Abstract
Developing heat transfer correlations for buoyancy-driven flows and mixed convection is challenging, especially if the fluid’s Prandtl (Pr) number is not close to 1. For advanced nuclear reactor (Generation IV) designs, the downcomer plays a crucial role in normal operation and loss-of-power scenarios. The fluid-flow behavior in the downcomer can involve forced, mixed, or natural convection. Characterizing the heat transfer for these changing regimes is a serious challenge, especially in the heat transfer deterioration region. In this paper, the downcomer is simplified to heated parallel plates. The high–Pr number fluid FLiBe (a mixture of lithium fluoride and beryllium fluoride) is considered for all simulations. Direct numerical simulations using the graphics processing unit–based spectral element code NekRS are performed for a wide range of the Richardson number, from 0 to 400, at two different FLiBe Pr numbers (12 and 24). This results in an unprecedented 74 cases in total. Each case’s Nusselt number is calculated to evaluate existing heat transfer correlations.
Moreover, we propose several new modifications for cases without satisfactory choice. As a result, several novel mixed-convection heat transfer correlations have been built for high–Pr number fluids. The correlations are expressed as a function of the buoyancy number, covering several mixed-convection regimes. The Pr number effect on the Nusselt number behavior is also analyzed in detail. We also propose a novel method to evaluate the heat transfer deterioration region. Modified Reynolds-Gnielinski forced-convection correlations are defined for the laminarization region, and a free-convection correlation is used for the natural-convection-dominated region. These correlations can describe well the trend in the heat transfer–deficient region.
Acronyms
BC: | = | boundary condition |
Bo: | = | buoyancy number |
CFL: | = | Courant-Friedrichs-Lewy condition |
DNS: | = | direct numerical simulation |
DOF: | = | degree of freedom |
GPU: | = | graphics processing unit |
Gr: | = | Grashof number |
HT: | = | heat transfer |
KP-FHR: | = | Kairos Power fluoride salt–cooled high-temperature reactor |
LES: | = | large eddy simulation |
MSR: | = | molten salt reactor |
Nu: | = | Nusselt number |
OCCA: | = | Open Concurrent Compute Abstraction |
Pe: | = | Peclet number |
Pr: | = | Prandtl number |
PN: | = | polynomial order |
Ra: | = | Rayleigh number |
RANS: | = | Reynolds-averaged Navier-Stokes |
Re: | = | Reynolds number |
Ri: | = | Richardson number |
rms: | = | root mean square |
SEM: | = | spectral element method |
St: | = | Strouhal number |
THF: | = | turbulence heat flux |
TKE: | = | turbulent kinetic energy |
Nomenclature
cp0 | = | = inlet FLiBe heat capacity |
Dh | = | = hydraulic diameter () |
f | = | = dimensional heat flux |
f* | = | = nondimensional heat flux |
k0 | = | = inlet FLiBe conductivity |
LZ2 | = | = heated length |
P* | = | = nondimensional pressure |
T | = | = temperature of working fluid (FLiBe) |
T* | = | = nondimensional temperature |
T0 | = | = inlet FLiBe temperature |
t* | = | = nondimensional time |
U | = | = inlet FLiBe velocity |
Greek | = | |
ΔT | = | = temperature difference between inlet and outlet of the bed |
µo | = | = inlet FLiBe dynamic viscosity |
ρ0 | = | = inlet FLiBe density |
ρ* | = | = nondimensional density |
Disclosure Statement
No potential conflict of interest was reported by the authors.