Dear Timo,
Really Thank you very very much. You clarified everything for me in an
amazing way and finally the results are going in the correct way now and
they make sense despite some numerical error modifying the pressure on
the upper and lower boundaries where the injection well is
Hi Mahmoud,
you also need to extract the correct energy carried by the fluid in the
production well. Otherwise your domain will heat up there.
For solution-dependent point sources you can use the split interface. First you
add your point sources (in addPointSources) only providing positions as
Dear Timo,
I cannot thank you enough for all your help and guidance. I wrote the
pointsource function as shown below. could you please let me know if it
is OK now or not ? I used 3 pointsources to represent each of the
production well and the injection well because I wanted to represent
> On 8. Apr 2021, at 13:42, Mahmoud Atef Mahmoud Mohamed Aboelseoud S277151
> wrote:
>
> Dear Timo,
>
> Thanks a lot for your reply. I didn't use the pointSources because I didn't
> know how to assign the temperature inside such function for the injection
> well because I want to impose a
Dear Timo,
Thanks a lot for your reply. I didn't use the pointSources because I
didn't know how to assign the temperature inside such function for the
injection well because I want to impose a rate and also a temperature.
I'm using the OnePNI model in my problem. I will try to be more
Dear Mahmoud,
what you are doing seems correct to me. You can get the relevant cell volume
with “scv.volume()” so you don’t have to compute that yourself.
You can also get the density with "elemVolVars[scv].density(phaseIdx)". But
that shouldn’t change anything if you already used the correct
