کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
200909 460524 2016 6 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Isothermal vapor–liquid equilibria measurements for binary systems of 2,3,3,3-tetrafluoropropene (HFO-1234yf) + 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) and 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) + 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244
ترجمه فارسی عنوان
اندازه گیری تعادل بخار و مایع ایزوترمال برای سیستم های دوتایی 2،3،3،3-تترافلو پروپران (HFO-1234yf) + 2-کلرو -3،3،3-تری فلو پروپران (HCFO-1233xf) و 2-کلرو -3،3، 3-trifluoropropene (HCFO-1233xf) + 2-chloro-1،1،1،2-tetrafluoropropane (HCFC-244
کلمات کلیدی
تعادل بخار و مایع؛ سیستم دودویی؛ 2،3،3،3-Tetrafluoroprop-1-خو. 2-کلرو -3،3،3-تری فلو پروپران؛ 2-Chloro-1،1،1،2-tetrafluoropropane
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


• Experimental VLE data for systems of HFO-1234yf + HCFO-1233xf and HCFO-1233xf + HCFC-244bb are reported.
• The HFO-1234yf + HCFO-1233xf system was measured from (293.15 to 313.15) K.
• The HCFO-1233xf + HCFC-244bb system was measured from (303.15 to 323.15) K.
• The Experimental data were correlated with the PR equation with vdW mixing rule.

This paper presents the measurements of isothermal vapor-Liquid equilibria (VLE) data for two binary systems of 2,3,3,3-tetrafluoropropene (HFO-1234yf) + 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) and 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) + 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb). The measurements were performed with an apparatus based on the static-analysis method. The HFO-1234yf + HCFO-1233xf system was measured at three temperatures from (293.15 to 313.15) K, and the HCFO-1233xf + HCFC-244bb system was measured at three temperatures from (303.15 to 323.15) K. The system of HFO-1234yf + HCFO-1233xf shows a small deviation from Raoult's law and dose not exhibit azeotropic behavior, while the system of HCFO-1233xf + HCFC-244bb exhibits near azeotropic behavior within the complete range of composition. All of the experimental data were correlated with the Peng–Robinson equations of state with the van der Waals mixing rules. Good consistency was obtained between the experimental data and correlated values for the both systems in the experimental temperature range. Thermodynamic consistency testing was also performed by the data-reduction method for the observed experimental data.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fluid Phase Equilibria - Volume 414, 25 April 2016, Pages 143–148
نویسندگان
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