首页|套管式CO2蒸发器的性能模拟与优化计算

套管式CO2蒸发器的性能模拟与优化计算

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为优化设计套管式CO2蒸发器,达到提高换热器效率的目的,采用稳态分布参数法对其建立仿真模型,并对模型精度进行实验验证.分析蒸发器内外部条件、结构参数对换热性能的影响,并分析干涸现象与管长的关系.结果表明:蒸发温度和质量通量对换热性能影响较大,蒸发温度由4℃降至-4℃,制冷量下降4 500 W/(m2·K);质量通量每升高100 kg/(m2·s),换热系数平均升高约1 000 W/(m2·K);在设计工况下,干涸前CO2流体所行进管路长度先下降再升高,且在蒸发温度为0℃达到最低点.在结构参数方面,外管管径为23 mm时,蒸发器换热效果较好.当冷冻水温度从11℃降至10℃时,压降下降3.5 kPa,明显低于其他温度情况下的压降情况.
Performance simulation and optimization calculation of casing CO2 evaporator
In order to optimize the design of casing CO2 evaporator and improve the efficiency of heat exchanger,a simulation model was established by using the steady state lumped parameter and the accuracy of the model was verified by experiments.The influences of internal and external conditions and structural parameters of evaporator on heat transfer performance were analyzed and the relationship between drying phenomenon and pipe length was analyzed.The results show that the evaporation temperature and mass flux have great influence on the heat transfer performance.When the evaporation temperature drops from 4 ℃ to-4 ℃,the cooling capacity decreases by 4 500 W/(m2·K).When the mass flux increases by 100 kg/(m2·s),the heat transfer coefficient increases by about 1 000 W/(m2·K)on average.In the design condition,the length of the pipeline traveled by CO2 fluid first decreases and then increases before drying out and reaches the lowest point at the evaporation temperature 0 ℃.In terms of structural parameters,the evaporator heat transfer effect is better when the diameter of outer tube is 23 mm.When the temperature of chilled water drops from 11℃ to 10 ℃,the pressure drop decreases by 3.5 kPa,which is significantly lower than the pressure drop under other temperature conditions.

casing CO2 evaporatorsteady state lumped parameter methodsimulation calculationheat transfer performance

杨俊兰、殷明

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天津城建大学能源与安全工程学院,天津 300384

套管式CO2蒸发器 稳态分布参数法 模拟计算 换热性能

天津市研究生科研创新资助项目天津市科技特派员项目天津市教委项目

2022SKYZ21322YDTPJC000202019KJ113

2024

化学工程
华陆工程科技有限责任公司

化学工程

CSTPCD北大核心
影响因子:0.438
ISSN:1005-9954
年,卷(期):2024.52(2)
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