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Membrane and Desalination Technologies - TCE Moodle Website

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590 J.P. Chen et al.<br />

4.3.2. Physical Cleaning Methods<br />

Physical cleaning methods depend on mechanical forces to dislodge <strong>and</strong> remove foulants<br />

from the membrane surface. Physical methods used include forward flushing, backward<br />

flushing, backwashing, vibrations, air sparge, <strong>and</strong> CO2 back permeation.<br />

FORWARD FLUSHING<br />

The purpose of a forward flush is the removal of a constructed layer of contaminants on the<br />

membrane through the creation of turbulence. A high hydraulic pressure gradient is in order<br />

during forward flush. When forward flush is applied in a membrane, the barrier that is<br />

responsible for dead-end management is opened. At the same time, the membrane temporarily<br />

performs cross-flow filtration, without the production of permeate.<br />

BACKWARD FLUSHING<br />

Permeate is always used for a backward flush <strong>and</strong> the backward flush pressure is about<br />

2.5 times more than the production pressure. The pressure on the permeate side of the<br />

membrane is higher than the pressure within the membranes. The pores of a membrane are<br />

flushed inside out, resulting from the higher pressure on the permeate side of the membrane<br />

than that within the membranes.<br />

AIR/WATER FLUSH<br />

Air is added to the forward flush to form air bubbles, causing turbulence which removes<br />

fouling from the membrane surface. The benefit of the air flush over the forward flush is that it<br />

uses a smaller pumping capacity during the cleaning process.<br />

PERMEATE BACK PRESSURE<br />

The pressure added on the product side reverses the normal water transport across the<br />

membrane. At the same time, the materials dislodged from the surface are carried away by the<br />

feed to brine flush simultaneously.<br />

VIBRATION<br />

The permeator is vibrated by a pneumatic hammer device attached to the pressure vessel.<br />

The materials dislodged from the surface are carried away by the feed to brine flush<br />

simultaneously.<br />

CO2 BACK PERMEATION<br />

This method is suitable for hollow fiber configuration. A high-pressure CO2 gas is<br />

introduced into product side through the internal fiber bores <strong>and</strong> removed through the fiber<br />

walls. The foulants lifted from the surface are carried away by a flush stream.<br />

Seven RO cleaning methods were compared for cleaning a hollow fiber: simple forward<br />

flush, reverse flow, permeate back pressure, vibration, air drain <strong>and</strong> water refill, air sparge,<br />

<strong>and</strong> CO2 back permeation (66). The results showed that the reverse flow technique (in which a

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