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NAMS 2002 Workshop - ICOM 2008

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Membrane Fouling III - RO & Biofouling – 4<br />

Thursday July 17, 4:00 PM-4:30 PM, Maui<br />

Role of Seawater Chemistry in Algal Biopolymer Fouling of Seawater RO<br />

Membranes<br />

X. Jin (Speaker), University of California Los Angeles, Los Angeles, California, USA -<br />

jinxuesky@ucla.edu<br />

E. Hoek, University of California Los Angeles, Los Angeles, California, USA<br />

A major fouling concern in seawater reverse osmosis (SWRO) plants is the<br />

increased biomass generated during algal blooms. Algae, bacteria, and their<br />

exudates are present in high concentrations, and thus, have the potential to foul<br />

RO membranes. Although, membrane fouling by colloids and dissolved organics<br />

has been studied extensively for brackish and wastewater applications, fouling<br />

behavior may be very different in seawater due to the high ionic strength and<br />

suppression of electrical double layer interactions. We hypothesize that short-<br />

range interfacial interactions will play a critical role in determining the rate and<br />

extent of SWRO membrane fouling and that seawater chemistry will strongly<br />

impact foulant-membrane interfacial interactions. As a first step towards<br />

understanding the role of seawater chemistry in SWRO membrane fouling, we<br />

have conducted a study of SWRO membrane fouling by algal biopolymers.<br />

Commercially available SWRO membranes - FilmTec SWHR (Dow Chemicals,<br />

Minneapolis, MN) and SWC3+ (Hydranautics, Oceanside, CA) - are used as<br />

model SWRO membranes. The two membranes were selected because they<br />

represent a relatively hydrophobic, rough membrane with significant carboxylic<br />

acid functionality at its interface (Hydranautics SWC3+) and a relatively<br />

hydrophilic, smooth membrane with relatively little carboxylic acid functionality at<br />

its interface (FilmTec SWHR). The former is expected to be more fouling prone<br />

due to attractive acid-base interactions and its rough, carboxylic acid rich<br />

interface. The latter membrane is expected to be relatively resistant to fouling<br />

due to repulsive acid-base interactions and its relatively smooth, non-<br />

carboxylated interface.<br />

Accelerated fouling experiments are carried out in a bench-scale SWRO<br />

simulator with 6 parallel flat-sheet membrane cells. Alginic acid - an acidic<br />

hetero-polysaccharide excreted by Brown algae - is spiked into synthetic<br />

seawater solutions with constant total dissolved solid (TDS) concentrations of 32<br />

g/L, but varied concentrations of major cations (e.g., sodium, magnesium,<br />

calcium). In addition, a real seawater matrix (Instant Ocean®) was also<br />

evaluated. Water flux and conductivity rejection are tracked with time. At the end<br />

of fouling experiments, cleaning is performed first using laboratory de-ionized<br />

(DI) water, followed by a 5 mM EDTA solution adjusted to pH 11 by NaOH

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