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Re: Help in meshing using GAMBIT! 26 Aug 2013 | 12:02 pm
Throughout your academic career, you will be asked to write an essay on many occasions. writing essays written from an author's personal point of view, but the definition is vague,
Swirl ratio 8 Aug 2013 | 02:59 pm
Hello everyone...I need to simulate swirl ratio of in-cylinder flows in CFX. can any body help me...Its very urgent..
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Convergence problem 26 Jul 2013 | 12:16 pm
Hello, in my Geometry, there are an inlet and 3 outlets, I know mass flow inlet and the mass fraction of each outlet. The flow is incompressible and laminar and I use Ansys Fluent 14.0 to solve it. I ...
sum of particles in a surface 25 Jul 2013 | 04:55 pm
Hi all, I'm running particles in a pipe in a transient simulation. How can i get a graph/histogram with the total particles that passed through 3 surfaces along the pipe?- I'l like to see the coalesen...
HOW TO GET CELL VALUE BY UDF? 24 Jun 2013 | 03:20 pm
Hi, Someone can help me please, I want get mass the fraction in one cell by using a UDF. The cell coordinate are x=0.015 and y=0.15. Domain *domain = Get_Domain(2); Thread *c_thread; thread_loop_c(...
Re: How can I calculate time-average velocity in transient simulation? 23 Jun 2013 | 05:35 pm
Hi, thanks for the code but it gives me Error:rpgetvar 'send' undefied variable... I am using solid-gas flow and I modified the code for it. compilation is fine but when I execute it iti gives me the...
How Can I Do Conjugate Heat Transfer 4 Jun 2013 | 03:24 pm
hi, how can i do Conjugate Heat Transfer in Gambit & Fluent step by step as a fin heat sink in a duct, please help me.
Re: What is DPM concentration in Fluent and how is it calculated? 4 Jun 2013 | 01:58 pm
Hallo Thx for the description, but I am still confused. For what is DPM concentration good for? Even with your Definition I have no clue: Quote DPM concentration = (Avg. particle mass in cell * Pa...
DPM partilce tracking 12 May 2013 | 11:53 am
Hi I read DPM particle tracking will consider the particle as a point.so my question is whether this model is sufficient to track the particle which driven through the fluid domain by drag force only....
