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高质量流速下立式螺旋管内汽液两相传热特性研究 总被引:2,自引:0,他引:2
对高质量流速下立式螺旋管内高压汽液两相流沸腾传热特性进行了试验研究,参数范围为:系统压力8.0~15.0MPa;质量流速2500~4000kg/m2s;壁面热流密度200~1000kW/m2;实验段为Φ14的不锈钢管弯制而成的螺旋管直径比为D/d=30.1的管圈,总长为2.335m,考察了热流密度和质量流速对两相传热的影响,分析核态沸腾和两相强制对流沸腾机理在螺旋管内两相传热中所起的作用,得到了局部传热系数的分布特性和平均传热系数计算关联式,首次发现高质量流速区域内螺旋管内汽液两相传热效果亦趋近于相同条件下直管内的换热系数,并对已有的结论进行了分类比较分析. 相似文献
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在压力2.5~4 MPa, 质量流量0.7~1.7 g/s, 热流密度0.06~1 MW/m2的实验条件下, 对煤油在内径1 mm, 长度300 mm竖直上升圆管内的流动与传热特性开展了实验研究, 并分析了传热系数随局部油温的变化及不同实验参数对传热的影响.结果表明, 超临界压力下煤油传热主要由自身物性和流动状态决定.超临界压力煤油传热过程大致可以分为3个区域:正常传热区传热强化区和传热恶化区.传热强化主要是湍流掺混增强和近壁面流体在拟临界温度附近物性剧烈变化的综合作用; 传热恶化则是因为壁温及近壁面流体温度远高于拟临界温度, 在近壁面发生了类似于亚临界状态下的“拟膜态沸腾”. 相似文献
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《工程热物理学报》2020,(7)
CO_2/DME(Dimethyl ether二甲醚)混合工质作为制冷剂既可以降低CO_2单独使用时过高的工作压力,又可抑制二甲醚的可燃性。针对跨临界热泵系统中制冷剂在超临界压力下放热时复杂的传热性能,本文对超临界CO_2/DME混合工质和超临界CO_2在螺旋管内流动冷却的换热过程进行了数值模拟研究。结果表明,与纯CO_2相比,在高温区CO_2/DME混合工质的换热性能更优;通过比较不同配比的CO_2/DME混合工质的换热特性,得到了不同温度范围对应的换热性能最优的CO_2/DME混合工质配比。此外,对固定质量比的CO_2/DME混合工质,分别分析了不同质量流速和热流密度下的流体温度、壁面温度及传热系数的变化规律,并与纯CO_2传热系数的变化进行了对比。该研究为制冷剂选取及热泵系统中气冷器的优化设计提供了理论依据。 相似文献
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低温冷冻靶是惯性约束核聚变装置的关键部件之一。冷冻靶靶丸位于黑腔内部,需要利用微管完成燃料充注。针对燃料在微管内发生气液相变后流入靶丸这一关键过程,研究了微通道流体与常规流体流动传热的差异。基于微通道特性对流体流动传热方程进行修正,同时建立了气液相变模型,对微充气管内燃料充注过程进行了数值计算分析。得到重力和表面张力的影响,在微通道中,重力作用可以忽略,表面张力起重要作用。得到了微尺度效应包括速度滑移和温度跳跃对流动传热过程的影响。对多种充气管结构进行比较分析,为选型提供指导。通过选择不同进口条件和出口条件,对充注量控制和充注条件选择提供了指导方案,实际充注时需要同时提高进口温度和压力,保证连续可控充注。 相似文献
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中空纤维膜换热器可同时实现传质传热, 该换热器可应用于吸收式制冷系统以改善制冷性能. 为探究该膜换热器在溴化锂吸收式制冷系统的运行工况下的传热传质特性, 搭建中空纤维膜换热器性能测试实验台, 采用控制变量法探究在热侧不同入口溶液流速、温度下该换热器的传热量及膜通量变化规律特性. 结果表明: 在热流体其它参数保持不变的情况下, 中空纤维膜换热器热侧溶液的入口流速由3.05 m/s 增至3.30 m/s 时, 换热器总传热量与膜通量均随之加大, 增幅分别为16.0%和2.2%; 该膜换热器的总传热量在冷侧溶液与热侧溶液入口温差10°C 至15°C 内, 增幅达到18.9%, 而膜通量受膜两侧溶液的入口温差变化影响较小, 增幅仅3.1%. 研究表示: 温度的变化对中空纤维膜换热器的传热传质性能影响更为显著, 而流速的变化对水分子的运动影响较小. 相似文献
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空隙率波是气液两相流系统的特殊物理现象,理解空隙率波的传播特性对揭示两相流流型转变与流速测量物理机理具有重要意义.本文首先考察了典型非线性系统的多尺度互相关特性,发现去趋势互相关分析方法可有效揭示系统的多尺度非线性动力学特征;然后,通过采集垂直上升小管径气液两相流电导传感器阵列上下游空隙率波动数据,提出采用多尺度去趋势互相关分析方法探测空隙率波传播的多尺度互相关特性,并提取了低尺度空隙率波互相关水平增长率;另外,通过计算空隙率波空间衰减因子,考察了气液两相流空隙率波传播的结构不稳定行为.结果表明,空隙率波结构的多尺度互相关特性与其空间衰减特性具有较好的物理关联性:对于气液两相流过渡流型,低尺度空隙率波互相关水平增长率较高,且与较为稳定的空隙率波传播特性相对应;而当气液两相流空隙率波明显衰减或放大时,空隙率波互相关水平增长速率一般较低. 相似文献
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Heat transfer in two-phase flow boiling of a dilute mixture of TiO2 nanoparticles in R141b base fluid in a smooth tube is investigated experimentally. Examining the obtained results reveals that enhancement of the convective heat transfer coefficient for the particle volume fractions of 0.01% and 0.03% in comparison with pure R141b is more pronounced for a higher volume fraction. The measured data also show that at higher vapor qualities, the improvement in heat transfer coefficient is greater. Moreover, the heat transfer coefficient decreases substantially with mass flux while an increase in saturation temperature leads to an improvement in this coefficient. 相似文献
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选择欧拉多相流模型和非平衡沸腾模型,用Fluent 软件对单边受热竖直向上平滑管进行了过冷流动沸腾换热的数值分析。研究了不同质量流速、进口温度和热流密度对对流换热系数和空泡份额的影响,并分析了它们对传热恶化的影响。 相似文献
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对Al2O3-合成油纳米流体在槽式太阳能集热管内的传热特性进行流体动力学数值模拟,重点考察纳米流体导热系数模型的影响.通过与管内Nusselt数半经验模型的预测结果对比,表明使用考虑布朗运动的纳米流体导热系数模型可较好地预测集热管内传热特性.研究表明纳米颗粒与流体基液的相对运动具有促进集热管内传热的作用.最后,定量研究... 相似文献
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�� Ƽ������ͨ�������������� 《核聚变与等离子体物理》2006,39(3):265-269
By using Fluent software with the Eulerian multiphase model and Non-equilibrium boiling model, the subcooled flow boiling heat transfers was numerically simulated in the plain upward vertical tubes under the condition of one-side heating. The influences of the different mass flux, inlet temperatures and heat flux on the heat transfer coefficient, the void fraction and heat transfer deterioration were investigated. 相似文献
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A model is presented to simulate the cooling processes during tumor cryosurgery with different kinds of flows through the cryoprobe. The heat flux between the cryoprobe wall and the tumor, the heat transfer coefficient under different inflow conditions are obtained numerically. The impact of the inlet mass flow rate, gas volume fraction on these parameters is investigated. It is found that the heat transfer coefficient decreased significantly when inflow changed from two-phase annular flow to droplet flow, and to gas flow. The inlet gas volume fraction and flow velocity only significantly affect the freezing ability of the probe when the inflow is gas or in droplet phase. Simulation of the tumor temperature profiles under different flow conditions show that the heat transfer coefficient is a crucial parameter in temperature prediction during cryosurgery. Results indicate that when the cryoprobe wall is assumed at a constant temperature conventionally, the cooling effect could be overestimated. It would be more reasonable to use the constant wall heat transfer coefficient to simulate the cooling progress under a specific flow. 相似文献
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M. K. Rathod 《实验传热》2013,26(1):40-55
Thermal performance of a latent heat storage unit is evaluated experimentally. The latent heat thermal energy storage system analyzed in this work is a shell-and-tube type of heat exchanger using paraffin wax (melting point between 58°C and 60°C) as the phase change material. The temperature distribution in the phase change material is measured with time. The influence of mass flow rate and inlet temperature of the heat transfer fluid on heat fraction is examined for both the melting and solidification processes. The mass flow rate of heat transfer fluid (water) is varied in the range of 0.0167 kg/s to 0.0833 kg/s (1 kg/min to 5 kg/min), and the fluid inlet temperature is varied between 75°C and 85°C. The experimental results indicate that the total melting time of the phase change material increases as the mass flow rate and inlet temperature of heat transfer fluid decrease. The fluid inlet temperature influences the heat fraction considerably as compared to the mass flow rate of heat transfer fluid during the melting process of the phase change material. 相似文献