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首页> 外文期刊>Energy Conversion & Management >Optimal design of a two-stage refrigeration cycle for natural gas pre-cooling in a gas refinery considering the best allocation of refrigerant
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Optimal design of a two-stage refrigeration cycle for natural gas pre-cooling in a gas refinery considering the best allocation of refrigerant

机译:用于燃气炼油厂的天然气预冷的两级制冷循环的最佳设计考虑到制冷剂的最佳分配

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Part of the process gas cooling in a sample gas refinery is provided by a two-stage vapor compression refrigeration cycle. This cycle has been designed only based on thermodynamics' objective function with propane refrigerant. A gas-turbine is used as the compressors' driver in this sample plant. In the present study, the complete investigation of this compression refrigeration cycle with its gas turbine, as a prime mover, has been redesigned by using the genetic algorithm, and refrigerant analyses. The cycle has been modeled in MATLAB software by considering the economic, thermodynamic, and environmental objective functions. The results show that the basic redesign of the cycle, with propylene as the best refrigerant, can improve the coefficient of performance from 1.42 to 2.01 in comparison to the available cycle. It also can reduce the nitrogen oxide and carbon monoxide emission from 30.74 to 29.7 ppm and 81.0 to 71.6 ppm, respectively, and it can reduce the cost of the product from 1091.5 $ to 781.5 $ per hour. In fact, by replacing propylene refrigerant with propane and multi-objective basic redesign, all three economic, thermodynamic, and environmental functions can be improved in comparison to the available cycle.
机译:样品气体炼油厂中的一部分过程气体冷却由两级蒸汽压缩制冷循环提供。该循环仅基于具有丙烷制冷剂的热力学的客观功能。燃气轮机用作该样品厂的压缩机驱动器。在本研究中,通过使用遗传算法和制冷剂分析,重新设计了与其燃气轮机的这种压缩制冷循环的完整研究。通过考虑经济,热力学和环境目标职能,该循环在MATLAB软件中进行了建模。结果表明,与可用循环相比,循环的基本重新设计与丙烯作为最佳制冷剂,可以从1.42到2.01改善性能系数。它还可以将氮氧化物和一氧化碳排放分别将氮氧化物和一氧化碳排放分别从30.74至29.7ppm和81.0至71.6ppm降低,并且可以将产品的成本从1091.5美元降至每小时781.5美元。事实上,通过用丙烷和多目标基本重新设计替代丙烯制冷剂,与可用循环相比,可以改善所有三种经济,热力学和环境功能。

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