A compendium of phase change enthalpies published in 2010 is updated to include the
period 1880–2015. Phase change enthalpies including fusion, vaporization, and …

As a part of a series of reviews, a compilation of systems for which high-pressure phase-
equilibrium data were published between 2000 and 2004 is given. Vapor–liquid equilibria …

Isothermal (Pxy) vapor–liquid equilibrium data for the CO 2+ 2, 3, 3, 3-tetrafluoroprop-1-ene
(R1234yf) binary system are reported at seven temperatures ranging from 283.15 K to …

Thermodynamic cycles such as the organic Rankine cycle (ORC), heat pump cycles and
refrigeration cycles are flourishing in both industrial and domestic fields. As a carrier of …

Equations of state are presented for the refrigerants 1, 1, 1, 2, 3, 3, 3-heptafluoropropane (R-
227ea) and 1, 1, 1, 3, 3-pentafluorobutane (R-365mfc). For R-227ea, the uncertainties in …

Abstract Isothermal Vapor–Liquid Equilibrium (VLE) data for the binary mixture of CO 2+ R-
1234ze (E)(trans-1, 3, 3, 3-tetrafluoroprop-1-ene) were measured using a static-analytic …

An extension of the SAFT-VR Mie equation of state is proposed to predict the properties of
multipolar fluids. The new model, referred to as multipolar M-SAFT-VR Mie, incorporates the …

Accurate knowledge of phase diagrams is an essential step for optimized chemical
engineering design and effective solution of engineering-related problem. As an example of …

Isothermal vapor–liquid equilibrium (VLE) data have been measured for the binary system
carbon dioxide (CO2)+ difluoromethane (R32) at eight temperatures between 283.12 and …

Accurate thermo-physical data are of utmost interest for the development of new efficient
refrigeration systems. Carbon dioxide (R744) and 1, 1-difluoroethane (R152a) are …