Abstract
When the flow behaviour of fluids is investigated with capillary-or rotational rheometers, adhesion of the fluid to the wall is normally one of the boundary conditions. For many fluids, especially for suspensions, this assumption is not valid. These fluids tend to slip at the wall. Therefore the normal evaluation of rheometer measurements leads to apparent but not compatible flow functions. The flow behaviour of these fluids can be characterized with two material functions which describe separately slipping in the boundary layer and shearing within the fluid. Only if both functions are known, correct predictions of flow processes are possible. A simple equipment to separate the shear function and the slip function is described.
Abbreviations
- Y* :
-
apparent shear rate
- Y *w :
-
apparent wall shear rate
- Yw :
-
wall shear rate corrected with Rabinowitsch and Weissenberg correction
- Ys :
-
reduced shear rate (slip corrected)
- Yws :
-
reduced wall shear rate (slip corrected)
- ν* (r):
-
velocity distribution in a capillary
- νG :
-
slip velocity (at the wall)
- ν* (r):
-
velocity distribution in a capillary (without slip)
- τ:
-
shear stress
- τ w :
-
wall shear stress
- VS :
-
total volume rate
- VG :
-
shear volume rate
- VG :
-
slip volume rate
- p 1 :
-
pressure in the reservoir channel of the capillary rheometer
- p 0 :
-
athmospheric pressure
- L :
-
capillary length
- R :
-
capillary radius
References
Mooney, M. 1931: Explicit formulas for slip and fluidity. J. Rheology 2, 210–222
Rabinowitsch, B. 1929: Über die Viskosität und Elastizität von Solen. Z. Phys. Chem. 145A, 1–26
Rautenbach, R.; Schlegel, D. 1969: F1ießverhalten dispers plastischer Materialien im Couette Rheometer. Chem.-Ing.-Techn. 41,369–374
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Gleißle, W., Windhab, E. The “Twin capillary” a simple device to separate shear- and slip-flow of fluids. Experiments in Fluids 3, 177–180 (1985). https://doi.org/10.1007/BF00280457
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DOI: https://doi.org/10.1007/BF00280457