Experimental and thermodynamic study of amyl acetate, amyl acetoacetate, and isoamyl acetoacetate in CO2 solvent

IF 7.2 2区 工程技术 Q1 CHEMISTRY, MULTIDISCIPLINARY Journal of CO2 Utilization Pub Date : 2024-08-01 DOI:10.1016/j.jcou.2024.102910
Hyun-Seok Lee , Divya Baskaran , Min-Soo Park, Hun-Soo Byun
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引用次数: 0

Abstract

Acetate ester compounds find widespread use in various applications such as surface coatings, ink formulations, pharmaceuticals, and adhesives. It is essential to investigate the phase transition behavior of amyl acetate, amyl acetoacetate, and isoamyl acetoacetate in high-pressure supercritical CO2 (SC-CO2). The vapor-liquid equilibria (VLE) of the SC-CO2 + amyl acetate, SC-CO2 + amyl acetoacetate, and SC-CO2 + isoamyl acetoacetate systems were examined at different temperatures (313.2 ≤ T ≤ 393.2 K) and pressures (1.67 ≤ P ≤ 20.76 MPa). The solubility curve of these systems shows Type-I phase behavior, and the critical points of these binary mixtures were observed between the critical properties of the pure components involved in the systems. The solubility of amyl acetate, amyl acetoacetate, and isoamyl acetoacetate in the SC-CO2 + amyl acetate, SC-CO2 + amyl acetoacetate, and SC-CO2 + isoamyl acetoacetate systems increases with increasing temperature at constant pressure. The two-parameter model of Peng-Robinson equation of state along with a mixing rule, accurately correlated the phase transition behavior and critical mixtures curves for all three systems. The binary interaction parameters (BIPs) were adjusted, and the minimum root mean square deviation percentage was identified for all three systems. The calculated error% was found to be within reasonable limits, with values of 4.95 %, 3.93 %, and 4.18 % for SC-CO2 + amyl acetate, SC-CO2 + amyl acetoacetate, and SC-CO2 + isoamyl acetoacetate systems, respectively. Furthermore, the interaction parameters for the SC-CO2 + amyl acetoacetate mixture was found to be temperature-dependent, and the tested linear regression correlation coefficient for the BIPs parameters of (kij) and (ηij) are 0.98533 and 0.99083, respectively. This is the first research study on the phase behavior of acetate ester compounds in SC-CO2 solvents, and the results have a significant impact on industries at different operating conditions.

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乙酸戊酯、乙酰乙酸戊酯和乙酰乙酸异戊酯在二氧化碳溶剂中的实验和热力学研究
醋酸酯类化合物广泛应用于表面涂层、油墨配方、药品和粘合剂等领域。研究乙酸戊酯、乙酰乙酸戊酯和乙酰乙酸异戊酯在高压超临界二氧化碳(SC-CO2)中的相变行为至关重要。在不同温度(313.2 ≤ T ≤ 393.2 K)和压力(1.67 ≤ P ≤ 20.76 MPa)下,研究了 SC-CO2 + 乙酸戊酯、SC-CO2 + 乙酰乙酸戊酯和 SC-CO2 + 乙酰乙酸异戊酯体系的汽液平衡(VLE)。这些体系的溶解度曲线显示出Ⅰ型相行为,并观察到这些二元混合物的临界点介于体系中纯组分的临界性质之间。在恒压条件下,乙酸戊酯、乙酰乙酸戊酯和乙酰乙酸异戊酯在 SC-CO2 + 乙酸戊酯、SC-CO2 + 乙酰乙酸戊酯和 SC-CO2 + 乙酰乙酸异戊酯体系中的溶解度随着温度的升高而增加。彭-罗宾逊(Peng-Robinson)状态方程的双参数模型以及混合规则准确地反映了这三个体系的相变行为和临界混合物曲线。对二元相互作用参数(BIPs)进行了调整,并确定了所有三个体系的最小均方根偏差百分比。计算出的误差率在合理范围内,SC-CO2 + 乙酸戊酯、SC-CO2 + 乙酰乙酸戊酯和 SC-CO2 + 乙酰乙酸异戊酯系统的误差率分别为 4.95 %、3.93 % 和 4.18 %。此外,还发现 SC-CO2 + 乙酰乙酸戊酯混合物的相互作用参数与温度有关,经测试,BIPs 参数 (kij) 和 (ηij) 的线性回归相关系数分别为 0.98533 和 0.99083。这是首次对醋酸酯类化合物在 SC-CO2 溶剂中的相行为进行研究,其结果对不同操作条件下的工业具有重要影响。
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来源期刊
Journal of CO2 Utilization
Journal of CO2 Utilization CHEMISTRY, MULTIDISCIPLINARY-ENGINEERING, CHEMICAL
CiteScore
13.90
自引率
10.40%
发文量
406
审稿时长
2.8 months
期刊介绍: The Journal of CO2 Utilization offers a single, multi-disciplinary, scholarly platform for the exchange of novel research in the field of CO2 re-use for scientists and engineers in chemicals, fuels and materials. The emphasis is on the dissemination of leading-edge research from basic science to the development of new processes, technologies and applications. The Journal of CO2 Utilization publishes original peer-reviewed research papers, reviews, and short communications, including experimental and theoretical work, and analytical models and simulations.
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