献
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在国家规定的热网管道的每米热损失下,其保温层厚度随着保温材料的导热系数及工质温度的不同而不同。利用导出的计算公式,通过计算,将以上四个参数的关系用图表的形式表示出来,以供在热网管道的保温中予以应用。 相似文献
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高温、电加热条件下电阻率与导热系数随温度变化明显,因此研究在此条件下的热传导具有十分重要的意义.运用MATLAB中的PDE工具箱,对高温条件下,几种不同材料的发热导体电加热过程中导热系数、电导率变化所引起的导热等问题进行了数值求解.结果表明:当发热导体半径R＞5 cm时,温度的变化对发热导体的导热系数和电导率影响显著. 相似文献
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液体导热系数的瞬态双热线测量 总被引：7，自引：0，他引：7
研究设计瞬态双热线液体导热系数测量仪,分析了该测试仪器的基本原理及其模型修正,并通过测量去离子水对该装置进行检定。通过与标准值比较,测量的平均误差为0.61%,最大误差为-0.9%,该装置有较高的测试精度。 相似文献
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混凝土是一种多相复合材料,其导热性受温湿度、孔隙率、骨料体积分数、龄期等多个因素的综合影响。通过试验研究了不同温度、饱和度、孔隙率、骨料体积分数、龄期等因素变化条件下水泥砂浆、骨料和混凝土导热系数的变化规律,结合Wiener边界理论,提出一种包含多因素影响的混凝土导热系数预测模型,分析了各因素与混凝土导热系数的相关性。结果表明,混凝土导热性的各影响因素之间具有明显的耦合作用特征,即混凝土含水率越高,温度变化对其导热性的影响越显著;混凝土导热系数随饱和度增大而增加,孔隙率越大,增幅越明显;随着骨料体积分数的增加,导热系数增大较明显。 相似文献
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岩土导热系数是地源热泵地埋管换热器的重要设计参数;测井单位深度换热量是地埋管换热器系统的设计依据。掌握工程区域岩土的热物性及换热性能,是保证地源热泵系统高效、稳定运行的关键。文章建立了现场测试岩土导热系数及换热量的方法,并结合沈阳浑南高新技术产业开发区某地源热泵工程,测试分析了岩土导热系数和测井单位深度换热量。结果表明,该区域的岩土具有较好的导热能力,适合采用地埋管地源热泵系统;在特殊地理条件下设计地源热泵系统方案前,应对拟建区域的地质条件进行全面勘探,以优选工程区域,为岩土热响应测试结果的可靠性提供保障。 相似文献
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介绍了将传统晶体硅商用太阳电池加装水冷器,改造为光伏-光热集成组件后的结构;通过热阻分析的方法,分析了该光伏-光热组件的传热特性;并通过实验,实际测量了该光伏-光热组件的传热性能,得到了导热热阻及其有效热导率,可为组件的进一步开发提供参考。 相似文献
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通过对板式换热器传热的理论分析和在干工况、喷淋工况下的实验研究,得出板式换热器在喷淋情形下空气侧喷淋水量对强化对流传热系数的影响关系,进而拟合出喷淋情形下空气侧的对流传热系数的关联式。同时为了综合考虑由于喷淋造成的换热器性能的变化,还对喷淋前后空气侧的阻力变化进行了测试分析。 相似文献
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A correction factor to the theoretical fin efficiency of serrated fins, reported in Part 1 and Part 2 of this report, was derived for an inline arrangement experimentally. The experiment was performed using an open‐type wind tunnel with six kinds of test finned‐tubes made of copper, carbon steel and stainless steel, which were arranged in one to five rows. Heat transfer measurement was done by the local thermal simulation method. The derived correction factor for the 1st row was the same as for staggered arrangement reported in Part 3, for the 2nd and deeper rows, however, a further correction was needed, which may be caused by the difference in the nonuniformity in heat transfer coefficient over the fin surface. © 2004 Wiley Periodicals, Inc. Heat Trans Asian Res, 33(4): 258–269, 2004; Published online in Wiley InterScience ( www.interscience.wiley.com ). DOI 10.1002/htj.20008 相似文献
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The fin efficiency of serrated fins was analyzed, and an analytical solution was derived as a function of modified Bessel functions. Two assumptions, i.e., thermal insulation at the end surfaces of segmented sections, and a uniform heat transfer coefficient over the fin surface, were employed in this analysis. To determine the effect of these assumptions, a heat transfer experiment was performed. From a comparison of the experimentally evaluated fin efficiencies with the analytical solution, a correction factor was obtained for a typical serrated fin configuration. © 1999 Scripta Technica, Heat Trans Asian Res, 28(6): 528–540, 1999 相似文献
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Recently, a critical problem of latent heat thermal energy storage remains the low thermal conductivity of phase change materials (PCMs), which can lead to low heat transfer rate. Structural optimization design is an effective solution for this problem. In this work, two horizontal shell-and-tube heat exchangers (HEs) with one inner tube (n = 1) and four inner tubes (n = 4) are designed keeping the same amount of PCM and water flow rate, and their melting and solidification thermal performance and heat transfer characteristics are compared. The results show that in comparison with one-inner-tube HE, the temperature of detected points are affected by both upper and lower inner tubes for four-inner-tube HE, thus the differences in phase change process appear. In addition, the phase change time reduction rates are 34.1%, 33.39%, 28.82% at Tin (inlet water temperature) = 75°C, 80°C, 85°C during charging process, and 17.2%, 27.69%, 36.67% at Tin = 10°C, 15°C, 20°C during discharging process, respectively. In comparison with the one-inner-tube HE, the theoretical efficiency of four-inner-tube HE is increased from 75.88% to 90.34%. Although more friction loss should be paid by four-inner-tube HE, a lower energy consumption and a higher heat-energy ratio are achieved. Based on the results of this study, the amount of cumulative heat per energy consumption is 1.52 × 108 and 2.88 × 108 for one-inner-tube and four-inner-tube HE, respectively. 相似文献
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The heat transfer rate and efficiency of TE (thermoelectric) cooling systems were investigated. The emphasis of the present study is focused on the use of large-scale TE refrigerators for air conditioning applications. A one-dimensional heat transfer analysis was performed to determine the cooling power and electricity consumption of the TE elements. The constant-property results are in good agreement with the variable-property solutions for TE materials and temperatures typical for air conditioning applications. A heat transfer analysis was also carried out for TE refrigerators equipped with a heat exchanger. Both parallel- and counter-flow heat exchangers were considered. Fluid temperature variations of these two flow arrangements were found to be quite different, but the efficiencies and cold fluid exit temperatures differed only slightly when a uniform current was used for all TE elements. If the length of the heat exchanger exceeds an optimal value, the cold fluid temperature begins to rise and the efficiency drops for both parallel- and counter-flow arrangements. The second law of thermodynamics was applied to the optimization of TE refrigerators operating between two constant-temperature reservoirs and between two flowing fluids. It was found that if a TE cooling system incorporates a heat exchanger, a nonuniform current distribution should be used to achieve the maximum efficiency and the lowest cold fluid temperature. The optimization results for TE refrigerators operating between two constant-temperature reservoirs are not applicable to TE cooling systems between two flowing fluids. The most energy-efficient current distribution for the parallel-flow arrangement is the one which increase in the direction of the cold fluid. 相似文献