Thank you for your tutorial ~ it has inspired me a lot! Thank you very much for your calculation example, which has a great effect on my understanding of Transpiration!😘😘😘
Hello, Sir! Thanks a lot for such a helpful video! I'm just doing research on this topic and your video helps me a lot. I have a question about geometry : how did you establish the boundary between the porous layer and the fluid flow? Please share your geometry if it's not difficult for you🙏.
I have a question. In porous media, 1. what is the residual saturation? and how does it affect the calculation? 2. Can I give the relative permeability for the phase2 with table as well like phase 1?
Thank you very much for the insightful tutorials. ❤️ Sir, can you please make a tutorial for liquid-vapor interface evaporation using schrage's evaporation model.
Hello Sir. Thanks for the video. I have seen you have used both Lee model (evaporation-condensation) and Raul's law (species mass transfer) to model the evaporation. What is the difference? What are the criteria to choose either of them. Thanks.
Can you tell me what macro should I use to incorporate source term in hydrogen diffusion through the metallic membrane as its calculation uses partial pressures of both sides of the membrane.
Great tutorial! Keep up the good work. I've learned a lot of good information. Can we use the evaporation-condensation model be used to model this same problem? I'm thinking why use the species concentration model is used especially since there is only one specie in the mixture. Can you please elaborate, thank you!
![[CFD] Porous Zones in CFD](/img/n.gif)
Absolutely great effort of knowledge sharing..
Thank you for your tutorial ~ it has inspired me a lot! Thank you very much for your calculation example, which has a great effect on my understanding of Transpiration!😘😘😘
Great video!! Thank you so much!!
Are you using normalized saturation value in the relative permeability table?
Great effort
Would it be possible to use "non-equilibrium thermal model" for this simulation?
Hello, Sir! Thanks a lot for such a helpful video! I'm just doing research on this topic and your video helps me a lot. I have a question about geometry : how did you establish the boundary between the porous layer and the fluid flow? Please share your geometry if it's not difficult for you🙏.
I have a question. In porous media, 1. what is the residual saturation? and how does it affect the calculation? 2. Can I give the relative permeability for the phase2 with table as well like phase 1?
Thank you very much for the insightful tutorials. ❤️
Sir, can you please make a tutorial for liquid-vapor interface evaporation using schrage's evaporation model.
Hello Sir. Thanks for the video. I have seen you have used both Lee model (evaporation-condensation) and Raul's law (species mass transfer) to model the evaporation. What is the difference? What are the criteria to choose either of them. Thanks.
Can you tell me what macro should I use to incorporate source term in hydrogen diffusion through the metallic membrane as its calculation uses partial pressures of both sides of the membrane.
Use define_source
how did you extract the tables to two column? i did mine and cannot work
Great tutorial! Keep up the good work. I've learned a lot of good information.
Can we use the evaporation-condensation model be used to model this same problem? I'm thinking why use the species concentration model is used especially since there is only one specie in the mixture. Can you please elaborate, thank you!
anyone pls tell how to open the file in discription on workbench
Your tutorial was very good, but when I did it, I got a floating point exception error that I don't know how to fix.
Hi! Could you solve it?
Can I use similar steps for 3D model?
Yes
Hi, shaven, kind request to simulate sintered wick laptop heat pipe (evaporation and condensation),
I have send you an email ,
@@icemanrajeev Did you model sintered wick heat pipe?
sir, is there any interface here between porous and fluid flow?
U need to model two domains and create a part
U can also create a interface
There must be connection between two fluids
@@shavantechnology3472 is it possible if i contact you through email?