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Optimal boiling temperature for ORC installation

机译:ORC安装的最佳沸腾温度

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In the paper a research on cost-effective optimum design boiling temperature for Organic Rankine Cycle utilizing low-temperature heat sources is presented. The ratio of the heat exchanger area of the boiler to the power output is used as the objective function. Analytical relations for heat transfer area as well power of the cycle are formulated. Evaporation temperature and inlet temperature of the heat source medium as well its mass flow rate are varied in the optimization method. The optimization is carried out for three working fluids, i.e. R 134a, water and ethanol. The objective function (economics profitability, thermodynamic efficiency) leads to different optimal working conditions in terms of evaporating temperature. Maximum power generation in the near-critical conditions of subcritical ORC is the highest. The choice of the working fluid can greatly affect the objective function which is a measure of power plant cost. Ethanol exhibits a minimum objective function but not necessarily the maximum cycle efficiency.
机译:在本文中,对利用低温热源的有机朗肯循环的经济有效的最佳设计沸腾温度进行了研究。锅炉的热交换器面积与功率输出之比用作目标函数。建立了传热面积和循环功率的解析关系。在优化方法中,热源介质的蒸发温度和入口温度以及其质量流量会发生变化。针对三种工作流体(即R 134a,水和乙醇)进行了优化。在蒸发温度方面,目标函数(经济收益,热力学效率)导致不同的最佳工作条件。在亚临界ORC的近临界条件下,最大发电量最高。工作流体的选择会极大地影响目标函数,该目标函数是电厂成本的度量。乙醇显示出最小的目标函数,但未必显示出最大的循环效率。

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