Skip to main content
Log in

A pseudo-time integral method for non-isothermal viscoelastic flows and its application to extrusion simulation

  • Original Contributions
  • Published:
Rheologica Acta Aims and scope Submit manuscript

Abstract

A pseudo-time integral scheme based on a finite streamline element method is developed to combine variable temperature with viscoelasticity. A specific KBKZ integral model for isothermal flow is transformed to its non-isothermal version by introducing a pseudo-time and applying the Morland-Lee hypothesis. The coupling between momentum and energy equations is through the time-temperature shifting factor by which the pseudo-time is defined. The observer time and the pseudo-time are simultaneously calculated when tracing the strain history for the stress calculation in a non-homogeneous temperature field. Using this scheme, a full non-isothermal numerical simulation of some IUPAC extrusion experiments is carried out. Results show that while the temperature distribution near the die exit plane is an important factor controlling extrudate swell, either self-heating inside the die tube or external cooling on the free surface dominantly determines the temperature distribution near the die exit when the wall temperature is kept constant, depending on whether the Péclet number is large or small. The hot layer effect predicted by the inelastic swell mechanism is confirmed and well illustrated by the computation. Calculations with reasonable thermal boundary conditions further convince us that the isothermal assumption in our earlier numerical simulation is a good approximation in this particular case.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

References

  1. Tanner RI (1985) Engineering Rheology. Oxford University Press

  2. Phuoc HB, Tanner RI (1980) J Fluid Mech 98:253

    Google Scholar 

  3. Tanner RI (1980) J Non-Newtonian Fluid Mech 6:289

    Google Scholar 

  4. Luo XL, Tanner RI (1986) J Non-Newtonian Fluid Mech 21:179

    Google Scholar 

  5. Luo XL, Tanner RI (1985) J Polym Engng Sci 25: 320

    Google Scholar 

  6. Morland LW, Lee EH (1960) Trans Soc Rheol 4:233

    Google Scholar 

  7. Luo XL, Tanner RI (1986) J Non-Newtonian Fluid Mech 22:61

    Google Scholar 

  8. Kearsley EA (1962) Trans Soc Rheol 6:253

    Google Scholar 

  9. Papanastasiou AC, Scriven LE, Macosko CW (1983) J Rheol 27:387

    Google Scholar 

  10. Luo XL, Tanner RI (1987) Int J Num Meth Engng, to appear

  11. Huynh BP (1983) J Non-Newtonian Fluid Mech 13:1

    Google Scholar 

  12. Meissner J (1975) Pure and Applied Chemistry 42:551

    Google Scholar 

  13. Pearson JRA, Richardson SM (1983) Computational Analysis of Polymer Processing. Applied Science Publications, London

    Google Scholar 

  14. Collins EA, Metzger A (1970) Polym Engng Sci 10:57

    Google Scholar 

  15. Christensen RM (1971) Theory of Viscoelasticity. Academic Press, New York

    Google Scholar 

  16. Matsumoto T, Bogue DC (1977) Trans Soc Rheol 21:453

    Google Scholar 

  17. Acierno D, Dalton JN, Rodriguez JM, White JL (1971) J Appl Polym Sci 15:2395

    Google Scholar 

  18. Gupta RK (1981) Ph.D Thesis, University of Delaware

Download references

Author information

Authors and Affiliations

Authors

Rights and permissions

Reprints and permissions

About this article

Cite this article

Luo, X.L., Tanner, R.I. A pseudo-time integral method for non-isothermal viscoelastic flows and its application to extrusion simulation. Rheol Acta 26, 499–507 (1987). https://doi.org/10.1007/BF01333733

Download citation

  • Received:

  • Issue Date:

  • DOI: https://doi.org/10.1007/BF01333733

Key words

Navigation