A pyrolysis-non-thermal plasma-catalytic system for the increased production of hydrogen-rich gas from waste biomass has been investigated. Plasma processing of the hydrocarbon pyrolysis gases produced a marked increase in total gas yield with plasma-catalysis producing a further modest increase. The product gases were mainly composed of H-2, CO and CO2, which were all increased under plasma and plasma-catalyst conditions. For example, H-2 yield increased from 1.0 mmol g(biomass)(-1) in the absence of plasma to 3.5 mmol g(biomass)(-1) with plasma and to 4.0 mmol g(biomass)(-1) with plasma-catalysis. In addition, in the absence of plasma, the hydrocarbon tar content in the product gas was 420 mg m(-3), but, for non-catalytic plasma conditions, this was reduced to 325 mg m(-3) and for plasma-catalytic steam reforming, the tar hydrocarbons were markedly reduced to 150 mg m(-3). The effect of increasing input power for the plasma processing (no catalyst) showed a large increase in total gas, H-2, CO and CO2 yield and corresponding decrease in hydrocarbon gas concentration. Plasma-catalysis showed that higher power input had only a small effect on gas yield. Plasma-catalysis was shown to produce lower catalyst coke deposition compared to non-plasma catalytic processing.