Solid–Liquid Equilibria for the CO2 + R143a and N2O + R143a Systems
暂无分享，去创建一个
[1] G. Nicola,et al. Solid−Liquid Equilibria for the Carbon Dioxide + 1,1-Tetrafluoroethane and Nitrous Oxide + 1,1-Tetrafluoroethane Systems , 2008 .
[2] F. Polonara,et al. Solid−Liquid Equilibria for the CO2 + R152a and N2O + R152a Systems , 2007 .
[3] F. Polonara,et al. Solid-liquid equilibria for the CO2 + N2O, CO2 + R32, and N2O + R32 systems , 2007 .
[4] F. Polonara,et al. Solid−Liquid Equilibria for the CO2 + R125 and N2O + R125 Systems: A New Apparatus , 2006 .
[5] J. Magee,et al. Molar Heat Capacity at Constant Volume of Trifluoromethane (R23) from the Triple-Point Temperature to 342 K at Pressures to 33 MPa , 2000 .
[6] Ž. Knez,et al. Comparison of different methods for determination of the S–L–G equilibrium curve of a solid component in the presence of a compressed gas , 2000 .
[7] J. Magee. Molar Heat Capacity at Constant Volume of 1,1-Difluoroethane (R152a) and 1,1,1-Trifluoroethane (R143a) from the Triple-Point Temperature to 345 K at Pressures to 35 MPa , 1998 .
[8] David R. Lide,et al. CRC HANDBOOK of THERMOPHYSICAL and THERMOCHEMICAL DATA , 1994 .
[9] F. Rossini,et al. Determination of freezing points and amounts of impurity in hydrocarbons from freezing and melting curves , 1941 .