Published online by Cambridge University Press: 31 January 2013
We report on near-turbulent thermal convection of a nematic liquid crystal heated from below in a cylindrical cell with an aspect ratio (diameter/height) equal to 0.50 for Rayleigh numbers   $2\times 1{0}^{7} \lesssim \mathit{Ra}\lesssim 3\times 1{0}^{8} $  and a Prandtl number of about 355. The Nusselt number
 $2\times 1{0}^{7} \lesssim \mathit{Ra}\lesssim 3\times 1{0}^{8} $  and a Prandtl number of about 355. The Nusselt number   $\mathit{Nu}$  as a function of
 $\mathit{Nu}$  as a function of   $\mathit{Ra}$  did not differ significantly from that of an isotropic fluid. In a vertical magnetic field
 $\mathit{Ra}$  did not differ significantly from that of an isotropic fluid. In a vertical magnetic field   $\mathbi{H}$ , we found
 $\mathbi{H}$ , we found   $\mathit{Nu}(H)/ \mathit{Nu}(0)= 1+ a(\mathit{Ra}){H}^{2} $ , with
 $\mathit{Nu}(H)/ \mathit{Nu}(0)= 1+ a(\mathit{Ra}){H}^{2} $ , with   $a(\mathit{Ra})= 0. 24{\mathit{Ra}}^{0. 75} ~{\mathrm{G} }^{- 2} $ . We present a model that describes the
 $a(\mathit{Ra})= 0. 24{\mathit{Ra}}^{0. 75} ~{\mathrm{G} }^{- 2} $ . We present a model that describes the   $H$  dependence in terms of a change of the thermal conductivity in the thermal boundary layers due to a field-induced director alignment.
 $H$  dependence in terms of a change of the thermal conductivity in the thermal boundary layers due to a field-induced director alignment.
Current address: Department of Physics & Center for the Study of Complex Systems, University of Michigan, Ann Arbor, MI 48109, USA.
 ${4}^{\prime } $
                     
                  -cyanobiphenyl. Phys. Rev. E
               49, 545–553.Google Scholar
                        ${4}^{\prime } $
                     
                  -cyanobiphenyl. Phys. Rev. E
               49, 545–553.Google Scholar $\Gamma = 0. 50$
                     
                   and Prandtl number
                        $\Gamma = 0. 50$
                     
                   and Prandtl number 
                     
                         $\mathit{Pr}= 4. 38$
                     
                  
               . J. Fluid Mech.
               676, 5–40.CrossRefGoogle Scholar
                        $\mathit{Pr}= 4. 38$
                     
                  
               . J. Fluid Mech.
               676, 5–40.CrossRefGoogle Scholar