The effects of alternative fuels on the combustion characteristics of a liquid fuel spray are examined. Fuel properties are varied and the effects of these variations on the structure (drop histories, temperatures, and species concentrations) of the spray flame are calculated. Also, a comparison is made of the differences in two spray flames fueled by a standard NATO fuel and a proposed alternative fuel. The calculations are performed using a reacting, two-phase, two-dimensional flow code that utilizes a Lagrangian calculation of droplet trajectories and an Eulerian approach for the gas-phase flowfield. Interactions between the drops and the gas phase are accomplished through the particle-source-in-cell technique with exchange of mass, momentum, and energy between the two phases. A global reaction scheme is used with the reaction rate determined by the minimum of either an Arrhenius rate or mixing rate. Fuel property changes that affect droplet size and volatility are shown to have significant effects on droplet trajectory patterns. However, for the flowfield examined in this paper (where the fuel spray core is very rich and the mixing of air with the fuel occurs at a relatively slow rate), these trajectory changes only moderately modify the fuel vaporization pattern within the spray.
NomenclatureAI = empirical constant a = air mass fraction B M = mass transfer number B T = thermal transfer number C D = drag coefficient C p = specific heat C 1 ,C 2 ,C / , = turbulence model constants D_ = droplet diameter D = Rosin-Rammler mean droplet diameter D T = tunnel diameter F D = drag force / = fuel mass fraction H f = fuel's heat of combustion h = enthalpy / = stoichiometric air/fuel ratio k = kinetic energy of turbulence k g = gas thermal conductivity L = latent heat of vaporization L e = eddy length MW = molecular weight m = mass m d = droplet mass flow ratê evap = droplet evaporation rate N = Rosin-Rammler exponent N d = number of droplets in a parcel P = pressure Pr = Prandtl number p = product mass fraction = fuel reaction rate per unit volume = kinetic-limited reaction rate = mixing-limited reaction rate Re = Reynolds number r = radial coordinate S = source term SMD = Sauter mean diameter T = temperature T b = boiling temperature a ft r £ Subscripts d eff Superscripts = time = eddy lifetime = transit time = total velocity = axial velocity component = radial velocity component = position vector = axial coordinate = number of carbon atoms = number of hydrogen atoms = diffusion coefficient = dissipation rate of turbulence = gas viscosity = fuel viscosity = density = standard deviation = fuel surface tension = turbulence model constants = droplet relaxation time = general flow variable = droplet = effective = fuel = gas phase = inlet = outlet = droplet surface = general variable or equivalence ratio = number of carbon atoms = number of hydrogen atoms = general variable = time-averaged value