文章摘要
王志伟,王文平,路广英.涂层导热系数变化对换热器传热的影响[J].,2021,20(6):556-562
涂层导热系数变化对换热器传热的影响
Influence of thermal conductivity of coatings on heat transfer performance of heat exchangers
投稿时间:2020-09-24  修订日期:2020-12-01
DOI:10.13738/j.issn.1671-8097.020223
中文关键词: 换热器效能法、涂层、导热系数、换热负荷
英文关键词: heat exchanger efficiency method  anti-corrosion coatings  thermal conductivity  heat transfer loads
基金项目:
作者单位E-mail
王志伟* 山西省城乡规划设计研究院有限公司 935984799@qq.com 
王文平 山西省城乡规划设计研究院有限公司  
路广英 山西省城乡规划设计研究院有限公司  
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中文摘要:
      采用换热器效能法,对不同种类换热器进行校核计算,研究换热工质为气气、气液、液液时,不同种类换热器的换热性能随涂层导热系数的变化趋势。结果表明,各种换热器的总传热系数皆随涂层导热系数的增加而增大,且在不同低温侧流体雷诺数下增加程度不同,雷诺数越大,增加程度越大。设定涂层厚度为200μm,涂层导热热阻所占比例随着涂层导热系数的增加在平板式空气预热器中的减小量最小,当冷流体雷诺数为8156时,从4.72%减小为0.25%,在可拆卸板式换热器中的减小量最大,当冷流体雷诺数为2843时,从53.4%减小为3.7%。当冷流体侧雷诺数取最大时,在平板式空气预热器、列管式省煤器和可拆卸板式换热器中,涂层导热系数分别达到0.175、0.922和31.5 W?(m?K)-1时,可以使换热器换热负荷达到设计值的99%。
英文摘要:
      The heat exchanger efficiency method is used to check and calculate different types of heat exchanger, in order to study the heat transfer performance of different types of heat exchanger changes with the thermal conductivity of coatings when the heat fluids are gas-gas, gas-liquid and liquid-liquid, respectively. The results show that the overall heat transfer coefficient of all kinds of heat exchangers increases with the increase of the thermal conductivity of the coatings, and the increase degree is different under the different Reynolds number of the fluid on the low temperature side. The greater the Reynolds number is, the greater the increase degree achieves. The thickness of coatings is set as 200μm, and the reduction of thermal resistance ratio of coating in flat air preheater is the smallest with the increase of thermal conductivity of coating, which reduces from 4.72% to 0.25% under cold fluid Reynolds number as 8156, while in removable plate heat exchanger is the largest, which reduces from 53.4% to 3.7% under cold fluid Reynolds number as 2843. Under the maximum Reynolds number of the cold fluid side, when the thermal conductivity of the coatings in the flat air preheater, the tubular economizer and the removable plate heat exchanger reaches 0.175, 0.922 and 31.5 W?(m?K)-1 , respectively, the heat transfer loads of the heat exchangers can reach 99% of the design values.
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