O. Jambal, T. Shigechi, G. Davaa and S. Momoki, “Effects of Viscous Dissipation and Fluid Axial Heat Conduction on Heat Transfer for Non-Newtonian Fluids in Ducts with Uniform Wall Temperature Part I: Parallel Plates and Circular Ducts,” International Communications in Heat Mass Transfer, Vol. 32, No. 9, 2005, pp. 1165-1173. doi:10.1016/j.icheatmasstransfer.2005.07.002

has been cited by the following article:

• TITLE: Heat Transfer with Viscous Dissipation in Couette-Poiseuille Flow under Asymmetric Wall Heat Fluxes

  AUTHORS: J. Sheela-Francisca, C. P. Tso, Dirk Rilling

  KEYWORDS: Viscous Dissipation; Couette-Poiseuille Flow; Newtonian Fluid; Nusselt Number; Brinkman Number; Constant Heat-Flux

  JOURNAL NAME: Open Journal of Fluid Dynamics, Vol.2 No.4, December 13, 2012

  ABSTRACT: Analytical solutions of temperature distributions and the Nusselt numbers in forced convection are reported for flow through infinitely long parallel plates, where the upper plate moves in the flow direction with constant velocity and the lower plate is kept stationary. The flow is assumed to be laminar, both hydro-dynamically and thermally fully developed, taking into account the effect of viscous dissipation of the flowing fluid. Both the plates being kept at specified and at different constant heat fluxes are considered as thermal boundary conditions. The solutions obtained from energy equation are in terms of Brinkman number, dimensionless velocity and heat flux ratio. These parameters greatly influence and give complete understanding on heat transfer rates that has potentials for designing and analyzing energy equipment and processes.