Abstract
Theapparent slip flow phenomenon of polymer solutions in capillary tubes is analyzed by a thermodynamic diffusion model. An approximate solution of the developing concentration profiles shows a significant decrease in the polymer wall concentration. The approximate concentration profiles are coupled with the concentration-dependent viscosity for aqueous polyacrylamide solutions to provide a priori predictions of the magnitude of the effective slip velocity at the wall. The results are in a reasonable agreement with the available apparent slip data for 1% and 0.5% solutions of partially hydrolyzed polyacrylamide.
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Abbreviations
- b :
-
parameter defined in eq. (12)
- C :
-
polymer mass concentration
- C p :
-
polymer concentration in weight percent
- d :
-
parameter defined in eq. (13)
- D :
-
tube diameter
- D 12 :
-
phenomenological diffusion coefficient for a polymer in a solvent
- D :
-
polymer mass diffusivity in polymer solution; eq. (9)
- f :
-
entropic potential; eqs. (5) and (17)
- J (2) :
-
diffusion flux of polymer
- k, k 0 :
-
power law parameter (consistency index) at the local and initial concentrations, respectively
- k m :
-
empirical relaxation time parameter: eq. (35)
- L :
-
tube length
- m :
-
empirical parameter; eq. (35)
- n, n 0 :
-
power-law parameter (flow-behavior index) at the local and initial concentrations
- N WS :
-
Weissenberg number; eq. (21)
- N pec :
-
Peclet number; eq. (15)
- p :
-
pressure
- Q :
-
total flow rate
- Q s :
-
flow rate increase due toapparent slip
- r :
-
radial position
- \(\bar r\) :
-
dimensionless radial position
- R :
-
tube radius
- R c :
-
universal gas constant
- T :
-
temperature
- v :
-
velocity
- V s :
-
effective slip velocity
- 〈V z 〉:
-
average axial velocity
- \(\bar V_z \) :
-
dimensionless axial velocity
- 〈V z 〉 NS :
-
average axial velocity in the absence of apparent slip effects
- V r :
-
radial velocity
- z :
-
axial position
- z * :
-
dimensionless axial position
- \(\dot \gamma \) :
-
shear rate
- \(\dot \gamma \) :
-
wall shear rate corrected for apparent slip effects
- θ :
-
fluid relaxation time
- θ NS :
-
relaxation time in the absence of apparent slip at\(\dot \gamma = \dot \gamma _{NS} \)
- τ :
-
shear stress
- τ w :
-
wall shear stress
- η :
-
local viscosity
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Cohen, Y., Metzner, A.B. An analysis of apparent slip flow of polymer solutions. Rheol Acta 25, 28–35 (1986). https://doi.org/10.1007/BF01369977
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DOI: https://doi.org/10.1007/BF01369977