The transfer performance and power requirements of unconfined sealed e
nd hollow fiber membranes were studied, Membrane modules, operated in
the sealed end mode, were pressurized with oxygen and placed within a
submerged rectangular jet discharge. This design is especially well su
ited for use in waters containing high solids concentrations. The memb
ranes have a greater degree of freedom for movement and are, therefore
, less likely to become fouled due to solids being lodged within the f
iber bundle. Furthermore, because the membranes are not enclosed withi
n a tubular shell, head losses across the membranes are reduced. In a
related study, Johnson et al. [1] developed a mass-transfer correlatio
n for unconfined membranes similarly situated within a circular jet di
scharge. In this study, the mass-transfer correlation developed for ci
rcular jets is verified experimentally for larger rectangular module d
esigns better suited for use in large scale applications. The headloss
es across the modules are characterized in detail as a function of wat
er flowrate and membrane spacing. These data are used to estimate the
power requirements for different designs under a variety of operating
conditions. The mass-transfer rates and corresponding power requiremen
ts for the unconfined configuration are compared with other membrane c
onfigurations. (C) 1998 Elsevier Science B.V.