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乙烯热力学相平衡模型及相图研究

Study on thermodynamic phase equilibrium model and phase diagram of ethylene
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摘要 研究了乙烯的热力学相平衡实验数据,给出了乙烯的气-固-液、固Ⅰ-固Ⅱ-液两个三相点温度和三相点压力以及临界温度和临界压力的推荐值;提出了系列乙烯热力学相平衡方程,包括冷凝曲线、熔融曲线Ⅰ、熔融曲线Ⅱ、熔融曲线Ⅰ+Ⅱ及升华曲线方程,拟合效果均优于文献方程;绘制了乙烯的热力学相图以及p-V和V-T相图;建立了乙烯的气-液相平衡的汽化焓方程,方程计算值的相对误差平均值为1.291%。 The experimental data of the thermodynamic phase equilibrium of ethylene was studied.The recommended values of temperature,pressure of ethylene for two three-phase points namely gas-solid-liquid,solid Ⅰ-solid Ⅱ-liquid respectively and the critical point temperature,pressure were given. A series of thermodynamic phase equilibrium equations of ethylene were proposed,including condensation curve,melting curve I,melting curve Ⅱ,melting curve Ⅰ + Ⅱ and sublimation curve equation. The fitting results were better than those of the literature equations. The thermodynamic phase diagram,p-V and V-T phase diagrams of ethylene were drawn. The evaporation enthalpy equation of vapor-liquid phase equilibrium of ethylene was established. The average relative error of the calculated value of the equation was 1.291%.
作者 蒋斯麒 孙丽丽 李进锋 苏洪 张军志 刘罡 Jiang Siqi;Sun Lili;Li Jinfeng;Su Hong;Zhang Junzhi;Liu Gang(Sinopec Engineering Incorporation,Beijing 100021,China)
出处 《石油化工》 CAS CSCD 北大核心 2022年第5期561-569,共9页 Petrochemical Technology
基金 中国石化青年创新基金(优秀青年创新基金)课题(421116)。
关键词 乙烯 相平衡 相图 汽化焓 ethylene phase equilibrium phase diagram evaporation enthalpy
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