Intermediate : Turek and Hron Benchmark
Fluid velocity fringes
*KEYWORD *TITLE *BOUNDARY_SPC_SET_BIRTH_DEATH *CONTROL_IMPLICIT_DYNAMICS *CONTROL_IMPLICIT_GENERAL *CONTROL_IMPLICIT_SOLUTION *CONTROL_TERMINATION *DATABASE_BINARY_D3PLOT *DATABASE_HISTORY_NODE *DATABASE_NODOUT *DEFINE_CURVE_TITLE *DEFINE_FUNCTION *ELEMENT_SHELL *ICFD_BOUNDARY_FREESLIP *ICFD_BOUNDARY_FSI *ICFD_BOUNDARY_NONSLIP *ICFD_BOUNDARY_PRESCRIBED_VEL *ICFD_BOUNDARY_PRESCRIBED_PRE *ICFD_CONTROL_ADAPT_SIZE *ICFD_CONTROL_FSI *ICFD_CONTROL_MESH *ICFD_CONTROL_OUTPUT *ICFD_CONTROL_TIME *ICFD_DATABASE_DRAG *ICFD_DATABASE_FLUX *ICFD_MAT *ICFD_PART *ICFD_PART_VOL *ICFD_SECTION *INCLUDE *MAT_ELASTIC *MESH_BL *MESH_BL_SYM *MESH_SURFACE_ELEMENT *MESH_SURFACE_NODE *MESH_VOLUME *NODE *PARAMETER *PART *SECTION_SHELL *SET_NODE_LIST *END
$----------------------------------------------------------------------------- $ $ Example provided by Iñaki (LSTC) $ $ E-Mail: info@dynamore.de $ Web: http://www.dynamore.de $ $ Copyright, 2015 DYNAmore GmbH $ Copying for non-commercial usage allowed if $ copy bears this notice completely. $ $X------------------------------------------------------------------------------ $X $X 1. Run file as is. $X Requires LS-DYNA MPP R8.0.0 (or higher) with double precision $X $X------------------------------------------------------------------------------ $# UNITS: Dimensionless. $X------------------------------------------------------------------------------ $X *KEYWORD *TITLE ICFD The Turek and Hron Benchmark problem $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 $ $ $ PARAMETERS $ $ $ $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 *PARAMETER R T_end 12.0 R dt_plot 0.05 $ $--- Fluid $ R v_inlet 2.0 R vel_rise 2.0 Rrho_fluid 1000. R mu_fluid 1. R dt_fluid 0.001 *INCLUDE mesh.k *INCLUDE struc.k $ $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 $ $ $ ICFD CONTROL CARDS $ $ $ $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 *ICFD_CONTROL_TIME $# ttm dt &T_end &dt_fluid *ICFD_CONTROL_FSI $# owc 0 *ICFD_CONTROL_MESH $# mgsf mstrat 2dstruc 1 *ICFD_CONTROL_ADAPT_SIZE $# asize 1 *ICFD_CONTROL_OUTPUT $# mslv 4 $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 $ $ $ ICFD PARTS/ SECTION/ MATERIAL $ $ $ $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 *ICFD_SECTION $# sid 1 *ICFD_MAT $# mid flg ro vis 1 1&rho_fluid &mu_fluid *ICFD_PART $# pid secid mid 1 1 1 *ICFD_PART $# pid secid mid 2 1 1 *ICFD_PART $# pid secid mid 3 1 1 *ICFD_PART $# pid secid mid 4 1 1 *ICFD_PART $# pid secid mid 5 1 1 *ICFD_PART $# pid secid mid 6 1 1 *ICFD_PART_VOL $# pid secid mid 10 1 1 $# spid1 spid2 spid3 spid4 spid5 spid6 1 2 3 4 5 6 $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 $ $ $ ICFD BOUNDARY/INITIAL CONDITIONS $ $ $ $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 *ICFD_BOUNDARY_PRESCRIBED_VEL $# pid dof vad lcid 1 1 1 1 *ICFD_BOUNDARY_PRESCRIBED_VEL $# pid dof vad lcid 1 2 1 2 *ICFD_BOUNDARY_PRESCRIBED_PRE $# pid lcid sf death birth 2 2 *ICFD_BOUNDARY_NONSLIP $# pid 3 *ICFD_BOUNDARY_NONSLIP $# pid 4 *ICFD_BOUNDARY_FSI $# pid 4 *ICFD_BOUNDARY_NONSLIP $# pid 5 *ICFD_BOUNDARY_NONSLIP $# pid 6 *ICFD_BOUNDARY_FSI $# pid 6 *DEFINE_FUNCTION $# dfid 1 $# function float h(float y, float time) { float fac,trise; trise = vel_rise; fac = v_inlet; if(time<=trise) return 1.5*4.0/0.1681*y*(0.41-y)*fac*0.5*(1-cos(time*pi/2)); return 1.5*4.0/0.1681*y*(0.41-y)*fac; } *DEFINE_CURVE_TITLE Pressure outlet $# lcid sidr sfa sfo offa offo dattyp 2 $# a1 o1 0.0 0.0 10000.0 0.0 $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 $ $ $ ICFD MESH KEYWORDS $ $ $ $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 *MESH_VOLUME $# volid 10 $# pid1 pid2 pid3 pid4 pid5 pid6 1 2 3 4 5 6 *MESH_BL $# pid nelth 3 1 *MESH_BL $# pid nelth 4 1 *MESH_BL $# pid nelth 5 1 *MESH_BL_SYM $# pid 1 *MESH_BL_SYM $# pid 2 $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 $ $ $ DATABASE (OUTPUT) $ $ $ $---+----1----+----2----+----3----+----4----+----5----+----6----+----7----+----8 *ICFD_DATABASE_FLUX $# pid 1 *ICFD_DATABASE_FLUX $# pid 2 *ICFD_DATABASE_DRAG $# pid 4 *ICFD_DATABASE_DRAG $# pid 5 *ICFD_DATABASE_DRAG $# pid 6 *DATABASE_BINARY_D3PLOT &dt_plot *END
An elastic cantilever plate is clamped behind a rigid cylinder under laminar flow circumstances. Three different test cases named FSI1, FSI2 and FSI3 are provided. This is a purely numerical benchmark problem where codes can be compared to one another but no experimental results exist.
References :
[1] S. Turek and J. Hron, Proposal for Numerical Benchmarking of Fluid-Structure Interaction between an Elastic Object and Laminar Incompressible Flow, pp. 371–385. Berlin, Heidelberg: Springer Berlin Heidelberg, 2006.
[2] S. Turek, J. Hron, M. Razzaq, H. Wobker, and M. Schäfer, Numerical Benchmarking of Fluid-Structure Interaction: A Comparison of Different Discretization and Solution Approaches, pp. 413–424. Berlin, Heidelberg: Springer Berlin Heidelberg, 2010.
[3] S. Turek, J. Hron, M. Mádlík, M. Razzaq, H. Wobker, and J. F. Acker, Numerical Simulation and Benchmarking of a Monolithic Multigrid Solver for Fluid-Structure Interaction Problems with Application to Hemodynamics, pp. 193–220. Berlin, Heidelberg: Springer Berlin Heidelberg, 2010.