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首页> 外文期刊>Computational thermal sciences >AN ASSESSMENT OF WORKING-FLUID MIXTURES USING SAFT-VR MIE FOR USE IN ORGANIC RANKINE CYCLE SYSTEMS FOR WASTE-HEAT RECOVERY
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AN ASSESSMENT OF WORKING-FLUID MIXTURES USING SAFT-VR MIE FOR USE IN ORGANIC RANKINE CYCLE SYSTEMS FOR WASTE-HEAT RECOVERY

机译:使用SAFT-VR MIE的工作液混合物在有机朗肯循环系统中用于废热回收的评估

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Working-fluid mixtures offer an improved thermal match to heat source streams in organic Rankine cycles (ORCs) over pure (single) fluids. In the present work we investigate the selection of working-fluid mixtures and component mixing ratios for an ORC system from a thermodynamic and economic point of view. A mathematical model of a subcritical, nonregenerative ORC is constructed. We employ the SAFT-VR Mie equation of state, a state-of-the-art version of the statistical associating fluid theory (SAFT), to predict the thermodynamic state properties and phase behavior of the fluid mixtures. The effect of the working-fluid mixture selection on the efficiency and power output from the cycle is investigated, as is its effect on the sizes of the various components of the ORC engine. This is done in order to appreciate the role that the fluid mixtures have on the investment/capital costs attributed to the installation of such a unit, intended for waste-heat recovery and conversion to power. Results of an ORC using a binary decane-butane mixture as the working fluid demonstrate a significant improvement in the cost per unit power output compared to the two pure fluid components. Specifically, the added costs of the four main ORC system components (pump, expander, and two heat exchangers) were found to be as low as 120-130 £/kW, 20-30% lower compared to the pure fluids.
机译:与纯(单)流体相比,工作流体混合物与有机朗肯循环(ORC)中的热源流具有更好的热匹配性。在当前的工作中,我们从热力学和经济的角度研究了ORC系统的工作流体混合物和组分混合比的选择。建立了亚临界非再生ORC的数学模型。我们使用统计关联流体理论(SAFT)的最新版本SAFT-VR Mie状态方程来预测流体混合物的热力学状态特性和相态。研究了工作流体混合物选择对循环效率和功率输出的影响,以及其对ORC发动机各个组件尺寸的影响。这样做是为了理解流体混合物在归因于这种单元的安装的投资/资金成本中的作用,该单元旨在用于废热回收和电力转换。使用二元癸烷-丁烷混合物作为工作流体的ORC结果表明,与两种纯流体组分相比,每单位功率输出的成本有了显着改善。具体而言,发现四个主要的ORC系统组件(泵,膨胀机和两个热交换器)的附加成本低至120-130 £ / kW,比纯流体低20-30%。

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