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A LIQUID-LIQUID EXTRACTION ABSORPTION REFRIGERATION CYCLE

机译:液-液萃取吸收制冷循环

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An absorption refrigeration cycle using liquid-liquid extraction is presented. A solvent, partially misciblewith a refrigerant (e.g., water) and immiscible with an absorbent (e.g., LiBr), is employed to extractrefrigerant from a weak absorption solution (e.g., 59.5% LiBr/H_2O); as a result, a strong absorption solution(e.g., 64% LiBr/H_2O) and a refrigerant-rich extract solution are achieved. The refrigerant in the extractsolution is recovered by cooling due to the change of the solubility of refrigerant with temperature. There isno evaporation of refrigerant involved in the generation, so the heat input required would be reduced.Calculations indicate that the COP of the cycle could be increased by 20~50% compared with conventionalsingle effect absorption cycles at higher generation temperature. This improvement is strongly dependent ongeneration temperature, circulation ratio of extract solution to refrigerant, specific heat of the extractsolution and effectiveness of the heat exchanger.
机译:提出了使用液-液萃取的吸收式制冷循环。使用一种可与制冷剂(例如水)部分混溶而不能与吸收剂(例如LiBr)混溶的溶剂,从弱吸收溶液(例如59.5%LiBr / H_2O)中提取制冷剂;结果,获得了强吸收溶液(例如64%LiBr / H_2O)和富含制冷剂的提取溶液。由于制冷剂的溶解度随温度的变化,通过冷却回收提取液中的制冷剂。计算结果表明,制冷剂没有蒸发,因此减少了所需的热量输入。计算表明,在较高的生成温度下,与传统的单效吸收循环相比,该循环的COP可提高20〜50%。这种改进在很大程度上取决于生成温度,萃取液与制冷剂的循环比,萃取液的比热以及热交换器的效率。

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  • 来源
  • 会议地点 Cologne(DE);Cologne(DE)
  • 作者

    S B Riffat; Y H Su;

  • 作者单位

    School of the Built Environment University of Nottingham University Park Nottingham NG7 2RD;

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