کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
201907 460576 2013 5 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Phase equilibrium for the binary mixture of {1,1-difluoroethane (R152a) + trans-1,3,3,3-tetrafluoropropene (R1234ze (E))} at various temperatures from 258.150 to 288.150 K
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Phase equilibrium for the binary mixture of {1,1-difluoroethane (R152a) + trans-1,3,3,3-tetrafluoropropene (R1234ze (E))} at various temperatures from 258.150 to 288.150 K
چکیده انگلیسی


• VLE data for {R152a + R1234ze} system were measured at four temperatures.
• Experiments adopt the static-analytic method.
• Correlation of VLE data was made using PR−HV−NRTL model.
• A zeotropic behavior was observed.

(Vapor + liquid) equilibrium (VLE) data for a binary system of {1,1-difluoroethene (R152a) + trans-1,3,3,3-tetrafluoropropene (R1234ze (E))} were measured by a static-analytic method at temperatures ranging from 258.150 to 288.150 K. All data were correlated by the Peng–Robinson equation of state (PR EoS) with the Huron–Vidal (HV) mixing rule involving the nonrandom two-liquid (NRTL) activity coefficient model. The correlated results show good agreement with the experimental data at each temperature point. The maximum average absolute relative deviation of pressure is 0.17%, while the maximum average absolute deviation of vapor phase mole fraction is 0.0020. Obviously the binary mixture is a zeotropic system at the measured temperature range.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fluid Phase Equilibria - Volume 355, 15 October 2013, Pages 99–103
نویسندگان
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