Development of a 200-kW Organic Rankine Cycle Power System for Low-Grade Waste Heat Recovery

Taehong Sung, K. Kim
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引用次数: 3

Abstract

In this study, we designed a new plate-type heat exchanger system for the previous shell-and-tube evaporator with the same heat rate and additional turbine safety measure. The new evaporator system consists of two plate heat exchangers; one for preheating and the other for subsequent evaporation and superheating. The separate design reduces the liquid level of the evaporator and lowers the risk of liquid inflow into the turbine. For an additional driving stability, a co-current flow configuration was used for the preheater so that a subcooled liquid is introduced to the evaporator instead of a liquid-vapor mixture. A detailed design of the plate heat exchangers was carried out using a commercial software. The new heat exchangers are 75% smaller in volume and 83% smaller in weight. The designed heat exchangers were manufactured and installed in the previous ORC system. The performance was evaluated using an electric heater and a cooling tower as a heat source and heat sink. For the test, the working fluid pump was operated at the design point turbine inlet pressure of 2.13 MPa. Meanwhile, the condensation conditions were not matched to the design point due to the weather effect. Under the analysis condition, the new evaporator system showed an evaporator heat rate of 1662 kW, which is 91% of the design value with a pressure loss of 46 kPa. We calculated a pressure loss of 62.8 kPa for the design point using an equation for simple friction loss. The results showed that our new evaporator system successfully replaced the previous one without big performance losses.
用于低品位废热回收的200kw有机朗肯循环动力系统的研制
本研究在原有管壳式蒸发器的基础上,设计了一种新的板式换热系统。新型蒸发器系统由两个板式换热器组成;一个用于预热,另一个用于随后的蒸发和过热。分离设计降低了蒸发器的液位,降低了液体流入涡轮的风险。为了增加驱动稳定性,预热器采用了共流配置,这样过冷液体就会被引入蒸发器,而不是液体-蒸汽混合物。利用商业软件对板式换热器进行了详细设计。新的热交换器体积缩小75%,重量减轻83%。所设计的热交换器是在以前的ORC系统中制造和安装的。使用电加热器和冷却塔作为热源和散热器对性能进行了评估。试验中,工作液泵在设计点涡轮进口压力2.13 MPa下运行。同时,由于天气的影响,凝结条件与设计点不匹配。在分析条件下,新蒸发器系统的蒸发器热率为1662 kW,为设计值的91%,压力损失为46 kPa。我们使用简单摩擦损失方程计算出设计点的压力损失为62.8 kPa。结果表明,新蒸发器系统成功地取代了原有的蒸发器系统,且没有造成较大的性能损失。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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