Viscosity of carbon dioxide in the liquid phase

The viscosity coefficient of liquid carbon dioxide has been measured along isotherms from the triple-point temperature (217 K) up to the critical temperature (304 K) at temperatures of 220, 230, 240, 260 and 280 K by means of a vibrating-wire viscometer. The measurements extended beyond both phase-transition lines into the coexistence region (superheated liquid) and into the solid range (undercooled liquid). The accuracy of the measurements is estimated to be 1%. The agreement with data of other authors is rather good. For the most part, the results show a linear pressure dependence in three neighbouring pressure ranges for the various isotherms with a common intersection with the negative pressure axis pi. The fluidity, the reciprocal of the viscosity, shows a linear dependence of the molar volume in adjacent density ranges. After reduction of the molar volume with the volumes of close packing, three sets of linear functions result with common intersections of the axis VB.

[1]  William Thomson,et al.  Mathematical and physical papers , 1880 .

[2]  W. Mccormick,et al.  Vibrating Wire Viscometer , 1964 .

[3]  W. Wakeham,et al.  The Transport Properties of Carbon Dioxide , 1990 .

[4]  F. Zernike,et al.  Theory of the Senftleben effect , 1939 .

[5]  A. Michels,et al.  The viscosity of argon at pressures up to 2000 atmospheres , 1954 .

[6]  H. Senftleben,et al.  Der Einfluß magnetischer Felder auf die innere Reibung von Gasen , 1937 .

[7]  J. Dymond The interpretation of transport coefficients on the basis of the Van der Waals model , 1975 .

[8]  E. Andrade,et al.  LVIII. A theory of the viscosity of liquids.—Part II , 1934 .

[9]  B. Alder,et al.  Studies in Molecular Dynamics. VIII. The Transport Coefficients for a Hard-Sphere Fluid , 1970 .

[10]  H. V. Hooff,et al.  The viscosity of argon at very high pressure, up to the melting line , 1980 .

[11]  R. LeSar,et al.  The influence of molecular shapes on the relative stability of solid phases: Application to N2O , 1992 .

[12]  H. Berg,et al.  The viscosity of methane at 25°C up to 10 kbar , 1988 .

[13]  A. J. Batschinski,et al.  Untersuchungen Aber die innere Reibnng der Flüssigkeiten. I , 1913 .

[14]  W. Wagner,et al.  A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple‐Point Temperature to 1100 K at Pressures up to 800 MPa , 1996 .

[15]  H. Berg,et al.  The working equations of a vibrating wire viscometer , 1989 .

[16]  N. Trappeniers,et al.  The viscosity of argon at high densities , 1986 .

[17]  H. Berg,et al.  The viscosity of methane at 273 K up to 1 GPa , 1992 .

[18]  M. J. Ball,et al.  Shear viscosity coefficients of compressed gaseous and liquid carbon dioxide at temperatures between 220 and 320 K and at pressures to 30 MPa , 1985 .

[19]  H. Berg,et al.  Working equation for a capillary viscometer with non-steady compressible flow , 1990 .

[20]  W. Mccormick,et al.  Viscosity of Liquid He II , 1963 .