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I.K. Marchevsky, V.V. Puzikova

22

ISSN 1812-3368. Вестник МГТУ им. Н.Э. Баумана. Сер. Естественные науки. 2017. № 5

   

   

  

τ

.

t

t

xy

u v

y x

(5)

Here

t

xx

and

t

yy

are normal Reynolds or subgrid stresses and

t

xy

is shear Reynolds

or subgrid stress. In cases of algebraic turbulence models or models with one

differential equation the turbulent kinetic energy is assumed to be zero and only eddy

viscosity value is computed. For example, in the Smagorinsky model [8] the eddy

viscosity is defined by the following formula:

2

2

2

2

= ( ) 2

.

t

S

u

v

u v

C

x

y

y x

       

 

 

    

 

    

(6)

Here

S

C

is the empirical constant (the Smagorinsky constant). Choice of the

S

C

value

depends on the numerical method used to solve the problem, because at LES approach

the accuracy of large-scale vortex structures resolution depends not only on the mesh,

but also on numerical method properties, in particular, numerical dissipation. If the

numerical dissipation is large, it is necessary to choose smaller values of

,

S

C

and if

numerical dissipation is small, the

S

C

value should be chosen larger.

For EVM with differential equations the governing equations, initial and

boundary conditions are given by the turbulence model. In the most general way, they

may be written as the following:

   



         



  

  

0

1 2 3

4

( ) = Prod Dis

[(

) ] Add;

( , 0) = ( ),

|

= ,

| = ,

= 0.

ib

K

t

v

r

r

n

(7)

Here

Prod

is the production term which describes the generation of Reynolds or

subgrid stresses;

Dis

is the destruction term;

Add

is the additional term;

and

are given by the particular turbulence model (Table 2).

Table 2

Itemization of symbols in (7) and rules for

t

computation for some turbulence

models [3]

Term

Spalart —

Allmaras

 

k



k



k

SST

k

k

k

Add

0

0

0

0

0

0

1

(1 )

k

F D

Prod

P

P

1.44

P

k

P

5

9

P

k

P

1

(0.44 0.11 )

t

F P

Dis

D

3/2

turb

k

l

2

1.92

k

3/2

turb

k

l

2

3

40

3/2

/

turb

k l

1

0.0828 0.0078

F

t

/1.3

t

/ 2

t

/ 2

t

 

1

(1 0.5 )

t

F

1

(0.856 0.356 )

t

F

t

1

f

2

0.09 /

k

/

k

1

0.31 /

k G