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Viscous heating correction for thermally developing flows in slit die viscometry

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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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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

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