Reduced Input

*KEYWORD

*TITLE

fluid_2d_bullet_interaction

*CONTROL_TERMINATION

$ endtim endcyc dtmin endeng endmas

.004 200000

$===========================================================================

$ Units:

$ rho (density): Kg/m^3

$ V (velocity): m/s

$ P (pressure): Pa

$ T (temperature): K

$============================================================================

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

$ Handle output of state and restart data

*DATABASE_BINARY_D3PLOT

$ dt/cycl lcdt beam npltc

2.e-5 0

*DATABASE_BINARY_D3DUMP

$ dt/cycl lcdt beam npltc

10000

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

*INCLUDE

struct_setup.k

*DUALCESE_MODEL

dcese_setup.k

*END

$---------------------------------------------------------------------------------------------------------------------------------

*KEYWORD

*INCLUDE

struct_mesh.k

$ Time step control for structure side

*CONTROL_TIMESTEP

$# dtinit tssfac isdo tslimt dt2ms lctm erode ms1st

1.0000E-7 0.900 0 0.000 0.000 0 0

$# dt2msf dt2mslc imscl unused unused rmscl

0.000 0 0 0.000

*DEFINE_CURVE_TITLE

minimum_time

$# lcid sidr sfa sfo offa offo dattyp

2 0 1.000 1.000 0.000 0.000 0

$# a1 o1

0.000 1.000000e-07

100.000000 1.000000e-07

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

*PART

$# title

Bullet_part

$# pid secid mid eosid hgid grav adpopt tmid

2 2 1 0 0 0 0 0

*SECTION_SHELL_TITLE

bullet_motion

$# secid elform shrf nip propt qr/irid icomp setyp

2 12 1.000000 2 1 0 0 1

$# t1 t2 t3 t4 nloc marea idof edgset

1.000000 1.000000 1.000000 1.000000 0.000 0.000 0.000 0

*MAT_RIGID_TITLE

bullet_material

$# mid ro e pr n couple m alias

1 7850.0 2.10E+11 0.200 0.000 0.000 0.000

$# cmo con1 con2

1.000 5. 7.

$#lco or a1 a2 a3 v1 v2 v3

0.000 0.000 0.000 0.000 0.000 0.000

$# title

*BOUNDARY_PRESCRIBED_MOTION_RIGID_ID

$# id heading

1bullet_part

$# pid dof vad lcid sf vid death birth

2 1 0 3 1.000000 01.0000E+28 0.000

*DEFINE_CURVE

$# lcid sidr sfa sfo offa offo dattyp

3 0 1.00E-6 1.0 0.000 0.000 0

$# a1 o1

0.0 0.0

1.0 340.0

2.0 500.0

5.0 1000.0

7.5 1250.0

10.0 1500.0

1.0e+05 1500.0

*end

$---------------------------------------------------------------------------------------------------------------------------

*KEYWORD

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

*DUALCESE_CONTROL_SOLVER

$ ieqns igeom iframeref

Euler 2D fixed

*DUALCESE_CONTROL_TIMESTEP

$ iddt cfl dtint

2 0.5 0.1e-6

*DUALCESE_CONTROL_LIMITER

$ idlmt alfa beta epsr

0 2.0 1.0 0.05

*DUALCESE_INCLUDE_MODEL

dcese_mesh.k

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

$ Setup the boundary conditions for fluid

$ open BCs

*DUALCESE_BOUNDARY_NON_REFLECTIVE_SEGMENT_SET

$ ssid

$ bottom solid BCs

*DUALCESE_BOUNDARY_REFLECTIVE_SEGMENT_SET

$ ssid

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

$ Setup the initial conditions for fluid

*DUALCESE_INITIAL

$ uic vic wic rhoic pic tic hic

0.0 0.0 0.0 1.12 101325. 300.0

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

$ Setup fluid properties

*DUALCESE_PART

$ pid mid eosid FSI-type MOVMSHALG

1 7 5 IBM

*DUALCESE_MAT_001

$ mid c1 c2 prnd

7 1.458e-6 110.4 0.72

*DUALCESE_EOS_IDEAL_GAS

$ eosid cv cp t0 v0

5 717.5 1004.5

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

$ Handle output of state and restart data

*DUALCESE_D3PLOT

density

pressure

temperature

velocity

$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$

*END