Group FIDAP

Group Description
Fluid dynamics, finite element matrices from Yousef Saad (SPARSKIT2 collection).
Names converted to Univ. of Florida naming convention (.mat changed to
.rua).

c------------------------------------------------------------------------c
c                           FIDAP MATRICES:                              c
c------------------------------------------------------------------------c
c  These  matrices are extracted from the examples provided by Fidap     c
c  The matrices are stored in Harwell-Boeing format                      c
c  For the physic of the problems, see detailed description in Fidap     c
c                                                                        c
c  Matrices extracted by:     Abdelkader Baggag  (baggag at cs.umn.edu)
c  with the help of Barry Rackner (bnr at msc.edu)
c									 c
c  For help or more informations, contact:				 c
c           Prof. Yousef Saad  (saad at cs.umn.edu)
c                                                                        c
c------------------------------------------------------------------------c
c            GENERAL INFORMATION ON THE PROBLEMS                         c
c------------------------------------------------------------------------c
c The elements used are Q2 for the velocity and P1 for the pressure      c
c for 2D problems and the so-called Brick elements (8 nodes) for 3D      c
c problems  (unless specified)					    	 c
c									 c
c We are solving the fully coupled Navier-Stokes Equations (unless       c
c specified), including the Temperature Equation for the Heat Transfer   c
c Problems and the Chemical Convection-Diffusion Equations for different c
c species                                                                c
c The Mesh is regular structured but not uniform                         c
c									 c
c                 | Kmax  				                 c
c		  |							 c
c                 |							 c
c  	 	  | 							 c
c		  |__________________ Jmax  		                 c
c                / 							 c
c               /     							 c
c	       /							 c
c             /								 c
c            / Imax							 c	
c------------------------------------------------------------------------c
c     This version is dated: June 09, 1994                               c
c------------------------------------------------------------------------c
c  ex1.mat  : 2D Transient Poiseuille Flow in a Pipe
c             Reynolds = 1.0
c             Imax = 9, Jmax = 5
c
c  ex2.mat  : 3D Steady Couette Flow
c             Reynolds = 1.0
c             Imax = 9, Jmax = 3
c
c  ex3.mat  : 2D Flow Past a Cylinder in Freestream
c             Reynolds = 40.0
c             Imax = 19, Jmax = 9
c
c  ex4.mat  : 2D Hamel Flow
c             Reynolds = 0.0
c             Imax = 9, Jmax = 5
c
c  ex5.mat  : Non-newtonian Flow in a Channel (Power Law Poiseuille Flow)
c             Reynolds = Power Law
c             
c  ex6.mat  : 2D Die Swell Problem
c             Capillary number = 1.0
c             Imax = 43, Jmax = 15
c
c  ex7.mat  : 2D natural Convection in a Square Enclosure
c             Rayleigh = 1000
c             Imax = 9, Jmax = 9
c
c  ex8.mat  : Developing Flow, Vertical Channel, Angle = 0.0
c             Rayleigh = 1000
c             Imax = 5, Jmax = 13
c
c  ex9.mat  : 2D Jet Impingement Cooling
c             Reynolds = 0.0 ; (Jet) = 300
c             Imax = 21, Jmax = 89
c
c  ex10.mat : 2D Flow over Multisteps in a Channel
c             Reynolds = 100 ; Prandtl = 0.6896
c             Imax = 13, Jmax = 5
c
c  ex11.mat : 3D Steady Flow; Cylinder and Flat Plate Heat Exchanger
c             Imax = 21; Jmax = 7; Kmax = 5 
c             Density = 1.0; Viscosity = 0.025; SpecifiHeat = 1.0; 
c             Conductivity = 3.760e-3
c
c  ex12.mat : 2D Flow Stokes Flow in Lid-Driven Wedge (28.5 Degree Angle)
c             Imax = 7; Jmax = 5
c             Density = 1.0; Viscosity = 5.0 
c
c  ex13.mat : Axisymmetric Flow through a Poppet Valve
c             Imax = 12; Jmax = 13
c             Steady, Newtonian, Axi-Symmetric, Isothermal, Nonlinear
c             Density = 3.122e-2; Viscosity = 6.77e-4
c
c  ex14.mat : 2D Isothermal Seepage Flow
c             Imax = 23; Jmax = 23
c             Density = 1000.0; Permeability = 100; Porosity = 0.5
c
c  ex15.mat : 2D Spin up of a Liquid in an Annulus                           
c             Imax = 7; Jmax = 7
c             Transient, Nonlinear, Newtonian, Cylindrical
c             Density = 1.0; Viscosity = 0.02
c
c  ex16.mat : 3D Flow Past a Heated Obstacle
c             Imax = 13; Jmax = 13; Kmax = 9
c             Nonlinear
c             Density = 1.0; Viscosity = 0.1; Conductivity = 0.1
c
c  ex17.mat : 3D Flow in a Rectangular Duct Around a 120 Degree Bend
c             Imax = 5; Jmax = 3; Kmax = 3
c             Nonlinear, Turbulent
c             Density = 1.74e-3; Viscosity = 1.84e-4  1.0 (Mixing)
c
c  ex18.mat : 2D Turbulent Flow Over a backward-Facing Step
c	      Imax = 5; Jmax = 9
c             Nonlinear, Turbulent (k-epsilon)
c             Density = 1.0; Viscosity = 2.2222e-5
c             
c  ex19.mat : 2D Developing Pipe Flow, Turbulent k-epsilon
c             Imax = 5; Jmax = 5
c             Nonlinear, Axi-Symmetric, Turbulent
c             Density = 1.0; Viscosity = 1.0e-5
c
c  ex20.mat : 2D Attenuation of a Surface Disturbance
c             Imax = 7; Jmax = 5
c             Transient, Nonlinear, free
c             Density = 1.0; Viscosity = 0.1
c
c  ex21.mat : 2D Growth of a Drop from a Nozzle
c             Imax = 5; Jmax = 3
c             Transient, Nonlinear, free, axi-symmetric
c             Density = 1.0; Viscosity = 1.0
c
c  ex22.mat : 2D Slot Coater
c             Imax = 6; Jmax = 3
c             Steady, Nonlinear, free
c             Density = 1.0; Viscosity = 0.1; SurfaceTension = 1.0
c
c  ex23.mat : 2D Fountain Flow in Injection Molding
c             Imax = 4; Jmax = 3
c             Nonlinear, Free
c             Density = 1.0; Viscosity = 2706.0
c
c  ex24.mat : 2D Unsymmetric Forward Roll Coating
c             Imax = 5; Jmax = 3
c             Nonlinear, Free
c             Viscosity = 1.0; Density = 1.0; SurfaceTension = 10
c
c  ex25.mat : 2D Drop Growth Resulting from a Moving Piston
c             Imax = 3; Jmax = 3
c             Transient, Nonlinear, Free, AxiSymmetric
c             Density = 1.0; Viscosity = 1.0; SurfaceTension = 10.0
c
c  ex26.mat : 2D surface Tension Gradient Driven Thermal Convection
c             Imax = 3; Jmax = 3
c             Steady, Nonlinear, Free, Weakly
c             Density = 1.0; Viscosity = 1.0; Surface Tension = variable;
c             Conductivity = 0.565
c
c  ex27.mat : 2D Crystal Growth Simulation
c             Imax = 3; Jmax = 3
c             Axisymmetric, Transient, Nonlinear, Free, Strongly     
c             Density = 1.0; Viscosity = 1.0; Conductivity = 0.051282
c
c  ex28.mat : 2D Two Merging Liquids with one External and an interior Interface
c             Imax = 7; Jmax = 6
c             Nonlinear, Steady, Free
c             Viscosity = 0.50; density = 
c
c  ex29.mat : 2D Turbulent flow in AxiSymmetric U-Bend: k-epsilon
c             Imax = 5; Jmax = 3
c             Nonlinear, Turbulent, Axisymmetric
c             Density = 1.0; Viscosity = 1.0e-5
c
c  ex30.mat : 3D Crystal Growth: Bridgman Technique
c             Imax = 11; Jmax = 7; Kmax = 3; MaxPoints = 999
c             Nonlinear, Strongly
c             Density = 1.0; Conductivity = 0.6; SpecifiHeat = 1.0 (Solid region)
c             density = 306; Viscosity = 4; Enthalpy = 4; Conductivity = 4 (Fluid Region)
c
c  ex31.mat : 2D Dilute Species Deposition on a Titled heated Plate
c             Imax = 7; Jmax = 3
c             Nonlinear, Weakly
c             Density = 1.0; Viscosity = 0.16; Conductivity = variable; Diffusivity = 0.15
c
c  ex32.mat : 2D radiation Heat Transfer in an Open Channel
c             Imax = 5; Jmax = 7
c             Nonlinear, weakly
c             Density = 1.3698; Conductivity = variable; Emissivity = variable
c
c  ex33.mat : 2D Radiation Heat Transfer in a Square Cavity
c             Imax = 7; Jmax = 7
c             Ra = 1.6e7; Rad = 5.88; Density = 1.3698; SpecifiHeat = 0.7300
c             Emissivity = 0.45--0.88
c             Nonlinear, Strongly 
c
c  ex34.mat : 2D Conduction Melting
c             Imax = 3; Jmax = 3
c             Transient, Nonlinear, Strongly
c             Density = 1.0; Conductivity = 0.1; Diffusivity = 1.0 (NonIsotropic)
c             Viscosity and Enthalpy definec on curves
c
c  ex35.mat : 2D Turbulent Flow in a Heated Channel
c             Imax = 41; Jmax = 7
c             Reynolds = 25960; k-epsilon
c             Nonlinear, Turbulent
c
c  ex36.mat : 2D Chemical Vapor Deposition in a Horizontal Reactor
c             Imax = 7; Jmax = 3
c             Nonlinear, Strongly 
c             Density = variable; Viscosity = variable defined on a curve
c             All the other properties are variable and defined on curves
c
c  ex37.mat : 3D Flow of Plastic in a profile extrusion Die
c             Imax = 7; Jmax = 9; Kmax = 5
c             Nonlinear, NonNewtonian, Weakly
c             Viscosity = variable; Conductivity = 1.0 
c
c  ex38.mat : Multiple Species Reaction A + 2B -----> 2C + D
c             Imax = 5; Jmax = 5
c             axisymmetric, nonlinear, weakly
c             all the properties are variable
c
c  ex39.mat : 3D Mixing Tank 2 Blades
c             Imax = 9; Jmax = 5; Kmax =7
c             Nonlinear
c             Density = 1.0; Viscosity = 1.0
c
c  ex40.mat : 3D Die Swell Problem on a Square Die
c             Imax = 5; Jmax = 11; Kmax = 5
c             Re = 1.0; Ca = inf
c             Viscosity = 1.0; Density = 0.5
c
c-----------------------------------------------------------------------
c-----------------------------------------------------------------------
Displaying collection matrices 1 - 20 of 35 in total
Id Name Group Rows Cols Nonzeros Kind Date Download File
436 ex5 FIDAP 27 27 279 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
406 ex1 FIDAP 216 216 4,317 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
429 ex32 FIDAP 1,159 1,159 11,047 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
418 ex21 FIDAP 656 656 18,964 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
430 ex33 FIDAP 1,733 1,733 22,189 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
419 ex22 FIDAP 839 839 22,460 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
426 ex29 FIDAP 2,870 2,870 23,754 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
422 ex25 FIDAP 848 848 24,369 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
416 ex2 FIDAP 441 441 26,839 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
434 ex4 FIDAP 1,601 1,601 31,849 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
424 ex27 FIDAP 974 974 37,652 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
420 ex23 FIDAP 1,409 1,409 42,760 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
438 ex7 FIDAP 1,633 1,633 46,626 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
421 ex24 FIDAP 2,283 2,283 47,901 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
437 ex6 FIDAP 1,651 1,651 49,062 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
427 ex3 FIDAP 1,821 1,821 52,685 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
432 ex36 FIDAP 3,079 3,079 53,099 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
407 ex10 FIDAP 2,410 2,410 54,840 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
408 ex10hs FIDAP 2,548 2,548 57,308 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market
412 ex14 FIDAP 3,251 3,251 65,875 Computational Fluid Dynamics Problem 1994 MATLAB Rutherford Boeing Matrix Market