Fluid Flow and Heat Transfer Analysis | Cross Flow Heat Exchanger | ANSYS Fluent Tutorial | CFD

DEAR SIR,

COULD YOU PLEASE SHARE THE CAD FILE ON THIS PROJECT!

I WILL BE DEEPLY THANKFUL TO YOU! PLEASE PLEASE SIR

how can make advanced sizing function "off" for custom meshing in ANSYS fluent (17.2) MESHINGICEM CFD

can i please have the file for this?

thank you

ANSYS SUMULATION OF Flat plate collector with reflector.

Thanks

I like your vídeo thanks for sharing!

Please show the same meshing but in ICEM CFD structer meshing

مرسی

Hi do you give Ansys fluent training if you do so please May I ask you to provide your email

Thank you sooooooooo much

Hello, thank for the video, I have a question, what should we do in the Inlet boundary conditions? thanks

Suggest a proper meshing type and solver for circular microchaneel

thanks so much this video so interested

For the solid, stainless steel, it is not iin fluent database. How to add?

For microchannel, the dimension should be at range of micrometers, u are using at metres. Why so? or can we easily scale down? Do suggest.

very helpful video... great job .

Is the Video all mute except the music in the beginning? Or am I missing something?
But great video anyway!

Can i get the link for geometry please

What is the impact of reverse flow in final result. Please comment

since i think there are missing BC, i tried these values and i got almost similar results as in the video:

heated pipe inlet (1-6): velocity 0.001 m/s, temperature 400~450 K
heated pipe outlet (1-6): temperature 400~450 K
inlet: velocity 0.002 m/s, temperature 300 K
outlet: temperature 300 K
pipe wall, pipe wall shadow, wall fluid domain: material steel

Thanks u , nice video

Thank you so much for the great education effort i hope that you can post us an earth air heat exchanger thanks a lot

The video is great but can you explain the theory behind the simulation or is there a link that you can provide that does explain it?

plz make Vedio on Geometry Twin screw compressor ..Thanks

what values did you put in "inlet" and "outlet" in boundary conditions"?? I think you have not mentioned that.

I m getting only the energy (blue line)graph after running calculation . Please help me for the same

Dear Sir
Thanks alot

i cant view the colour during results ....after giving streamline in fluid domain

I have some doubt in the project......can you plz send the file in email?

I am using PCM material inside the pipes... So along with PCM liquid factor ...I am getting pipewall liquid factor...
Though it should be 0 ..I am getting it as 0.7 . Can u please say where did I do mistake

Can you kindly suggest that, If we use a condensate pump at the exit of anair heat exchanger, which will only get activated if a certain pressure (above atmosphere) is reached, then what exit boundary condition we can use ?

The pressure at the exit drops below atmospheric, But the condensate pump only gets actuated after a certain pressure at exit is achieved.

there are two bodies of different materials in contact with each other. One body is heated to a temperature of 200 degrees, and the other 20 degrees. How to make a thermal analysis in ANSYS to look at the temperature distribution and temperature stresses caused by heating a body with a temperature of 20, if a body with a temperature of 200 degrees cools down from contact with a body with a temperature of 20, as well as from contact with the environment?

NICE

You forgot to specify the inlet velocity of the cold fluid

Sir can you send me this file for my project work?

Thanks! this helped me a lot. Can u tell me why you used Simplec, Green-gauss cell based instead of Coupled, Green-gauss node based?

In the residuals graphs, it showed only for energy, not for velocity and mass. How to fix it?

can we use this for batteryb simualtion

I have some issues with my simulation, in BC menu there are three contact regions which are set to interface. and also there are six walls with heat flux set to zero.(I did the simulation with 3 tubes) unfortunately there is no "coupled" option for walls. how can I resolve this problem?

how can I get the amount of heat tranafer in my result?

there is one big problem, you didn't apply a proper boundery condition for hp wall. if it's set by default to zero heat flux, the whole simulation is wrong, since there won't be any heat transfer.

please help.
somehow "heated piped 1" become "wall" (in boundary conditions). how can i remake it to "velocity-inlet"?

i tried plotting the velocity ans streamline ...it performs the calculations ..but i dont get to see the colorful plots on the screen ......how to get them

i need help please 'how to heat oil in cup'

What are the initial and boundary conditions missing? I can't seem to find the outer fluid domain.
Thank you

amazing tutorial, but i would like some complexity like, the heater is a copper pipe(most of the time) so add him into the problem and if i have convection and conductivity(as a real problem) how do i do?
thanks a lot