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/MAT/B-K-EPS - ITYP=0 - Boundary Conditions Material for Flow Analysis with Turbulence

Description

This law enables to model a gas inlet condition by providing data from stagnation point. Gas is supposed to be a perfect gas. Input card is similar to /MAT/LAW11 (BOUND), but introduces two new lines to define turbulence parameters.

law11_ityp0

Format

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/MAT/B-K-EPS/mat_ID

mat_title

 

 

 

 

 

 

Ityp

 

Psh

FscaleT

 

 

 

 

 

Ityp =0 – Gas Inlet (from stagnation point data)

(1)

(2)

(3)

(4)

(5)

(6)

(7)

(8)

(9)

(10)

node_IDv

 

symbol_y

 

 

Cd

 

 

fct_IDρ

 

 

 

 

 

 

 

 

 

fct_IDp

 

 

 

 

 

 

 

Blank Format

fct_IDk

fct_IDε

 

 

 

 

cμ

Pr / Prt

 

 

fct_IDT

fct_IDQ

 

 

 

 

 

 

 

 

hmtoggle_plus1Flag Definition

Field

Contents

SI Unit Example

mat_ID

Material identifier

(Integer, maximum 10 digits)

 

mat_title

Material title

(Character, maximum 100 characters)

 

Initial stagnation density

(Real)

Reference density used in E.O.S (equation of state)

Default (Real)

Ityp

Boundary condition type (Comment 1)

(Integer)

= 0: gas inlet (from stagnation point data)

= 1: liquid inlet (from stagnation point data)

= 2: general inlet/outlet

= 3: non-reflecting boundary

 

Psh

Pressure shift (Comment 2)

(Real)

symbol_Pa

FscaleT

(Optional) Time scale factor (Comment 3)

(Real)

 

node_IDv

(Optional) Node identifier for velocity computation (Comment 3)

(Integer)

= 0:

> 0:

 

symbol_y

Perfect gas constant

(Real)

 

Cd

Discharge coefficient (Comment 5)

Default = 0.0 (Real)

 

fct_IDρ

Function identifier for stagnation density (Comment 3)

(Integer)

= 0:

> 0:

 

fct_IDp

Function identifier for stagnation pressure (Comment 3)

(Integer)

= 0:

> 0:

 

Initial stagnation pressure (Comment 3)

(Real)

symbol_Pa

Initial turbulent energy

(Real)

symbol_J

Initial turbulent dissipation

(Real)

symbol_J

fct_IDk

(Optional) Function identifier for turbulence modeling

(Integer)

= 0:

> 0:

 

fct_IDε

(Optional) Function identifier for turbulence modeling

(Integer)

= 0:

> 0:

 

csymbol_u

Turbulent viscosity coefficient

Default = 0.09  (Real)

 

Diffusion coefficient for k parameter

Default = 1.00  (Real)

 

Diffusion coefficient for E1 parameter

Default = 1.30  (Real)

 

Pr / Prt

Ratio between Laminar Prandtl number (Default 0.7) and turbulent Prandtl number (Default 0.9).

(Real)

 

fct_IDT

(Optional) Function identifier for inlet temperature (Comments 3 and 6)

(Integer)

= 0: T = Tadjacent

= n:

 

fct_IDQ

(Optional) Function identifier for inlet heat flux (Comments 3 and 6)

(Integer)

= 0: no imposed flux

= n:

 

hmtoggle_plus1Comments
1.Provided gas state from stagnation point is used to compute inlet gas state.

A set of equations including Total Enthalpy formulation, Adiabatic Law and Equation of State allows for the complete definition of the inlet state:

   

2.The PSH parameter enables shifting the output pressure which also becomes P-PSH. If using PSH=P(t=0), the output pressure will be symbol_dp, with an initial value of 0.0.
3.If no function is defined, then related quantity remains constant and set to its initial value. However, all input quantities can be defined as time dependent function using provided function identifiers. Abscissa functions can also be scaled using FscaleT parameter which leads to use f (Fscalet * t) instead of f(t).
4.Inlet velocity ratioin is used in Bernoulli theory, fixed velocity.
5.Discharge coefficient accounts for entry loss and depends on shape orifice.

mat_bound_sharpedge

6.With thermal modeling, all thermal data (, …) can be defined with /HEAT.
7.It is not possible to use this boundary material law with multi-material ALE laws 37 (BIMAT) and 51 (MULTIMAT).

See Also:

Material Compatibility