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Optimal design and thermo-economic analysis of an integrated power generation system in natural gas pressure reduction stations

机译:天然气减压站综合发电系统的优化设计和热经济分析

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摘要

A massive amount of byproduct energy of natural gas including pressure and cold energy is released during the natural gas depressurization process in pressure reduction stations. In this paper, a novel integrated power generation system is proposed to make joint use of the byproduct energy in pressure reduction stations and low-grade heat. The integrated system consists of two subsystems: a natural gas expansion subsystem recovers the pressure energy of natural gas, an organic Rankine cycle subsystem retrieves the cold energy of natural gas and low-grade heat. A multi-objective optimization model which comprehensively considers the thermodynamic and economic performance of the proposed system is established. Optimal determination of key design parameters including intermediate temperature and minimum approach temperatures is investigated under different heat source conditions. Based on the optimization results, the thermo-economic analysis of the proposed system is conducted to give guidance for further optimization. The simulation result shows that there exhibit positive linear correlations between optimal intermediate temperature and minimum approach temperatures with heat source conditions. With the optimized parameters, the performance of the proposed system is enhanced compared to the separated natural gas expansion and organic Rankine cycle systems. Net power output and exergy efficiency are improved by 17.15% and 22.37%. The cost of electricity is reduced by 42.23%. This paper provides an efficient solution to retrieve the byproduct energy in pressure reduction stations as well as low-grade heat.
机译:在减压站的天然气减压过程中,释放了大量的天然气副产物能量,包括压力和冷能。本文提出了一种新型的综合发电系统,以联合利用减压站中的副产物能量和低级热量。集成系统由两个子系统组成:天然气膨胀子系统可回收天然气的压力能,有机朗肯循环子系统可回收天然气的冷能和低品位热量。建立了多目标优化模型,该模型综合考虑了所提出系统的热力学和经济性能。在不同的热源条件下,研究了关键设计参数的最佳确定,包括中间温度和最低进站温度。根据优化结果,对所提出系统进行热经济分析,为进一步优化提供指导。仿真结果表明,在最佳中间温度和最小进场温度之间,与热源条件呈正线性关系。通过优化的参数,与分离的天然气膨胀和有机朗肯循环系统相比,该系统的性能得到了增强。净功率输出和火用效率分别提高了17.15%和22.37%。电力成本降低了42.23%。本文提供了一种有效的解决方案,可用于回收减压站中的副产品能量以及低品位热量。

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