Numerical simulation of the laminar flow and heat transfer of the viscoelastic duct flows with the entrance effects

Abstract

In this study, the three dimensional flow and heat transfer of viscoelastic fluid has been modeled with the Giesekus constitutive equation. In the most previous research, they focused on the fully developed region of flow which is due to the lack of comprehensive research in this field , the studding of the viscoelastic flow in the developing region seems be essential. The governing equation that should be solved are : mass, momentum and energy conservation with the Giesekus constitutive equation that are descried with the finite difference method and solved by the artificial compressibility method on the staggered grid. It should be noted that, with this constitutive equation, the second normal stress difference is non-zero and therefore the secondary flow in the cross section are formed and will be visible. The dependency of the fluid property to temperature is one of the advantages of this research. Due to the dominant group of the viscoelastic fluid are melt polymers and in this situation, the variation of the temperature is high, therefore this assumption seems be necessary. The results in the fully developed zone are in good agreement with the other reported results.

Keywords


 [1] Gao SX, Hartnett JP (1996), Heat transfer behavior of reiner-rivlin fluids in rectangular ducts, Int. J. Heat Mass Transfer 39: 1317–1324.
 [2] Syrjälä S (1998), Laminar flow of viscoelastic fluids in rectangular ducts with heat transfer, Int. Commun. Heat Mass Transfer 25: 191–204.
 [3] Giesekus H (1965), Sekundärströmungen in viskoelastischen Flüssigkeiten bei stationärer und periodischer Bewegung, Rheol. Acta 4: 85–101.
 [4] Debbaut B, Avalosse T, Dooley J, Hughes K (1997), On the development of secondary motions in straight channels induced by the second normal stress difference: experiments and simulations, J. Non-Newtonian Fluid Mech. 69: 255–271.
 [5] Debbaut B, Dooley J (1999), Secondary motions in straight and tapered channels: Experiments and three dimensional finite element simulation with a multimode differential viscoelastic model, J. Rheol. 43: 1525–1545.
 [6] Yue P, Dooley J, Feng JJ (2007), A general criterion for viscoelastic secondary flow in pipes of noncircular cross section, J. Rheol. 52(1): 315–332.
 [7] Boutabaa M, Helin L, Mompean G, Thais L (2009), Numerical study of Dean vortices in developing Newtonian and viscoelastic flows through a curved duct of square cross-section, J. Comptes Rendus Mechanique. 337: 40–47.
 [8] Tanoue S, Naganawa T and Iemoto Y (2006), Quasi-three-dimensional simulation of viscoelastic flow through a straight channel with a square cross section, J. Soc. Rheol., Jpn. 34: 105–113.
 [9] Robert E, Gaidos, Darby R (1988), Numerical simulation and change in type in the developing flow of a nonlinear viscoelastic fluid, J. Non-Newtonian Fluid Mech, 29: 59–79.
[10] Nikoleris T, Darby R (1989), Numerical simulation of the non-isothermal flow of a nonlinear viscoelastic fluid in a rectangular channel, J. Non-Newtonian Fluid Mech, 31: 193–207.
[11] Oldroyd JG (1956), Some steady flows of the general elastico-viscous liquid, Proc. R. Soc. London, Ser. A 283: 115–133.
[12] Hatzikiriakos SG, Dealy JM (1991), Wall slip of molten high-density polyethylene, Sliding plate rheometer studies, J. Rheology, 35: 497–523.
[13] Hatzikiriakos SG and Dealy JM (1992), Wall slip of molten high-density polyethylene, II Capillary rheometer studies, Journal of Rheol, 36: 703–741.
[14] Denn MM (1992), Surface-induced effects in polymer melt flow, Theoretical and Applied Rheology, Elsevier, New York: 45–49.
[15] Hill DA, Hasegawa T and Denn MM (1990), On the apparent relation between adhesive failure and melt fracture, J. Rheol, 34: 891–918.
[16] Mark JE (1996), Physical properties of polymers Handbook, American Institute of Physics, New York.