Transport phenomena-mass transfer

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Discussion Overview

The discussion revolves around the mass transfer of contaminants in a river, specifically under conditions of laminar flow without reactions. Participants are exploring the formulation of equations governing this process and addressing boundary conditions relevant to the problem.

Discussion Character

  • Technical explanation
  • Debate/contested
  • Mathematical reasoning

Main Points Raised

  • One participant presents an equation for mass transfer but expresses doubt about its correctness due to discrepancies with numerical solutions.
  • Several participants emphasize the importance of sharing information directly in the post rather than through external files for security reasons.
  • Another participant reviews the proposed equations and boundary conditions, suggesting that while the formulation appears acceptable, the solution method may be incorrect.
  • There is a discussion about the boundary conditions, with one participant questioning their accuracy and another suggesting that the boundary condition at z=0 may need to be adjusted to reflect a concentration of zero.
  • A participant mentions obtaining different results from a COMSOL simulation, indicating a potential issue with their approach or assumptions.
  • There are suggestions to consider transient behavior rather than steady state, as the real system is turbulent, although one participant insists on simplifying the problem to laminar and steady state for analysis.
  • Another participant points out that the boundary condition at z=0 being set to a constant concentration leads to unrealistic results, recommending a reevaluation of this condition.

Areas of Agreement / Disagreement

Participants express differing views on the appropriateness of the boundary conditions and the solution methods. There is no consensus on the correct formulation or approach, and multiple competing perspectives remain throughout the discussion.

Contextual Notes

Participants highlight that the physical system's behavior may not align with the steady-state assumption, and the boundary conditions specified may not accurately capture the dynamics at play. The discussion reflects ongoing uncertainty regarding the correct mathematical treatment of the problem.

anni
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Hello everyone,

I would like to obtain the equation for mass transfer of contaminant in a river. Here the fluid flow is laminar and I don't have reaction. I solved it and obtained this equation, but I think this equation is wrong because when I solved it numerically I got wrong answers. Would you please help?
Thanks a lot
 

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You might get more and better answers if you post the information directly in the post. I for one will not open a DOCX file from a stranger because of the security risk. PDF is slightly better, but still a problem.

You can copy/paste text, and even screen shots into a post. Just make sure the photos are easy to read on any screen, including phones.
 
anorlunda said:
You might get more and better answers if you post the information directly in the post. I for one will not open a DOCX file from a stranger because of the security risk. PDF is slightly better, but still a problem.

You can copy/paste text, and even screen shots into a post. Just make sure the photos are easy to read on any screen, including phones.
Thank you for comment
 
anorlunda said:
You might get more and better answers if you post the information directly in the post. I for one will not open a DOCX file from a stranger because of the security risk. PDF is slightly better, but still a problem.

You can copy/paste text, and even screen shots into a post. Just make sure the photos are easy to read on any screen, including phones.
Thank you for comment. Here is screen shots:
 
1586697275724.png

1586697309966.png

1586697330705.png

1586697359045.png
 
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Thank you so much for your reply. I try to obtain mass transfer of contaminants in a river. I suppose that my problem is laminar flow and I don't have reaction. I suppose that (A= contaminate particles, B=water)
X= depth, Z= length and Y= width of river
Boundary conditions: at x=0 , Z=0 CA=CA0 and at Z=delta (depth of river) dCA/dx=0
Vz= V(1-x/delta)
Vz(1-x/delta)dCA/dz= -DAB (d^2CA/dx^2)
I don't know my way is correct or not and if it is correct how should I continue it?

Thanks
 
I see the equations you are trying to solve and understand the physical problem you are trying to solve. Your formulation looks OK to me. But your solution method to this set of partial differential equations in x and z (as presented in the screen shots) is totally incorrect. You also alluded to a numerical solution. Is that different from what is shown in the screen shots? The solution to the partial differential equation and boundary conditions you formulated is ##C(x,z)=C_{A0}##.
 
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Chestermiller said:
I see the equations you are trying to solve and understand the physical problem you are trying to solve. Your formulation looks OK to me. But your solution method to this set of partial differential equations in x and z (as presented in the screen shots) is totally incorrect. You also alluded to a numerical solution. Is that different from what is shown in the screen shots?
Thank you so much for your reply. are the boundary conditions correct or not?
 
Today I solved them in another way. I suppose that Vz=Vz, max and solved the equation. But now the obtained results were completely different with Comsol simulation. I don't know where is my problem.
 
  • #10
Maybe you want the BC at z = 0 to be C = 0?
 
  • #11
I supposed that where the contaminant is pouring in the river is X=0 and Z=0
 
  • #12
anni said:
I supposed that where the contaminant is pouring in the river is X=0 and Z=0
Then in your steady state formulation, it is going to propagate downstream and fill the entire region. Check it out. Substitute ##C(x,z)=C_{A0}## in your differential equation and BCs. You will find that it satisfies them exactly. And, since the equations are linear, it is the unique solution.
 
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  • #13
Chestermiller said:
Then in your steady state formulation, it is going to propagate downstream and fill the entire region. Check it out. Substitute ##C(x,z)=C_{A0}## in your differential equation and BCs. You will find that it satisfies them exactly. And, since the equations are linear, it is the unique solution.
I am not if I understood what you mean. Do you mean the equation and my BCs are correct?
 
  • #14
anni said:
I am not if I understood what you mean. Do you mean the equation and my BCs are correct?
What I am saying is that the solution to your equations as formulates is ##C(x,z)=C_{A0}##. Your differential equation is OK, but there is a problem with how you are specifying the boundary conditions. The correct formulation depends on the precise details of what is happening at the boundaries in the actual physical system. The boundary conditions you have specified does not capture the essence of what is happening at the boundaries in the actual physical system you are trying to describe.
 
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  • #15
Thank you so much for your explanations. So, what Bcs should I specified to obtain correct result?
 
  • #16
anni said:
Thank you so much for your explanations. So, what Bcs should I specified to obtain correct result?
As I said, it depends on the details of the actual physical system. Also, maybe you want to be looking at the transient behavior of the system, rather then the steady state behavior?

I got to go now. Be back later.
 
  • #17
In real system it is not steady state and it is turbulent. But I can solve it simply, I suppose that it is laminar and steady state.
 
  • #18
The thing that is causing the problem with your analysis is the boundary condition at z = 0. As long as it is ##C_{A0}##, it is going to be that value throughout the solution domain at steady state. You just can't have the entire stream flowing into the region at that concentration. Try the calculation with this value set to zero, just to see how the solution comes out.
 
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  • #19
Chestermiller said:
The thing that is causing the problem with your analysis is the boundary condition at z = 0. As long as it is ##C_{A0}##, it is going to be that value throughout the solution domain at steady state. You just can't have the entire stream flowing into the region at that concentration. Try the calculation with this value set to zero, just to see how the solution comes out.
[/QUO
Thank you so much
 
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  • #20
I solved the problem again but I don't know what should I do for next step.
1.png

2.png

3.png
 

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