Subjected to an oscillating flow rate, a compressor may feed additional (ex
citational) energy into the attached piping system. The relation between th
is additional energy input and the instantaneous behavior of a centrifugal
compressor stage is dealt in a first part. Modeling the Stage behavior by t
aking into account either inertia of the enclosed fluid mass or a first-ord
er transient element or transient stall in any component leads to a differe
nt energy input. The energy input at a flow rate oscillation of given frequ
ency, and amplitude was calculated as a function of the slope of the charac
teristic and the reduced frequency applying a previously published model to
describe the instantaneous behavior of the stage. In this model transient
stall in the diffuser is taken into account. At reduced frequencies above u
nity the energy input of the diffuser was reduced by a considerable amount
due to the specified instantaneous behavior of the diffuser. This indicates
a potential to reduce the additional energy input of the diffuser either b
y increasing the rime constant of the stall process or by increasing the mi
ld surge frequency. For the investigated diffuser size the required reduced
frequencies imply mild surge frequencies in a range being too high for ind
ustrial application (>200 Hz). Still, this method turned out to give useful
insight into the link between the instantaneous behavior of the compressor
and its energy input. In a second part for the same centrifugal compressor
the energy contribution of several stage segments during mild surge oscill
ations was determined from detailed instantaneous measurements. As a result
, the contribution of each stage segment to the conservation of the wild su
rge pulsation emerges. Although at the investigated mild surge frequencies
the stage segments no longer behave strictly quasi-steadily, their contribu
tion to the additional energy input is found to be mainly determined by the
slope of their quasi-steady characteristic.