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Membrane and Desalination Technologies - TCE Moodle Website

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<strong>Desalination</strong> of Seawater by Reverse Osmosis 595<br />

Table 13.6<br />

Water production cost (1996) (65)<br />

Items Cost (USD/1,000 gal)<br />

Sulfuric acid (130 ppm) 0.03<br />

Scale inhibitor (3 ppm [Flocon-100]) 0.03<br />

Chlorine (10 ppm) 0.01<br />

Sodium hydroxide (40 ppm) 0.03<br />

Electricity power 0.34<br />

Labor cost 0.19<br />

Miscellaneous 0.1<br />

Total 0.73<br />

6. RECENT ADVANCES IN RO TECHNOLOGY FOR SEAWATER<br />

DESALINATION<br />

<strong>Desalination</strong> is becoming popular because of the decrease in reliable water sources <strong>and</strong><br />

increase in the global population. The total desalination capacity of the world is estimated to be<br />

40 million m 3 /day (70), whereas the seawater desalination accounts for 24.5 million m 3 /day<br />

(71). As discussed earlier, RO technology is one of the widely using seawater desalination<br />

technologies. In order to meet the dem<strong>and</strong>, RO technology has to be improved in many<br />

aspects, <strong>and</strong> deficiencies in the technology must be minimized. Recent developments in the<br />

field of RO desalination of seawater to avoid the deficiencies are discussed in this section.<br />

About 70% of the operating cost of seawater RO desalination is the energy cost (72). On<br />

the contrary, energy is as important as water <strong>and</strong> is becoming scarce. Therefore, energy<br />

recovery devices <strong>and</strong> alternative energy sources receive the attention of the scientific community.<br />

Energy recovery devices discussed earlier in this chapter are modified further in<br />

recent studies. A novel “fluid switcher” is introduced to the energy recovery devices. It is said<br />

that the hydraulic recovery efficiency is increased to 76.83% after the introduction of the<br />

“fluid switcher” (73). Alternative renewable energy sources are evaluated for the seawater<br />

RO desalination, especially for the small communities in rural areas where electricity is not<br />

available. A plant with capacity of 20 m 3 /day was evaluated for the possibilities of using<br />

photovoltaic (PV) array as the energy source. Modeling study showed that the solar-driven<br />

plant is a favorable energy option compared to a fully diesel-driven or diesel-assisted PV-RO<br />

plant (74). In another study, solar organic rankine cycle engines are proposed for a plant with<br />

a capacity of 15 m 3 /day (75). Wave energy is another option proposed for small-scale<br />

seawater RO desalination plants. RO plant with a pressure exchanger intensifier <strong>and</strong> with<br />

specific energy consumption less than 2 kWh/m 3 was recognized as the promising location<br />

where the wave energy can be utilized (76). Possibility of use of the energy from fuel cells<br />

(77), PV energy (78), <strong>and</strong> hydrostatic pressure (79) was evaluated as well.<br />

Attention has been paid to improving the recovery of the RO membrane. A high recovery<br />

seawater RO desalination system has been developed in Japan. The system is based on two

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