使用二元各向同性混合物作为地热能应用工作流体的双压蒸发 ORC 的热经济学研究与多目标比较优化

Q1 Chemical Engineering
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引用次数: 0

摘要

这篇论文对双压蒸发有机郎肯循环系统进行了能量、放能和放能经济(3E)分析,该系统采用二十种不同的二元各向同性混合物作为工作流体,用于地热田发电。为此,对所设计的系统进行了建模,引用了质量和能量守恒定律,并进行了放能和成本平衡分析。利用特定能耗成本计算(SPECO)程序,对系统的能耗经济性进行了深入分析。基于多目标遗传算法对每种混合物进行了比较优化,以便利用低压和高压阶段的压力系数、混合物分数、低压和高压热交换器的夹点温差以及高压热交换器的过热度等设计变量,同时实现能效最大化和总成本费用最小化。为此,绘制了包含所有 20 种不同二元各向同性混合物的系统的帕累托前沿。通过 LINMAP 决策技术得出每种混合物的最佳点。随后,再次利用 LINMAP 找到首选混合物。优化结果表明,考虑到每小时 88.0651 美元的低成本和 64.07 % 的高能效之间的权衡,该系统的最佳工作流体为 R123/C2Butene (96.89/3.11) 混合物。最后,考虑到最佳工作流体,绘制了放能流程图,以提供系统各部分的放能流量和放能破坏量。在建议的系统中,放能破坏主要发生在低压预热器中,其值为 1061 千瓦,其次是低压涡轮机和冷凝器,分别约为 669 千瓦和 266 千瓦。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Thermo-economic investigation and comparative multi-objective optimization of dual-pressure evaporation ORC using binary zeotropic mixtures as working fluids for geothermal energy application
This contribution performs an energy, exergy, and exergoeconomic (3E) analysis of a dual-pressure evaporation organic Rankine cycle system employing twenty different binary zeotropic mixtures as working fluids for power production from a geothermal field. To this end, the designed system is modeled, invoking the mass and energy conservation laws and the exergy and cost balance analyses. Specific Exergy Costing (SPECO) procedure is utilized to provide practical insights into the exergoeconomic aspect of the system. Comparative optimization based on the multi-objective genetic algorithm is accomplished for each mixture in order to simultaneously maximize the exergy efficiency and minimize the total cost rate using the design variables of pressure factor in low-pressure and high-pressure stages, mixture fraction, pinch point temperature differences in low-pressure and high-pressure heat exchangers, and degree of superheat in the high-pressure heat exchanger. In this regard, the Pareto frontiers are drawn for the system with all twenty different binary zeotropic mixtures. The optimal point for each mixture is obtained via the decision-making technique of LINMAP. Subsequently, the LINMAP is re-utilized to find the preferred mixture. The optimization results suggest the R123/C2Butene (96.89/3.11) mixture for this system as the optimum working fluid, considering a trade-off between a low-cost rate of $88.0651 per hr and a high exergy efficiency of 64.07 %. Finally, the exergy flow diagram is plotted to provide the exergy flow rate and the amount of exergy destruction in each segment of the system considering the optimal working fluid. In the proposed system, exergy destruction chiefly occurs within the low-pressure preheater with a value of 1061 kW, followed by the low-pressure turbine and condenser with magnitudes of about 669 kW and 266 kW, respectively.
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来源期刊
International Journal of Thermofluids
International Journal of Thermofluids Engineering-Mechanical Engineering
CiteScore
10.10
自引率
0.00%
发文量
111
审稿时长
66 days
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