A material balance closure calculation is presented to test the consistency of a previously published model of a parallelplate electrochemical reactor. New expressions are used in this procedure to calculate the average concentration of species i and the average current density for reaction j from the predicted concentration and potential distributions. Also, the previously presented model equations are simplified by assuming that the axial concentration gradient for species i can be approximated by a step change from the known feed concentration to the unknown outlet concentration. This one-step model provides a qualitative evaluation of cell performance and adds insight into understanding of the previous model, while providing substantial...
A common problem in the electrowinning industry is that of maintaining a uniform current density Acr...
A mathematical model to calculate tertiary current distributions in electrochemical reactors is pres...
A simplified, one-dimensional, macroscopic model for porous electrode re-actors with forced convect...
A material balance closure calculation is presented to test the consistency of a previously publishe...
A model is presented for a parallel plate electrochemical reactor which has electrodes that are the ...
A model is presented for a parallel plate electrochemical reactor which has electrodes that are the ...
A mathematical model is presented for a system comprised of a parallel plate electrochemical reactor...
A method is presented for determining the effects of time dependence, axial diffusion, and axial mig...
A parallel-plate electrochemical reactor model with multiple reactions at both electrodes and anolyt...
An algebraic model for a parallel plate, zinc/bromine flow cell is presented and used to predict var...
A model is presented for the reduction of hexavalent chromium in a parallel-plate electrochemical re...
Several industrial sites are now undergoing remediation to remove toxic waste that has managed to ma...
An electrochemical process is being developed for recovering metals from shredded waste electrical a...
A simple model for a parallel plate, zinc/bromine flow cell and associated storage tanks is presente...
A continuous reduction in the cross-section area is analysed as a means of improving mass-transfer i...
A common problem in the electrowinning industry is that of maintaining a uniform current density Acr...
A mathematical model to calculate tertiary current distributions in electrochemical reactors is pres...
A simplified, one-dimensional, macroscopic model for porous electrode re-actors with forced convect...
A material balance closure calculation is presented to test the consistency of a previously publishe...
A model is presented for a parallel plate electrochemical reactor which has electrodes that are the ...
A model is presented for a parallel plate electrochemical reactor which has electrodes that are the ...
A mathematical model is presented for a system comprised of a parallel plate electrochemical reactor...
A method is presented for determining the effects of time dependence, axial diffusion, and axial mig...
A parallel-plate electrochemical reactor model with multiple reactions at both electrodes and anolyt...
An algebraic model for a parallel plate, zinc/bromine flow cell is presented and used to predict var...
A model is presented for the reduction of hexavalent chromium in a parallel-plate electrochemical re...
Several industrial sites are now undergoing remediation to remove toxic waste that has managed to ma...
An electrochemical process is being developed for recovering metals from shredded waste electrical a...
A simple model for a parallel plate, zinc/bromine flow cell and associated storage tanks is presente...
A continuous reduction in the cross-section area is analysed as a means of improving mass-transfer i...
A common problem in the electrowinning industry is that of maintaining a uniform current density Acr...
A mathematical model to calculate tertiary current distributions in electrochemical reactors is pres...
A simplified, one-dimensional, macroscopic model for porous electrode re-actors with forced convect...