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

URGENT!!!!!!!!!!!!total numebr of particles

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   February 20, 2006, 10:05
Default URGENT!!!!!!!!!!!!total numebr of particles
  #1
antonietta
Guest
 
Posts: n/a
hi, I'd like to calculate the numebr of particles which are injected from a surface, when I apply the discrete phase model defining an ejection released fropm a specific surface. I mean, if I have for example 8 tracked stream, does it mean that I have 8 particles? And in this case, 8 particle for each stream or in total? thanks
  Reply With Quote

Old   February 20, 2006, 10:19
Default Re: URGENT!!!!!!!!!!!!total numebr of particles
  #2
HS
Guest
 
Posts: n/a
In the discrete phase model your particles are represented by parcels. A parcel will appear as a "particle" if you plot it in the domain, but is really a representative for a number (or even a fraction) of real particles. This is depending on the total mass flow-rate and initial diameter/density you choose. You can color your particle traces by the number of particles per parcel while post-processing. If you are doing unsteady particle tracking (or using a spray breakup model), FLUENT will inject one parcel per injection stream and timestep. If doing steady-state simulations, a number of parcels equal to the number of injection streams will be followed throughout the domain. Note that stochastic tracking may alter the number of computational parcels (but not the number of real particles).
  Reply With Quote

Old   February 20, 2006, 13:04
Default Evaporataion in DPM
  #3
yooceframandi
Guest
 
Posts: n/a
Dear friend;

I use DPM but i have not "evaporated" fate in report window,while the temperature of system is more than droplet vaporization temperature.

and the diameter of droplets is reducing!!!

what is the problem?
  Reply With Quote

Old   February 21, 2006, 03:15
Default Re: Evaporataion in DPM
  #4
HS
Guest
 
Posts: n/a
Most probably, there is no problem. Once again, remember that it is not individual droplets you track in the domain but computational parcels. Thus, one parcel could represent many droplets. If vaporization is going on, FLUENT will calculate the mass loss due to vaporization according to the heat- and mass transfer laws used and thus the diameters will decrease. However, a single parcel can only represent droplets of a single set of properties, so all diameters will decrease the same. This means that the evaporation fate will only happen to your parcel once all droplets have evaporated, which they will of course do at exactly the same instant in time.

To summarize: You track a parcel that represent many droplets, but all with the same properties. Just as if it was a single droplet, the diameter will decrease during evaporation. The fate "evaporated" in the report summary only applies to parcels that have been fully evaporated within the domain.

/HS
  Reply With Quote

Old   February 21, 2006, 04:21
Default Re: Evaporataion in DPM
  #5
yooceframandi
Guest
 
Posts: n/a
DEAR HS;

thanks for useful help.

can i patch a mass of droplet in domail aithout injection?

and can i define a particle with solid content? i mean: solid+liquid (wet-solid).

i mean can i use combusting particle?

regards
  Reply With Quote

Old   February 21, 2006, 07:11
Default Re: Evaporataion in DPM
  #6
HS
Guest
 
Posts: n/a
* can i patch a mass of droplet in domail aithout injection?

I am no expert but I don't think this is possible with the discrete phase model in FLUENT. You would have to create injections and modify them through UDFs instead I guess.

* and can i define a particle with solid content? i mean: solid+liquid (wet-solid).

Yes that is possible in the Materials panel for your discrete phase species.

* i mean can i use combusting particle?

Yes. There are even pre-defined particle types that are suited for combustion and also wet combustion. Look in the manual for more info on this!

Good luck!

/Henrik

  Reply With Quote

Old   February 21, 2006, 08:01
Default Re: Evaporataion in DPM
  #7
MANOJKUMAR
Guest
 
Posts: n/a
Hello Sir, I asked one question what is the composition of the LDO and how to create PDF file for that. In my case 350 mm is dia of air and injection is given at center of this hole. So how to find the velocity of this air. I give velocity of injection is 100m/s and dia is 0.3 and flow rate is 0.0059 kg/sec. Any method to find this calculation. Thanking u

  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
how to determine the number of particles injected. welch FLUENT 2 January 18, 2024 04:08
Particles are not hitting the wall CedricVH OpenFOAM Bugs 23 May 19, 2016 20:29
trying to simulate two-phase jet flow with particles in surface injection ajkratos FLUENT 5 March 3, 2015 21:33
particles model ati_ros61 FLOW-3D 3 December 6, 2009 16:03
effect of ventilation on particles problem Jules FLUENT 0 June 10, 2002 14:41


All times are GMT -4. The time now is 07:54.