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Numerical Heat Transfer, Part B: Fundamentals
An International Journal of Computation and Methodology
Volume 69, 2016 - Issue 5
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Original Articles

Performance analyses of the IDEAL algorithm combined with the fuzzy control method for 3D incompressible fluid flow and heat transfer problems

, , , , &
Pages 432-446 | Received 08 Sep 2015, Accepted 24 Nov 2015, Published online: 02 May 2016
 

ABSTRACT

IDEAL proposed by the present author is an efficient segregated algorithm for solving the incompressible fluid flow and heat transfer problems. However, its convergence rate is greatly influenced by the under-relaxation factor. The convergence rate under an optimum under-relaxation factor is dozens of times quicker than that under the most unfavorable under-relaxation factor. To lessen the influence, the IDEAL algorithm combined with a fuzz control method, called IDEAL+FC, is introduced to automatically regulate the values of the under-relaxation factor for accelerating the iteration convergence. Finally, it is demonstrated that IDEAL+FC is superior to IDEAL in terms of convergence rate and robustness. The rapid convergence rate can be achieved by IDEAL+FC even if the initial under-relaxation factor is the most unfavorable value.

Nomenclature

a=

coefficient in the discretized equation

b=

constant term in the discretized equation

Cp=

specific heat, J · kg−1 · K−1

d=

maximum residual

D=

tube outer diameter, m

e=

ratio of the residuals between two successive iteration levels

f=

friction factor

p=

pressure, Pa

R=

fuzzy relation

Re=

Reynolds number

Su,Sv,Sw ST=

source term introduced by the grid nonorthogonality

T=

temperature, K

u, v, w=

velocity components in x, y, z directions, m · s−1

U, V, W=

contravariant velocity components in ξ, η, ζ directions, m · s−1

y=

twist ratio

α=

under-relaxation factor

ϕ=

general variable

η=

dynamic viscosity, Pa · s

λ=

thermal conductivity, W · m−1 · K−1

μ=

membership function

ν=

kinematic viscosity, m2 · s−1

θ=

inclination angle, °

ρ=

density, kg · m−3

ξ, η, ζ=

nonorthogonal curvilinear coordinates

Δα=

change of the under-relaxation factor

Subscript=
e=

referring to the ratio of the residuals

e, w, n, s, t, b=

grid interface

n=

current iteration level

n-1=

previous iteration level

nb=

neighboring grid points

P=

main grid point

T=

referring to temperature

u, v, w=

referring to u, v, w velocities

Δα=

referring to the change of the under-relaxation factor

Superscript=
NB, NS=

negative big, negative small

PB, PM, PS=

positive big, positive medium, positive small

T=

referring to temperature

u, v, w=

referring to u, v, w velocities

0=

previous iteration

Nomenclature

a=

coefficient in the discretized equation

b=

constant term in the discretized equation

Cp=

specific heat, J · kg−1 · K−1

d=

maximum residual

D=

tube outer diameter, m

e=

ratio of the residuals between two successive iteration levels

f=

friction factor

p=

pressure, Pa

R=

fuzzy relation

Re=

Reynolds number

Su,Sv,Sw ST=

source term introduced by the grid nonorthogonality

T=

temperature, K

u, v, w=

velocity components in x, y, z directions, m · s−1

U, V, W=

contravariant velocity components in ξ, η, ζ directions, m · s−1

y=

twist ratio

α=

under-relaxation factor

ϕ=

general variable

η=

dynamic viscosity, Pa · s

λ=

thermal conductivity, W · m−1 · K−1

μ=

membership function

ν=

kinematic viscosity, m2 · s−1

θ=

inclination angle, °

ρ=

density, kg · m−3

ξ, η, ζ=

nonorthogonal curvilinear coordinates

Δα=

change of the under-relaxation factor

Subscript=
e=

referring to the ratio of the residuals

e, w, n, s, t, b=

grid interface

n=

current iteration level

n-1=

previous iteration level

nb=

neighboring grid points

P=

main grid point

T=

referring to temperature

u, v, w=

referring to u, v, w velocities

Δα=

referring to the change of the under-relaxation factor

Superscript=
NB, NS=

negative big, negative small

PB, PM, PS=

positive big, positive medium, positive small

T=

referring to temperature

u, v, w=

referring to u, v, w velocities

0=

previous iteration

Acknowledgments

This work was supported by the National Natural Science Foundation of China (51476054) and the Program for New Century Excellent Talents in University (NCET-13-0792) and the BIPT-POPME-2015.

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