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Performance study of supplying cooling load and output power combined cycle using the cold energy of the small scale LNG

机译:小型LNG冷能供冷负荷与输出功率联合循环的性能研究

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摘要

The gasification process of small flows of liquefied natural gas also releases large amounts of cold energy and pressure energy. In order to effectively utilize the cold energy and the pressure energy, a combined cycle for supplying cooling load and output power was proposed. In the combined cycle, one refrigeration cycle for food frozen storage, two refrigeration cycles for food cooling storage, two chilled water cycles for air conditioning, R717 is used as working substance of refrigeration cycles. The exergy efficiency and performance coefficient of the combined cycle were analyzed. The exergy efficiency of evaporator is the lowest, the exergy efficiency of each expander and condenser is higher than that of the pump in refrigeration cycles. The exergy efficiency of evaporator, expander, pump and condenser increases with the increase of evaporation temperature of R717 refrigerant. The power consumption of the each chilled water pump for air conditioning is higher than that of the 8717 pumps in refrigeration cycles. LNG pump power consumption is lower than that of two chilled water pumps. As the outlet pressure of the NG expander decreases, and the pressure at the inlet of the NG expander increases, the total pump power consumption and the system total expansion output power increases. Among the system total expansion output power, NG expander accounts for more than 2/3. With the increase of the outlet pressure of the NG expander, the system exergy efficiency and the performance coefficient of combined cycle decreases. With the increase of the inlet pressure of the NG expander, the exergy efficiency of the system increases. However the inlet pressure of NG expander rises resulting in reduction in the performance coefficient of the system. And at the same inlet and outlet pressure of NG expander, the mass flow rate of NC increases, the exergy efficiency and the performance coefficient of the system hardly changes. When the mass flow rate of NG is 1 kg/s, and the inlet and outlet pressures of NG expander are 10000 kPa and 600 kPa, the exergy efficiency and the performance coefficient of the system reaches 85.19% and 6.525 respectively. (C) 2019 Elsevier Ltd. All rights reserved.
机译:少量液化天然气的气化过程还会释放大量的冷能和压力能。为了有效地利用冷能和压力能,提出了一种联合循环来提供冷却负荷和输出功率。在联合循环中,一个冷冻食品冷冻循环,两个冷冻食品冷冻循环,两个冷水循环空调,R717被用作冷冻循环的工作物质。分析了联合循环的火用效率和性能系数。在制冷循环中,蒸发器的火用效率最低,每个膨胀机和冷凝器的火用效率高于泵的火用效率。蒸发器,膨胀器,泵和冷凝器的火用效率随R717制冷剂蒸发温度的升高而增加。在制冷循环中,用于空调的每个冷冻水泵的功率消耗都比8717泵的功率消耗高。 LNG泵的能耗低于两个冷冻水泵的能耗。随着NG膨胀器出口压力的降低,以及NG膨胀器入口压力的增加,泵的总功率消耗和系统总的膨胀输出功率都会增加。在系统总扩展输出功率中,NG扩展器占2/3以上。随着天然气膨胀器出口压力的增加,系统的火用效率和联合循环的性能系数降低。随着NG膨胀器入口压力的增加,系统的火用效率提高。但是,NG膨胀机的入口压力会升高,导致系统性能系数降低。在NG膨胀机入口压力和出口压力相同的情况下,NC的质量流量增加,系统的火用效率和性能系数几乎不变。当天然气的质量流量为1 kg / s,天然气膨胀机的入口和出口压力分别为10000 kPa和600 kPa时,系统的火用效率和性能系数分别达到85.19%和6.525。 (C)2019 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Energy》 |2019年第1期|36-44|共9页
  • 作者单位

    Tianjin Univ Commerce, Tianjin Key Lab Refrigerat Technol, Tianjin 300134, Peoples R China;

    Tianjin Univ Commerce, Tianjin Key Lab Refrigerat Technol, Tianjin 300134, Peoples R China;

    Tianjin Univ Commerce, Tianjin Key Lab Refrigerat Technol, Tianjin 300134, Peoples R China;

    Tianjin Univ Commerce, Tianjin Key Lab Refrigerat Technol, Tianjin 300134, Peoples R China;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    R717 supplying cooling load; Output power; Combined cycle; Cold energy; Small scale LNG;

    机译:R717提供冷却负荷;输出功率;联合循环;冷能;小型LNG;

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