Enabling the Out of Office Auto Response feature in Outlook (also called Vacation Mode by some) is a handy way of letting co-workers or customers know your away from the Office (vacation / holiday etc..) and not checking email regularly.
Turning on the feature is very simple both from the Outlook desktop client (outlook 07) and remotely using the Outlook Web Access client.
How to Screencast:
How-to Enable the Microsoft Outlook Out of Office Assistant (Auto Response)
Open Outlook, Click Tools, Out of Office Assistant
Click Radio Button I am currently Out of the Office, Type the Text you wish to be sent to the people who send you email (note my example text below) and Click OK
The text Out of Office will be displayed on the bottom right corner of your Outlook client as a reminder that your Out of Office Assistant is enabled and your Out of Office Auto-Reply will respond to anyone who sends you email.
I think Microsoft did this because many people (myself included) forget to turn off the Out of Office Assistant when they return to the office.
Granted, only 1 Out of Office auto-reply will be sent to each Sender however the reminder is handy.
The Out of Office Reminder also has another purpose, Disabling the Out of Office Auto-Reply Assistant!
To Disable simply Click the Down Arrow on the Out of Office Reminder and Click Turn off Out of Office auto-replies
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Top Deals of the DayFluent FAQ
From CFD-Wiki
This article contains questions and answers on the use of
products (mainly Fluent and Gambit). Please feel free to add questions and answers here!
There are two answers to this question: Fluent (the company) is a CFD software company that is now part of ANSYS Inc.
Fluent (the software package) is a popular commercial CFD package.
Gambit is a meshing software package that is typically purchased with Fluent.
The documentation provided by Fluent is actually quite good, so it is a very good place to start. Fluent also provides tutorials and documentation
site, which is open to everyone with a
(full) license. Without a full commercial license, it is possible to use the tutorials given at , or you may be able to register to use the user services center through other channels (e.g. through the university program).
There are also some good tutorials available at
and at various other places on the web (Google is a good place to start).
It is important to understand that the quality of the answer to your question depends upon how well you ask your question.
Many of the questions posted on the Fluent forum are so poorly posed that it is very difficult to understand what the poster is actually asking.
Here are some suggestions to avoid this problem:
Make sure your question is as clear, concise, and as specific as possible.
Other forum readers are unlikely to spend time trying to decipher a garbled question.
Give a clear general description of what class of problem and/or application you are working on before you start asking specific questions. This will aid other forum readers to better understand your specific questions.
Describe precisely what you have done yourself to try and solve your problem, giving examples.
Depending on your problem, you should try to include the following:
If you are asking a mesh quality related question then include some sample images of your mesh, including the boundary layer.
If you are asking a UDF question then include a copy of your existing code file as an attachment or in your post using &pre& tags to keep the code legible.
Create the image on your local machine e.g. skew_mesh.jpg
Upload the image to
Copy the link "Thumbnail for websites"
Paste the link into your post e.g. &a href=&http://img91.imageshack.us/my.php?image=pipeym8.jpg& target=&_blank&&&img src=&http://img91.imageshack.us/img91/5681/pipeym8.th.jpg& border=&0& alt=&Free Image Hosting at www.ImageShack.us& /&&/a&
If you have more than one file, zip them into a single file.
Upload the file to
Scroll down to "I don't want a collector's account right now. Just give me the download-link." and click it.
Scroll down until you see the link e.g. http://rapidshare.de/files//audio.log.html
The floating point error has been reported many times and discussed a lot. Here are some of the answers found in the Fluent Forum:
From numerical computation view point , the basic operations performed by computer are represented inside computer in what is called floating point numbers. The errors that are either because of invalid numeric computation initiated by user or limitation of machine that is used are floating point errors.
1)Invalid Operations:- Simplest example is if one uses Newton Raphson root finding method to solve f(x)=0 and for some Nth iteration if we get x = x(N) such that
derivative of function f(x), f'(x(N))=0 then formula for calculating next iterate
x(N+1) = x(N) - f(x(N))/f'(x(N)) requires division by f'(x(N)) which is zero. Here you get divide by zero type of floating point error.
2) Over or Underflow:- Another type is having data with either too large or too small magnitude called 'overflow' or 'underflow' respectively.Such data cannot be physically represented on computer for direct processing by arithmetic processing part of Processor.
3) Rounding off errors&:- While rounding off a decimal number , some significant digits are lost which cannot be recovered .
e.g. if we round off 0.1 to integer (not greater than it called 'floor' of the given no.) then it is zero. If this value if further used for computation then it may lead to several errors.
SOLVER AND ITERATION -----I think if you set shorter time step, it may be good. Or changing little Under-Relaxiation-Factors, it may be good. In my experience, I set 1/3 Under-Relaxiation-Factors as default.? -----?also lower the values of under relaxation factor and use the coupled implicit solver? -----?Try to change under-relaxation factors and if it is unsteady problem maybe time step is to large.? -----?you can improve the ratio in the solve--control--limits, maybe that can help.? -----?you will need to decrease the Courant number? -----?If you still get the error, initialize the domain with nothing to 'Compute from...' Then click 'init'. Again select the surface from which you want to compute the initial values & iterate. This should work.? -----?Another reason could be a to high courant number - that means, that the steps between two iterations are too large and the change in the results is too large as well (high residuals)?
GRID PROBLEMS -----?this error comes when I start scaling grid. in gambit, all my dimension is in mm, when in fluent i convert it in meter using buttone SCALE. after it, when i iterate, about hundred iteration, this error appeared. but when i not scale my drawing to m...and let it be as in gambit..then the iteration is success. -----?hi I think you should check your mesh grid mesh is very high. your problem solve by selection a low mesh.? -----?Your mesh is so heavy that your computers resources are not enough. try to use coarser mesh.?
BOUNDARY CONDITIONS -----?In my case I had set a wall boundary condition instead of an axis boundary condition and then FLuent refuses to calculate telling me 'floating point error'.? -----?Your Boudary Conditions do not represent real physis.? -----?wrong boundary condition definition might cause the floating point error. For example setting an internal boundary as interior? -----?Once I had the problem, simulating a 2D chamber with a symmetry BC. I set the symmetry somewhere as ?axe symmetric? and the floating point error occur? -----?check the turbulence parameter you set. reduce the turbulence intensity to less that one for first, say 50 iterations.
MULTI PROCESSOR ISSUES -----"I've had similar problems recently with floating point errors on a multi processor simulation. The solution for my problem seems to be to run on a single processor, where it runs fine....??
WRONG INITIATION ----- Initiating the case with wrong conditions may lead to floating point error when the iterations start.
In the latest Fluent release,6.3.26 these are referred as density based and pressure based solvers.
The coupled solver will solve all equations (conservation equations for mass, momentum and energy) simultaneously instead of sequentially (the equations are segregated from one another). You should use the coupled solver when the velocity and pressure are strongly coupled (high pressures and high velocities), but very long calculation times may be required when you use the coupled solver.
In the coupled solvers, the Species Diffusion Term is always included in the energy equation.
When you use the segregated solver, FLUENT allows you to specify anisotropic conductivity for solid materials
From the :
Choice of solvers depends heavily on the model being solved. The segregated solver solution is based on the pressure, while the coupled solver solution is based on density. This makes the segregated solver better at low speed flows and the coupled solver better at solving transonic / supersonic cases. I wouldn't recommend the coupled solver at any flows below Mach .4 (until the pressure based coupled solver comes out in the next release of Fluent). I've used the Segregated solver up to Mach 1.5 with great results, but the higher speed, the more mesh dependent you become (because the segregated solver tends to "smooth out" shocks), so you have to pay a lot of attention to your meshing.
The coupled solver tends to be more stable with the defaults settings. The segregated solver tends to be very sensitive to the allowable limits. When trying to get a solution with the segregated solver, DO NOT increase the turbulent viscosity ratio limit (unless you have a great reason to based on past experience or the physics of your current model truly exceeding that limit, but I've never even heard of that being realistic). Instead limit the pressure and temperature limits to reasonable limits (i.e. Plimits = Pstatic +/- (2 * dynamic pressure), and calculate the appropriate temps). You need to give the solution "room to move" while it reaches a solution, but you don't want to give it enough room where it goes out to some totally impossible numbers, and the limits help prevent this.
The problem can be caused by improper values for the boundary condition turbulence parameters.
Check the fluent manual (which is kind of more like a textbook), about modeling turbulence.
For the case of internal flow, you basically have to consider the physical state of the fluid upon entrance to your control volume.
If the fluid is coming into your volume from a fully developed turbulent pipe flow, it will have more turbulent energy than from a stagnant fluid.
Think of lots of little vortices, which mostly mix things up, and those all have kinetic energy associated).
This energy can be expressed as a nondimensional Intensity (a percentage is used).
In addition, a Length parameter is specified.
If you have pressure drop versus velocity data, you can fit the following equation through the data:
is the pressure drop and
is the velocity. The coefficients
are related to the Fluent variables for the permeability , and the pressure coefficient
is the thicknes of the medium.
what pressures at inlet and outlet should specified in natural convection?
Fluent cannot presently compute boundary layer instability and subsequent transition to turbulence using a RANS approach (ke, SST, RSM etc).
CFX has a new feature to do this, so perhaps it will be incorporated into Fluent soon as they are both owned by ANSYS.
You therefore have two options&:
1. If you know the point of transition (like on an aircraft wing) from experimental data or DNS simulations, you can impose laminar flow in some regions by meshing a separate fluid region, and enabling "laminar zone" for this region in boundary settings.
That is also useful in heat transfer cases, if for example you have turbulent flow one side of a thermal wall, and natural convection on the other side.
2. A "near-wall" turbulence approach&: Either k-omega, SST, or Low Reynolds k-E (which you have to select from the "Turbulence modelling/expert" menu), will damp turbulence near to the wall, either by empirical damping of turbulent "k" (Low Reynolds k-E) or by full solution of the omega equation on a fine enough mesh (k-omega/SST).
If you have flows in small gaps in a larger, turbulent domain, in which large lengthscales of turbulence of course could not be supported, the flow will re-laminarise in a physically sensible (although perhaps not mathematically exact) manner.
These models will also MAINTAIN laminar flow in external boundary layers, PROVIDED that you have a fine enough mesh (use the laminar mesh distribution guidelines in Fluent manual, too coarse a mesh will lead to non-physical turbulence generation in the BL).
BUT they will maintain this laminar flow and evolution of the laminar profile (in the absence of significant disturbance by separation or impingement at the wall) forever, no spontaneous instability or transition to turbulence will occur.
So check the length-based Reynolds numbers of walls where you think there will be undisturbed laminar boundaries, that there is not expected to be spontaneous transition of these BLs.
I would do it that way:
1. solve the flow for incompressible medium, without energy equation. Set the density close to the density, that you expect at the present pressure and temperature. The solution for the flow dosn't has to be completely convergent, but the residuals should be on the way down.
2. Apply energy equation and compressibility of the gas and set the present pressure with operating condition option. You might do some iteration steps as well. Sometimes they are not necessary
3. Apply the thermal BC
Rotating cylinder problem ( assume circular ), can be done easily by specifying angular velocity on the cylinder wall. As i observed no need of moving mesh for this case. you need to specify the rotation axis with respect to which your cylinder is rotating.
They limit the influence of the previous iteration over the present one. If you choose small values it may prevent oscillations in residuum developing. At the same time the solution may need more time to converge.
Keep the default values as they are given in FLUENT. You can decrease them gradually if necessary. Momentum 0.6, pressure 0.1, k 0.4, eps 0.4, mass source 1, viscosity 1.
There are not to many tutorials out there on this, probably due to the wide variety of things you can do with the UDF interface.
The documentation the Fluent provides is pretty good once you know what you are trying to do (chapter 8 of the UDF manual has examples).
UDF programming is easier if you have C programming experience, so it is advisable to learn a little C programming, then do some of the simple cases that Fluent provides, then tackle the problem you really want to solve.
The simplest way to add a UDF into Fluent is to write your UDF in the C programming language and then use Define -& User-Defined -& Functions to either interpret or compile your UDF.
It can then be loaded.
Fluent provides good documentation of the UDF interface with numerous examples, so read that before trying too much.
Yes and no.
To hook your UDF into Fluent, you'll probably have to use one of the DEFINE_* macros that Fluent provides, and this is most easily done using C.
However, you can write routines that are used in the routines that are defined with the DEFINE_* macros in other languages and then link them together.
This requires some knowledge of mixed language programming, Makefiles, the text user interface (TUI), and is not necessarily very portable.
An example using Fortran is given in Section 5.4.1 of the Fluent UDF Manual (version 6.3).
On Unix-like machines, GCC is the compiler of choice.
On Windows machines, Microsoft Visual C++ is the compiler of choice (GCC may also work on Windows- if anyone has firsthand knowledge of this, please share).
The free Express Edition of the Microsoft compiler also works.
The answer depends upon what exactly has happened.
If Fluent complains about not being able to find a compiler, then check to make sure that the compiler is properly installed.
On Windows machines, it is possible to install the Visual C++ compiler without fully setting up the command line compiler (which Fluent needs to be able to find).
During the installation process, you need to select the "register environment variables" option.
Failure to do so will likely lead to complaints about things being "not recognized as an internal or external command, operable program or batch file" or missing DLL's.
It is theoretically possible to fix this issue by setting the appropriate environment variables, but keep in mind that even when nmake can be found there still may be DLL issues.
The easy path is probably reinstallation of Visual Studio (taking special care to make sure that the command line interface is set up properly), but the reinstallation path is always perilous.
If you have long-term experience using Windows you should probably know the risks, and if you don't you should consult an expert.
If you are interpreting, keep in mind that not everything that is supported for compiled UDF's is supported for interpreted UDF's.
This is true both for the UDF interface and the C language.
If you are doing something pretty involved and it fails inexplicably, try compiling to see if that makes a difference.
There is also the possibility of coding errors.
Keep in mind that your source code gets run through the C preprocessor (to change the Fluent macros into C code), so unintended interactions are very possible.
This is a Windows/Visual Studio issue.
In order to compile your UDF, Fluent needs to know where the nmake program is located, and it currently can't find it.
If you open up a command window and enter "nmake", you should probably get the same message.
See the previous question/answer.
This commonly occurs due to a faulty operation of some kind.
For example, user-defined memory (UDM) is not allocated until initialization, so attempting to access a UDM variable before initialization can lead to a segmentation fault.
Try to isolate the cause, and then look for places where your expectation of what is available may not match reality.
Finally, keep in mind that if you do something really bad, you may need to restart Fluent before even a fixed UDF will work.
In the Fluent Launcher, there is a tab called "Environment". On this tab there is a check box "Setup Compilation Environment for UDF", which has to be checked. If this is not enough, and the compilation still fails, then the udf.bat file should be edited.
The following has to be added
set MSVC_DEFAULT=%ProgramFiles%\Microsoft Visual Studio 10.0
if exist "%MSVC_DEFAULT%\vC\vcvarsall.bat" set MSVC=%MSVC_DEFAULT%
if not "%MSVC%" == "" goto msvc_env10
msvc_env10
set MSVC_VERSION=10
call "%MSVC%\VC\vcvarsall.bat" x86
goto msvc_end
Basically it tries to run the vcvarsall.bat script.
That is it!
The questions surfacing in the discussion forum are most of the time solved with some simple steps.
As they are mentioned frequently it may be appropriate to mention the solution steps here:
Install Visual Studio. Most of the time the Visual C++ 2008 Express Edition
is recommended. On my system it even works with the new Visual Studio 2010 Professional Release Candidate .
Set the correct environment variables. Browse your way through the Windows system control to 'System'. There you will find a section 'Advanced system settings'. In the following dialog go to the 'Advanced' tabulator and click on 'Environment variables' (lower right corner). Go through the 'System variables' list and search for the 'Path' entry. Add the following to the variable: C:\Program Files (x86)\Microsoft Visual Studio 10.0\Common7\TC:\Program Files (x86)\Microsoft Visual Studio 10.0\VC\C:\Program Files\ANSYS Inc\v120\fluent\ntbin\win64. Adjust this entry to your system concerning the installation directories!
The Visual Studio entry should point to the location where 'nmake.exe' is located. If this file is missing while trying to compile your UDF you will be fine with this step. If other files are missing during the compilation find their location on you hard disc and add their directory to the PATH entry.
Run FLUENT from the Visual Studio command prompt! This is what most of the users don't know. Start the Visual Studio command prompt which comes with your Visual Studio installation. It is the familiar Windows style command prompt. Navigate to the directory, where your FLUENT files are and start FLUENT by entering 'fluent'. Don't use symbols on your desktop or start menue entries to start FLUENT. (This does not apply to 64bit systems! See this .)
This problem sometimes looks similar to the one concerning the missing 'nmake'.
Install Visual Studio. Most of the time the Visual C++ 2008 Express Edition
is recommended. On my system it even works with the new Visual Studio 2010 Professional Release Candidate .
Set the correct environment variables. Browse your way through the Windows system control to 'System'. There you will find a section 'Advanced system settings'. In the following dialog go to the 'Advanced' tabulator and click on 'Environment variables' (lower right corner). Go through the 'System variables' list and search for the 'Path' entry. Add the following to the variable: C:\Program Files (x86)\Microsoft Visual Studio 10.0\Common7\TC:\Program Files (x86)\Microsoft Visual Studio 10.0\VC\C:\Program Files\ANSYS Inc\v120\fluent\ntbin\win64. Adjust this entry to your system concerning the installation directories! The Visual Studio entry should point to the location where 'nmake' is located.
Install a Software Development Kit (SKD) for 64bit systems. This may be the difference between 32bit and 64bit systems. I have used the .NET Framework 2.0 Software Development Kit (SDK) (x64) from 2006
because it is explicitly for 64bit systems and I was not sure if more recent versions are for 64bit systems as well.
Start FLUENT from the SDK command prompt. Do not use the Visual Studio command prompt, use the SDK command prompt! Go to the directory your case is in and type 'fluent'.
There are several ways to do this (both inside and outside of Fluent), and all have merits, so there is probably no "best" way.
There are two approaches to using Fluent to generate the graphics: use Fluent to generate the movie (using Solve-&Animate-&Define...) or use Fluent to generate individual frames of an animation (by generating a hardcopy image at appropriate intervals, then assemble the animation with an external program.
Many available postprocessing tools (e.g. Tecplot) can also generate animations, so saving complete data files for use with the postprocessor can also be a path to a animation.
The answer here depends upon what you need.
For maximum accuracy, use a lossless format (e.g. PPM).
The disadvantage of the lossless formats is usually the size of the files.
For smaller file size, use a format like JPEG, which will lose some detail.
In some cases, the loss of detail will not be be easy to see, while it may be in others.
The Text User Interface (TUI) is a command-line-like interface to Fluent.
The TUI is accessed through the main Fluent (hit enter while in the main Fluent window), with a menu system and the ability to execute Scheme programs.
Fluent's documentation compares the menu system to the UNIX directory structure.
Since it is text base, you can create and modify sequences of TUI commands using a simple text editor (see journal files below).
When Fluent starts, you are in the "root" menu: press enter and you'll see something like this:
To access the plot menu, just type in "plot" and then press enter.
To bring up the available commands, press enter again:
change-fft-ref-pressure file-set/
circum-avg-axial
flamelet-curves
residuals-set/
circum-avg-radial
histogram-set/
solution-set/
plot-direction
To exit a menu, simply type "q" and press enter (the rough equivalent of "cd .." in Unix).
The TUI also understands command abreviations, so "pl/rs" is interpreted as "plot/residuals-set".
A journal file is a series of TUI commands stored in a text file.
The file can be written in a text editor or generated by Fluent as a transcript of the commands given to Fluent during your session.
A journal file generated by Fluent will include any GUI operations (in a TUI form, though).
This is quite useful if you have a series of tasks that you need to execute, as it provides a shortcut.
To record a journal file, start recording with File -& Write -& Start Journal..., perform whatever tasks you need, and then stop recording with File -& Write -& Stop Journal...
Any line beginning with a ; (semicolon) is treated as a comment.
Suppose we have a boundary named "south" that we want to set as a wall.
The command is
/define/boundary-conditions/zone-type south wall
which sets the zone "south" as a wall.
The details (moving wall, etc.) can then be accessed be executing
/define/boundary-conditions/wall south
in the text user interface.
one example:
//define/materials/delete
//define/materials/delete
//define/materials/change-create
incompressible-ideal-gas
piecewise-linear
piecewise-linear
piecewise-linear
display set-window 1
&; if window nr. 1 is the window you want to be hardcopied
//display/set/windows/scale/form
&; setting the options for the graph (colourmap)
//display/set/color-ramp
//display/set/hardcopy/color
&; setting the options for the window&
//display/set/hardcopy/driver
//display/set/hardcopy/y-res
//display/set/hardcopy/x-res
//display/set/hardcopy/inv
//display/hard
filename.tiff
//display/set/hardcopy/inv
//display/hard
filename_inv.tiff
This could be achieved by running it from journal file. The example journal file that runs two cases is given as:
file read-case-data xxx1.cas
solve dual-time-iterate yyy1
file write-case-data zzz1.cas
file read-case-data xxx2.cas
&; for discard cas dialog
solve dual-time-iterate yyy2
file write-case-data zzz2.cas
Another example:
rcd filemname.cas
wcd filemname.cas
Have a look at this discussion:
The best way to loop in a journal file (or the text user interface) is to use one of the Scheme programming language's looping constructs.
There isn't too much documentation related to fluent and its own implemented scheme language. Here it comes a document written in german that explains some of the variables and functions: []. An english version of it can be found at: [].
A list of fluent variables and functions with some comments and examples is provided here:
Any contribution to this list is welcome.
- a short debugging session of a fluent udf using gdb.
To merge two mesh files the suggested utility is tmerge. The syntax of tmerge is simple.
utility tmerge -3d file1 file2 finalfile
To join the two interior faces use:
Grid-&Fuse
from the menu with Fluent.
This could be done with the help of menu solve-&Execute Commands .
Here are two examples:
Steady Case
file/export/fug/File_grid-%n
file/export/fud/File_data-%n pressure velocity-magnitude x-velocity y-velocity z-velocity ()
Unsteady Case
file/export/fug/File_grid-%t
file/export/fud/File_data-%t pressure velocity-magnitude x-velocity y-velocity z-velocity ()
You can chose the frequency of export from the Execute Command panel.
adverse pressure gradient
Boundary Conditions
Boundary Layer
Computational Fluid Dynamics
Detached Eddy Simulation
Discrete Phase Model
Finite Difference Method
Finite Element Method
Finite Volume Method
Flux Difference Splitting
Flux Vector Splitting
Advection Upstream Splitting Method
Graphical User Interface
Large Eddy Simulation
Monotone Upstream-centered Scheme for Conservation Laws
Moving and Deforming Mesh
Probability Density Function
Quadratic Upstream Interpolation for Convective Kinematics
Reynolds Averaged Navier-Stokes
Reynolds Stress Model
Semi-Implicit Method for the Pressure-Linked Equation
Shear Stress Transport
Text User Interface
User defined function
Under Relaxation Factor
Volume Of Fluid
See the answer in the .
Before opening your file "X.dbs", Gambit looks for a file named "X.lok" to determine the status of your file.
If it finds the .lok file, you'll get the above error message (or something like it).
If you are in a multi-user environment, you should check that it is not actually already open elsewhere, but in other situations the most likely reason that there is still a X.lok file is that Gambit encountered a problem the last time X.dbs was open.
Deleting the .lok file should solve your problem.
A: It is mathematically impossible to create an all-quad mesh with an odd number of intervals on the outer edge loop. If this is inconvenient for you, you may consider a quad-dominant mesh (mostly quads, with a few triangles), or even an all-triangle mesh. Many users achieved good solutions with triangle surface meshes and prism (wedge) boundary layers.
Gambit's boundary layers allow you to generate specific semi-structured grids topologies on faces that grow out from an edge or edges.
You can specify the initial cell height, the growth rate, and a transition pattern that changes the edge-parallel interval count.
There are several default settings, which can affect the quality of boundary layers. For cases with sharp corners, normal and offset smoothing can greatly improve quality. Such smoothing is off by default because it requires significantly more computation time.
A: This is because the triangles on the tops of the pyramids have very high skewnesses which can prevent tet meshing. Consider a quad face with a 10-to-1 aspect ratio. Connect opposite corners to create diagonals. This is the "top view" of the pyramid that would be created on this face. The triangles are very highly skewed. It is recommended that your quad faces bounding a region to be tet-meshed have aspect ratios of 5-to-1 or lower.
A: Your problem is most likely that you have small gaps where the local surface mesh sizes are much larger than the gap sizes. Refining the surface meshes in those areas is likely to solve the problem.
A: For a valid conformal mesh, mesh nodes on the faces at the interface of the two parts have to be matching within
a tolerance. Then, you can either merge the nodes (using Tgrid) or fuse the zones (using Fluent). If you use Tgrid to merge the duplicate nodes, the resulting surface at the interface will have the boundary type as "wall" which should be changed to "interior" if both sides of the interface have same cell (fluid) zone. Fluent automatically converts the resulting surface after fuse to be of "interior" type if both sides of it has the same cell (fluid) zone.
Also, if you are not using Tgrid, you need to use tfilter tmerge3d to merge the meshes together before reading them into Fluent. Tgrid does the same when you load multiple mesh files at a time.
A: Try this approach - consider the meshing options in this order: Single-Block Structured, Multi-Block Structured, Multi-Block Hybrid/Mixed, Fully Unstructured.
Gambit can generate most of the cells types and topologies that Fluent can use (with the notable exception of nonconformal meshes).
Here are some guidelines/suggestions:
If you can generate a single-block structured mesh for your problem, then stop there. There is no need to go further.
If your solution is having problem around a corner (or the like), try multi-block structured mesh. If you are getting improved solution, then stop there.
If you still have problems around different part of the corner, try the unstructured mesh, with high density mesh around the corner.
Before going to a fully unstructured mesh, try making only the problem region unstructured.
If the solution is good, then stop there.
If one part of the mesh still requires special attention, then you can use Fluent's adaptive unstructured facility to refine the mesh until the solution is acceptable.
Ideally, you should still get a mesh independent solution.
It is very important to be able to control every part of your mesh so that you can get good solution everywhere. This is more difficult with unstructured meshes.
For many geometries, if you can use a structured mesh you will end up with fewer cells (this is particularly true in three dimensions).
It is a good idea to use structured-type meshes in regions that will allow it, and use unstructured meshes everywhere else.
Don't forget that Fluent can handle prismatic cells.
If you have an unstructured surface mesh, Gambit can generate a layer of prismatic cells that will resolve boundary layers without requiring a (fully) structured mesh.
A: To run Gambit in "batch" mode, prepare a journal file (e.g., "test.jou"), then use the command&: gambit test -in test.jou
"misclassified graph coedge - probably geometrical problem"
-& you can try healing the volumes
-& deleting the volume (without lower geometry), healing and uniting the faces, then build the volume again
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