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

Multi-step combustion mechanism

Register Blogs Community New Posts Updated Threads Search

Like Tree6Likes

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   March 19, 2015, 05:38
Smile
  #21
Member
 
Howar
Join Date: Mar 2015
Posts: 53
Rep Power: 11
Howard is on a distinguished road
Quote:
Originally Posted by wenxu View Post
Hi,Howar,

That's not difficult to simulate gas mixture combustion with flameletFoam. If you want use SLF, then you can keep combustion model not changed. Just generate a new flamelet library with your gas mixtures instead of CH4 with the released version. Flamelet equations can be solved with cantera which in the released version or FlameMaster.

regards,
wenxu
Sorry, what is SLF?
Howard is offline   Reply With Quote

Old   April 8, 2015, 16:57
Default
  #22
New Member
 
Sihan Jin
Join Date: Apr 2015
Posts: 2
Rep Power: 0
jsh331 is on a distinguished road
Quote:
Originally Posted by wenxu View Post
Now, i know how to manipulate multi-step reactions. But as far as i know, there is no multi-step combustion models built in OF.
  1. laminar
  2. PaSR---derived from laminar, can be used in turbulence.
  3. diffusion,FSD,infinitelyFastChemistry, these three all derived from singleStepCombustion
If i want to implement muti-step reaction (combustion model which not only consider chemistry time but also turbulence mixing time), what should i derived the class? That's mean which class should i derived from?
Now i have compiled the EBU model succeed and i design i case to use this model. (i almost substitute the EBU model for the chemistry class. that's means when laminar calss calculate the reaction Rate R(Yi), then it will use the new class EBU to calculate the R(Yi). ) ANY ideas can give me? Thank you!!!!



best Regards,
wen
Hi Wen
Why do you say that Laminar and PaSR combustion models are not for multi-step combustion? Actually I have a problem simulating constant volume combustion using reactingFoam. My geometry is a box with ignition at the center and a 4 step mechanism of CH4 & air is implemented. It's filled with CH4 and air initially. Turbulence model is k-epsilon and I'm testing laminar and PaSR combustion model. It turns out that laminar works pretty good but PaSR doesn't work as what I expect. So could you pls help me figure out my problem?

Sihan
jsh331 is offline   Reply With Quote

Old   April 10, 2015, 04:45
Default
  #23
New Member
 
Ali Kadar
Join Date: Oct 2014
Location: Delft
Posts: 25
Rep Power: 11
flowAlways is on a distinguished road
Hi Sehan,
You are correct, infact the Chalmers PaSR model is very similar to the successful EDC approach by Magnussen. It takes into account both the turbulent time scale and the chemical time scale while determining the reaction rate. The chemical timescale is determined by solving the reaction system’s ODEs fully coupled, and finding the characteristic time for that system. So it is meant to take into account a multi-step reaction mechanism.
You can find more about PaSR here
http://www.tfd.chalmers.se/~valeri/book-chapt7.pdf
http://powerlab.fsb.hr/ped/kturbo/op...olmPhD2008.pdf
http://web.ist.utl.pt/jose.neves.rod...2011-FINAL.pdf

In the PaSR model the reaction rate is determined as
reactionRate_PaSR = kappa*reactionRate_laminar
kappa ~ 1 when t_chemical >> t_mix so your results with laminar and PaSR will be similar only when the rate is kinetics controlled and not mixing controlled(that is when the flow is laminar and reactions are slow).

what is your reaction mechanism? Can you maybe send your case to me ?
__________________
A good solution is one which does justice to the inner nature of the problem- Cornelius Lanczos in a letter to Albert Einstein on March 9, 1947
flowAlways is offline   Reply With Quote

Old   April 10, 2015, 11:36
Default
  #24
New Member
 
Sihan Jin
Join Date: Apr 2015
Posts: 2
Rep Power: 0
jsh331 is on a distinguished road
Quote:
Originally Posted by flowAlways View Post
Hi Sehan,
You are correct, infact the Chalmers PaSR model is very similar to the successful EDC approach by Magnussen. It takes into account both the turbulent time scale and the chemical time scale while determining the reaction rate. The chemical timescale is determined by solving the reaction system’s ODEs fully coupled, and finding the characteristic time for that system. So it is meant to take into account a multi-step reaction mechanism.
You can find more about PaSR here
http://www.tfd.chalmers.se/~valeri/book-chapt7.pdf
http://powerlab.fsb.hr/ped/kturbo/op...olmPhD2008.pdf
http://web.ist.utl.pt/jose.neves.rod...2011-FINAL.pdf

In the PaSR model the reaction rate is determined as
reactionRate_PaSR = kappa*reactionRate_laminar
kappa ~ 1 when t_chemical >> t_mix so your results with laminar and PaSR will be similar only when the rate is kinetics controlled and not mixing controlled(that is when the flow is laminar and reactions are slow).

what is your reaction mechanism? Can you maybe send your case to me ?
Hello Ali,

Thanks for your explanation. My problem is I keep adding energy, but the reaction rate is too small when I use PaSR model. Pls find my case in the attachment.

--Sihan
Attached Files
File Type: zip Constant volume combustion.zip (80.3 KB, 82 views)
jsh331 is offline   Reply With Quote

Old   July 9, 2015, 05:50
Default
  #25
Member
 
Howar
Join Date: Mar 2015
Posts: 53
Rep Power: 11
Howard is on a distinguished road
Quote:
Originally Posted by wenxu View Post
Now, i know how to manipulate multi-step reactions. But as far as i know, there is no multi-step combustion models built in OF.
  1. laminar
  2. PaSR---derived from laminar, can be used in turbulence.
  3. diffusion,FSD,infinitelyFastChemistry, these three all derived from singleStepCombustion
If i want to implement muti-step reaction (combustion model which not only consider chemistry time but also turbulence mixing time), what should i derived the class? That's mean which class should i derived from?
Now i have compiled the EBU model succeed and i design i case to use this model. (i almost substitute the EBU model for the chemistry class. that's means when laminar calss calculate the reaction Rate R(Yi), then it will use the new class EBU to calculate the R(Yi). ) ANY ideas can give me? Thank you!!!!



best Regards,
wen
Hello, Friends. I am now trying to do combustion simulation in OpenFOAM, since I need to use multistep mechanism, I would like to ask which solver I can use? You mentioned before that this is no model for multistep mechanism? Thank you!
Howard is offline   Reply With Quote

Old   July 9, 2015, 06:09
Default
  #26
Member
 
Howar
Join Date: Mar 2015
Posts: 53
Rep Power: 11
Howard is on a distinguished road
Quote:
Originally Posted by jsh331 View Post
Hi Wen
Why do you say that Laminar and PaSR combustion models are not for multi-step combustion? Actually I have a problem simulating constant volume combustion using reactingFoam. My geometry is a box with ignition at the center and a 4 step mechanism of CH4 & air is implemented. It's filled with CH4 and air initially. Turbulence model is k-epsilon and I'm testing laminar and PaSR combustion model. It turns out that laminar works pretty good but PaSR doesn't work as what I expect. So could you pls help me figure out my problem?

Sihan
Hi, Sihan Jin. I also want to use multistep mechanism. I tried the PaSR model but it doesn't work. So I would like to ask how you solve your problem? Thank you!
Howard is offline   Reply With Quote

Old   July 9, 2015, 07:37
Default
  #27
Senior Member
 
Freedom
Join Date: May 2014
Posts: 209
Rep Power: 12
wenxu is on a distinguished road
ReactingFoam maybe the choice for non-premixed flame. Just add reactions in the reaction dictionary.

Regards,
Wen
wenxu is offline   Reply With Quote

Old   January 6, 2016, 07:18
Default
  #28
New Member
 
Tomladian Bucinara
Join Date: Jan 2015
Posts: 18
Rep Power: 11
Tom123 is on a distinguished road
Hi Shian,

May you upload your 4-step reaction mechanism of CH4? I try to find it. thank you.

Tom
Tom123 is offline   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
reduced reaction mechanism for methane combustion using FLUENT vnm ANSYS 1 August 9, 2016 09:25
How to write k and epsilon before the abnormal end xiuying OpenFOAM Running, Solving & CFD 8 August 27, 2013 15:33
Time step, Number of time step, Maxximum Iterations per time step sandisk FLUENT 0 July 18, 2011 02:57
Time step for combustion simulation AdidaKK CFX 11 December 3, 2009 11:47
Could anybody help me see this error and give help liugx212 OpenFOAM Running, Solving & CFD 3 January 4, 2006 18:07


All times are GMT -4. The time now is 07:13.