کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
202318 460597 2011 5 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Study on gas–liquid equilibria with the UNIFAC model for the systems of synthesizing dimethyl carbonate
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Study on gas–liquid equilibria with the UNIFAC model for the systems of synthesizing dimethyl carbonate
چکیده انگلیسی

Gas–liquid equilibrium (GLE) data for the binary systems of {CO + DMC} and {O2 + DMC} were respectively measured at 298.15–313.15 K and at 2.0–9.0 MPa. The modified UNIFAC model proposed by Sander et al. [10] was employed to correlate the experimental and literature GLE data for the binary systems of {CO + DMC}, {O2 + DMC} and {CO2 + DMC} in a wide range of temperatures and pressures. At the same time, the missing energy parameters unm of the carbonate group –OCOO– with the group CO, O2, CO2 and –CH3 in the modified UNIFAC model were determined. It is indicated that the calculated GLE data using the new UNIFAC parameters are consistent with the experimental GLE data in this work and in literature. The results of this work are necessary and helpful for the UNIFAC database, which not only extend the application field of the UNIFAC model, but also are useful for the design of reactor and separation apparatus in DMC production.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fluid Phase Equilibria - Volume 302, Issues 1–2, 15 March 2011, Pages 269–273
نویسندگان
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