化工进展 ›› 2018, Vol. 37 ›› Issue (06): 2109-2115.DOI: 10.16085/j.issn.1000-6613.2017-1805

• 化工过程与装备 • 上一篇    下一篇

网纹内管双套管双管板安全型换热器的传热性能

马乾1, 刘雪东1,2, 温传美1, 谢红笑1, 尹传忠1   

  1. 1 常州大学机械工程学院, 江苏 常州 213164;
    2 江苏省绿色过程装备重点实验室, 江苏 常州 213164
  • 收稿日期:2017-08-29 修回日期:2017-11-29 出版日期:2018-06-05 发布日期:2018-06-05
  • 通讯作者: 刘雪东,教授,研究方向为能源化工装备结构创新与优化、粉体工程设备与技术。
  • 作者简介:马乾(1992-),男,硕士研究生。
  • 基金资助:
    江苏省产学研前瞻性联合研究项目(BY2016029-16)。

Heat transfer performance of double tube and double tube sheet safety heat exchanger with the reticulate inner tube

MA Qian1, LIU Xuedong1,2, WEN Chuanmei1, XIE Hongxiao1, YIN Chuanzhong1   

  1. 1 School of Mechanical Engineering, Changzhou University, Changzhou 213164, Jiangsu, China;
    2 Jiangsu Key Laboratory of Green Process Equipment, Changzhou University, Changzhou 213164, Jiangsu, China
  • Received:2017-08-29 Revised:2017-11-29 Online:2018-06-05 Published:2018-06-05

摘要: 以网纹内管型双套管双管板安全型换热器为研究对象,采用内外管接触面积当量法,将网纹内管与外管内壁的接触面积当量成对应接触面积的直槽管;借助计算流体力学(CFD)软件采用数值模拟的方法对内管为当量的直槽管换热器传热性能进行了研究,换热器管壳两侧的介质均为水,分别将空气和水两种介质填充至隔绝腔内,模拟不同入口流量条件下传热特性;引入接触修正系数,在传统传热系数经验公式的基础上,结合网纹管模型特点,获得网纹内管安全型换热器传热系数计算公式,并对不同工况下换热器的传热系数进行理论计算;建立网纹内管安全型换热器传热特性评价实验台。结果表明:内外管接触面积当量法在处理网纹内管安全型换热器传热特性时具有可行性,基于接触修正系数的传热系数工程经验公式计算结果可靠;数值模拟结果、理论计算结果及实验结果具有较好的吻合趋势;隔绝腔介质分别为水及空气时,网纹内管的传热效率比内管为光管分别提高约24%和40%。

关键词: 安全型换热器, 网纹内管, 双套管双管板, 传热特性, 当量接触面积

Abstract: In order to study the double tube and double tube sheet safety heat exchanger with the reticulated inner tube, the internal and external tube contact area equivalent method was used. The contact area of the reticulated inner tube and the outer wall of the outer tube was equivalent to the correspond contact area of a straight groove tube. CFD software was used to simulate the heat transfer performance of the heat exchanger with the straight groove tube as inner tube. The fluid of the tube and shell are both water. Air and water were filled in the safety chamber respectively to simulate the heat transfer characteristics under different inlet flow conditions. The contact correction coefficient was introduced, based on the traditional empirical formula of heat transfer coefficient, and combined with the characteristics of the reticulated tube model, the calculation formula of the heat transfer coefficient of reticulated inner tube safety heat exchanger was obtained. The heat transfer coefficients of the heat exchanger under different working conditions were calculated theoretically. The experiment for evaluation of heat transfer characteristics of the reticulated inner tube safety heat exchanger was established. Results indicated that the internal and external contact area equivalent method is feasible when dealing with the heat transfer characteristics of the reticulated inner tube safety heat exchanger. The empirical formula of heat transfer coefficient based on contact correction coefficient is reliable. The results of numerical simulation, theoretical calculation and experimental results have a good coincidence trend. The heat transfer efficiency of the reticulated inner tube is 24% and 40%, respectively, higher than that of the smooth inner tube when the safety chamber is filled with water and air.

Key words: safety heat exchanger, reticulated inner tube, double tube and double tube sheet, heat transfer characteristic, equivalent contact area

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