Boundary condition problem for diffusion equation

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Discussion Overview

The discussion revolves around boundary conditions for the diffusion equation in the context of a chemical introduced into a channel domain. Participants explore the implications of different boundary conditions when the assumption of no dispersion at the channel's outlet is invalid. The scope includes theoretical considerations and potential applications in computational fluid dynamics.

Discussion Character

  • Exploratory
  • Technical explanation
  • Debate/contested

Main Points Raised

  • One participant presents a matrix for a numerical solution and questions the validity of the boundary condition c(a,t)=0 when chemical dispersion cannot be ignored.
  • Another participant suggests a limit condition, stating that as a approaches infinity, c(a,t) approaches 0.
  • A third participant outlines various boundary condition options, including specified concentration, zero flux, specified flux, and convective mass transfer, noting that many combinations exist in practice.
  • Another participant clarifies that if there is no flux crossing a boundary, the gradient of the flux normal to the boundary is zero, leading to the condition ∂c/∂x = 0 for a one-dimensional problem.

Areas of Agreement / Disagreement

Participants present multiple competing views on appropriate boundary conditions, indicating that the discussion remains unresolved regarding the best approach when chemical dispersion is considered.

Contextual Notes

Limitations include the dependence on specific definitions of boundary conditions and the potential for various interpretations of flux and concentration at the boundaries.

brambram
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BOUNDARY CONDITION PROBLEM
I have came up with matrix for numerical solution for a problem where chemical is introduced to channel domain, concentration equation:

δc/δt=D*((δ^2c)/(δx^2))-kc

assuming boundary conditions for c(x,t) as : c(0,t)=1, c(a,t)=0. Where a is channel's length.

What if domain is not-infinite (as it is above) and we cannot assume that the chemical is not dispersed at the end of the channel- so the boundary condition c(a,t)=0 is no longer valid?

What boundary condition can we use when we cannot assume that the chemical is not dispersed at the outlet of the channel? Can you state it or not? How about computational fluid dynamics boundary conditions options?
 
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##\lim_{a\to\infty} c(a,t)=0##?
 
At the two ends of the sample, you can have a wide variety of different combinations of boundary conditions:

Specified concentration c = C(t)
Zero flux: δc/δx = 0
Specified flux: -D ∂c/∂x = [itex]\phi[/itex](t)
Convective mass transfer: -D ∂c/∂x = k (c - c)

There are an infinite number of others also, but these are the ones you run into most often in practice.
 
If there is no flux crossing a boundary, then the gradient of the flux normal to the boundary is 0.

For a 1-D problem like yours, that means ##\partial c/\partial x = 0##
 

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