A number of platinum catalysts for the decomposition of 98% hydrogen peroxide, based on different substrates, geometries, and sizes, have been prepared using different procedures. The catalysts have undergone a set of dedicated tests for screening their catalytic activity and their thermomechanical resistance in order to identify the most efficient and suitable catalyst to be used for a pulsed monopropellant propulsion system. An experimental test campaign on a 20 N monopropellant thruster prototype has been carried out with the aim of assessing the capability of the finally selected new Pt∕α-Al 2 O 3 catalysts of effectively decomposing 98% hydrogen peroxide and the attainable propulsive performance in steady-state conditions for the future assessment of the propulsive performance of the intrinsically unsteady new propulsion concept. The catalysts have been able to decompose up to 1 liter of 98% H 2 O 2 with very good efficiencies (hc > 95% and hΔT ≥ 90%) and without any pellet breakage or catalytic degradation. The thrust profile has been particularly smooth and the experimental specific impulse measured at sea level with the matched conical nozzle has been 130 s, which corresponds to an extrapolated vacuum specific impulse for a high-expansionarea-ratio bell-contoured nozzle higher than 185 s. Nomenclature A = catalytic bed cross-sectional area, which is equal to= theoretical thrust coefficient, which is equal to γ 2∕γ1 γ1∕γ−1 2∕γ−11−p e ∕p C γ−1∕γ p p e −p a ∕p C A e ∕A t fγ; A e ∕A t ; p a ∕p C c = characteristic velocity, which is equal to p C A t ∕m, m∕s c theo = theoretical characteristic velocity, which is equal to which is equal to RT∕γ p γ1∕2 γ1∕2γ−1 , m∕s D = catalytic bed diameter, m D e = nozzle exit diameter, m D t = nozzle throat diameter, m F = thrust, N G = bed load or mass flux, which is equal to m∕A, kg∕s · m 2 g = gravitational acceleration at sea level, m∕s 2 I sp = specific impulse, which is equal to F∕mg, s I sp exp vacuum = vacuum specific impulse extrapolated from the experimental results, s L = catalytic bed length, m m = propellant mass flow rate, kg∕s or g∕s p C = chamber pressure, Pa or bar p CATBEDinlet = inlet catalytic bed pressure, Pa or bar p ENGINEinlet = inlet engine pressure (after the firing valve and before the injector), Pa or bar p TANK = tank pressure, Pa or bar R = gas constant of the exhaust gases, J∕kg · K S BET = specific surface area, m 2 ∕g T ad = adiabatic decomposition temperature, K or°C T amb = ambient temperature, K or°C T C = combustion chamber temperature, K or°C T i = initial temperature, K or°C T TANK = propellant temperature inside the tank, K or°C T 3;4 = temperatures at different stations along the bed, K or°C t max = time to reach the peak temperature, s t 90% = thrust rise time, s α conical = conical half angle, deg γ = specific heat ratio of the exhaust gases Δp CATBED = pressure drop across the catalytic bed, which is equal to p CATBEDinlet −p C , Pa or bar Δp ENGINE = pressure drop across the engine, which is equal to p ENGINEinlet − p C , Pa or ba...