Electrochimica Acta 46 (2000) 381 – 387
Comparison of the performance of a reactor equipped with
a Ti/Pt and an SS anode for simultaneous cyanide removal
and copper recovery
L. Szpyrkowicz
a,
*, S.N. Kaul
b
, E. Molga
c
, M. DeFaveri
d
a
Department of Enironmental Sciences, Uniersity of Venice, Dorsoduro 2137, 30123 Venice, Italy
b
National Enironmental Engineering Research Institute, Nagpur 440 020, India
c
Chemical and Process Engineering Department, Warsaw Technical Uniersity, ul. Warynskiego 1, 00 645 Warsaw, Poland
d
Faculty of Agriculture, Catholic Uniersity of Piacenza, . Emilia Parmense 84, 29100 Piacenza, Italy
Received 26 November 1999; received in revised form 24 March 2000
Abstract
The paper presents the results of a study on the destruction of copper complexed cyanides and the simultaneous
recovery of copper in a lab-scale batch electrochemical reactor. The performance of the reactor equipped with a
stainless steel (SS) plate anode is compared with the data relative to the process conducted with a Ti/Pt anode having
the same overall size. Both reactors operated at various initial pH values under galvanostatic conditions. Under highly
alkaline conditions in situ generation of a CuO catalyst on the anode surface was observed in both the reactors. The
observed mass transport coefficient, showing both the effects of reaction kinetics and mass transfer, was a function
of pH value and, only secondly, of the anode material. The highest value of (k
l
A )
obs
, equal to 0.24033 cm
3
s
-1
was
obtained for a Ti/Pt anode reactor operating at the pH of 13. Under these very alkaline conditions the performance
of the reactor equipped with the Ti/Pt anode at high initial Cu concentration proved slightly better than the
performance with the SS anode. The energy consumption for the pH 13 was a function E =a /[Cu] +b, where a and
b are the constants characteristic for each of the two reactors. © 2000 Elsevier Science Ltd. All rights reserved.
Keywords: Cyanide electro-oxidation; Ti/Pt anode; SS anode; Cu electrodeposition; Metal plating wastewater
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electrocatalytic properties towards cyanide oxidation.
Particular problems arise when dealing with the cyanide
complexed by such metals as iron, copper or zinc, due
to the high chemical stability of these complexes. The
electroxidation of complexed cyanide was found feasi-
ble, but it manifests a slower kinetics as compared to
the electroxidation of free cyanide [6–9]. It was found
that under particular conditions the process can, how-
ever, be enhanced by the presence of copper ions in the
solution. In this case the formation of some kind of
deposit was noticed on the anode surface at long elec-
trolysis time. Hine et al. [4] postulated that this dark
blue or black deposit consists of cupric oxyhydroxide.
Hwang et al. [7] analyzed the film deposited on the
1. Introduction
Destruction of the cyanide present in solution in the
ionic form using electrochemical methods, as an alter-
native to a traditional chemical oxidation, has been
proved to be feasible by several authors [1–5]. For the
removal of simple cyanide various anode materials were
successfully used: Pt, Ni, PbO
2
. All of them manifested
* Corresponding author. Tel.: +39-41-5298591; fax: +39-
41-2578591.
E-mail address: lidia@unive.it (L. Szpyrkowicz).
0013-4686/00/$ - see front matter © 2000 Elsevier Science Ltd. All rights reserved.
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