Effects of Separator and Terminal on the Current Distribution in Parallel‐Plate Electrochemical Flow Reactors

1982 ◽  
Vol 129 (8) ◽  
pp. 1670-1678 ◽  
Author(s):  
Johnsee Lee ◽  
J. R. Selman
2020 ◽  
Vol 873 ◽  
pp. 114359 ◽  
Author(s):  
Tzayam Pérez ◽  
Luis F. Arenas ◽  
Daniel Villalobos-Lara ◽  
Nan Zhou ◽  
Shuncai Wang ◽  
...  

2022 ◽  
Author(s):  
A. A. Folgueiras-Amador ◽  
J. W. Hodgson ◽  
R. C. D. Brown

Organic electrosynthesis in flow reactors is an area of increasing interest, with efficient mass transport and high electrode area to reactor volume present in many flow electrolysis cell designs facilitating higher rates of production with high selectivity. The controlled reaction environment available in flow cells also offers opportunities to develop new electrochemical processes. In this chapter, various types of electrochemical flow cells are reviewed in the context of laboratory synthesis, paying particular attention to how the different reactor environments impact upon the electrochemical processes, and the factors responsible for good cell performance. Coverage includes well-established plane-parallel-plate designs, reactors with small interelectrode gaps, extended-channel electrolysis cells, and highly sophisticated designs with rapidly rotating electrodes to enhance mass transport. In each case, illustrative electrosyntheses are presented.


2011 ◽  
Vol 89 (1) ◽  
pp. 163-167 ◽  
Author(s):  
Armando I. Vazquez Aranda ◽  
Eduardo R. Henquín ◽  
Israel Rodríguez Torres ◽  
José M. Bisang

1999 ◽  
Vol 64 (5-6) ◽  
pp. 341-347
Author(s):  
Konstantin Popov ◽  
Slavisa Pesic ◽  
Tanja Kostic

It was shown that the current density-cell voltage curves recorded in a cell with parallel plate electrodes for different distances between the edges of the electrodes and side walls of the cell can be used to determine the current distribution in cells of the Haring-Blum type.


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