The eneryg of sprayed and atomized drops is considered. It is shown th
at the efficiency of production of interfacial energy, by a process of
spraying and atomization, that involves a conjugate bulk pressure-vol
ume energy, cannot exceed a theoretical limit of 60%. The upper limit
of conversion of enthalpy and the Gibbs free energy to interfacial ene
rgy cannot exceed 60%, regardless of the spraying process by which the
latter is produced. This efficiency then depends also on the pressure
of the ambient phase and on the entropy density of the drops. Higher
levels of pressure and entropy density increase the proportion of the
bulk energy in the total energy of the drops. This can result in a dra
stic decrease in the efficiency, i.e., of energy conversion to interfa
cial energy, from the upper limit of 60%, down to a few percent. A cha
racteristic drop radius, for which the levels of bulk and interfacial
energy are matched, is defined for sprayed and atomized drops. It is s
hown that low efficiency is expected when spraying and atomization pro
cess yield drops that are significantly larger than the characteristic
size. Moment distribution functions are defined. These functions are
used to characterize the relative weight that is carried by different
size fractions of the drops regarding their contribution to bulk and i
nterfacial energies, and to the efficiency of spraying and atomization
processes. Drops that are larger than the expectation of drop size ar
e the prime source for the low efficiency of spraying and atomization,
whereas the smaller drops enhance the efficiency. Finally, the low ef
ficiency of spraying and atomization processes can be attributed to th
e properties of the sprayed drops, at this low efficiency is a consequ
ence of their inherent energy partitioning and is not due exclusively
to the nature of the process by which they have been produced.