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Numerical Heat Transfer, Part B: Fundamentals
An International Journal of Computation and Methodology
Volume 70, 2016 - Issue 1
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Original Articles

Immersed boundary method for the simulation of heat transfer and fluid flow based on vorticity–velocity formulation

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Pages 25-46 | Received 04 Sep 2015, Accepted 16 Jan 2016, Published online: 24 Jun 2016
 

ABSTRACT

The present paper, based on the vorticity–velocity formulation of the Navier–Stokes equations, proposes an immersed boundary method for the simulation of heat transfer problems within a geometrically complex domain. The desired boundary conditions are imposed by the direct modification of the initial conditions of vorticity transport and energy equations using smooth interpolations. The time advancement of both transport equations is performed by the explicit fourth-order Runge–Kutta method. One of the main objectives of this paper is to present global smooth interpolations to evaluate the local Nusselt number. The forced convection of moving and fixed circular cylinders, natural convection problem in complex geometries, and the mixed convection between two concentric cylinders—at various Reynolds numbers—are studied.

Nomenclature

A=

base circle radius

aik=

coefficients of cubic function

B=

amplitude

C=

number of undulations

d=

cylinder diameter

dk=

Euclidean distance

dik=

Euclidean distance between i, k

D=

solution domain

=

D together with boundary

Di=

inner diameter

ez=

unit vector in z direction

F=

interpolation function

g=

acceleration due to gravity

h=

convective heat transfer

i=

imaginary unit

k=

thermal conductivity

keq=

equivalent thermal conductivity

k1=

wave number in x direction

|k|2=

wave number magnitude

k=

perpendicular wave number

L=

wake length

=

linear term in Fourier space

M=

number of nodes in fluid

n=

normal unit vector

N=

total number of nodes

=

nonlinear term in Fourier space

Nc=

number of points used in the least square fit

Pr=

Prandtl number

Q=

cubic function

r=

radial direction

=

radius about point k

Rw=

radius of influence

Ra=

Rayleigh number

Re=

Reynolds number

=

nondimensional time

T=

total time

T=

temperature

u=

velocity vector

U0=

cylinder velocity

W=

weight function

α=

thermal diffusivity

β=

volume expansion coefficient

φ=

generic variable

Φ=

weight function for minimization

Γs=

solid boundary

ΓD=

boundary of domain

ω=

vorticity

ν=

kinematic viscosity

λ=

distance ratio

Ωf=

fluid region

Subscripts=
Sol=

solenoidal parameter

Superscripts=
BC=

boundary conditioned parameter

Nomenclature

A=

base circle radius

aik=

coefficients of cubic function

B=

amplitude

C=

number of undulations

d=

cylinder diameter

dk=

Euclidean distance

dik=

Euclidean distance between i, k

D=

solution domain

=

D together with boundary

Di=

inner diameter

ez=

unit vector in z direction

F=

interpolation function

g=

acceleration due to gravity

h=

convective heat transfer

i=

imaginary unit

k=

thermal conductivity

keq=

equivalent thermal conductivity

k1=

wave number in x direction

|k|2=

wave number magnitude

k=

perpendicular wave number

L=

wake length

=

linear term in Fourier space

M=

number of nodes in fluid

n=

normal unit vector

N=

total number of nodes

=

nonlinear term in Fourier space

Nc=

number of points used in the least square fit

Pr=

Prandtl number

Q=

cubic function

r=

radial direction

=

radius about point k

Rw=

radius of influence

Ra=

Rayleigh number

Re=

Reynolds number

=

nondimensional time

T=

total time

T=

temperature

u=

velocity vector

U0=

cylinder velocity

W=

weight function

α=

thermal diffusivity

β=

volume expansion coefficient

φ=

generic variable

Φ=

weight function for minimization

Γs=

solid boundary

ΓD=

boundary of domain

ω=

vorticity

ν=

kinematic viscosity

λ=

distance ratio

Ωf=

fluid region

Subscripts=
Sol=

solenoidal parameter

Superscripts=
BC=

boundary conditioned parameter

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