Premium
Electrochemical conversion of sulfur dioxide with a rotating cylinder electrode working as anode or cathode
Author(s) -
Fornés Juan P,
González Gabriel A,
Bisang José M
Publication year - 2016
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.4567
Subject(s) - sulfuric acid , electrochemistry , anode , sulfur , cathode , electrolyte , electrode , materials science , separator (oil production) , sulfur dioxide , lead dioxide , inorganic chemistry , metallurgy , chemistry , physics , thermodynamics
BACKGROUND A batch electrochemical reactor with a rotating cylinder electrode is analysed for the transformation of sulfur dioxide into either sulfuric acid or colloidal sulfur. RESULTS Potentiostatic experiments carried out at 30 °C and 500 rpm with 5 g L −1 SO 2 in 0.5 mol L −1 H 2 SO 4 conclude that −0.7 V, against SCE, represents an appropriate potential for the sulfur production at a 316 L stainless steel cathode. The figures of merit were: 0.15 kg m −3 h −1 space time yield and 39.7 kWh kg −1 for specific energy consumption. Galvanostatic experiments at 30 °C and 1000 rpm with three‐dimensional electrodes identify graphite felt as a promising anodic material. Using a gas phase of 5% SO 2 in nitrogen and 0.5 mol L −1 H 2 SO 4 as supporting electrolyte, a macrokinetic current density of 100 mA cm −2 represents an appropriate value, being the space time yield 7.58 kg m −3 h −1 with 2.86 kWh kg −1 specific energy consumption. CONCLUSION An electrochemical reactor with a rotating cylinder electrode showed a good performance for the production of colloidal sulfur. Sulfur dioxide was also converted into sulfuric acid including a separator in a reactor with a three‐dimensional rotating cylinder anode and co‐current gas and liquid flows. © 2014 Society of Chemical Industry