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Viscosity behavior of mixtures of CO2 and lubricant oil

机译:CO2和润滑油混合物的粘度行为

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Experimental data on the viscosity of mixtures of CO2 and lubricant oil were acquired and correlated using an excess-property approach based on the classical Eyring liquid viscosity model. Three oils of different types and viscosity grades (alkylbenzene AB ISO 32, mineral MO ISO 50 and polyol ester POE ISO 68) were evaluated at temperatures ranging from 36.5 to 82oC. The excess activation energy for viscous flow was successfully correlated as a function of temperature and concentration using Redlich-Kister polynomial expansions with up to three terms. Large departures from the ideal solution viscosity behavior have been identified in all mixtures. The nature of the observed deviations has been explored in the light of their dependence on temperature, refrigerant concentration and oil type. The Katti and Chaudry (1964) model of the activation energy of viscous flow displayed the best correlation of the experimental data, with RMS deviations of 4.6% (AB ISO 32), 3.3% (MO ISO 50) and 2.8% (POE ISO 68).
机译:获取了有关CO2和润滑油混合物粘度的实验数据,并使用了基于经典Eyring液体粘度模型的过剩方法进行关联。在36.5至82oC的温度范围内评估了三种不同类型和粘度等级的油(烷基苯AB ISO 32,矿物MO ISO 50和多元醇酯POE ISO 68)。使用Redlich-Kister多项式展开式(最多三个项),成功地将粘性流的过量活化能与温度和浓度函数相关联。在所有混合物中均已发现与理想溶液的粘度行为有很大的出入。已根据温度,制冷剂浓度和油类类型对偏差的性质进行了探索。粘性流的活化能的Katti和Chaudry(1964)模型显示了实验数据的最佳相关性,RMS偏差分别为4.6%(AB ISO 32),3.3%(MO ISO 50)和2.8%(POE ISO 68) )。

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