TY - JOUR
T1 - Simultaneous correlation of saturated viscosities of pure gases and liquids using the significant structure theory
AU - Cruz-Reyes, Gustavo
AU - Luna-Bárcenas, Gabriel
AU - Alvarado, J. Francisco Javier
AU - Sánchez, Isaac C.
AU - Macías-Salinas, Ricardo
PY - 2005/3/16
Y1 - 2005/3/16
N2 - The significant structure theory (SST) for liquid viscosities, originally proposed by Eyring, coupled with a cubic equation of state was used for the simultaneous correlation of gas and liquid viscosities of pure fluids (polar and nonpolar) at saturated conditions. The SST visualizes a liquid as having both "solidlike" and "gaslike" degrees of freedom with "fluidized vacancies" of molecular size randomly distributed throughout a quasi-lattice structure. In this context, the viscosity of a liquid is calculated from two main components: a gaslike ηg and a solidlike ηs contribution. The first viscosity contribution ηg represents the viscosity of a pure fluid at dilute gas conditions (low-pressure viscosity). The method of Chung et al. based on the Chapman-Enskog kinetic theory of gases was used to calculate ηg. The second contribution ηs captures the solidlike effects on viscosity. This quantity was calculated by means of Eyring's absolute rate theory. All the thermodynamic properties required in the viscosity model were computed via the use of a well-known cubic equation of state (Soave-Redlich-Kwong or Peng-Robinson) thus allowing the simultaneous correlation of gas-liquid viscosities along their coexistence curve. The resulting model was satisfactorily validated in the representation of experimental saturated gas and liquid viscosities of a highly polar compound (water) and a nonpolar fluid (propane) over a wide range of temperatures (from near the triple point up to the critical region of the fluid of interest).
AB - The significant structure theory (SST) for liquid viscosities, originally proposed by Eyring, coupled with a cubic equation of state was used for the simultaneous correlation of gas and liquid viscosities of pure fluids (polar and nonpolar) at saturated conditions. The SST visualizes a liquid as having both "solidlike" and "gaslike" degrees of freedom with "fluidized vacancies" of molecular size randomly distributed throughout a quasi-lattice structure. In this context, the viscosity of a liquid is calculated from two main components: a gaslike ηg and a solidlike ηs contribution. The first viscosity contribution ηg represents the viscosity of a pure fluid at dilute gas conditions (low-pressure viscosity). The method of Chung et al. based on the Chapman-Enskog kinetic theory of gases was used to calculate ηg. The second contribution ηs captures the solidlike effects on viscosity. This quantity was calculated by means of Eyring's absolute rate theory. All the thermodynamic properties required in the viscosity model were computed via the use of a well-known cubic equation of state (Soave-Redlich-Kwong or Peng-Robinson) thus allowing the simultaneous correlation of gas-liquid viscosities along their coexistence curve. The resulting model was satisfactorily validated in the representation of experimental saturated gas and liquid viscosities of a highly polar compound (water) and a nonpolar fluid (propane) over a wide range of temperatures (from near the triple point up to the critical region of the fluid of interest).
UR - http://www.scopus.com/inward/record.url?scp=14844345808&partnerID=8YFLogxK
U2 - 10.1021/ie049070v
DO - 10.1021/ie049070v
M3 - Artículo
AN - SCOPUS:14844345808
SN - 0888-5885
VL - 44
SP - 1960
EP - 1966
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 6
ER -