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−1SO2 in 0.5 mol L−1H2SO4 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% SO2 in nitrogen and 0.5 mol L−1H2SO4 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