CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > FLUENT

DPM reaction

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   October 29, 2002, 03:14
Default DPM reaction
  #1
Alexandre
Guest
 
Posts: n/a
Hi,

I would like to use the DPM model to model a surface reaction but I don't want to use species. The problem is burning of solid powder.

I wrote some udfs to model the change in particle diameter, mass and the mass and energy sources.

I want to use only air and dpm (oxydizer is in the solid body). Burning of powder releases air + energy.

When I use the inert dpm model putting udf as law1 I got problems.

Anyone could help?
  Reply With Quote

Old   November 9, 2002, 21:40
Default Re: DPM reaction
  #2
Jin-Wook LEE
Guest
 
Posts: n/a
Hmmmm, it seems to be impossible to set such a problem by the current Fluent version. But many problem can be overcomed by the 'NEW IDEA' or 'REASONABLE APPROXAIMATION'. For simple example, when my friend said that it was impossible to model soild sulphar reacction by Fluent because Fluent DPM combustion model is only for coal combustion. But, as you may know, it is very simple by replacing C(s) to S(s).

Let me see.

Current DPM reaction model is based on : Solid + gas_1 --> gas_2 + Q

But you want to model : Solid + gas_1 --> gas_1 + Q

So my idea to model your problem is that set the gas_1 and gas_2 as nearly same in every aspects, including properties & molecular weight and so on. And treat gas_1 and gas_2 as different gas for the Fluent setting. But when you interprete the result, treat two species as the same one.

For example, set as,

Solid(0.01kg) + gas_1(10kg) --> gas_2(10.01kg) + Q

Molecular weight of gas_1 is 10kg/kmol, and that of gas_2 is 10.01kg/kmol. Then the behavior of gas_1 and gas_2 is nearly same. Fairly small assumption and approximation is included, but this approach might work.

Please remember that this is only my idea. I never tried this approach. But I think that 'WHY NOT ?' because 'mathematically(computational aspect) it is perfect' and 'physically it is very reasonable'.

And if you have good result by using this approach, please let me know (because I should have my patent for this idea, (joke)).

Sincerely, Jinwook

  Reply With Quote

Old   November 12, 2002, 01:48
Default Re: DPM reaction
  #3
Alexandre
Guest
 
Posts: n/a
Thanks for the answer.

It is however not applicable in my case since the ratio is very different from 0.01 / 10.

I succeed (?!?) to model something using an DPM-source UDF.

Thanks anyway.
  Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
DPM - Solid reaction sega Fluent UDF and Scheme Programming 3 April 13, 2014 21:58
Segmentation fault in running alternateSteadyReactingFoam,why? NewKid OpenFOAM 18 January 20, 2011 16:55
reaction in UDF(DEFINE_VR_RATE) louiza FLUENT 3 October 13, 2010 23:59
chemical reaction - decompostition La S. Hyuck CFX 1 May 23, 2001 00:07
chemical reaction - howto Dan Sorensen Siemens 1 February 21, 2000 09:20


All times are GMT -4. The time now is 03:56.