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Isothermal and Isobaric Vapor-Liquid Equilibria of α-Pinene+ cis-Pinane + 1-Hexanol System

Isothermal and Isobaric Vapor-Liquid Equilibria of α-Pinene+ cis-Pinane + 1-Hexanol System
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摘要 This paper presents the isothermal and isobaric vapor-liquid equilibria measured with an inclined ebulliometer for α-pinene + cis-pinane + 1-hexanol system at temperatures of 368.15K, 383.15 K and 408.15K, and at pressures of 26.66 kPa and 53.33 kPa. The measured ternary results are analyzed using the UNIQUAC equation with the temperature-dependent binary parameters. Satisfactory agreements are obtained between the experimental results and the theoretical analysis. This paper presents the isothermal and isobaric vapor-liquid equilibria measured with an inclined ebul-liometer for α-pinene + cis-pinane + 1-hexanol system at temperatures of 368.15 K, 383.15 K and 408.15 K, and at pressures of 26.66kPa and 53.33kPa. The measured ternary results are analyzed using the UNIQUAC equation with the temperature-dependent binary parameters. Satisfactory agreements are obtained between the experimental results and the theoretical analysis.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2004年第1期92-95,共4页 中国化学工程学报(英文版)
基金 Supported by the National Natural Science Foundation of China (No. 29976035) the Natural Science Foundation of Zhejiang Province (No. RC01051).
关键词 Antoine equation EBULLIOMETER Powell optimization UNIQUAC α-松萜 顺式蒎烷 1-己醇 等温线 等压汽液均衡
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