{'fraction_non_alphanumeric': 0.026353276353276354, 'fraction_numerical': 0.0405982905982906, 'mean_word_length': 4.445736434108527, 'pattern_counts': {'":': 0, '<': 0, '<?xml version=': 0, '>': 0, 'https://': 0, 'lorem ipsum': 0, 'www.': 0, 'xml': 0}, 'pii_count': 0, 'substrings_counts': 0, 'word_list_counts': {'cursed_substrings.json': 0, 'profanity_word_list.json': 0, 'sexual_word_list.json': 0, 'zh_pornsignals.json': 0}}
Electrochemical conversion of sulfur dioxide with a rotating cylinder electrode working as anode or cathode

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 SO2 in 0.5 mol L−1 H2SO4 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−1 H2SO4 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