|
[Sponsors] |
How to plot gas void fraction distribution along pipe depth at different time steps |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
April 28, 2020, 05:49 |
How to plot gas void fraction distribution along pipe depth at different time steps
|
#1 |
New Member
Shahriar Mahmud
Join Date: Mar 2016
Posts: 6
Rep Power: 10 |
Hi,
I have a vertical upward multiphase flow problem where while diesel is flowing upwards, it is desorbing gas with time and depth (desorption happening due to pressure reduction while going up). I have specified constant mass transfer coefficient in the setup. Now I want to see the gas (methane) void fraction at different depths at different time steps. So, my plot will be void fraction vs depth (or vice versa) where the it will contain different distribution curves for for different time steps. Hope someone can help. I am using ANSYS 2020 version FYI. Thanks. |
|
April 28, 2020, 16:44 |
Voidage Plot
|
#2 |
Senior Member
|
Fluent does not maintain data for each time-step. Hence, you will have to extract data at a preset frequency, say, every 5 or 10 or, if you want, every time-step. Since you want a single graph, you can either create multiple lines passing through the domain and have multiple graphs at each time-step or you can use plot commands. There are two options within plot command (this can be done only via commands), caa and car, implying circumferentially-averaged-axial and circumferentially-averaged-radial. What you need to use is caa. You have to ensure proper definition of axis in the cell zone conditions. Default axis direction is (0 0 1). If yours is different, do change it before using the command. You will also have to specify how many sections you want to use along the axis. The maximum possible is the number of cells in the axial direction. You can use a very high number and Fluent will automatically limit it to the maximum. With caa, Fluent determines a single value at one axial location, which is average of all the cells located at that axial location.
__________________
Regards, Vinerm PM to be used if and only if you do not want something to be shared publicly. PM is considered to be of the least priority. |
|
Tags |
desorption, mass transfer, multiphase flow |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
bash script for pseudo-parallel usage of reconstructPar | kwardle | OpenFOAM Post-Processing | 42 | May 8, 2024 00:17 |
[solidMechanics] Support thread for "Solid Mechanics Solvers added to OpenFOAM Extend" | bigphil | OpenFOAM CC Toolkits for Fluid-Structure Interaction | 686 | December 22, 2022 10:10 |
[Other] Contribution a new utility: refine wall layer mesh based on yPlus field | lakeat | OpenFOAM Community Contributions | 58 | December 23, 2021 03:36 |
mass flow in is not equal to mass flow out | saii | CFX | 12 | March 19, 2018 06:21 |
Floating point exception error | lpz_michele | OpenFOAM Running, Solving & CFD | 53 | October 19, 2015 03:50 |