A performance analysis is presented for the vapour compression parallel fee
d multiple effect evaporation water desalination system. The systems includ
e mechanical (MVC) and thermal (TVC) vapour compression, The system models
take into account the dependence of the stream physical properties on tempe
rature and salinity, thermodynamic losses, temperature depression in the va
pour stream caused by pressure losses and non-condensable gases, flashing w
ithin the effects, and the presence of flashing boxes. The analysis is perf
ormed as a function of the brine distribution configuration (parallel or pa
rallel/cross flow), the top brine temperature, the temperature of the brine
blowdown, and the temperature difference of the compressed vapour condensa
te and the brine blowdown. The analysis is focused on variations in the par
ameters that control the product cost, which includes the specific heat tra
nsfer area, the thermal performance ratio, the specific power consumption,
the conversion ratio, and the specific flow rate of the cooling water. Resu
lts show consistent behaviour with industrial practice, where the thermal p
erformance ratio of the TVC system decreases at higher top brine temperatur
es, while the specific power consumption of the MVC systems decreases at hi
gher temperatures. Also, the specific heat transfer area for all configurat
ions decreases at higher operating temperatures. The conversion ratio is fo
und to depend on the brine flow configuration and to be independent of the
vapour compression mode. For the parallel flow configuration, the conversio
n ratio decreases with the increase of the operating temperature. On the ot
her hand, the conversion ratio for the parallel/cross flow system decreases
with the increase of the brine blowdown temperature. Predictions of both m
odels show good agreement with field data.