Abstract
The mass transfer conditions in a hydrocyclone cell have been analysed and an approximate plug-flow model has been developed to describe metal ion depletion during batch recycle operation. The resulting concentration-time relationship and reaction rate equation has been shown to describe satisfactorily the experimental data obtained for the electrodeposition of copper and silver from dilute solutions. Moreover, these relationships have enabled the evaluation of mass transfer coefficients in the hydrocyclone cell.
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Abbreviations
- a 1,a 2,b :
-
numerical exponents
- C :
-
concentration (mol dm−3)
- C o :
-
initial bath concentration (mol dm−3)
- C(0):
-
cell inlet concentration (mol dm−3)
- C(L):
-
cell outlet concentration (mol dm−3)
- k :
-
rate constant (h−1)
- K :
-
mass transfer coefficient (ms−1)
- K L :
-
volumetric mass transfer coefficient = 2πRLK (m3 s−1)
- L :
-
‘active’ length of the cylindrical cathode (m)
- Q :
-
volumetric flow rate (m3 s−1)
- r :
-
inside radius of the conical part of the cell
- r A :
-
reaction rate of component A (mol dm−3 h−1)
- R :
-
inside radius of the cylindrical part of the cell (m)
- t :
-
time
- u :
-
vertical (axial) velocity in the annulus
- U :
-
cell voltage (V)
- υt :
-
horizontal (tangential) velocity in the annulus
- V B :
-
volume of the reservoir/bath
- V R :
-
volume of the cell/reactor
- τB :
-
residence of time of the reservoir
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Dhamo, N. An electrochemical hydrocyclone cell for the treatment of dilute solutions: approximate plug-flow model for electrodeposition kinetics. J Appl Electrochem 24, 745–750 (1994). https://doi.org/10.1007/BF00578089
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DOI: https://doi.org/10.1007/BF00578089