Reduced Input

*KEYWORD
$
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$
*DUALCESE_CONTROL_SOLVER
$ icese igeom iframe MixSelect
$ Euler axis fixed hybrid
Euler 2D fixed hybrid
*DUALCESE_CONTROL_TIMESTEP
$ iddt cfl dtint
1 .7 1.e-3
*DUALCESE_CONTROL_LIMITER
$ idlmt alfa beta epsr
2 2. 1.0 .0
$
*DUALCESE_INCLUDE_MODEL
fluid_m2h.k
$
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$
$ Setup the boundary conditions for fluid
$
*DUALCESE_BOUNDARY_NON_REFLECTIVE_SEGMENT_SET
$ ssid
5
2
3
$
$ Solid BCs (up & down)
$
*DUALCESE_BOUNDARY_REFLECTIVE_SEGMENT_SET
$*DUALCESE_BOUNDARY_AXISYMMETRIC_SEGMENT_SET
$*DUALCESE_BOUNDARY_SOLID_WALL_SEGMENT_SET
$ ssid
1
$
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$
$ Setup the initial conditions for fluid
$
*DUALCESE_INITIAL_HYBRID
$ z1 ra uic vic wic rho_1 rho_a rho_b
.9999999 0.0 0.0 0.0 0.0 1.0 1.0 1.0
$ pic tic
0.001
$
*DUALCESE_INITIAL_HYBRID_SET
$ ssid idef_func
62
$ z1 ra uic vic wic rho_1 rho_a rho_b
1.0e-8 1.0 0.0 0.0 0.0 1.0 1.0 1.0
$ pic tic
0.3
*DUALCESE_INITIAL_HYBRID_SET
$ ssid idef_func
63
$ z1 ra uic vic wic rho_1 rho_a rho_b
1.0e-8 1.0 0.0 0.0 0.0 1.0 1.0 1.0
$ pic tic
0.001
$
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$
$ Setup fluid properties
$
*DUALCESE_PART_MULTIPHASE
$ pid ReactinID EosSet_id mid FSI-type MOVMSHALG
1 3 11
*DUALCESE_EOS_SET
$ Setid inert_eosid react_eosid product_eosid
11 5 6 7
*DUALCESE_EOS_JWL
$ eosid A B R1 R2 Gama0 rho0 e0
5 100.4 -0.04 10.0 1.5 0.8 1.0 0.0
$ Cv
0.006569
$ 12.514
*DUALCESE_EOS_JWL
$ eosid A B R1 R2 Gama0 rho0 e0
$ 6 692.51 -0.045 11.3 1.13 0.8938 1.0 0.0
6 692.51 -0.045 11.3 1.13 0.8938 1.0 0.5446e-2
$ Cv
0.0066
$ 12.573
*DUALCESE_EOS_JWL
$ eosid A B R1 R2 Gama0 rho0 e0
$ 7 13.18 0.57 6.2 2.2 0.5 1.0 0.0
7 13.18 0.57 6.2 2.2 0.5 1.0 0.06141
$ Cv
0.0027
$ 5.1435
$
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*DUALCESE_REACTION_RATE_IG
$ react_id Ign aa bb xx Grow1 cc dd
3 4.0e+6 0.22 0.667 7.0 6389.32 0.667 1.0
$ 3 13.18 0.22 0.667 7.0 6389.32 0.667 1.0
$ yy Grow2 ee gg zz IGmax G1max G2min
3.0 33.71 0.667 0.667 1.0 0.02 0.8 0.8
$
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$
$ Handle output of state and restart data
$
*DUALCESE_D3PLOT
density
pressure
velocity
total_energy
internal_energy
temperature
$
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*END