关联了能够在整个浓度范围预测[mmim]DMP/CH3OH溶液蒸汽压参数的UNIFAC模型和预测过量焓参数的Wilson模型.基于上述模型,对[mmim]DMP/CH3OH吸收式制冷单效循环热力特性进行了仿真分析.结果表明;[mmim]DMP/CH3OH单效制冷的循环倍率高于LiBr/H2O和NH3/H2O系统;[mmim]DMP/CH3OH单效制冷循环COP略低于LiBr/H2O系统,但在整体性能上要高于NH3/H2O系统.
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