A Multidimensional Data Set for Diesel Combustion Model Validation: I - Initial Conditions, Pressure History and Spray Shapes

Models for droplet transient heating: Effects on droplet evaporation, ignition, and break-up

“…The specific heat capacity of vapour at constant pressure is approximated as [59]: when T < T cr , and zero otherwise. The density of liquid is approximated as [58] ρ l = 1104.98 − 1.9277T + 0.003411T 2 − 3.2851 × 10 −6 T 3…”

“…where T cr = 725.9 K and T b = 536.4 K, when T < T cr , and zero otherwise. The specific heat capacity of liquid in J·kg −1 ·K −1 is approximated as [59]: c l = 264 + 6.33T − 0.00296T 2 . The specific heat capacity of vapour at constant pressure is approximated as equal to that of n-dodecane [59].…”

“…The specific heat capacity of liquid in J·kg −1 ·K −1 is approximated as [59]: c l = 264 + 6.33T − 0.00296T 2 . The specific heat capacity of vapour at constant pressure is approximated as equal to that of n-dodecane [59]. The saturated vapour pressure is assumed to be equal to [57]: when 620 T < T cr K 0 when T T cr K The density of liquid is approximated as [58]: ρ l = 840/[1 + 0.00067(T − 288)].…”

“…The saturated vapour pressure is assumed to be equal to [57]: when 620 T < T cr K 0 when T T cr K The density of liquid is approximated as [58]: ρ l = 840/[1 + 0.00067(T − 288)]. The thermal conductivity of liquid in W·m −1 ·K −1 is presented in Table 1 [56] The surface tension is approximated as [59]:…”

Advanced models of fuel droplet heating and evaporation

“…The specific heat capacity of vapour at constant pressure is approximated as [393] c pv Z 380:63 C 4:1372 T C 2:004 !10 K4 T 2 K1:8009 !10 K6 T 3 C 7:7875 !10 K10 T 4 K1:0152 !10 K13 T 5 :…”