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超临界CO2在螺旋槽管式换热器中的冷却换热

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为了研究超临界CO2(SCO2)在螺旋槽管式换热器中的冷却换热特性,采用数值模拟方法对比研究了不同热流密度下,SCO2在不同通道内流动时冷却换热系数和湍流动能.为了更合理地评价各工况下冷却换热的综合性能,从压降和传热系数角度,提出一个综合评价因子EF.研究结果表明:在SCO2进行冷却换热时,其换热系数主要受定压比热容和湍流动能的影响.当SCO2在内管通道内流动时,换热系数低,但压降更小,故综合评价因子EF较大.同时,在所研究工况中,存在最佳热流密度值为-40 000 W/m2,使EF达到最大值2.001 26,此时SCO2冷却换热综合性能最优.
Cooling heat transfer of supercritical CO2 in spiral grooved tube heat exchanger
In order to study the cooling heat transfer characteristics of SCO2 in spiral grooved tube heat exchanger,the cool-ing heat transfer coefficient and turbulent kinetic energy of SCO2 flowing in different channels were studied under the conditions of various density of heat flow rate by numerical simulation method.A comprehensive evaluation factor EFwas proposed from the perspective of pressure drop and heat transfer coefficient to reasonably evaluate the comprehensive performance of flow cooling heat transfer under different working conditions.The results show that the heat transfer coefficient of SCO2 is mainly affected by specific heat at constant pressure and the turbulent kinetic energy.When SCO2 flows in the inner tube channel,the heat transfer coefficient is low,but the pressure drop is small,so the comprehensive evaluation factor EF is large.At the same time,in the studied working conditions,the optimal density of heat flow rate is-40 000 W/m2.So that the maximum EF value is 2.00 126.At this time,the comprehensive performance of SCO2 cooling heat transfer is optimal.

Heat transferSupercritical CO2Density of heat flow rateCoefficient of heat transferNumerical simulation

王栋、陶银双、鲁月红、陶乐仁

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安徽工业大学建筑工程学院,马鞍山 243002

上海理工大学能源与动力工程学院,上海 200093

传热 超临界CO2 热流密度 换热系数 数值模拟

国家自然科学基金安徽高校自然科学研究重点项目

51608001KJ2017A055

2024

低温与超导
中国电子科技集团公司第十六研究所

低温与超导

北大核心
影响因子:0.243
ISSN:1001-7100
年,卷(期):2024.52(1)
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