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Membrane and Desalination Technologies - TCE Moodle Website

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

construction so that the waste heat from the facilities can be properly h<strong>and</strong>led <strong>and</strong> the water<br />

pollution is minimized. For the newly built distillation systems, the thermal discharge is not a<br />

major concern because brine water with high temperatures is cooled by the raw feed water.<br />

2.7.2. Materials for Construction<br />

The corrosive nature of high-temperature brines, acid pretreatments, <strong>and</strong> chemical scaling<br />

can cause plant failure. Presently, the only acceptable construction materials for wetted<br />

surfaces in high-temperature systems are an austenitic stainless steel. Anodized aluminum<br />

<strong>and</strong> many thermoplastic materials are acceptable for use in low-temperature systems.<br />

2.7.3. Energy for Operation<br />

Operation of distillation is mainly energy driven. The crude oil prices have increased by<br />

almost 100% in the last 2 years. It is, therefore, important to consider the energy cost for<br />

operations <strong>and</strong> a sound forecast of the same is essential.<br />

2.7.4. Characteristics of Raw Water<br />

The important parameters of raw water are TDS, salt contents, organic contents (TOC),<br />

<strong>and</strong> temperature. The availability of raw water is also important.<br />

2.7.5. Final Disposal of Waste Brine<br />

The waste brine has high temperatures <strong>and</strong> TDS. Thus, it must be properly treated before it<br />

is discharged to nearby waters. Cooling <strong>and</strong> IX are recommended for its treatment.<br />

3. ELECTRODIALYSIS<br />

3.1. Introduction<br />

ED was commercially introduced in the early 1960s, about 10 years before the introduction<br />

of RO. The development of ED provides a cost-effective technology to remove salt from<br />

seawater. ED is also used in water <strong>and</strong> wastewater treatment, food processing, <strong>and</strong> chemical<br />

<strong>and</strong> pharmaceutical manufacturing.<br />

In ED, ionic components are removed from aqueous solutions through the IX membranes<br />

using the driving force of an electric field. The membrane is selective <strong>and</strong> semipermeable <strong>and</strong><br />

it only allows the passage of either the anions or the cations. The separation is because of the<br />

nature of charged substances rather than the difference in their sizes. In seawater desalination,<br />

the dissolution of salt leads to the formation of positively charged cations such as Na + ,Ca 2+ ,<br />

<strong>and</strong> Mg 2+ <strong>and</strong> negatively charged anions such as Cl - . The cations <strong>and</strong> the anions are attracted<br />

to the cathode <strong>and</strong> the anode, respectively, which are subsequently removed. As a result, the<br />

water after treatment carries less ionic substances. A typical electrodialysis plant operates at<br />

50–90% conversion <strong>and</strong> this conversion value is determined by the brine recirculation rate.<br />

An ED system can operate over a wide pH range (pH 1.0–13.0) as well as a wide temperature<br />

range (up to 43 C). The cost for O&M of ED (EDR) is slightly higher than that for RO.<br />

The drawback of this process is that the surfaces of membranes can be easily fouled. Thus,<br />

a modified process of EDR was developed. By intermittently reversing the polarity, the

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