write UDF for the dpm model

Lxy2018 · June 19, 2018, 10:21

hi!
Now I need to write UDF about the dpm model used for post processing. The function of the UDF is to calculate concentration distribution from the trajectories.
1.unfortunately, I couldn't find related macor of the loop of particle trajectories in the user's manual.could someone please provide macor and instruction about it?
2.how to get the particle residence time?
P_TIME (p)-P_TIME 0(p) is right?

Thanks!

haghasa · June 19, 2018, 19:53

Compile and use this UDF:

Code:

#include "udf.h"
DEFINE_ON_DEMAND(loop_over_injections_particles)
{
	Domain *domain = Get_Domain(1);

        Injection *I;
        Particle *p;

	Injection *Ilist = Get_dpm_injections();  /* get the name of injections and store them in the Ilist */

	loop(I, Ilist)
	{
                loop(p, I->p)
                {
                /* do whatever you want with that particle */
                }
	}
}

For example, you want to calculate the concentration at the end of calculation:
(make sure to add one UDMI)

Code:

#include "udf.h"
#include "dpm.h"

DEFINE_EXECUTE_AT_END(get_dpm_conc)
{
  Domain *d = Get_Domain(1);

  Injection *I;
  Particle *p;

  Injection *Ilist = Get_dpm_injections();
 
  cell_t c;
  Thread *t;

  loop(I, Ilist)
    {
      loop(p,I->p)
		{
		  c = P_CELL(p);
		  t = P_CELL_THREAD(p);  
		  C_UDMI(c, t, 0) += P_N(p) * P_MASS(p)/C_VOLUME(c, t);
		}
    }
}

And for Residence Time:
(make sure to define pointer* p based on previous UDFs)

Code:

(P_TIME(p) - p->time_of_birth)  /* its in the dpm_types header file*/

Lxy2018 · June 19, 2018, 23:51

Hi haghase,
Thanks for your reply.
In a paper,I found a formula to calculate the concentration.

C=M*sum(dt (i,j))/Vj
where _M is the number flow rate of each trajectory, V is the volume of a computational cell for use in concentration calculations, dt is the particle residence time, and subscript (i,j) represents the ith trajectory and the jth cell.

so based on your code,I try to write the UDF using the formula,but i don't if it's correct.
Thanks!
#include "udf.h"
#include "dpm.h"

Domain *domain

enum
{
* Concentration
* NUM_OF_USED_UDM

}；

int UDM_checked=0;
viod reset_UDM_s(void);

int* check_for_UDM(void)
{
* Thread*t;
* if(UDM_checked)
* return UDM_checked;

* thread_loop_c(t,domain)
** {
**** if(FLUID_THREAD_P(t))
**** if(NULLP(THREAD_STORAGE(t,SV_UDM_I)))
**** return 0;
*** };

** UDM_checked=1;
** reset_UDM_s();
** return UDM_checked；
}；

void
reset_UDM_s(void)
{

** Thread*t;
** cell_t c;
** int i;
**
** if(!check_for_UDM())
** return;
**
** Message("Resetting User Defined Memory...\n");

** thread_loop_c(t,domain)
** {
***** if(NNULLP(THREAD_STORAGE(t,SV_UDM_I)))
******* {
********** begin_c_loop(c,t)
*********** {
************** for(i=0;i<NUM_OF_USED_UDM;i++)
************** C_UDMI(c,t,i)=0.;
************ }
*********** end_c_loop(c,t)
******** }
****** else
******** {
*********** Message("Skipping CELL thread no.%d..\n",THREAD_ID(t))
********* }
*** }
***** Message("---Done.\n");
}

DEFINE_DPM_SCALAR_UPDATE(Concentration,cell,thread ,initialize,p)

{
*
* Domain *d=Get_Domain(1);

* real V;
* real M;
* real T;

* Injection *I
* Tracked_Particle *p;

* Injection *Ilist=Get_dpm_injection();

* Thread *t;
* cell_t c;
* int initialize;

** thread_loop_c(t,domain)
* {
*** begin_c_loop(c,t)
*** {
****** loop(I,Ilist)
******** {
************ loop(p,p->p)
************ {
*************
*************** V=C_VOLUME(c,t);
*************** M=P_MASS(p);
*************** T=P_TIME(p)-P_TIME0(p);
*************** C_UDMI(c,t,i)+=M*T/V
************* }
********** }
**** }
**** end_c_loop(c,t)
** }
}

obscureed · June 21, 2018, 06:20

Hi Lxy2018,

It could be useful to take a step back and consider the bigger picture: The flow model can be steady or transient, and the particle tracking can be steady or unsteady. All four combinations are possible (though, for me, steady flow and unsteady DPM is an unfamiliar one).

There are fundamental differences between steady DPM and unsteady DPM. In steady DPM, when each parcel is released, it is followed from its injection point to its eventual end point (which can be "escape" at an inlet, or "trap" at a wall, or "incomplete" when reaching the maximum number, for example). So, parcels only exist during those bursts of tracking. If you look for parcels at any other moment (for example, DEFINE_ON_DEMAND or DEFINE_ADJUST), there will be none. A parcel represents some fraction of the total mass flowrate released in that injection: each parcel is representative of a certain mass flowrate of particles, in [kg/s] -- look at TP_FLOW_RATE(tp).

In unsteady DPM, each parcel advances in timestepping. When the timestepping stops, parcels are still there, each in a specific fluid cell. (A parcel not in a fluid cell should presumably have died somehow.) A parcel represents some fraction of the injection mass flowrate integrated over a timestep during injection -- so each parcel actually represents a mass of particles, in [kg], or the equivalent number of particles [not necessarily integer] -- look at TP_N(tp).

I mention this distinction because it makes a fundamental difference to when/where you can get information about parcels, and what information you should be looking for. I think your efforts so far have been heading towards unsteady DPM -- is that correct? (But in that case, is it correct to use the formula that you quote from a paper? -- you need to work this out for yourself.)

By the way, in either case, the mass flowrate or number in a parcel may need to be adjusted by a factor of TP_STOCHASTIC_NTRIES(p) if you are using multiple stochastic tries in the turbulent dispersion model of DPM. I don't know why the parcels aren't diluted by this factor at the start, but they aren't.

You may also need to consider what happens when the particles in a parcel change after injection -- for example, losing mass by evaporation; changes due to reaction; breakup etc. I can't offer guidance on all these cases, so the advice has to be to do some very careful test cases that check that the total amounts make sense.

I hope this helps. Good luck!
Ed

obscureed · June 21, 2018, 06:22

Taking a further step back, if you activate "Interaction with Continuous Phase" and re-run, then Fluent automatically calculates DPM Mass Concentration in all fluid cells.

obscureed · June 21, 2018, 06:49

And now getting into detail:

Please compile and debug your UDF before posting it. Your current code has several typing errors etc that you can and should remove for yourself.

If you wrap the code in your posts with "CODE ... \CODE" tabs (in square brackets), then the indentation spaces will be displayed. The # button in the editor automates this. Adding your own indentation with asterisks is just confusing.

There was a change sometime around Fluent version 17, where the distinction between Tracked_Particle *tp and Particle *p was emphasised. The distinction is rather technical, but the summary is that Tracked_Particle is the normal data structure that UDFs interact with, and so we look up TP_MASS(tp) etc. If you are not using the latest version of Fluent, I advise you to update. We should all start using the recent syntax.

TP_TIME0(tp) is the time when a Tracked_Particle *tp entered the cell that it currently inhabits. (There are also other quantities such as TP_MASS0 etc). The parcel may then take multiple timesteps, and each one will involve a call to any UDFs of type DEFINE_DPM_SCALAR_UPDATE that are actively hooked in. Therefore, you should not do cell-by-cell accumulation in this kind of UDF -- multiple particle timesteps will cause multiple accumulations and double-counting. If you are planning to add parcel effects to cells during the tracking of parcels, you should consider using DEFINE_DPM_SOURCE, which is called when the tp is about to the leave a cell (for example, to enter another).

But then (back to the big picture about steady or unsteady DPM tracking), do you really want to add parcel effects to cells during the tracking of parcels? This is a good plan (probably the only plan) for steady tracking. For unsteady tracking, you might want to calculate the overall concentration only occasionally. For this purpose, the templates provided by Haghasa are a very useful starting-point.

Good luck!
Ed

gush · June 23, 2018, 10:44

hi i am currently also dealing with similar problem. i think the code is something like below (more or less). i say so because i compared the results of the code itself and fluent (interaction with continuous phase option) but they are not quite same. can anyone also try this and share comments please? thanks in advance!

#include "udf.h"

/*initialize the user defined memory (UDM) for all cells*/

DEFINE_ON_DEMAND(Zero_UDM)
{
Domain *domain;
cell_t c;
Thread *t;

domain=Get_Domain(1);

thread_loop_c(t,domain)
{
begin_c_loop(c,t)
{
C_UDMI(c,t,0) = 0.0;
}
end_c_loop(c,t)
}
Message("\nUser Define memory is now initialized!\n");
}

real dt;
DEFINE_DPM_SCALAR_UPDATE(Part_Con,c,t,initialize,p )
{
Set_User_Memory_Name(0,"UDM0: PSI_C");

dt = (P_TIME(p) - P_TIME0(p));
C_UDMI(c,t,0) += P_FLOW_RATE(p)*dt/C_VOLUME(c,t);
}

obscureed · June 23, 2018, 17:33

Hi Gush,

First thing: please see my earlier comment that DEFINE_DPM_SCALAR_UPDATE is definitely not a good plan here. DEFINE_DPM_SOURCE is much better, at least for steady DPM tracking.

What version of Fluent are you using? I'd always advise updating unless you have a good reason not to.

Good luck!
Ed

gush · June 23, 2018, 18:07

Quote:

Originally Posted by obscureed

Hi Gush,

First thing: please see my earlier comment that DEFINE_DPM_SCALAR_UPDATE is definitely not a good plan here. DEFINE_DPM_SOURCE is much better, at least for steady DPM tracking.

What version of Fluent are you using? I'd always advise updating unless you have a good reason not to.

Good luck!
Ed

hi ed!

thanks for the reply. i am using 16.0.

so you advice to use DEFINE_DPM_SOURCE for this? should i also revise the rest of the code? what do you think?

actually it seems working somehow, but there is something wrong with it! maybe because of the reason you say?!

Lxy2018 · July 17, 2018, 22:38

Quote:

Originally Posted by haghasa

Compile and use this UDF:

Code:

#include "udf.h"
DEFINE_ON_DEMAND(loop_over_injections_particles)
{
	Domain *domain = Get_Domain(1);

        Injection *I;
        Particle *p;

	Injection *Ilist = Get_dpm_injections();  /* get the name of injections and store them in the Ilist */

	loop(I, Ilist)
	{
                loop(p, I->p)
                {
                /* do whatever you want with that particle */
                }
	}
}

For example, you want to calculate the concentration at the end of calculation:
(make sure to add one UDMI)

Code:

#include "udf.h"
#include "dpm.h"

DEFINE_EXECUTE_AT_END(get_dpm_conc)
{
  Domain *d = Get_Domain(1);

  Injection *I;
  Particle *p;

  Injection *Ilist = Get_dpm_injections();
 
  cell_t c;
  Thread *t;

  loop(I, Ilist)
    {
      loop(p,I->p)
		{
		  c = P_CELL(p);
		  t = P_CELL_THREAD(p);  
		  C_UDMI(c, t, 0) += P_N(p) * P_MASS(p)/C_VOLUME(c, t);
		}
    }
}

And for Residence Time:
(make sure to define pointer* p based on previous UDFs)

Code:

(P_TIME(p) - p->time_of_birth)  /* its in the dpm_types header file*/

Hi gush!
I tried to use your code to calculate the concentration ,but under the steady condition using steady particle tracking,I found the value of the contour of concentration is 0 when I clicked "Graphics->particle Tracks->track". So I added "Message" in your code,and the TUI didn't display the content of the "Message".
I'm traping into the problem,please help me.
Thanks!

Lxy2018 · July 17, 2018, 22:55

Quote:

Originally Posted by obscureed

And now getting into detail:

Please compile and debug your UDF before posting it. Your current code has several typing errors etc that you can and should remove for yourself.

If you wrap the code in your posts with "CODE ... \CODE" tabs (in square brackets), then the indentation spaces will be displayed. The # button in the editor automates this. Adding your own indentation with asterisks is just confusing.

There was a change sometime around Fluent version 17, where the distinction between Tracked_Particle *tp and Particle *p was emphasised. The distinction is rather technical, but the summary is that Tracked_Particle is the normal data structure that UDFs interact with, and so we look up TP_MASS(tp) etc. If you are not using the latest version of Fluent, I advise you to update. We should all start using the recent syntax.

TP_TIME0(tp) is the time when a Tracked_Particle *tp entered the cell that it currently inhabits. (There are also other quantities such as TP_MASS0 etc). The parcel may then take multiple timesteps, and each one will involve a call to any UDFs of type DEFINE_DPM_SCALAR_UPDATE that are actively hooked in. Therefore, you should not do cell-by-cell accumulation in this kind of UDF -- multiple particle timesteps will cause multiple accumulations and double-counting. If you are planning to add parcel effects to cells during the tracking of parcels, you should consider using DEFINE_DPM_SOURCE, which is called when the tp is about to the leave a cell (for example, to enter another).

But then (back to the big picture about steady or unsteady DPM tracking), do you really want to add parcel effects to cells during the tracking of parcels? This is a good plan (probably the only plan) for steady tracking. For unsteady tracking, you might want to calculate the overall concentration only occasionally. For this purpose, the templates provided by Haghasa are a very useful starting-point.

Good luck!
Ed

Hi Ed!
thanks for your reply!
After reading your message,I think I need to calculate concentration in steady and unsteady condition,respectively.Under the steady condition,I tend to use steady particle tracking.so the formula I found in a paper doesn't suit this case.but it could be used in the unsteady condition with steady particle tracking.Now I have a question.when I use unsteady calculation with steady particle tracking,how do I identify that particle is being calculated?
Thanks

Nitesh_Sahu · November 5, 2018, 12:44

I am having a problem can somebody help out

Macro - P_INIT_LF is not recognised in UDF for initial liquid fraction in Ansys-19 and the dpm header files also contain only Macro - P_INIT_LMF but what this signifies is not mentioned anywhere can someone help me with this its urgent!!!!

qin chunqiu · May 17, 2020, 09:31

Quote:

Originally Posted by haghasa

Compile and use this UDF:

Code:

#include "udf.h"
DEFINE_ON_DEMAND(loop_over_injections_particles)
{
	Domain *domain = Get_Domain(1);

        Injection *I;
        Particle *p;

	Injection *Ilist = Get_dpm_injections();  /* get the name of injections and store them in the Ilist */

	loop(I, Ilist)
	{
                loop(p, I->p)
                {
                /* do whatever you want with that particle */
                }
	}
}

For example, you want to calculate the concentration at the end of calculation:
(make sure to add one UDMI)

Code:

#include "udf.h"
#include "dpm.h"

DEFINE_EXECUTE_AT_END(get_dpm_conc)
{
  Domain *d = Get_Domain(1);

  Injection *I;
  Particle *p;

  Injection *Ilist = Get_dpm_injections();
 
  cell_t c;
  Thread *t;

  loop(I, Ilist)
    {
      loop(p,I->p)
		{
		  c = P_CELL(p);
		  t = P_CELL_THREAD(p);  
		  C_UDMI(c, t, 0) += P_N(p) * P_MASS(p)/C_VOLUME(c, t);
		}
    }
}

And for Residence Time:
(make sure to define pointer* p based on previous UDFs)

Code:

(P_TIME(p) - p->time_of_birth)  /* its in the dpm_types header file*/

The P_TIME(p)-p->time_of_birth may present the time from the releasing to current. While the PSI_C method need the residence time of a certain particle in a given cell. This could be get by P_TIME(p)-P_TIME0(p).
The problem I am facing is that when using the P_TIME(p)-p->time_of_birth, the compile is right but the result is not so good, on the other hand, when using the P_TIME(p)-P_TIME0(p), the complining is wrong with words "xxx state xxxx".

June 19, 2018, 10:21	write UDF for the dpm model	#1
Lxy2018 New Member Li Xiaoying Join Date: Jun 2018 Posts: 8 Rep Power: 7	hi! Now I need to write UDF about the dpm model used for post processing. The function of the UDF is to calculate concentration distribution from the trajectories. 1.unfortunately, I couldn't find related macor of the loop of particle trajectories in the user's manual.could someone please provide macor and instruction about it? 2.how to get the particle residence time? P_TIME (p)-P_TIME 0(p) is right? Thanks!

June 19, 2018, 23:51		#3
Lxy2018 New Member Li Xiaoying Join Date: Jun 2018 Posts: 8 Rep Power: 7	Hi haghase, Thanks for your reply. In a paper,I found a formula to calculate the concentration. C=Msum(dt (i,j))/Vj where _M is the number flow rate of each trajectory, V is the volume of a computational cell for use in concentration calculations, dt is the particle residence time, and subscript (i,j) represents the ith trajectory and the jth cell. so based on your code,I try to write the UDF using the formula,but i don't if it's correct. Thanks! #include "udf.h" #include "dpm.h" Domain domain enum { * Concentration * NUM_OF_USED_UDM }； int UDM_checked=0; viod reset_UDM_s(void); int* check_for_UDM(void) { * Threadt; if(UDM_checked) * return UDM_checked; * thread_loop_c(t,domain) { if(FLUID_THREAD_P(t)) if(NULLP(THREAD_STORAGE(t,SV_UDM_I))) return 0; * }; UDM_checked=1; reset_UDM_s(); return UDM_checked； }； void reset_UDM_s(void) { Threadt; * cell_t c; int i; if(!check_for_UDM()) return; Message("Resetting User Defined Memory...\n"); thread_loop_c(t,domain) { *** if(NNULLP(THREAD_STORAGE(t,SV_UDM_I))) *** { ****** begin_c_loop(c,t) ******* { ********** for(i=0;i<NUM_OF_USED_UDM;i++) ********** C_UDMI(c,t,i)=0.; ******** } ******* end_c_loop(c,t) **** } ** else **** { ******* Message("Skipping CELL thread no.%d..\n",THREAD_ID(t)) ***** } * } ***** Message("---Done.\n"); } DEFINE_DPM_SCALAR_UPDATE(Concentration,cell,thread ,initialize,p) { * * Domain d=Get_Domain(1); real V; * real M; * real T; * Injection I Tracked_Particle p; Injection Ilist=Get_dpm_injection(); Thread t; cell_t c; * int initialize; ** thread_loop_c(t,domain) * { * begin_c_loop(c,t) * { **** loop(I,Ilist) **** { ******** loop(p,p->p) ******** { ********* *********** V=C_VOLUME(c,t); *********** M=P_MASS(p); *********** T=P_TIME(p)-P_TIME0(p); ************* C_UDMI(c,t,i)+=MT/V ********** } ****** } } end_c_loop(c,t) } } Last edited by Lxy2018; June 20, 2018 at 22:30.

June 21, 2018, 06:20		#4
obscureed Senior Member Join Date: Sep 2017 Posts: 246 Rep Power: 11	Hi Lxy2018, It could be useful to take a step back and consider the bigger picture: The flow model can be steady or transient, and the particle tracking can be steady or unsteady. All four combinations are possible (though, for me, steady flow and unsteady DPM is an unfamiliar one). There are fundamental differences between steady DPM and unsteady DPM. In steady DPM, when each parcel is released, it is followed from its injection point to its eventual end point (which can be "escape" at an inlet, or "trap" at a wall, or "incomplete" when reaching the maximum number, for example). So, parcels only exist during those bursts of tracking. If you look for parcels at any other moment (for example, DEFINE_ON_DEMAND or DEFINE_ADJUST), there will be none. A parcel represents some fraction of the total mass flowrate released in that injection: each parcel is representative of a certain mass flowrate of particles, in [kg/s] -- look at TP_FLOW_RATE(tp). In unsteady DPM, each parcel advances in timestepping. When the timestepping stops, parcels are still there, each in a specific fluid cell. (A parcel not in a fluid cell should presumably have died somehow.) A parcel represents some fraction of the injection mass flowrate integrated over a timestep during injection -- so each parcel actually represents a mass of particles, in [kg], or the equivalent number of particles [not necessarily integer] -- look at TP_N(tp). I mention this distinction because it makes a fundamental difference to when/where you can get information about parcels, and what information you should be looking for. I think your efforts so far have been heading towards unsteady DPM -- is that correct? (But in that case, is it correct to use the formula that you quote from a paper? -- you need to work this out for yourself.) By the way, in either case, the mass flowrate or number in a parcel may need to be adjusted by a factor of TP_STOCHASTIC_NTRIES(p) if you are using multiple stochastic tries in the turbulent dispersion model of DPM. I don't know why the parcels aren't diluted by this factor at the start, but they aren't. You may also need to consider what happens when the particles in a parcel change after injection -- for example, losing mass by evaporation; changes due to reaction; breakup etc. I can't offer guidance on all these cases, so the advice has to be to do some very careful test cases that check that the total amounts make sense. I hope this helps. Good luck! Ed yezhonghua likes this.

Thread Tools	Search this Thread
Show Printable Version Email this Page	Search this Thread: Advanced Search
Display Modes
Linear Mode Switch to Hybrid Mode Switch to Threaded Mode

Similar Threads
Thread	Thread Starter	Forum	Replies	Last Post
mesh file for flow over a circular cylinder	Ardalan	Main CFD Forum	7	December 15, 2020 13:06
[Helyx OS] Helyx-OS (GUI for SnappyHexMesh	elvis	OpenFOAM Community Contributions	210	January 30, 2017 18:57
Water subcooled boiling	Attesz	CFX	7	January 5, 2013 03:32
UDF for linear PTT model implementation	dpitz	Fluent UDF and Scheme Programming	1	February 4, 2011 10:08
UDF for Heat Exchanger model	francois louw	FLUENT	2	July 16, 2010 02:21

June 21, 2018, 06:22		#5
obscureed Senior Member Join Date: Sep 2017 Posts: 246 Rep Power: 11	Taking a further step back, if you activate "Interaction with Continuous Phase" and re-run, then Fluent automatically calculates DPM Mass Concentration in all fluid cells.

June 21, 2018, 06:49		#6
obscureed Senior Member Join Date: Sep 2017 Posts: 246 Rep Power: 11	And now getting into detail: Please compile and debug your UDF before posting it. Your current code has several typing errors etc that you can and should remove for yourself. If you wrap the code in your posts with "CODE ... \CODE" tabs (in square brackets), then the indentation spaces will be displayed. The # button in the editor automates this. Adding your own indentation with asterisks is just confusing. There was a change sometime around Fluent version 17, where the distinction between Tracked_Particle tp and Particle p was emphasised. The distinction is rather technical, but the summary is that Tracked_Particle is the normal data structure that UDFs interact with, and so we look up TP_MASS(tp) etc. If you are not using the latest version of Fluent, I advise you to update. We should all start using the recent syntax. TP_TIME0(tp) is the time when a Tracked_Particle *tp entered the cell that it currently inhabits. (There are also other quantities such as TP_MASS0 etc). The parcel may then take multiple timesteps, and each one will involve a call to any UDFs of type DEFINE_DPM_SCALAR_UPDATE that are actively hooked in. Therefore, you should not do cell-by-cell accumulation in this kind of UDF -- multiple particle timesteps will cause multiple accumulations and double-counting. If you are planning to add parcel effects to cells during the tracking of parcels, you should consider using DEFINE_DPM_SOURCE, which is called when the tp is about to the leave a cell (for example, to enter another). But then (back to the big picture about steady or unsteady DPM tracking), do you really want to add parcel effects to cells during the tracking of parcels? This is a good plan (probably the only plan) for steady tracking. For unsteady tracking, you might want to calculate the overall concentration only occasionally. For this purpose, the templates provided by Haghasa are a very useful starting-point. Good luck! Ed

June 23, 2018, 10:44		#7
gush Member yun Join Date: Jul 2015 Posts: 37 Rep Power: 10	hi i am currently also dealing with similar problem. i think the code is something like below (more or less). i say so because i compared the results of the code itself and fluent (interaction with continuous phase option) but they are not quite same. can anyone also try this and share comments please? thanks in advance! #include "udf.h" /initialize the user defined memory (UDM) for all cells/ DEFINE_ON_DEMAND(Zero_UDM) { Domain domain; cell_t c; Thread t; domain=Get_Domain(1); thread_loop_c(t,domain) { begin_c_loop(c,t) { C_UDMI(c,t,0) = 0.0; } end_c_loop(c,t) } Message("\nUser Define memory is now initialized!\n"); } real dt; DEFINE_DPM_SCALAR_UPDATE(Part_Con,c,t,initialize,p ) { Set_User_Memory_Name(0,"UDM0: PSI_C"); dt = (P_TIME(p) - P_TIME0(p)); C_UDMI(c,t,0) += P_FLOW_RATE(p)*dt/C_VOLUME(c,t); }

June 23, 2018, 17:33		#8
obscureed Senior Member Join Date: Sep 2017 Posts: 246 Rep Power: 11	Hi Gush, First thing: please see my earlier comment that DEFINE_DPM_SCALAR_UPDATE is definitely not a good plan here. DEFINE_DPM_SOURCE is much better, at least for steady DPM tracking. What version of Fluent are you using? I'd always advise updating unless you have a good reason not to. Good luck! Ed

November 5, 2018, 12:44		#12
Nitesh_Sahu New Member IIT DELHI Join Date: Nov 2018 Posts: 1 Rep Power: 0	I am having a problem can somebody help out Macro - P_INIT_LF is not recognised in UDF for initial liquid fraction in Ansys-19 and the dpm header files also contain only Macro - P_INIT_LMF but what this signifies is not mentioned anywhere can someone help me with this its urgent!!!!