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首页> 外文期刊>International Journal of Thermophysics >Measurement of Vapor–Liquid Equilibrium for the DME + Diisopropyl Ether Binary System and Correlation for the DME + CO2 + Diisopropyl Ether Ternary System
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Measurement of Vapor–Liquid Equilibrium for the DME + Diisopropyl Ether Binary System and Correlation for the DME + CO2 + Diisopropyl Ether Ternary System

机译:DME +二异丙醚二元体系的汽-液平衡测量及DME + CO 2 +二异丙醚三元体系的相关性

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摘要

Vapor–liquid equilibrium (VLE) data have been measured with a static-type VLE apparatus for the dimethyl ether (DME)–diisopropyl ether (DIPE) binary system at five temperatures within the range from 293.04 K to 352.70 K. An isothermal correlation for the experimental data has been carried out based on the Peng-Robinson equation of state. The regressed binary interaction parameters were used to estimate VLE for the DME–CO2–DIPE ternary system at 298.15 K. From the study, it is demonstrated that DIPE is an excellent absorbent for separation in the DME synthesis process from syngas.
机译:蒸汽-液体平衡(VLE)数据已使用静态类型VLE装置对二甲醚(DME)-二异丙醚(DIPE)二元系统在293.04 K至352.70 K的五个温度下进行了测量。实验数据是根据彭-罗宾逊状态方程进行的。利用回归二元相互作用参数估算了DME-CO 2 -DIPE三元体系在298.15 K时的VLE。研究表明,DIPE是DME合成中分离的优良吸收剂合成气处理。

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