多通道平行流扁管-紧凑式翅片相变蓄热器蓄/放热性能

工业余热浪费严重、利用率较低且实际应用过程中受到时间和空间的限制,需要高效蓄热技术和装置来解决此类问题。提出一种将多通道平行流扁管与紧凑式翅片相结合的新型相变蓄热器,以水为载热流体,月桂酸为相变材料。实验研究了载热流体注入方式、流量、入口温度对蓄热器蓄/放热性能的影响,并分析小温差下蓄热器的传热特性。结果显示,该蓄热器相变材料填充率为82.5%,紧凑式翅片的采用极大强化了相变材料侧换热过程,蓄/放热性能优良。当载热流体入口温度分别为45℃和41℃时,相变材料约在270 min和75 min完成相变,最小蓄/放热温差可达2℃,最小温差时的平均蓄热比功率为25.18 W/kg,平均取热比功率为20.23 W/kg。

采用扩展温度振荡法测量超临界CO_2扁管内对流换热特性

As a natural working,fluid carbon dioxide (CO 2) has shown great potential in refrigeration and air conditioning industry. The heat transfer and pressure drop performance of supercritical CO 2 in pipes is necessary for gas-cooler design. This paper presents an experimental investigation of supercritical CO 2 heat transfer characteristics using temperature oscillation method.Considering the variable fluid temperature, an extended and more reasonable temperature oscillation model is built and used for heat transfer coefficient evaluation. The convective heat transfer coefficient of supercritical CO 2 flowing in an aluminum multi-channel flat pipe is measured for the first time.Experiments are performed under one typical pressure and temperature condition.The experimental setup and data acquisition as well as processing program are described in detail. New dimensionless heat transfer data in the form of Nusselt number via Reynolds number are given and analyzed.The results could be a good reference to gas-cooler design.The paper also supplies a general model or tool for determining local convective heat transfer coefficient which can be used more widely.

多通道平行流扁管梯级相变蓄热系统传热性能

针对多通道平行流扁管单级蓄热装置在蓄取热过程中温差逐渐减小,传热不均匀的问题,本文提出了多通道平行流扁管梯级相变蓄热系统,系统包括两级蓄热装置,装置里分别填充52#石蜡和月桂酸作为蓄热材料。以水作为载热流体,实验研究了不同进口温度、不同流量下换热流体对梯级蓄热系统蓄取热特性的影响。实验结果显示,与流量相比,换热流体进口温度对梯级蓄热系统传热性能有更大的影响。当换热流体进口温度增加(减少)或换热流体流量增加(减小),梯级蓄热装置的蓄(取)热时间减少,蓄(取)热功率增加。