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Hydrofluoroolefin-based novel mixed refrigerant for energy efficient and ecological LNG production

机译:基于氢氟烯烃的新型混合制冷剂,用于高效节能和生态LNG生产

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摘要

To satisfy the worldwide demand for energy, the liquefied natural gas (LNG) industry has grown significantly in the past three decades owing to its low CO2emissions and high thermal efficiency compared to the other available energy resources. However, the process of natural gas liquefaction is generally considered to be energy-intensive. In this context, a novel hydrofluoroolefin (HFO-1234yf)-based mixed refrigerant, with the advantages of zero ozone depletion and minimal global warming potential, is proposed to liquefy natural gas in an ecological and energy-efficient manner. A new liquefaction cycle using the HFO-based mixed refrigerant is developed to fully utilize its potential. The results reveal that the overall energy requirement for natural gas liquefaction can be reduced by 46.4% compared with a single mixed refrigerant process, 42.5% compared with a dual mixed refrigerant process, and 36.3% compared with the Linde–single mixed refrigerant process. Economic analysis based on the capacity parameters of each equipment is also performed to emphasize the commercial feasibility of the proposed LNG process. The proposed HFO-based mixed refrigerant system provides an innovative solution to improve the ecological aspects and energy efficiency of natural gas liquefaction processes.
机译:为了满足全球能源需求,与其他可利用的能源相比,液化天然气(LNG)行业的二氧化碳排放量低且热效率高,因此在过去的三十年中取得了长足的发展。然而,天然气液化的过程通常被认为是能量密集的。在此背景下,提出了一种新型的基于氢氟烯烃(HFO-1234yf)的混合制冷剂,其具有零臭氧消耗和最小的全球变暖潜能的优点,以生态和节能的方式液化天然气。开发了使用基于HFO的混合制冷剂的新液化循环,以充分利用其潜力。结果表明,与单混合制冷剂工艺相比,天然气液化的总能量需求可降低46.4%,与双混合制冷剂工艺相比可降低42.5%,与林德-单混合制冷剂工艺相比可降低36.3%。还基于每个设备的容量参数进行了经济分析,以强调所提出的液化天然气工艺的商业可行性。拟议的基于HFO的混合制冷剂系统提供了创新的解决方案,可改善天然气液化过程的生态方面和能源效率。

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