TY - JOUR
T1 - Numerical study of magneto-fluid-mechanic combined free-and-forced convection heat transfer
AU - Al-Khawaja, M. J.
AU - Agarwal, R. K.
AU - Gardner, R. A.
PY - 1998/2/1
Y1 - 1998/2/1
N2 - Fully-developed, laminar, steady, free-and-forced convection heat transfer in an electrically-conducting fluid flowing in an electrically-insulated, horizontal, circular pipe (with its wall subjected to a uniform heat flux) in a vertical, uniform, transverse magnetic field was solved numerically using several finite difference schemes for Grashof numbers from 0 to 106 and Hartmann numbers from 0 to 500. For high Hartmann numbers, a refinement of the mesh in the radial direction was necessary in the Hartmann boundary layer and relaxation techniques were needed to have a convergent solution. Velocity profiles, temperature profiles and local and average Nusselt numbers are reported for combined free-and-forced convection.
AB - Fully-developed, laminar, steady, free-and-forced convection heat transfer in an electrically-conducting fluid flowing in an electrically-insulated, horizontal, circular pipe (with its wall subjected to a uniform heat flux) in a vertical, uniform, transverse magnetic field was solved numerically using several finite difference schemes for Grashof numbers from 0 to 106 and Hartmann numbers from 0 to 500. For high Hartmann numbers, a refinement of the mesh in the radial direction was necessary in the Hartmann boundary layer and relaxation techniques were needed to have a convergent solution. Velocity profiles, temperature profiles and local and average Nusselt numbers are reported for combined free-and-forced convection.
KW - Forced convection
KW - Heat transfer
KW - Natural convection
UR - http://www.scopus.com/inward/record.url?scp=0344457317&partnerID=8YFLogxK
U2 - 10.1016/S0017-9310(98)00172-0
DO - 10.1016/S0017-9310(98)00172-0
M3 - Article
AN - SCOPUS:0344457317
SN - 0017-9310
VL - 42
SP - 467
EP - 475
JO - International Journal of Heat and Mass Transfer
JF - International Journal of Heat and Mass Transfer
IS - 3
ER -