Difference between revisions of "OpenFOAM/C3/Simulating-Hagen-Poiseuille-flow/English-timed"
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| 01:56 | | 01:56 | ||
− | | Type of solver used here is | + | | Type of '''solver''' used here is '''IcoFOAM'''. |
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| 02:01 | | 02:01 | ||
− | |It is a '''Transient Solver''' It is used for ''' | + | |It is a '''Transient Solver'''. It is used for '''in-compressible, laminar flow''' of Newtonian fluids. |
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| 02:08 | | 02:08 | ||
− | | '''Pressure Boundary Conditions '''used | + | | '''Pressure Boundary Conditions '''used- |
− | + | at '''Inlet: fixed Pressure''' | |
− | + | at '''Outlet: fixed Pressure''' | |
+ | at '''Walls: Zero Gradient'''. | ||
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|02:19 | |02:19 | ||
− | | '''Velocity Boundary Conditions''' used | + | | '''Velocity Boundary Conditions''' used - |
+ | at '''Inlet: pressure Inlet Velocity''' | ||
+ | at '''Outlet: zero Gradient''' | ||
+ | at '''Walls: fixed Value'''. | ||
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| 02:28 | | 02:28 | ||
− | | For executing this case, | + | | For executing this case- first, let's create the '''case directory''' in the ''''icoFoam'''' folder and give it some name. I have named it as '3dpipe'. |
− | + | ||
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| 02:41 | | 02:41 | ||
− | | To know the location of this folder, go through the tutorial on ''' | + | | To know the location of this folder, go through the tutorial on '''Lid driven cavity'''. Copy this '0' (zero), 'constant' and 'system' folders of '''lid driven cavity''' problem in the newly created folder. |
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| 02:54 | | 02:54 | ||
− | | Let's go inside the | + | | Let's go inside the '3dpipe' folder. |
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| 03:05 | | 03:05 | ||
− | | Now, let's go into the | + | | Now, let's go into the '0' folder and open the 'P' file. This is the''' pressure boundary condition''' file. |
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| 03:14 | | 03:14 | ||
− | | Note that the dimensions are in ''' | + | | Note that the dimensions are in '''meter square per second square (m2/s2)'''. |
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| 03:20 | | 03:20 | ||
− | | Hence the | + | | Hence the pressure value in '''pascals''' is divided by the density, that is, 1000 Kg/m3 (Kg per meter cube)''' and written here. |
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| 03:32 | | 03:32 | ||
− | | File containing the '''velocity boundary | + | | File containing the '''velocity boundary conditions '''is as seen. Let's open the file. We can see the '''velocity boundary conditions''' for '''inlet, outlet''' and '''fixed walls'''. |
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| 03:43 | | 03:43 | ||
− | | Let's close the file and come out of the | + | | Let's close the file and come out of the '0' folder. |
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| 03:48 | | 03:48 | ||
− | | To see the '''blocking | + | | To see the '''blocking''' strategy, let me switch back to the '''slide'''s. |
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| 03:54 | | 03:54 | ||
− | | To create a '''3D | + | | To create a '''3D''' geometry of a pipe, I have made a '''2D''' circular '''geometry '''and extruded the length in z-direction. |
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| 04:03 | | 04:03 | ||
− | | Numbering | + | | Numbering pattern is as shown. You can also see the dimensions of the mesh. |
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| 04:16 | | 04:16 | ||
− | | Let's go into the folder | + | | Let's go into the folder 'constant', and then 'polyMesh'. Let's open the 'blockMeshDict' file. You can see the '''vertices, logs, edges''' and '''boundaries''' for inlet, outlet and '''fixed wall'''. |
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| 04:37 | | 04:37 | ||
− | | Let's close the file and | + | | Let's close the file and let's come out of the '''polyMesh''' folder. |
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| 04:42 | | 04:42 | ||
− | | We see the | + | | We see the 'transportProperties' file. Let's open the file. Note the '''dynamic viscosity '''value, here, is 1 e-06. |
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Revision as of 15:57, 30 June 2016
Time | Narration |
00:02 | Hello and welcome to the spoken tutorial on Simulating Hagen-Poiseuille flow in OpenFOAM. |
00:09 | In this tutorial, we will see:
|
00:25 | To record this tutorial, I am using:
|
00:38 | To practice this tutorial, learner should have the knowledge of basic Fluid Dynamics and Hagen-Poiseuille flow |
00:46 | Here is, Hagen-Poiseuille Flow diagram. We can see the dimensions and boundaries of the pipe. |
00:52 | Viscosity of the fluid used, that is, water is given. Pressure at the inlet is 20 Pascals and at the outlet is 0 Pascals. |
01:04 | As it is an in compressible flow, only the pressure difference is of importance. |
01:10 | Formulas and Analytical Solution:
For Hagen-Poiseuille flow, Pressure drop along the pipe is: P1 minus P2 equals 32 mew U average L upon D square. |
01:25 | By substituting the values from the previous diagram, we get U average equals to 0.208 meters per second. Maximum Velocity is given as: two times the average velocity which would be 0.416 meters per second. |
01:44 | Reynolds Number for the flow is: U average into D upon nu, that comes out to be 2080. Hence, the flow is transient. |
01:56 | Type of solver used here is IcoFOAM. |
02:01 | It is a Transient Solver. It is used for in-compressible, laminar flow of Newtonian fluids. |
02:08 | Pressure Boundary Conditions used-
at Inlet: fixed Pressure at Outlet: fixed Pressure at Walls: Zero Gradient. |
02:19 | Velocity Boundary Conditions used -
at Inlet: pressure Inlet Velocity at Outlet: zero Gradient at Walls: fixed Value. |
02:28 | For executing this case- first, let's create the case directory in the 'icoFoam' folder and give it some name. I have named it as '3dpipe'. |
02:41 | To know the location of this folder, go through the tutorial on Lid driven cavity. Copy this '0' (zero), 'constant' and 'system' folders of lid driven cavity problem in the newly created folder. |
02:54 | Let's go inside the '3dpipe' folder. |
02:58 | I have already copied the folders into my 3dpipe folder and modified the files in it. |
03:05 | Now, let's go into the '0' folder and open the 'P' file. This is the pressure boundary condition file. |
03:14 | Note that the dimensions are in meter square per second square (m2/s2). |
03:20 | Hence the pressure value in pascals is divided by the density, that is, 1000 Kg/m3 (Kg per meter cube) and written here. |
03:29 | Let's close the file. |
03:32 | File containing the velocity boundary conditions is as seen. Let's open the file. We can see the velocity boundary conditions for inlet, outlet and fixed walls. |
03:43 | Let's close the file and come out of the '0' folder. |
03:48 | To see the blocking strategy, let me switch back to the slides. |
03:54 | To create a 3D geometry of a pipe, I have made a 2D circular geometry and extruded the length in z-direction. |
04:03 | Numbering pattern is as shown. You can also see the dimensions of the mesh. |
04:11 | To see the blockMeshDict file, let's minimize the slides. |
04:16 | Let's go into the folder 'constant', and then 'polyMesh'. Let's open the 'blockMeshDict' file. You can see the vertices, logs, edges and boundaries for inlet, outlet and fixed wall. |
04:37 | Let's close the file and let's come out of the polyMesh folder. |
04:42 | We see the 'transportProperties' file. Let's open the file. Note the dynamic viscosity value, here, is 1 e-06. |
04:53 | Let's close the file and come out of the 'folder ''constant' . |
04:59 | Let's go into the 'system' folder.Now, let's have a look at the 'controlDict' file. |
05:07 | The solution converges after 18 seconds therefore the final time step is kept 19.The time step has been set to 1e-03. |
05:20 | Let's close the file.Let's close the 'Home' folder. |
05:26 | Now to execute the case, we will, first, go inside the '3dpipe' folder through terminal.Let's open the terminal by pressing 'control', 'alt' and 't' key, altogether. |
05:40 | Type run and press Enter |
05:44 | Type cd (space) tutorials and press Enter |
05:50 | Type cd (space) incompressible and press Enter |
05:55 | Type cd (space) icoFoam and press Enter |
05:59 | Type cd (space) 3Dpipe and press Enter |
06:05 | Now to create the mesh, type blockMesh and press Enter. Meshing has been done. |
06:16 | To start the iterations type icoFoam and press Enter. We see the iterations are running. |
06:27 | Iterations has been done.After the iterations end type paraFoam for postprocessing the results and press Enter. It will open the" paraview". This is " paraview" |
06:41 | Let's click on Apply on the left hand side of the Object inspector menu to see the geometry. |
06:49 | Let's rotate the geometry for a better view. |
06:52 | Click on the active variable control menu and select U in the drop-down menu. |
07:01 | At the top, in VCR toolbar, click on Play button. |
07:06 | Go to Object Inspector menu, go to Display, click on Rescale to data range. |
07:16 | To view the half section, go to the toolbar named common, click on Clips go to object inspector menu properties and press Apply.Lets Zoom in |
07:35 | Let's open the color legend. |
07:38 | We can see the maximum velocity is near to the actual maximum velocityi.e 0.4 metersp/s |
07:46 | To view the graph Go to Filtersat the top Data Analysisand press Plot Over Lines. |
07:56 | Press Y axis and press Apply. |
08:00 | We can see the parabolic profile for Hagen-Poiseuille flow. |
08:05 | Let's close the graph. lets Close ParaView.And switch to the slides. |
08:12 | In this tutorial we have learned:
|
08:30 | As an assignment,
Change the geometry parameters such as length and diameter. Change the corresponding pressure ratio. and Use the fluid of different viscosity. |
08:43 | Watch the video available at the following link * It summarises the Spoken Tutorial project.If you do not have good bandwidth, you can download and watch it |
08:54 | The Spoken Tutorial Project Team Conducts workshops using spoken tutorials Gives certificates for those who pass an online test For more details, please write to contact at spoken hyphen tutorial dot org |
09:11 | Spoken Tutorial Project is a part of the Talk to a Teacher project It is supported by the National Mission on Education through ICT, MHRD, Government of India More information on this Mission is available at spoken hyphen tutorial dot org slash NMEICT hyphen Intro |