Question about the maxwell-stefan equations written in fluent theory guide
TAGGED: fluent, multicomponent, multicomponent-diffusion
-
-
October 4, 2024 at 4:35 amkimjh12Subscriber
Hi, I have question about maxwell-stefan equations written in the fluent theory guide Fluent 2024 R2.
In chapter 7.1.1.3.2, there are definitions and equations related to Maxwell-Stefan equations.Â
My question is the formula $M_{w,m}$ which is defined as $\sum_{i=1}^N\frac{Y_i}{M_{w,i}}$, where $Y_i$ is a mass fraction of $i$th species, and $M_{w,i}$ is a molecular weight of $i$th species.
Also, there is a remark related to the formula; 'a subscript used to define a mean molecular weight in the mixture'.
I wonder if the expression is defined properly.
In my thought, $M_{w,m}$ should be inverse of $\sum_{i=1}^N\frac{Y_i}{M_{w,i}}$.Â
The proof is as follows. By using the related quantities between mass fraction $Y_i$ and mole fraction $X_i$, $\sum_{i=1}^N\frac{Y_i}{M_{w,i}}$ is equal to $\sum_{i=1}^N\frac{X_iM_{w,i}}{\sum_{j=1}^N X_jM_{w,j}}\frac{1}{M_{w,i}}$.
Since $\sum_{i=1}^N X_i=1$ by definition of the mole fraction, we can further simplify the expression. As a result, $\sum_{i=1}^N\frac{Y_i}{M_{w,i}}$ is equal to $\frac{1}{\sum_{j=1}^N\frac{X_j}{M_{w,j}}}$, which is inverse of the mean molecular weight in the mixture.Â
Thank you.Â
-
October 24, 2024 at 4:17 pmAhmed HussienAnsys Employee
Your logic seems correct. I will further investigate and let you know.Â
-
October 25, 2024 at 7:35 pmAhmed HussienAnsys Employee
Â
I checked this and you are right. There is a typo in the documentation and it will be fixed in the next release. However, the implementation in the code is correct. It should not affect the solution in your case.
Â
-
- You must be logged in to reply to this topic.
- Non-Intersected faces found for matching interface periodic-walls
- Unburnt Hydrocarbons contour in ANSYS FORTE for sector mesh
- Help: About the expression of turbulent viscosity in Realizable k-e model
- Script error Code: 800a000d
- Cyclone (Stairmand) simulation using RSM
- Fluent fails with Intel MPI protocol on 2 nodes
- error udf
- Diesel with Ammonia/Hydrogen blend combustion
- Mass Conservation Issue in Methane Pyrolysis Shock Tube Simulation
- Script Error
-
1236
-
543
-
523
-
225
-
209
© 2024 Copyright ANSYS, Inc. All rights reserved.