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板式气冷器中超临界CO2侧表面换热系数研究OA北大核心CSTPCD

Study on heat transfer coefficient of supercritical CO2 side surface of plate gas cooler

中文摘要英文摘要

为了探究板式气冷器中主导超临界CO2侧表面换热系数h最值出现的因素及最值点的中移对平均换热系数大小的影响,采用基于MATLAB的换热器分布参数分析方法,研究了超临界CO2侧表面换热系数h沿气冷器板片上的分布规律,并针对h最值出现的主导因素、改变板片尺寸和流量使最值点移动对平均换热系数的影响进行研究.结果表明,伪临界温度对板式气冷器中h最值的出现更具有决定性;一定压力下的Cp最大值会随着压力的增加不断增大,但伪临界温度逐渐降低;减小板片尺寸或者增大质量流量,可以使得平均换热系数增加,对应的换热量也会增大,而且由质量流量增加所带来的换热量增加幅度在3种工况下分别为12.72%,12.79%,11.75%,同时压降也会增加;当h最大值保持在6 170 W/(m2·K)或5 120 W/(m2·K)附近时,最值点中移不会使平均换热系数增加明显,而且对应的换热量也会减小.

In order to study the effect of the factors leading to the occurrence of the maximum surface heat transfer coefficient h on the supercritical CO2 side in plate gas coolers and the effect of shifting this maximum point on the average heat transfer coefficient,a MATLAB-based distributed parameter analysis method for heat exchangers was employed to investigate the distribution pattern of the surface heat transfer coefficient h along the plates of the gas cooler,and examine the dominant factors contributing to the appearance of h's maximum values,as well as the effects of changing plate dimensions and flow rates on moving the maximum point and its effect on the average heat transfer coefficient.The simulation results indicate that the pseudocritical temperature plays a decisive role in the occurrence of h's maximum values in the plate gas coolers;the maximum Cp at a given pressure increases with pressure,but the pseudocritical temperature gradually decreases;Reducing the size of the plates or increasing the mass flow rate can increase the average heat transfer coefficient,and correspondingly,the heat transfer rate will also increase.Moreover,the increases in heat transfer rate brought by the increased mass flow rate are respectively 12.72%,12.79%,11.75%across three different conditions,although the pressure drop will also increase.However,when the maximum value of h is maintained around 6 170 W/(m2·K)or 5 120 W/(m2·K),shifting the maximum value point does not significantly increase the average heat transfer coefficient,and the corresponding heat transfer rate will also decrease.

卢国强;顾众;谢晶;陈旭升

上海海洋大学 食品学院,上海 201306||上海冷链装备性能与节能评价专业技术服务平台,上海 201306上海海洋大学 食品学院,上海 201306||上海冷链装备性能与节能评价专业技术服务平台,上海 201306||浙江英诺绿能科技有限公司,杭州 310051上海海洋大学 食品学院,上海 201306||上海冷链装备性能与节能评价专业技术服务平台,上海 201306||上海水产品加工及贮藏工程技术研究中心,上海 201306||食品科学与工程国家级实验教学示范中心(上海海洋大学),上海 201306浙江英诺绿能科技有限公司,杭州 310051

机械工程

板式气冷器超临界CO2表面换热系数最值与最值点

plate gas coolersupercritical CO2surface heat transfer coefficientmaximum value and maximum point

《压力容器》 2024 (006)

43-51 / 9

国家现代农业产业技术体系资助项目(CARS-47)

10.3969/j.issn.1001-4837.2024.06.007

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