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Phase equilibria of palm oil, palm kernel oil, and oleic acid + supercritical carbon dioxide and modeling using Peng-Robinson EOS

机译:棕榈油,棕榈仁油和油酸+超临界二氧化碳的相平衡,并使用Peng-Robinson EOS进行建模

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摘要

Vapor-liquid equilibria of the binary supercritical carbon dioxide (scCO2) + oleic acid, scCO2 + palm oil, and scCO2 + palm kernel oil were measured at a wide range of temperatures from 333.2 to 373.2 K and pressures from 8.5 to 35 MPa in a circulation-type phase equilibrium apparatus. The samples from liquid and vapor phases were analyzed using UV-vis spectrometer and a liquid hold-up equipment. The phase equilibrium data were correlated with Peng-Robinson Equation of State (PR-EOS) using Wong-Sandler mixing rule and optimum values of binary interaction parameters were determined. The relative deviation between experimental data and predicted data was in the range of 6.9-8.7%, suggesting that the PR-EOS with Wong-Sandier mixing rule is capable of predicting the vapor-liquid equilibria of oleic acid + scCO2, palm oil + scCO2, and palm kernel oil + scCO2.
机译:在333.2至373.2 K的宽温度范围和8.5至35 MPa的压力范围内,对二元超临界二氧化碳(scCO2)+油酸,scCO2 +棕榈油和scCO2 +棕榈仁油的汽液平衡进行了测量。循环型相平衡仪。使用紫外可见光谱仪和液体滞留设备分析液相和气相样品。使用Wong-Sandler混合规则,将相平衡数据与Peng-Robinson状态方程(PR-EOS)进行关联,并确定二元相互作用参数的最佳值。实验数据和预测数据之间的相对偏差在6.9-8.7%范围内,这表明采用Wong-Sandier混合法则的PR-EOS能够预测油酸+ scCO2,棕榈油+ scCO2的气液平衡。 ,以及棕榈仁油+ scCO2。

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