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Messages 1324 - 1353 of 1972   Oldest  |  < Older  |  Newer >  |  Newest
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1324
Hi Michael, You can either modify the preconfig file with user configuration options such as USE_NUMERIC, or you can create a preprocessor that defines...
Moffat, Harry K
hkmoffat
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Oct 2, 2006
3:43 pm
1325
Hi Alejandro, I think Cantera or the python interpreter of cti files may read/write files to a windows system directory. This causes problems when the user ...
Moffat, Harry K
hkmoffat
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Oct 2, 2006
4:05 pm
1326
Hi Dan, I have fixed one aspect of this problem within the CVS code. Previously, after initialization, if the mole or mass fractions were not set in the CTI or...
Moffat, Harry K
hkmoffat
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Oct 2, 2006
10:08 pm
1327
Hi Harry and Dan, I checked out and built Cantera from CVS today, but am still getting very strange results from a simple Fortran example problem: PROGRAM...
Michael Johnson
vitalianimal
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Oct 3, 2006
8:39 pm
1328
Hi Mike, When I ran your program, adding the line double precision meanMolarMass, intEnergy_mass I obtained: 28.8507043 -84549.2746 That must mean there is an...
Moffat, Harry K
hkmoffat
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Oct 3, 2006
9:31 pm
1329
I have been trying to simulate a piston using cantera in C++. I have succeeded in creating walls etc.. I am however stuck when it comes to using the Fourier...
camilleriwilliam
camilleriwil...
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Oct 4, 2006
9:32 pm
1330
Yup, that worked. Thanks, Karl. Rick ... -- Rick Muller rpmuller@......
Rick Muller
Rick_Muller
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Oct 4, 2006
9:37 pm
1331
I was wondering where can I get a propane full mechanism from, can anyone help? thank you...
tsolomech
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Oct 4, 2006
9:37 pm
1332
Hi users, I would like to perform several calculations with free_h2_air.py and extract laminar flame velocities at different phis and temperatures. The code...
didomax77
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Oct 4, 2006
9:45 pm
1333
I've noticed some differences between the behavior of Cantera simulations generated from the GRI reaction mechanism with those from the H2O2 subset that's in...
Rick Muller
Rick_Muller
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Oct 4, 2006
9:46 pm
1334
Hi, I'm trying to get information on how to use the "solve" function that can be used to solve a steady-state problem by combined damped Newton iteration and...
amolinao88
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Oct 6, 2006
8:07 pm
1335
I did some more digging, and I have the answer to my own question. The following reaction is in GRI30, but not in the H2/O2 subset: H+O2+M<=>HO2+M...
Rick_Muller
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Oct 11, 2006
3:13 pm
1336
When we added the line below: double precision meanMolarMass, intEnergy_mass to our code, things worked fine for every call. Was unaware that subroutines...
Dan Smyth
dan_gaidin_ut
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Oct 13, 2006
5:31 pm
1337
I believe that I finally found these calls (reportParams and update). We'll try it. Dan Smyth...
Dan Smyth
dan_gaidin_ut
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Oct 13, 2006
5:34 pm
1338
The reason you need to declare it as double precision is that it begins with "m" (or "i"), so Fortran implicitly assumes it is an integer function. The best...
David Goodwin
dggoodwin
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Oct 13, 2006
11:52 pm
1339
Hello, I am having a problem with the multicomponent diffusion model in C++. I can call without problems tr->getThermalDiffCoeffs(D_t); ...
michael.oevermann
michael.oeve...
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Oct 16, 2006
12:08 pm
1340
The problem seems to be that you are calling setSpeciesFluxes with zeros for the array sizes. The third parameter should be the length of the grad_X array, and...
David Goodwin
dggoodwin
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Oct 16, 2006
4:24 pm
1341
Dera friends I am a new user of Cantera and I would like to ask you how to calculate heat of combustion and heat of reaction of H2-air mixture I look forward...
mateuszzb
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Oct 19, 2006
12:11 pm
1342
The reference documentation for Cantera has been updated. See http:// www.cantera.org/ref...
David Goodwin
dggoodwin
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Oct 20, 2006
12:01 pm
1343
Hi, I am new to cantera and although i went through the steps of installation properly, i am still unsure if i have completely installed cantera. I installed...
smenon_md
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Oct 23, 2006
1:08 pm
1344
Hello, running the flame1.py burner stabilized flame simulation I recognized that the concentration of H2O (water) is at z=0 about a third of the final...
hdoe71
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Oct 23, 2006
1:10 pm
1345
The initial mass fraction of the species at z = 0, will in general not be the same as the specified mass fraction for the flame models because the boundary ...
E David Huckaby
e.david.huckaby@...
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Oct 23, 2006
1:33 pm
1346
The non-zero product concentrations at the inlet are real, and are due to upstream diffusion of the products. This effect will be more pronounced at low...
David Goodwin
dggoodwin
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Oct 23, 2006
3:52 pm
1347
Mea culpa! It is no bug, but a very nice piece of software! I recognized the underestimated effect of back-diffusion in the calculations playing a little bit...
hdoe71
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Oct 24, 2006
8:17 pm
1348
Mea culpa! I've posted the topic on saturday morning. Meanwhile, after playing a little bit with the mass flux and pressure, I recognized that the ...
hdoe71
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Oct 24, 2006
8:22 pm
1349
There used to be a very handy pdf or ppt file that instructed one on how to build Cantera using Visual Studio .Net. I can't find that file on the...
rahunt_xyz
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Oct 25, 2006
6:26 pm
1350
Guillaume, Have you tried changing the loglevel in the equilibrate command? If loglevel is > 0, an html file will be written with debug information. If...
Josh Freeh
jkfreeh99
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Oct 25, 2006
10:32 pm
1351
Jonathan - I'm getting a similar issue with the Mixture class on a Mac (OS X 10.4.8, Matlab 2006b, Cantera from CVS): The errors are (among other things)... ...
Josh Freeh
jkfreeh99
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Oct 25, 2006
10:33 pm
1352
I have found the error. In the final state, the smoke's temperature is about 850K, and the thermo properties of condensed-phase speciesH2O(L) are defined...
Guillaume
dtcafd
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Oct 30, 2006
4:35 pm
1353
Hi Ashish I'm struggling with the same Problem as you did! When I install the progs. in the same order as you did and I get this Error Message. If you have...
omez_de
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Oct 30, 2006
4:36 pm
Messages 1324 - 1353 of 1972   Oldest  |  < Older  |  Newer >  |  Newest
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