The goal of this experimental project was to design and fabricate a reactor and membrane test cell to dissociate hydrogen sulfide (H 2 S) in a nonthermal plasma and to recover hydrogen (H 2 ) through a superpermeable multi-layer membrane. Superpermeability of hydrogen atoms (H) has been reported by some researchers using membranes made of Group V transition metals (niobium, tantalum, vanadium, and their alloys), but it was not achieved at the moderate pressure conditions used in this study. However, H 2 S was successfully decomposed at energy efficiencies higher than any other reports for the high H 2 S concentration and moderate pressures (corresponding to high reactor throughputs) used in this study.Several pulsed corona discharge (PCD) reactors were fabricated and used during this project. Prior to experiments involving H 2 S, methane (CH 4 ) was used as a non-toxic reactant to evaluate the performance of the reactor. These experiments were also valuable for determining the potential to co-process H 2 S and CH 4 as a method of sweetening natural gas. The products of the direct methane conversion experiments included hydrogen, acetylene, and higher hydrocarbons. The reactor was a co-axial cylinder (CAC) corona discharge reactor, pulsed with a thyratron switch. The reactor was designed to accommodate relatively high flow rates (655×10 -6 m 3 /s), representing a pilot scale easily converted to commercial scale. Parameters expected to influence methane conversion, including pulse frequency, charge voltage, capacitance, residence time, and electrode material, were investigated. Conversion, selectivity and energy consumption were measured or estimated. C 2 and C 3 hydrocarbon products were analyzed with a mass spectrometer (MS). Methane conversions as high as 51% were achieved. The products were typically 50-60% acetylene, 20% propane, 10% ethane and ethylene, and 5% propylene. First law thermodynamic energy efficiencies for the system (electrical and reactor) were estimated to range from 6 to 38%, with the highest efficiencies occurring at short residence time and low power input (low specific energy), where conversion is the lowest (less than 5%). The highest methane conversion of 51% occurred at a residence time of 18.8 s with a flow rate of 39.4×10 -6 m 3 /s (5 ft 3 /h) and a specific energy of 13,000 J/l using niobium and platinum coated stainless steel tubes as cathodes. Under these conditions, the first law efficiency for the system was 8%. Under similar reaction conditions, methane conversions were ~50% higher with niobium and platinum coated stainless steel cathodes than with a stainless steel cathode.The effect of capacitance, cathode material, gas flow rate (residence time) and specific energy on methane conversion, energy efficiency and product selectivity were all examined during the methane experiments. Ethane and acetylene appeared to be formed primarily from dimerization of CH 3 radicals and CH radicals, respectively, while ethylene appeared to be formed mainly from the dehydrogenation of ethane. At ...