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Convective heat transfer measurements in a vapour-liquid-liquid three-phase direct contact heat exchanger

机译:蒸气-液-液三相直接接触换热器中的对流传热测量

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摘要

Energy usage is increasing around the world due to the continued development of technology, and population growth. Solar energy is a promising low-grade energy resource that can be harvested and utilised in different applications, such solar heater systems, which are used in both domestic and industrial settings. However, the implementation of an efficient energy conversion system or heat exchanger would enhance such low-grade energy processes. The direct contact heat exchanger could be the right choice due to its ability to efficiently transfer significant amounts of heat, simple design, and low cost. In this work, the heat transfer associated with the direct contact condensation of pentane vapour bubbles in a three-phase direct contact condenser is investigated experimentally. Such a condenser could be used in a cycle with a solar water heater and heat recovery systems. The experiments on the steady state operation of the three-phase direct contact condenser were carried out using a short Perspex tube of 70 cm in total height and an internal diameter of 4 cm. Only a height of 48 cm was active as the direct contact condenser. Pentane vapour, (the dispersed phase) with three different initial temperatures (40_(°) C , 43.5_(°) C and 47.5_(°) C ) was directly contacted with water (the continuous phase) at 19_(°) C . The experimental results showed that the total heat transfer rate per unit volume along the direct contact condenser gradually decreased upon moving higher up the condenser. Additionally, the heat transfer rate increases with increasing mass flow rate ratio, but no significant effect on the heat transfer rate of varying the initial temperature of the dispersed phase was seen. Furthermore, both the outlet temperature of the continuous phase and the void fraction were positively correlated with the total heat transfer rate per unit volume, with no considerable effect of the initial temperature difference between the dispersed and continuous phases.
机译:由于技术的不断发展和人口的增长,全世界的能源使用量正在增加。太阳能是一种有前途的低等级能源,可以在不同的应用中进行收集和利用,例如在家庭和工业环境中使用的太阳能加热器系统。然而,有效的能量转换系统或热交换器的实施将增强这种低等级的能量过程。直接接触式热交换器可能有效的选择,因为它能够有效地传递大量热量,设计简单且成本低廉。在这项工作中,实验研究了与戊烷蒸气气泡在三相直接接触式冷凝器中的直接接触冷凝相关的热传递。这种冷凝器可以与太阳能热水器和热回收系统一起循环使用。使用总高度70厘米,内径4厘米的短有机玻璃管对三相直接接触式冷凝器进行稳态操作的实验。直接接触式冷凝器的高度只有48厘米。戊烷蒸气(分散相)具有三个不同的初始温度(40_(°)C,43.5_(°)C和47.5_(°C))直接与水(连续相)在19_(°)C接触。实验结果表明,沿着直接接触冷凝器的每单位体积的总传热速率随着向冷凝器的上方移动而逐渐降低。另外,传热速率随着质量流率比的增加而增加,但是没有看到改变分散相的初始温度对传热速率的显着影响。此外,连续相的出口温度和空隙率均与每单位体积的总传热速率呈正相关,而分散相和连续相之间的初始温差没有显着影响。

著录项

  • 来源
    《Heat and mass transfer》 |2018年第6期|1697-1705|共9页
  • 作者单位

    Department of Science, University of Misan,College of Applied Science, Department of Engineeion/ Chemical Engineering;

    Department of Chemical and Process Engineering, Faculty of Engineering and Physical Sciences, University of Surrey;

    Engineering Technical College, Al-Furat Al-Awsat Technical University;

    Department of Chemical and Process Engineering, Faculty of Engineering and Physical Sciences, University of Surrey;

    Department of Chemical and Process Engineering, Faculty of Engineering and Physical Sciences, University of Surrey;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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