Modélisation des Systèmes de Production de Froid. Doctorat thesis (2010) , Université de Batna 2.

dc.contributor.authorMADANI Hakim
dc.date.accessioned2023-05-08T09:09:09Z
dc.date.available2023-05-08T09:09:09Z
dc.date.issued2017-01-12
dc.description.abstractAccurate thermo-physical data are of utmost interest for the development of new efficient refrigeration systems. Carbon dioxide (R744) and 1,1-difluoroethane (R152a) are addressed here. Isothermal (vapor + liquid) equilibrium data are reported herein for (R744 + R152a) binary system in the (258–343) K temperature range and in the (0.14 to 7.65) MPa pressure range. A reliable ‘‘static-analytic” method taking advantage of two online ROLSITM micro capillary samplers is used for all thermodynamic measurements. The data are correlated using our in-house ThermoSoft thermodynamic model using the Peng–Robinson equation of state, the Mathias–Copeman alpha function, the Wong–Sandler mixing rules, and the NRTL model.
dc.identifier.urihttp://dspace.univ-batna2.dz/handle/123456789/1347
dc.language.isofr
dc.titleModélisation des Systèmes de Production de Froid. Doctorat thesis (2010) , Université de Batna 2.
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