On Operating a Nanofiltration Membrane for Olive MillWastewater Purification at Sub- and Super-Boundary Conditions
Metadata
Show full item recordEditorial
MDPI
Materia
Membranes Membrane fouling Boundary flux
Date
2017-07-14Referencia bibliográfica
Stoller, M.; Ochando-Pulido, J.M.; Field, R. On Operating a Nanofiltration Membrane for Olive Mill Wastewater Purification at Sub- and Super-Boundary Conditions. Membranes 2017, 7, 36. https://doi.org/10.3390/membranes7030036
Abstract
In the last decades, membrane processes have gained a significant share of the market
for wastewater purification. Although the product (i.e., purified water) is not of high added value,
these processes are feasible both technically and from an economic point of view, provided the flux is
relatively high and that membrane fouling is strongly inhibited. By controlling membrane fouling,
the membrane may work for years without service, thus dramatically reducing operating costs and the
need for membrane substitution. There is tension between operating at high permeate fluxes, which
enhances fouling but reduces capital costs, and operating at lower fluxes which increases capital
costs. Operating batch membrane processes leads to increased difficulties, since the feed fed to the
membrane changes as a function of the recovery value. This paper is concerned with the operation of
such a process. Membrane process designers should therefore avoid membrane fouling by operating
membranes away from the permeate flux point where severe fouling is triggered. The design and
operation of membrane purification plants is a difficult task, and the precision to properly describe
the evolution of the fouling phenomenon as a function of the operating conditions is a key to success.
Many reported works have reported on the control of fouling by operating below the boundary flux.
On the other hand, only a few works have successfully sought to exploit super-boundary operating
conditions; most super-boundary operations are reported to have led to process failures. In this
work, both sub- and super-boundary operating conditions for a batch nanofiltration membrane
process used for olive mill wastewater treatment were investigated. A model to identify a priori the
point of transition from a sub-boundary to a super-boundary operation during a batch operation
was developed, and this will provide membrane designers with a helpful tool to carefully avoid
process failures.