Thank you very much.
Best,
Xiang
On Wed, Oct 23, 2019 at 4:42 PM Wolfgang Bangerth
wrote:
>
> > Thank you for your reply. I will try it. The equations are: > [...]
>
> Both step 31 and 32 will be good starting points. The only difference is
> that you have Darcy flow instead of Stokes flow, bu
> Thank you for your reply. I will try it. The equations are: > [...]
Both step 31 and 32 will be good starting points. The only difference is
that you have Darcy flow instead of Stokes flow, but that should be easy
to incorporate into these programs.
Best
W.
--
--
Hi, Wolfgang,
Thank you for your reply. I will try it. The equations are:
[image: image.png]
[image: image.png]
where T is temperature, p is pressure, u is flow rate. K is hydraulic
conductivity which is constant, κ and λ are the coefficients of heat
transfer. T1 means the temperature at boundary
On 10/22/19 10:57 PM, Xiang Sun wrote:
>
> Thank you for your reply. I am learning dealii to build up a geothermal
> model,
> which includes a Laplace equation and a heat transfer considering both
> convection and diffusion. The Laplace equation describes a pressure
> distibution in a site wit
Hi, Wolfgang,
Thank you for your reply. I am learning dealii to build up a geothermal
model, which includes a Laplace equation and a heat transfer considering
both convection and diffusion. The Laplace equation describes a pressure
distibution in a site with several wellbores. The heat transfer
On 10/22/19 10:41 AM, Xiang Sun wrote:
>
> In step-31, why did you define the residual by multiplying T^(a-1)? What does
> "a" mean? Thank you very much.
I assume you mean here?
https://dealii.org/developer/doxygen/deal.II/step_31.html#Stabilizationweakformandspacediscretizationforthetemperature
Hi,
In step-31, why did you define the residual by multiplying T^(a-1)? What
does "a" mean? Thank you very much.
Best,
Xiang
--
The deal.II project is located at http://www.dealii.org/
For mailing list/forum options, see
https://groups.google.com/d/forum/dealii?hl=en
---
You received this
