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Flow Regime Map For Condensation From Superheated Vapor

机译:用于从过热蒸汽的冷凝的流动制度映射

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An update on the flow regime map for condensation inside horizontal smooth round tubes accounting for the nonequilibrium existed in a vapor compression system is introduced. It is usually by default to assume that a flow regime map should be made between bulk quality 1 and 0. However, the temperature gradient required by condensation means that the thermal equilibrium assumed in a thermodynamic point of view does not exist in a real condenser, especially at the entrance stages of a condenser in a vapor compression system. By focusing on the development of the liquid film when the superheated vapor is condensed on the tube wall whose temperature is below saturation temperature at the corresponding pressure, the real onset and end of condensation could be theoretically calculated. The flow regime map, therefore, should be constructed in between the real onset and end of condensation that are manually set as superficial quality 1 and 0. Two-phase flows of R32, R134a, R1234ze(E), R245fa and R1233zd(E) under mass fluxes from 100 to 400 kg/m~2-s, heat fluxes from 5 to 10 kW/m~2, and tube diameters of 4.0 and 6.1 mm at saturation temperatures of 30 and 50°C are observed in transparent tube-in-tube heat exchangers where refrigerants are cooled by glycol. The visualizations shows three deficiencies in a conventional flow map. First, a conventional flow map does not provide any information beyond quality 1 and 0 where there is two-phase flow as mentioned above. Second, at the entrance stages of the condensation, the film-forming mechanism guarantees an annular flow. This mechanism, however, is usually not employed in a conventional flow map. Third, the conventional flow regime map does not provide information for both micro and macro tubes. The flow map for those two different sized tubes are usually separately made while putting surface tension into the picture could potentially unify them. The transition criteria with the non-equilibrium is taken into account are redefined and the new flow regime map addresses the issues above. A comparison between visualization and the prediction of the new flow map shows good agreement.
机译:介绍了用于在蒸汽压缩系统中存在的水平光滑圆形管内的冷凝的流动制度图的更新。默认情况下,通常应该在散装质量1和0之间进行流动制度映射。然而,冷凝所需的温度梯度意味着在真正的冷凝器中,在热力学的角度下假设的热平衡不存在,特别是在蒸汽压缩系统中的冷凝器的入口阶段。通过专注于当过热的蒸汽在温度低于相应压力下饱和温度的管壁上的液体膜的开发时,可以理论地计算实际起始和冷凝的真实发作和结束。因此,流动制度图应该在手动设定为浅表质量1和0的凝结凝结结束之间构建的.R32,R134a,R1234ze(e),R245fa和R1233ZD(E)的两相流量在100至400kg / m〜2-s的质量通量下,在透明管中观察到从5至10kW / m〜2-2的热通量,从5至10kW / m〜2的热通量,4.0和6.1mm,在透明的管道中观察到30%和50°C的管直径 - 管式热交换器,用乙二醇冷却制冷剂。可视化在传统流程图中显示了三种缺陷。首先,传统的流程​​图不提供超出质量1和0的任何信息,其中存在如上所述的两相流。其次,在冷凝的入口阶段,成膜机构保证了环形流动。然而,这种机制通常不在传统流程图中使用。第三,传统的流动制度图不能为微观和宏管提供信息。这两个不同尺寸管的流程图通常单独制作,同时将表面张力放入图像中可能均匀统一它们。考虑到非平衡的过渡标准被重新定义,新的流程制度映射解决了上述问题。可视化与新流程图的预测之间的比较显示了良好的一致性。

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