World experience defines hydrogen as the most perspective energy carrier. Producing hydrogen by electrolysis helps effectively solve the problem of peak loads and failures arising from the different structure of energy consumption during the day . Thermoelectrochemical cycles of producing hydrogen are intensively studied in Kharkov Polytechnic Institute, Kharkov, Ukraine. Further development of hydrogen production by electrolysis of water associated with implementation of Hybrid Sulfur cycle or "Westinghouse cycle") [1]. It is a two–step process, first a low–temperature electrochemical step (1): 2H2O + SO2 H2 + H2SO4 (1) and second a high temperature (2): H2SO4 H2O + SO2 + 0,5 O2 (2) The clear advantage of the Hybrid Sulfur Cycle process is that the standard reversible voltage E0 of the net cell reaction (2) is only 0.17 V. For comparison, conventional water electrolysis requires E0 = 1.23 V. In laboratory–scale tests, the realized cell voltage of SO2 depolarization electrolysis has been 0.5¼1.3 V, depending on the current density and other operational parameters compared with the 1.8¼2.0 V of commercial alkaline water electrolysis. Thus, SO2 depolarization electrolysis would require 25¼60 % of the electrical energy required for direct water splitting by conventional electrolysis. The electrochemical process is far from technical implementation and intensively studied in recent years.Hybrid Sulfur cycle was intensively studied for practical implementation with using platinum, gold and palladium anodes . Further investigation is connected with using more affordable anode materials. According to the E–pH diagram, ruthenium, molybdenum, tungsten and their oxides are defined to be most perspective catalytic materials. Active porous anode was obtained by covering the graphite basis by active carbon, Pt, MoO3, RuO2, WO3. Covering with active carbon was prepared by impregnating the graphite basis in sugar solution, followed by drying and thermal decomposition. The other composite coatings were prepared by impregnating a sugar solution and brine H2[PtCl6], (NH4)6Mo7O24·4H2O, (NH4)4W5O17, followed by drying and thermal decomposition at 600...650 K. The cylindrical anodes have diameter 20 mm and thickness 5 mm. They were inserted into a special current source, consisting of a current–conducting tubes with welded sample holder (Fig. 1). Samples were fixed in a holder nut. Current supply material – titanium coated PTFE. Current–voltage measurements were carried out in plastic cell with anode and cathode separation space cation exchange membrane. Electrode potentials were measured relative to a mercury sulfate reference electrode and converted to the normal hydrogen electrode.
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