Behera Uma Sankar, Shim Jiyun, Lee Hyun Seong, Byun Hun-Soo
Department of Chemical and Biomolecular Engineering, Chonnam National University, Yeosu, Jeonnam 59626, South Korea.
ACS Omega. 2025 Jul 30;10(31):35230-35240. doi: 10.1021/acsomega.5c05424. eCollection 2025 Aug 12.
The demand for alkyl lactates (methyl, ethyl, propyl, and butyl) has risen significantly due to their unique properties and wide industrial applications. Accurate vapor-liquid equilibrium data are vital for the design and optimization of separation techniques involving these compounds, particularly in systems using supercritical carbon dioxide (SC-CO) as a solvent. In this study, the phase transition of binary systems of CO + lactate (methyl, ethyl, propyl, butyl) was investigated at various temperatures (313.2, 333.2, 353.2, 373.2, and 393.2 K) and pressures up to 18.48 MPa, using elevated-pressure phase equilibrium equipment based on the synthetic method. Notably, comprehensive isothermal phase behavior data for these binary systems across a wide mole fraction range and high-pressure conditions are scarce. The pressure-temperature plots revealed that the critical mixture boundary connects the critical points of SC-CO and the respective alkyl lactates. For all four systems, enhanced miscibility was observed as the lactate mole fraction increased under isothermal conditions, accompanied by a decrease in pressure. The phase transition observed aligns with Type-I, Van Konynenburg and Scott. Enhanced miscibility was observed across all systems as the mole fraction of lactate increased under isothermal conditions with a corresponding decrease in pressure. The experimental bubble point data were correlated using the Peng et al. equation of state (PR EoS) combined with van der Waals one-fluid mixing rules. The binary interaction parameters ( and η ) were optimized as follows: methyl lactate ( = -0.030, η = -0.090), ethyl lactate ( = 0.000, η = -0.085), propyl lactate ( = 0.035, η = -0.060), and butyl lactate ( = 0.040, η = -0.050). The model exhibited good agreement with experimental results, with root-mean-square deviation (RMSD) values of 3.92, 4.08, 6.46, and 6.79% for the CO + methyl lactate, ethyl lactate, propyl lactate, and butyl lactate systems, respectively.
由于乳酸烷基酯(甲酯、乙酯、丙酯和丁酯)具有独特的性质和广泛的工业应用,其需求量已显著上升。准确的气液平衡数据对于涉及这些化合物的分离技术的设计和优化至关重要,特别是在以超临界二氧化碳(SC-CO₂)作为溶剂的系统中。在本研究中,使用基于合成法的高压相平衡设备,在不同温度(313.2、333.2、353.2、373.2和393.2 K)和高达18.48 MPa的压力下,研究了CO₂ + 乳酸酯(甲酯、乙酯、丙酯、丁酯)二元体系的相变。值得注意的是,关于这些二元体系在宽摩尔分数范围和高压条件下的全面等温相行为数据很少。压力-温度图显示,临界混合物边界连接了SC-CO₂和相应乳酸烷基酯的临界点。对于所有四个体系,在等温条件下,随着乳酸酯摩尔分数增加,观察到互溶性增强,同时压力降低。观察到的相变符合I型,即范康年伯格和斯科特型。在等温条件下,随着乳酸酯摩尔分数增加,所有体系的互溶性均增强,同时压力相应降低。使用Peng等人的状态方程(PR EoS)结合范德华单流体混合规则对实验泡点数据进行了关联。二元相互作用参数(κ和η)优化如下:乳酸甲酯(κ = -0.030,η = -0.090),乳酸乙酯(κ = 0.000,η = -0.085),乳酸丙酯(κ = 0.035,η = -0.060),乳酸丁酯(κ =