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May 19, 2010, 13:32 |
Patching
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#1 |
New Member
Jan
Join Date: Nov 2009
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What should be done to show that the column to be used is already filled with water?
Is this what is called patching? Please explain the step by step procedure. |
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May 20, 2010, 02:17 |
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#2 |
Super Moderator
Maxime Perelli
Join Date: Mar 2009
Location: Switzerland
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patching is more usefull if you want to initialize a subdomain, ie: zone (not all the domain) with a value.
There are some options, but basically you need to specifiy the zone you will patch (for instance in gambit create a volume which describes your column, and define a separated fluid_domain on this volume). Then when you want to patch, just select this fluid domain Check help, especially Chapter 25.14.2 "Patching values in selected cells"
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In memory of my friend Hervé: CFD engineer & freerider |
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May 20, 2010, 02:28 |
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#3 |
New Member
Jan
Join Date: Nov 2009
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thanx..
So i assume you are saying if the column is fully filled with water(or say any fluid) nothing needs to be done? If u define certain material does fluent assume it to be fully filled in the domain? |
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May 20, 2010, 03:57 |
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#4 |
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Maxime Perelli
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if your domain consits in the column, and if the entire column is filled with a fluid, then you don't need to use patch.
If you are working with VOF, then set the right VOF-value in the initialization
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In memory of my friend Hervé: CFD engineer & freerider |
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May 20, 2010, 13:27 |
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#5 |
New Member
Jan
Join Date: Nov 2009
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thanx for the clarification!
i have some more trivial doubts if you would like to answer.. Is 2D rectangular mesh apt for solving gas-liquid (O2 species) mass transfer? I am using segregated-unsteady solver. Or should i go with 3D mesh and steady state solver? i posted the question a few days back.. http://www.cfd-online.com/Forums/flu...as-liq-mt.html Also now i am defining a source term for mass in liquid and the gas phase. But i am unsure of the values i should put in their.(signs and the conventions) Please elucidate! If my approach is wrong please correct me. Any help is thoroughly appreciated. |
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May 21, 2010, 02:21 |
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#6 |
Super Moderator
Maxime Perelli
Join Date: Mar 2009
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I have no experience, and no idea about mass transfer
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In memory of my friend Hervé: CFD engineer & freerider |
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May 21, 2010, 14:59 |
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#7 |
New Member
Jan
Join Date: Nov 2009
Posts: 21
Rep Power: 17 |
Anyone else please?
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May 21, 2010, 15:21 |
mass Transfer
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#8 |
Senior Member
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using source / sink terms, running mass transfer calculations can be done using any mesh any dimension (1D, 2D, 3D).
Signs / convention Linearise your source term..if negative elements exist (good for your stability), push it to the left side of the transport eqn. What is + and what is - in the source ..only you can answer. For example, lets say liquid is converted to vapor - boiling, in this case, mass transfer for the liquid is - and for the vapor ..its + ..so, designing the source/sink terms is "modeling" and its a unique challenge for CFDer's Good luck.
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May 21, 2010, 15:37 |
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#9 |
New Member
Jan
Join Date: Nov 2009
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thanx CFD toy
that was helpful... One more pls... I defined liquid as primary phase and air as secondary phase.. But when in species model i define phase properties of the two phases as mixture-template to activate species in the two phases, both primary and secondary phase turn to mixture-template. Is it ok? Since i want only liquid phase to be present in column initially. |
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May 24, 2010, 11:40 |
patching mixture
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#10 | |
Senior Member
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Any model, mixture (VOF etc), eulerian multi-fluid can be used. When you patch, you indicate the vf of a given phase and appropriately the properties are calculated. For example, vf=0.5 each phase => viscosity = alpha1*primary_phase_visc1+alpha2*secondary_phase_ visc2 etc
same applied for other properties (cp, rho, etc). If you patch liquid to the domain, only liquid properties will be present and basically, if you do not want to solve for species in liquid, then you should put a condition in your udf that if vf_liquid > 0.5 etc..no mass transfer etc. Hope this helps. Quote:
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