The hydrocarbon tar content in the plasma system was approximately twice the hydrocarbon tar content in the plasma-catalytic system. Moreover, the higher the input power, the lower the product gas hydrocarbon tar content. The optimum result obtained was < 135 mg m-3 product gas hydrocarbon tar content for a plasma-catalytic system with an input power of 80 W which produced a hydrocarbon tar reduction of 68% compared to the hydrocarbon tar produced with the pyrolysis-catalysis process.
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