CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > FLUENT

Modeling electrochemical reactions for water treatment

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   March 15, 2017, 11:05
Smile Modeling electrochemical reactions for water treatment
  #1
Member
 
Liam
Join Date: Aug 2013
Posts: 40
Rep Power: 12
Many is on a distinguished road
Dear all,

I am a beginner with FLUENT add-on module for Fuel Cells and Electrolysis.

My aim is to describe the degradation of several substances present in a water flow when electricity is added to the system.As far as I know, this is the opposite mechanism of fuel cells.

I am in the early beginning, but firs thing should be to understand which module I have to use. Is the Electrolysis model suitable for my purpose? I have read about the SOFC and PEMFC models, it seems that they are implemented for fuel cells (oxygen and hydrogen+a catalyst produces electricity and water). My process is just the inverse: I have water and an electrical current and I want to see the behaviour of several species, leading to clean water.

So can I start playing with the Electrolysis module of the add-on? Is it suitable for water liquid?

Thanks in advance and sorry for this stupid question. I have found a lot of info related to PEMFC and SOFC, but it is still unclear to me how to model the reverse process.

Best,

Many
Many is offline   Reply With Quote

Old   March 15, 2017, 15:20
Default
  #2
Senior Member
 
piu58's Avatar
 
Uwe Pilz
Join Date: Feb 2017
Location: Leipzig, Germany
Posts: 744
Rep Power: 15
piu58 is on a distinguished road
Electrolysis happens at the surfaces only. The problem of the fluid flow is a secondary one. The main problem is the electrical field.

The kinetic properties of the electrode processes may be described by a single number, the polarisation parameter by Carl Wagner. This can be taken into account by a Neumann boundary condition.

A reason for taking into account the fluid flow may be the mass transport to the surface. It may be expressed by the thickness of the diffusion layer, which depends on the thickness of the Prandl layer. The maximal reaction rate is controlled by the last transport step, the diffusion.
__________________
Uwe Pilz
--
Die der Hauptbewegung überlagerte Schwankungsbewegung ist in ihren Einzelheiten so hoffnungslos kompliziert, daß ihre theoretische Berechnung aussichtslos erscheint. (Hermann Schlichting, 1950)
piu58 is offline   Reply With Quote

Old   March 16, 2017, 04:07
Smile
  #3
Member
 
Liam
Join Date: Aug 2013
Posts: 40
Rep Power: 12
Many is on a distinguished road
Hi Piu58 and thank you for your reply.

I cannot conclude from your answer which of the options I mentioned (PEMFC, SOFC and Electrolysis) is the most suitable for modeling the degradation of some wastewater components due to the catalysis produced using an electrical current...

It will be really helpful to know the model I need to use in FLUENT, so I can focus on the details of this model.

All your answers will be really appreciated!

Best,

Many
Many is offline   Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
How are chemical reactions stored after parsing? DanielW OpenFOAM Programming & Development 3 June 7, 2018 14:39
Max number of (elementary) reactions in combustion modeling with Fluent 14 fahdme FLUENT 0 April 17, 2013 15:38
Modeling chemical reactions in aqueous solvents CPUcruncher Main CFD Forum 0 February 17, 2012 16:47
Modeling the flow patterns in a membrane bioreactor for wastewater treatment tutorial shadyenany FLUENT 9 September 15, 2011 17:01
Representing Electrochemical reactions rock ANSYS 0 February 17, 2010 15:16


All times are GMT -4. The time now is 05:23.