化工进展 ›› 2016, Vol. 35 ›› Issue (12): 3783-3792.DOI: 10.16085/j.issn.1000-6613.2016.12.008

• 化工过程与装备 • 上一篇    下一篇

过热/过冷对内回热有机朗肯循环影响的热力学分析

徐荣吉, 张晓晖, 闫美玉, 王瑞祥, 许淑惠   

  1. 北京建筑大学北京市建筑能源综合高效综合利用工程技术研究中心, 北京 100044
  • 收稿日期:2016-05-24 修回日期:2016-08-02 出版日期:2016-12-05 发布日期:2016-12-05
  • 通讯作者: 徐荣吉(1981-),男,博士,讲师,研究方向为位太阳能热利用以及传热传质。E-mail:xurongji@bucea.edu.cn。
  • 作者简介:徐荣吉(1981-),男,博士,讲师,研究方向为位太阳能热利用以及传热传质。E-mail:xurongji@bucea.edu.cn。
  • 基金资助:
    国家自然科学基金(51506004)、北京市自然科学基金(3162009)及北京市教委科技计划(KM201410016001)项目。

Thermal dynamics analysis on the organic Rankine cycle (ORC) with internal heat regenerator at superheated and subcooling conditions

XU Rongji, ZHANG Xiaohui, YAN Meiyu, WANG Ruixiang, XU Shuhui   

  1. Beijing University of Civil Engineering and Architrcture, Beijing Engineering Research Centre of Sustainable Energy and Buildings, Beijing 100044, China
  • Received:2016-05-24 Revised:2016-08-02 Online:2016-12-05 Published:2016-12-05

摘要: 内回热是简单有效提高有机朗肯循环(ORC)效率的基本方法。由于循环过程的改变,使循环的热力学规律发生了变化。以R245fa为工质,对回热器的回热过程和机理进行了深入分析,提出了基于对数传热温差的内回热器性能计算方法,并利用热力学分析方法,分析了过热温度、过冷温度对内回热有机朗肯循环(IHORC)性能的影响。研究结果发现,内回热减少了循环的蒸发负荷和冷凝负荷,提高了循环效率。随着过热温度的增加,循环效率和膨胀机输出功均几乎呈线性增加。根据循环过冷温度大小,过冷分为一般过冷和深度过冷两种情况:一般过冷时,随着过冷温度的增加,虽然回热器的换热量和换热效率逐渐升高,但是,循环效率逐渐降低,蒸发负荷、冷凝负荷逐渐增加;深度过冷时,循环效率、回热器换热量、回热器效率快速增加,蒸发负荷和冷凝负荷快速降低,回热器能量回收作用开始突显。一般过冷与深度过冷的临界点是回热器出口蒸气干度,当干度小于1时进入深度过冷状态。内回热过程的“回热量”受限于乏气工质的放热量,因此,内回热循环适用于蒸发冷凝温差大、过热和深度过冷工况。

关键词: 热力学, 有机朗肯循环, 内回热, 过热, 过冷

Abstract: Internal heat recovery is a simple and effective way to improve the thermal performance of basic organic Rankine cycle(ORC). Thermodynamics regularity of the cycle is changed due to the process changes of the cycle. The heat recovery process and mechanism of the internal heat regenerator was deeply analysed and R245fa was used as working fluid. A new method that can calculate the performance of the internal regenerator was proposed based on logarithmic temperature difference. The effects of superheat and subcooling temperature on the thermal performance of the IHORC were thermodynamicly analyzed. The results indicated that the evaporation and condensation load was reduced and the thermal efficiency of the cycle was improved. The cycle efficiency and the expander work output were increased almost linearly with the increase of the superheating temperature. According to the subcooling temperatures,there were two kinds of sulbcooling:subcooling and deep subcooling. Under supercooling condition,cycle efficiency gradually decreased,evaporation and condensation load gradually increased with the increase of the subcooling temperature though the heat transfer and efficiency of the regenerator gradually increased. Under deep supercooling condition,for the reason of the heat recovery the cycle efficiency and the heat transfer and efficiency of the regenerator increased with the decrease of the evaperation and condensation load. The critical point of subcooling and deep subcooling depended on the outlet steam dryness. It was deep subcooling when the dryness of less than 1. The recovered heat was restricted by the exhaust gas. The internal regenerative ORC was suitable for conditions of high temperature difference between evaporation and condensation temperature,overheating and deep subcooling.

Key words: thermaldynamics, organic Rankine cycle, internal heat recovery, superheat, subcooling

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