Abstract
The injection moulding of thermoplastics involves, during mould filling, flows of hot polymer melts into mould networks, the walls of which are so cold that frozen layers form on them. An analytical study of such flows is presented here for the case when the Graetz and Nahme numbers are large and the Pearson number is small. Thus the flows are developing and temperature differences due to heat generation by viscous dissipation are sufficiently large to cause significant variations in viscosity (but the difference between the entry temperature of the polymer to a specific part of the mould network and the melting temperature of the polymer is not).
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Abbreviations
- Br :
-
Brinkman number
- Gz :
-
Graetz number
- h :
-
half-height of channel or disc
- h * :
-
half-height of polymer melt region in channel or disc
- L :
-
length of channel or pipe
- m :
-
viscosity shear-rate exponent
- Na :
-
Nahme number
- p :
-
pressure
- P :
-
pressure drop
- Pe :
-
Péclet number
- Pn :
-
Pearson number
- Q :
-
volumetric flowrate
- r :
-
radial coordinate in pipe or disc
- R :
-
radius of pipe
- Re :
-
Reynolds number
- R i :
-
inner radius of disc
- R o :
-
outer radius of disc
- R * :
-
radius of polymer melt region in pipe
- T :
-
temperature
- T ad :
-
adiabatic temperature rise
- T e :
-
entry polymer melt temperature
- T m :
-
melting temperature of polymer
- T max :
-
maximum temperature
- T 0 :
-
reference temperature
- T w :
-
wall temperature
- \(\bar T\) :
-
flow-average temperature rise
- u r :
-
radial velocity in pipe or disc
- u x :
-
axial velocity in channel
- u y :
-
transverse velocity in channel or disc
- u z :
-
axial velocity in pipe
- w :
-
width of channel
- x :
-
axial coordinate in channel or modified radial coordinate in disc
- y :
-
transverse coordinate in channel or disc
- z :
-
axial coordinate in pipe
- α :
-
thermal conductivity of molten polymer
- \(\hat \alpha\) :
-
thermal conductivity of frozen polymer
- β :
-
scaled dimensionless axial coordinate in channel or pipe or radial coordinate in disc
- β 0 :
-
undetermined integration constant
- γ :
-
heat capacity of molten polymer
- ζ :
-
viscosity temperature exponent
- η :
-
dimensionless transverse coordinate in channel or disc
- η * :
-
dimensionless half-height of polymer melt region in channel or disc
- H * :
-
scaled dimensionless half-height of polymer melt region in channel or disc or radius of polymer melt region in pipe
- θ :
-
dimensionless temperature
- θ * :
-
dimensionless wall temperature
- Θ :
-
scaled dimensionless temperature
- λ :
-
numerical constant
- µ :
-
viscosity of molten polymer
- µ 0 :
-
consistency of molten polymer
- π′ :
-
dimensionless pressure gradient
- Π′ :
-
scaled dimensionless pressure gradient
- ϱ :
-
density of molten polymer
- σ :
-
dimensionless radial coordinate in pipe or disc
- σ i :
-
dimensionless inner radius of disc
- σ * :
-
dimensionless radius of polymer melt region in pipe
- ϕ :
-
dimensionless streamfunction
- Ф :
-
scaled dimensionless streamfunction
- χ :
-
dummy variable
- ψ :
-
streamfunction
- ω :
-
similarity variable
- Ω :
-
similarity variable
References
Pearson JRA (1985) Mechanics of Polymer Processing. Elsevier Applied Science, London
Richardson SM (1983) Chapter 5 in: Pearson JRA, Richardson SM (eds) Computational Analysis of Polymer Processing. Applied Science, London
Richardson SM (1986) Chapter 4 in: Advances in Transport Processes 6
Pearson JRA (1978) Polymer Eng Science 18:222
Richardson SM (1983) Rheol Acta 22:223
Richardson SM (1985) Rheol Acta 24:497
Richardson SM (1985) Rheol Acta 24:509
Richardson SM, Pearson HJ, Pearson JRA (1980) Plastics Rubber: Processing 5:55
Richardson SM (1986) Rheol Acta 25 (in press)
Richardson SM (1986) Rheol Acta 25 (in press)
Pearson JRA (1977) J Fluid Mech 83:191
Ockendon H (1979) J Fluid Mech 93:737
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Richardson, S.M. Injection moulding of thermoplastics: Freezing of variable-viscosity fluids.. Rheol Acta 25, 180–190 (1986). https://doi.org/10.1007/BF01332137
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DOI: https://doi.org/10.1007/BF01332137