Page 352 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
P. 352

P1: JDW
                                           June 22, 2007
                                                        14:25
            AT029-Manual
  AT029-08
                        AT029-Manual-v7.cls
         332 CHARACTERIZATION AND PROPERTIES OF PETROLEUM FRACTIONS













                                                         (a) Gases



























                                                        (b) Liquids

                               FIG. 8.1—Viscosity of several light hydrocarbons versus temperature at atmo-
                             spheric pressure. Taken with permission from Ref. [2].

           --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
         where μ is in cp, T r is the reduced temperature, and ξ is a  where units of μ and ξ are the same as in Eq. (8.4). For de-
         parameter that has a dimension of inverse viscosity and is ob-  fined gas mixtures at low pressures, Eq. (8.6) may be used
         tained from kinetic theory of gases. The factor 0.987 comes  with T c , P c , and M calculated from Kay’s mixing rule (Eq. 7.1).
         from the original definition that unit of atm was used for P c .In  However, when viscosity of individual gases in a mixture are
         the above equation P c , T c , and M are in bar, kelvin, and g/mol,  known, a more accurate method of estimation of mixture vis-
         respectively. In cases where data on gas viscosity is available,  cosity is provided by Wilke, which can be applied for pressures
         it would be more appropriate to determine ξ from viscosity  with P r < 0.6 [1, 5]:
         data rather than to calculate it from the above equation. Reli-
         ability of this equation is about 3–5%. For some specific com-  μ m =  N    x i μ i
         pounds such as hydrogen, the numerical coefficients in Eq.        i=1    N  x j φ ij
                                                                               j=1
         (8.4) are slightly different and in the same order as given in the  (8.7)  1       −  1 2          1      1 4  	 2
                                                                                                2
         DIPPR manual are 47.65, −20.0, −0.858, +19.0, and −3.995.    φ ij = √  1 +  M i  1 +  μ i  M j
         In the 1997 edition of the API-TDB [5], the more commonly          8     M j        μ j   M i
         used correlation developed earlier by Stiel and Thodos [7] is  This semiempirical method is recommended by both API-
         recommended:
                                                              TDB and DIPPR for calculation of viscosity of gas mixtures
                           −4
                μξ = 3.4 × 10 T r 0.94          for T r ≤ 1.5  of known composition at low pressures. Accuracy of this
        (8.6)
                             −4
                μξ = 1.778 × 10 (4.58T r − 1.67) 0.625  for T r > 1.5  equation is about 3% [5, 8]. In the above relation φ ij  = φ ji .












   Copyright ASTM International
   Provided by IHS Markit under license with ASTM             Licensee=International Dealers Demo/2222333001, User=Anggiansah, Erick
   No reproduction or networking permitted without license from IHS  Not for Resale, 08/26/2021 21:56:35 MDT
   347   348   349   350   351   352   353   354   355   356   357