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《可再生能源》2016,(5)
运行模式对地埋管换热器的热交换性能具有显著影响。文章借助桂林理工大学建立的地源热泵实验平台,对桂林地区地源热泵制冷工况下3种运行模式进行试验,研究地源热泵的运行状况及管壁温度变化特性,分析运行模式对地埋管热交换性能的影响规律。研究结果表明:3种运行工况下,地源热泵机组的性能系数COP分别为4.30,4.03,3.48,竖埋管单位管长换热量为14.4~32.8 W/m,水平埋管单位管长换热量为14.8~17.9W/m;地埋管的管壁温度随着地源热泵的运行发生变化,其恢复程度与停机时间的长短有关;间歇运行模式有利于土壤温度场的恢复,提高地埋管换热器的热交换性能;停运比Ps-o由0变化到1时,热泵机组性能系数COP增加了15.8%。 相似文献
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为了缓解埋管区域土壤的热量堆积问题,提出了埋管换热器按内中外、块状、间隔三种分区运行的策略,利用CFD软件建立了10×10的井群换热模型,对地源热泵系统在三种分区与不分区运行策略下运行十年进行数值模拟,分析不同分区运行策略对土壤温度分布和土壤热堆积特性的影响。模拟结果可知:不分区、内中外分区、块状分区、间隔分区四种运行策略下埋管区域的平均温度分别为25.23、23.31、23.06、23.28℃,最高温度分别为40.62、32.77、40.65、38.93℃;分区运行较不分区运行可以有效缓解热堆积作用,埋管区域整体温度较不分区运行时降低了2.00℃左右,内中外分区策略可以显著缓解埋管区域热堆积。 相似文献
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为了研究地埋管换热器在变负荷下连续运行与间歇运行的换热性能,基于有限长线热源渗流模型建立竖直地埋管钻孔外准三维非稳态传热模型,应用叠加原理计算钻孔群中钻孔壁温度场及地埋管内流体温度场。在存在地下水水平渗流的情况下,研究了变负荷连续运行模式下不同渗流速度、不同运行工况及不同钻孔位置对地埋管换热器的换热性能的影响。结果表明,在连续运行模式下,边缘位置的钻孔及较大的渗流速度能够增强地埋管换热器的换热性能;在间歇运行模式下,地埋管换热器的运行份额越小,其制冷效果越好,反之,制冷效果越差;在间歇运行工况下,土壤温度能在系统间歇期内得到一定程度的恢复,从而更好地提高地热能的利用率。 相似文献
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文章综合考虑热泵机组和埋管侧循环水泵总的运行能耗,建立了地源热泵系统耦合仿真平台,研究了不同地埋管换热流体速度对系统运行性能的影响,并进一步分析了不同因素对最佳运行流速的影响规律。研究结果表明,系统最佳运行流速为0.2~0.4 m/s,与0.6 m/s相比,系统全年运行能耗至少可降低7.2%~8.5%。土壤的热导率和比热容、管间距、回填材料以及管壁粗糙度和水泵效率基本不影响最佳运行流速范围。随着压缩机整体效率提高,最佳运行流速降低0.2~0.3 m/s,系统年运行能耗进一步降低了10.7%~11.7%。 相似文献
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针对深井地埋管换热系统运行原理,根据地埋管换热器热阻-热容优化模型,建立深井地埋管井孔内、外非稳态柱坐标传热模型。基于环渤海湾盆地埋深1 000~2 000 m热储层水文地质条件,采用双连续介质空间耦合有限元数值计算方法,分析深井地埋管典型配置参数取值对于地埋管换热性能的影响程度。研究结果表明:深井地埋管换热性能随着系统运行时间的推移出现衰减趋势,至供暖季末期(120.0 d)深井地埋管换热量下降20%左右;当深井地埋管循环水量由10增大到60 m3/h时,深井地埋管平均换热量提高150.80 kW,同时循环水泵耗功率也相应提高26.00 kW;深井地埋管埋深由1 600提高到2 400 m时,平均换热量提高113%,耗功率提高50%;当进水套管直径由168提高到299 mm时,平均换热量提高10%,耗功率降低27%。 相似文献
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In this study, experiments were carried out to study the effects of baffle overlap proportion on the shell-side flow resistance and heat transfer performance of the shell-and-tube heat exchangers with helical baffles (STHXsHB). Three STHXsHB with an overlap proportion of 10% and helix angles of 20°, 30°, and 40° were tested. Comparisons were made of the experimental data of the STHXsHB with the same helix angles but 50% overlap proportion. The theory of entransy dissipation was employed to evaluate the irreversible loss in STHXsHB with different helix angles and overlap proportions. The results indicated that both the baffle overlap proportion and the helix angle have a great effect on the shell-side flow resistance and heat transfer. For a given helix angle, the comprehensive performance of STHXsHB with small overlap proportion is always better than that with large overlap proportion at the same mass flow rate or Reynolds number on the shell side. However, for the same heat transfer area, working conditions, and helix angle, the STHXsHB with large baffle overlap proportion has less irreversibility in the heat exchange process, according to the theory of entransy dissipation. In addition, experimental results demonstrated that the configuration of the relatively large helix angle and baffle overlap proportion is the preferred alternative in STHXsHB. 相似文献
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A simple method for predicting the thermal performance of multistage heat exchangers is proposed. The technique involves an area weighting scheme of the reseated Colburn J factors. The method is developed for, and probably limited to, applications with indirect contact, direct transfer heat exchangers operated in series. However, condensing heat exchangers are amenable to this technique, and thus it offers more flexibility and wider applicability than previously proposed methods. Experimental data for a two-stage, condensing heat exchanger are reported, and the behavior is compared to the predictive scheme with moderate success. While the behavior of multistage heat exchangers may be affected by interstage spacing, the data from the experiments do not allow quantification of the impact of this effect. 相似文献
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The types of maldistributions and their causes are discussed. Where possible, means of-avoiding or curing the problem are given. While the performance loss is often small, there are associated mechanical problems that can be severe. 相似文献
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提出一种新型的能源桩换热管型式,即深层埋管式能源桩。利用Comsol Multiphysics建立三维方法模拟桩体-土体传热,一维方法模拟管内水动态传热传质的数值模型,考虑了土体温度随深度的变化,模拟出口水温随时间的变化规律并计算换热量,比较深层埋管式与传统的1-U型、1-W型能源桩的换热量,分析了桩径、桩体导热系数、桩体密度、桩体比热容等不同参数对新型深层埋管式能源桩换热量的影响。模拟结果表明:以运行50 h为例,深层埋管式的总体换热量比1-U型、1-W型分别高122%、54%;而对于单位管长换热量,深层埋管式比1-U型、1-W型分别高9%、50%,桩径从0.5 m增加到1 m,换热量增加14.3%;桩体导热系数从1.2 W/(m∙K) 增大至2.5 W/(m∙K),换热量增加9.6%;桩体密度从1 800 kg/m3增大到2 600 kg/m3,换热量增大0.8%;桩体比热容从637 J/(kg∙K) 增大到1 037 J/(kg∙K),换热量增大1.1%。因此深层埋管式的热性能优于传统1-U型和1-W型,在满足能源桩力学性能的前提下,为了提高深层埋管式能源桩换热性能,可以适当增大桩径。对于桩体材料的选择,应该选择导热系数较高的材料。密度和比热容对换热量的提升影响不大。 相似文献
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Fouling in shell-and-tube heat exchangers was modeled by combining Hasson's ionic diffusion model for scaling from CaCO3 solutions with a model for predicting the temperature distribution developed by Gaddis and Schlünder. Using the computed results, clean heat exchanger design rules were tested for fouling conditions. The effects of fouling on the efficiency of heat exchanger configurations were determined. 相似文献