Mass transport and flow dispersion in the compartments of a modular 10 cell filter-press stack
Ponce de León, Carlos, Whyte, Ian, Reade, Gavin W., Male, Stewart E. and Walsh, Frank C. (2008) Mass transport and flow dispersion in the compartments of a modular 10 cell filter-press stack. Australian Journal of Chemistry, 61, (10), 797-804. (doi:10.1071/CH07161).
Full text not available from this repository.
Flow dispersion, pressure drop, and averaged mass transport measurements have been made to characterize the reaction environment in an industrial scale electrochemical reactor. The 10 cell filter-press stack was operated with a relatively low mean linear velocity in the range 0.6 to 6.2 cm s–1. Flow dispersion was studied by a perturbation–response technique by electrolyte conductivity measurements at the reactor outlet. Mass transport coefficients were evaluated from the first order reaction decay of dissolved bromine (Br3–) which was anodically generated from 1 mol dm–3 NaBr (aq). Each cell consisted of two 0.72 m2 projected area electrodes separated by a cationic membrane, and each electrolyte compartment contained a high-density polyolefin turbulence promoter. The electrodes consisted of a carbon/polyethylene core with a layer of an activated carbon–poly(vinylidene difluoride) composite on each side. Comparison is made with the mass transport characteristics of a similar system that contains five bipolar cells.
|Digital Object Identifier (DOI):||doi:10.1071/CH07161|
|Keywords:||activated carbon electrode, bromide ion, bromine, energy storage, filter-press cells, flow dispersion, mass transport, pressure drop, redox flow battery, reaction environment, tribromide ion|
|Subjects:||T Technology > TP Chemical technology
Q Science > QD Chemistry
|Divisions:||University Structure - Pre August 2011 > School of Engineering Sciences > Engineering Materials & Surface Engineering
|Date Deposited:||07 Oct 2008|
|Last Modified:||06 Aug 2015 02:51|
|RDF:||RDF+N-Triples, RDF+N3, RDF+XML, Browse.|
Actions (login required)