Abstract
A perturbation analysis is presented for the steady-state radial flow of a third-order fluid between two parallel disks. The results include previous perturbation analyses in which various other rheological models were used. The pressure drop needed to maintain the radial flow is less than that for the Newtonian creeping-flow solution because of fluid inertia and shear-thinning viscosity, whereas the normal stresses have the opposite effect. Possible use of the “radial flow viscometer” for experimental evaluation of second-order constants is also discussed. Finally, molecular stretching in the flow system is examined using the elastic dumbbell model for a polymer molecule.
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Abbreviations
- A2, A11, A3, ...:
-
Dimensionless constants in the third-order fluid [see equations (30) and (31)]
- c mn :
-
Coefficients in a function of the form C given in equation (34)
- d mn :
-
Coefficients in a function of the form D given in equation (35)
- h :
-
Half distance between the two disks
- H :
-
Spring constant of Hookean dumbbell
- i, j, k, m, n :
-
Indices
- K :
-
Boltzmann's constant
- M :
-
A dimensionless normal stress difference, (τ rr−τθθ)h/η 0 V
- Mi, Mij:
-
Functions in the expansion for M [see equation (39)]
- jackie :
-
Molecular weight of the macromolecules
- jackie :
-
Number density of polymer molecules
- N :
-
A dimensionless normal stress difference, (τ rr−τzz)h/η 0 V
- Ni, Nij:
-
Functions in the expansion for N [see equation (38)]
- Ñ :
-
Avogadro's number
- P :
-
Dimensionless pressure, (p+τ zz)h/η 0 V
- Pi, Pij:
-
Functions in the expansion for P [see equation (36)]
- ΔP :
-
Dimensionless pressure drop, P(R, ±1)−P(R 1, ±1)
- ΔP N :
-
Newtonian creeping-flow result for ΔP
- Q :
-
Volume rate of flow
- r :
-
Radial coordinate
- r 0 :
-
Radius of the orifice on the upper disk
- r 1 :
-
Radius of the disk
- R :
-
Dimensionless radial coordinate, r/h
- R 1 :
-
Dimensionless radius of the disk, r 1/h
- 〈jackie 2〉:
-
Average value of the square of the dumbbell length jackie
- 〈jackie 2〉 eq :
-
Value of 〈jackie 2〉 at equilibrium
- Re :
-
Reynolds number, ρVh/η 0
- t :
-
Time
- T :
-
Dimensionless shear stress, τ rzh/τ0 V
- Ti, Tij:
-
Functions in the expansion for T [see equation (37)]
- jackie :
-
Absolute temperature
- U :
-
Dimensionless radial velocity, v r/V
- Ui, Uij:
-
Functions in the expansion for U [see equation (32)]
- v :
-
Velocity vector
- V :
-
Characteristic velocity, Q/4πr 1 h
- W :
-
Dimensionless axial velocity, v z/V
- W i :
-
Functions in the expansion of W [see equation (33)]
- x, y, z :
-
Cartesian coordinates
- z :
-
Axial coordinate
- Z :
-
Dimensionless axial coordinate, z/h
- α :
-
Dimensionless parameter in Spriggs four-constant model
- α1, α2, α11, ...:
-
Constants in the third-order fluid
- \(\dot \gamma \) :
-
Shear rate; magnitude of the \(\dot \gamma \) tensor [defined by \(\dot \gamma \) = \(\sqrt {(1/2)(\dot \gamma :\dot \gamma )]} \)
- \(\dot \gamma \) :
-
Rate-of-strain tensor \((\dot \gamma _{ij}= \partial v_j /\partial x_i+ \partial v_i /\partial x_j)\)
- ε :
-
Dimensionless parameter in Spriggs four-constant model
- ζ(α):
-
Riemann zeta function of α
- η :
-
Non-Newtonian viscosity
- η 0 :
-
Zero-shear-rate viscosity
- η s :
-
Solvent viscosity
- [η]0 :
-
Zero-shear-rate intrinsic viscosity
- θ :
-
Tangential coordinate
- λ :
-
Time constant in Spriggs four-constant model
- λ H :
-
Time constant for Hookean dumbbells
- ρ :
-
Density of fluid
- τ :
-
Stress tensor
- τ p :
-
Polymer contribution to τ
- τ s :
-
Solvent contribution to τ
- Ψ1, Ψ2:
-
Primary and secondary normal stress coefficients
- ω :
-
Vorticity tensor \((\omega _{ij}= \partial v_j /\partial x_i- \partial v_i /\partial x_j )\)
- D/Dt :
-
Substantial or material derivative
- D/Dt:
-
Corotational or Jaumann derivative
- o:
-
Derivative with respect to Z
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Co, A., Bird, R.B. Slow viscoelastic radial flow between parallel disks. Appl. Sci. Res. 33, 385–404 (1977). https://doi.org/10.1007/BF00411821
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DOI: https://doi.org/10.1007/BF00411821