Thermodynamic Performance Evaluation of Liquid-vapor Separation Plate Condenser
摘要
将分液冷凝强化传热思想应用于板式冷凝器中
建立了相应的物理和数学模型. 计算了相同换热面积的7种结构分液板式冷凝器的平均传热系数和总压降
同时采用惩罚因子(Penalty Factor
PF)和㶲损这两个指标对其性能进行评价. 计算结果表明: 分液效率越高
分液板式冷凝器的综合性能越好. 在分液效率为100%
质量流量为0.08~0.12 kg/s范围内
与相同面积的非分液板式冷凝器相比
分液板式冷凝器的PF值降低14.6%
㶲损减少2.6%~6.1%; 当质量流量为0.1 kg/s
平均干度为0.3~0.75
分液板式冷凝器的PF值均小于非分液板式冷凝器
而平均干度大于0.45时
分液板式冷凝器㶲损小于非分液板式冷凝器.
Abstract
“Liquid-separation condensation” theory is applied for performance enhancement in the plate condenser
with the physical and mathematical models built. Seven liquid-separation plate condensers having the same heat transfer area are proposed for heat transfer coefficient and pressure drop comparison. Their performances are evaluated by employing the penalty factor (PF) and exergy destruction. Results show that the higher the liquid-vapor separation efficiency
the better is the performance of the liquid-separation plate condensers. Compared with the conventional plate condenser with the same heat transfer area
the liquid-separation plate condenser has 14.6% lower PF and 2.6~6.1% smaller exergy destruction when the liquid-vapor separation efficiency is 100% and the mass flux is in the range of 0.08~0.12 kg/s. Moreover
when the mass flux is 0.1 kg/s
the penalty factor (PF) of liquid-separation plate condenser is lower with the vapor quality ranging between 0.3~0.75
and the exergy destruction of liquid-separation plate condenser is superior only when the vapor quality is higher than 0.45.
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references
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