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首页> 外文期刊>The Journal of Chemical Thermodynamics >High-pressure (vapour plus liquid) equilibria for ternary systems composed by {(E)-2-hexenal or hexanal plus carbon dioxide plus water}: Partition coefficient measurement
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High-pressure (vapour plus liquid) equilibria for ternary systems composed by {(E)-2-hexenal or hexanal plus carbon dioxide plus water}: Partition coefficient measurement

机译:由{(E)-2-己或己醛加二氧化碳加水}组成的三元系统的高压(蒸气加液体)平衡:分配系数测量

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A new apparatus based on a static-analytic method assembled in this work was utilised to perform high-pressure (vapour + liquid) equilibria measurements of aqueous ternary systems. This work includes values of isothermal partition coefficients between CO2 and water of two apple aroma constituents, (E)-2-hexenal and hexanal. Additionally, this work reports new experimental (vapour + liquid) equilibria measurements for the ternary systems (CO2 + (E)-2-hexenal + water) and (CO2 + hexanal + water), at fixed liquid phase composition (600 mg . kg(-1)), at temperatures of (313, 323 and 333) K and at pressures from (8 to 19) MPa. Vapour liquid interphase was checked and monitored visually for all the systems studied in this work. No liquid immiscibility was observed at the composition, temperatures and pressures studied. In order to suggest reasonable operation conditions for fractionation of aromas with dense carbon dioxide, partition coefficients of the aroma compounds between CO2 and water along with their separation factors from water were calculated. Partition coefficients of (E)-2-hexenal between CO2 and water were in the range of (6 to 91) and where found to be near six times higher than those of hexanal (9 to 17). Very high separation factors from water were observed (similar to 10(4)) especially for (E)-2-hexenal. The highest separation factor, for both compounds, was found at a temperature of 313 K and pressures from (12 to 14) MPa. (C) 2015 Elsevier Ltd. All rights reserved.
机译:基于这项工作中组装的基于静态分析方法的新设备被用来执行水性三元系统的高压(蒸气+液体)平衡测量。这项工作包括两个苹果香气成分(E)-2-己和己醛的二氧化碳和水之间的等温分配系数值。此外,这项工作还报告了在固定液相组成(600 mg。kg)下,三元系统(CO2 +(E)-2-己烯醛+水)和(CO2 +己醛+水)的新实验(蒸气+液体)平衡测量。 (-1)),温度为(313、323和333)K,压力为(8至19)MPa。对于这项工作中研究的所有系统,均对蒸汽液体的中间相进行了检查和视觉监控。在所研究的组成,温度和压力下未观察到液体不溶混性。为了建议使用浓二氧化碳分馏香气的合理操作条件,计算了香气化合物在CO2和水之间的分配系数以及它们与水的分离因子。 (E)-2-己烯在二氧化碳和水之间的分配系数在(6至91)的范围内,发现其接近己醛(9至17)的六倍。观察到非常高的与水的分离因子(类似于10(4)),尤其是对于(E)-2-hexenal。对于这两种化合物,在313 K的温度和(12至14)MPa的压力下发现了最高的分离系数。 (C)2015 Elsevier Ltd.保留所有权利。

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