LIANG Ji-zhao. Estimation of vortical region length of rubber compound during entry flow [J]. Plastics Rubber and Composites Processing and Applications, 1996, (10):495-498.
[2]
LIANG Ji-zhao. Planar entry converging flow during extrusion of polymer melts [J]. Polymer-Plastics Technology and Engineering, 2007(5):475-480.doi:10.1080/03602550701297087.
[3]
KWON Y, LEONOV A I. Stability constraints in the formulation of viscoelastic constitutive equations [J]. Journal of Non-Newtonian Fluid Mechanics, 1995(1):25-46.
[4]
MEERVEL J V D. Note on thermodynamic consistency of the integral Pom-Pom model [J]. Journal of Non-Newtonian Fluid Mechanics, 2002, (1/3):291-299.
[5]
LIANG Ji-zhao. Determination of the entry region length of viscoelastic fluid flow in a channel [J]. Chemical Engineering Science, 1998, (17):3185-3187.doi:10.1016/S0009-2509(98)00155-9.
[6]
TANNER R I, NASSERI S. Simple constitutive models for linear and branched polymers [J]. Journal of Non-Newtonian Fluid Mechanics, 2003(1):1-17.
[7]
SIMHAMBHATLA M, LEONOV A I. On the rheological modeling of viscoelastic polymer liquids with stable constitutive-equations [J]. Rheologica Acta, 1995(3):259-273.
[8]
ZATLOUKAL M. Differential viscoelastic constitutive equations for polymer melts in steady shear and elongational flows [J]. Journal of Non-Newtonian Fluid Mechanics, 2003, (2/3):209-222.
[9]
MCLEISH T C B, LARSON R G. Molecular constitutive equations for a class of branched polymers:The Pom-Pom model [J]. Journal of Rheology, 1998(1):81-110.doi:10.1122/1.550933.
[10]
VERBEETEN W M H, PETERS G W M, BAAIJENS F P T. Differential constitutive equations for polymer melts:Extended Pom-Pom model [J]. Journal of Rheology, 2001(4):823-843.doi:10.1122/1.1380426.
[11]
LAUN H M, SCHUCH H. Transient elongational viscosities and drawability of polymer melts [J]. Journal of Rheology, 1989(1):119-175.
