Green" propellants based on Ionic-liquids (ILs) like Ammonium DiNitramide and Hydroxyl Ammonium Nitrate have recently been developed as reduced-hazard replacements for hydrazine. Compared to hydrazine, ILs offer up to a 50% improvement in available density-specific impulse. These materials present minimal vapor hazard at room temperature, and this property makes IL's potentially advantageous for "ride-share" launch opportunities where hazards introduced by hydrazine servicing are cost-prohibitive. Even though ILs present a reduced hazard compared to hydrazine, in crystalline form they are potentially explosive and are mixed in aqueous solutions to buffer against explosion. Unfortunately, the high water content makes IL-propellants difficult to ignite and currently a reliable "cold-start" capability does not exist. For reliable ignition, IL-propellants catalyst beds must be pre-heated to greater than 350 C before firing. The required preheat power source is substantial and presents a significant disadvantage for SmallSats where power budgets are extremely limited. Design and development of a "micro-hybrid" ignitor designed to act as a "drop-in" replacement for existing IL catalyst beds is presented. The design requires significantly lower input energy and offers a smaller overall form factor. Unlike single-use "squib" pyrotechnic ignitors, the system allows the gas generation cycle to be terminated and reinitiated on demand.
Nomenclature= ignitor nozzle exit area, cm 2 A surf = droplet surface area, cm 2 a = Van der Waal parameter, kPa-m 6 /kg-mol 2 B flux = HAN decomposition mass flux, g/s-cm 2 b = Van der Waal parameter, m 3 /kg-mol = ignitor discharge coefficient C p ign = ignitor exhaust products specific heat at constant pressure, J/kg-K = HAN-solution injector discharge area, cm 2 C pc = mean specific heat of gaseous products in chamber, J/kg-K C p HAN = specific heat of pure HAN, J/kg-K C p H2O = specific heat of pure water, J/kg-K = HAN-solution specific heat, J/kg-K D droplet = atomized HAN-solution droplet size, mm f = HAN mass fraction in solution 2 H c = total enthalpy of gaseous products in chamber, J = chamber enthalpy rate, W = enthalpy rate of injected HAN-solution, W = total output enthalpy rate of ignitor, W h ign = specific output enthalpy of ignitor, J/kg L chamber = HAN decomposition length, cm L vap H2O = latent heat of vaporization of water, J/g M HAN = moles of HAN in solution or collected in chamber M H2O = moles of water in solution or collectrd in chamber M ign = moles of ignotor exhaust products collected in chamber M w = generic m,olecular weight term, kg/kg-ml M W HAN = molecular weight of pure HAN, 96.04 kg/kg-mol M W H2O = molecular weight of pure water, 18.02 kg/kg-mol M W HAN/H2O = molecular weight of HAN-solution m c = total fluid mass collected in chamber, g m HAN = total HAN mass collected in chamber, g m ign = total ignitor product mass collected in chamber, g m H2O = total water mass collected in chamber or mass of water in atomozed solution droplet, g = vaporization mass flo...