The dynamic propulsive performance of a saturated steam reaction jet is analyzed and compared with experimental results at vacuum thrust levels up to 0.015 Ib. The techniques used to obtain accurate test results for a low-thrust, dynamic mode of operation are described. Impulse bit size /bit? steam consumption, and specific impulse / are characterized in terms of thruster geometry, gas properties, and command pulse width 0 C . For 6 C < 50 msec, transient effects cause a loss in / (e.g., 10% for 6 C = 20 msec); steady-state / varies from 85 to 108 sec for saturation temperatures of 150° to 300°F. System performance of the steam reaction jet is compared with that of 9 other gases for equal temperatures and thrust levels. The results indicate that steam is competitive with subliming solids and superior to the propellants stored as gases. However, the NH 3 system, stored as a liquid, has a higher / eff . The steam system requires 20% more heating power (12 w/mlb thrust) than the subliming solid and twice more than NHs, but the danger of line clogging due to solidification is somewhat less. At very low thrust levels, or if the installation is such that a weight penalty for the power source is not incurred, a steam system may be attractive.A 0 a*(2/ 7 yi*/2 V c acoustic velocity = equivalent orifice-to-nozzle area ratio = a\/an ozzle discharge coefficient = w m /P c A t K n thrust coefficient thrust correlation factor = F m /(P c C/At)ideal exhaust velocity coefficient or impulse efficiency characteristic velocity = a*/y[2/(y + l)](7+D/2(7-D diameter thrust, Ibf proportionality constant in Newton's second law enthalpy specific impulse, Ibf-sec/lbm impulse bit ( per pulse), Ibf-sec effective system specific impulse, Ibf-sec/lbm total impulse, Ibf-sec mechanical equivalent of heat ipirical decay time integration factor I P c d0 I P s 0d = 0.0685 choked nozzle flow factor = a* [2/(y -f ; = empirical rise time integration factor I P c d0 I P s 0 r 0.69 k = system factor in Eq. (9) to account for electric heater and minimum gage tank weights (0.87 for gases and 0.80 for liquids and solids) I = nozzle length M = Mach number = u/a* 2fTl = molecular weight N r = Reynolds number = Dup/v N k = Knudsen number = (7r T /2) 1/2 (M/N r ) P = pressure R = universal gas constant T = temperature u = velocity V, v = volume and specific volume, respectively w, w = weight and weight flow rate, respectively x = fraction of condensate present in flow y = pressure ratio transformation = [1 -(F C /P 5 )] 1/2 y. = [1 -(P a /P,)V»7 = ratio of specific heats 5 = surface tension e = nozzle expansion ratio 77 = efficiency B = time v = viscosity £ = Te/Tr p, a = density and working stress, respectively; (p/ J -S as an d incipient condensation, respectively m = measured or delivered Downloaded by UNIVERSITY OF MICHIGAN on February 19, 201...