Abstract
In the thermally developing region, dπ yy /dx| y=h varies along the flow direction x, where π yy denotes the component of stress normal to the y-plane; y = ±h at the die walls. A finite element method for two-dimensional Newtonian flow in a parallel slit was used to obtain an equation relating dπ yy /dx/ y=h and the wall shear stress σω0 at the inlet; isothermal slit walls were used for the calculation and the inlet liquid temperature T0 was assumed to be equal to the wall temperature. For a temperature-viscosity relation η/η0 = [1+β(T−T0]−1, a simple expression [(hdπ yy /dx/ y=h )/σ w0] = 1−[1-F c(Na)] [M(χ)+P(Pr) ·Q(Gz −1)] was found to hold over the practical range of parameters involved, where Na, Gz, and Pr denote the Nahme-Griffith number, Graetz number, and Prandtl number; χ is a dimensionless variable which depends on Na and Gz. An order-of-magnitude analysis for momentum and energy equations supports the validity of this expression. The function F c(Na) was obtained from an analytical solution for thermally developed flow; F c(Na) = 1 for isothermal flow. M(χ), P(Pr), and Q(Gz) were obtained by fitting numerical results with simple equations. The wall shear rate \(\dot \gamma _{w0} \)at the inlet can be calculated from the flow rate Q using the isothermal equation.
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Abbreviations
- x,y :
-
Cartesian coordinates (Fig. 2)
- ξ,ζ:
-
dimensionless spatial variables [Eq. (16)]
- κ:
-
dimensionless variable, κ: = Gz(x)−1
- χ:
-
dimensionless variable [Eq. (28)]
- t,t * :
-
time, dimensionless time [Eq. (16)]
- υ, ν:
-
velocity vector, dimensionless velocity vector
- υ x , νξ :
-
velocity in x-direction, dimensionless velocity
- υ y , νζ :
-
velocity in y-direction, dimensionless velocity
- V :
-
average velocity in x-direction
- π yy , πζζ * :
-
normal stress on y-planes, dimensionless normal stress
- σ:
-
shear stress on y-planes acting in x-direction
- σ w , σ w * :
-
value of shear stress stress at the wall, dimensionless wall shear stress
- σ w0, σ w0 * :
-
wall shear stress at the inlet, dimensionless variable
- \(\dot \gamma \), \(\dot \gamma \) * :
-
rate-of-strain tensor, dimensionless tensor
- \(\dot \gamma _w ,\dot \gamma _{w0}\) :
-
wall shear rate, wall shear rate at the inlet
- Q :
-
flow rate
- T, T 0, θ:
-
temperature, temperature at the wall and at the inlet, dimensionless temperature
- h, w :
-
half the die height, width of the die
- l,L :
-
the distance between the inlet and the slot region, total die length
- T 2, T 3, T 4 :
-
pressure transducers in the “High Shear Rate Viscometer (HSRV)” (Fig. 1)
- P, P2, P3:
-
pressure, liquid pressures applied to T 2 and T 3
- η, η0, η* :
-
viscosity, viscosity at T = T 0, dimensionless viscosity
- β:
-
viscosity-temperature coefficient [Eq. (8)]
- k :
-
thermal conductivity
- C p :
-
specific heat at constant pressure
- Re :
-
Reynolds number
- Na :
-
Nahme-Griffith number
- Gz :
-
Graetz number
- Pr :
-
Prandtl number
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Fluid Dynamics International Inc, Evanston, Illinois, USA
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Ko, Y.S., Lodge, A.S. Viscous heating correction for thermally developing flows in slit die viscometry. Rheola Acta 30, 357–368 (1991). https://doi.org/10.1007/BF00404195
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DOI: https://doi.org/10.1007/BF00404195