Reverse osmosis membrane seawater desalination

Although the principal appHcation of reverse osmosis membranes is still desalination of brackish water or seawater to provide drinking water, a significant market is production of ultrapure water. Such water is used in steam boilers or in the electronics industry, where huge amounts of extremely pure water with a total salt concentration significantly below 1 ppm are required to wash siUcon wafers. 

Reverse osmosis processes for desalination were first appHed to brackish water, which has a lower I DS concentration than seawater. Brackish water has less than 10,000 mg/L IDS seawater contains greater than 30,000 mg/L IDS. This difference in IDS translates into a substantial difference in osmotic pressure and thus the RO operating pressure required to achieve separation. The need to process feed streams containing larger amounts of dissolved soHds led to the development of RO membranes capable of operating at pressures approaching 10.3 MFa (1500 psi). Desalination plants around the world process both brackish water and seawater (15). 

Reverse osmosis membrane process, 27 637 Reverse osmosis membrane cleaning citric acid application, 6 647 Reverse-osmosis membranes, 75 811, 825 development of, 75 797 Reverse osmosis models, 27 638-639 Reverse osmosis permeators, 76 19 Reverse osmosis seawater desalination process, 26 85 Reverse osmosis systems blending in, 26 80-81 brackish and nanofiltration, 26 80-83 Reverse osmosis technology... 

Albany International Research Co. has developed an advanced hollow fiber composite reverse osmosis membrane and module under the name of Quantro II . This composite membrane is comprised of a porous hollow fiber substrate on which has been deposited a rejection barrier capable of fluxes of commercial importance at high rejection of dissolved salts at elevated temperatures. Resistance to active chlorine has been demonstrated. Proprietary processes have been developed for spinning of the fiber, establishment of the rejection barrier and processing of the fiber to prepare modules of commercial size. Prototype modules are currently in field trials against brackish and seawater feed solutions. Applications under consideration for this membrane include brackish and seawater desalination as well as selected industrial concentration processes. 

R.E. Larson, J.E. Cadotte and R.J. Petersen, The FT-30 Seawater Reverse Osmosis Membrane-element Test Results, Desalination 38, 473 (1981). 

A number of membrane materials and membrane preparation techniques have been used to make reverse osmosis membranes. The target of much of the early work was seawater desalination (approximately 3.5 wt% salt), which requires membranes with salt rejections of greater than 99.3 % to produce an acceptable permeate containing less than 500 ppm salt. Early membranes could only meet... 

The reverse-osmosis membrane process is considered universally as the most promising technology for brackish and seawater desalination [18]. Potential directions for reducing desalination costs may be deduced by analyzing the cost of the components. 

Reverse osmosis membranes can be divided into subclasses according to their solute/water selectivity and operating pressure regimes. Figure 30 shows a number of commercial membranes developed for seawater and brackish desalination, and for nanofiltration. These include cellulose ester and polyamide asymmetric membranes available since the 1960s, and high-performance composite membranes developed in the 1970s. Collectively, they make it possible to produce potable water from virtually all saline water sources. 

FIGURE 30 Performance of some commercial reverse osmosis membranes for (a) seawater desalination (test conditions 56 bar 25°C 3.5% NaCI feed) (b) low-pressure desalination (15 bar 25°C 1500 mg/liter NaCI feed) and (c) ultralow-pressure nanofiltration applications (7.5 bar, 25°C 500 mg/liter NaCI feed). 

S. Ebrahim and H. El-Dessouky, Evaluation of commercial cleaning agents for seawater reverse osmosis membranes. Desalination 99, 169-188 (1994). 

Reverse osmosis membrane is widely used in seawater and brackish water desalination processes. Compared to traditional distillation, there is no energy-intensive phase change involved in membrane processes. Therefore, desalination with RO membrane is more energy efficient. In addition to the traditional desalination processes, RO membranes have also found wide application in industrial and municipal wastewater treatment, in pure water production for the electronic and pharmaceutical industries, and in the food industries. 

As of the end of 1984, the desalination of brackish water accounted for 82% of capacity. This is due to the fact that early reverse osmosis membranes were incapable of single stage seawater desalination and, thus, they were limited to brackish water desalination. Within the last 10 years, significant advances have been made in both the flux and rejection capability of membranes and reverse osmosis is technically able to desalt seawater in a single stage. In the recent past, it has been an effective competitor to the distillation process in seawater desalination. In fact, reverse osmosis is now beginning to replace existing distillation capacity in the Middle East.4... 

The PA-300 membrane was the first composite reverse osmosis membrane to be used successfully in a major seawater desalination facility-the 3.2 MGD plant at Jeddah, Saudi Arabia.35 Much of the original membrane in this plant, as well as replacement membrane, is believed to be RC-100 (the TDI-based analog) because of its greater stability and retention of salt rejection. The Jeddah plant was truly a pioneer installation for spiral-wound composite membranes. Even though it was attended by a variety of start-up and operating problems, mostly unrelated to the membranes,36 it continues to operate successfully at this date. 

Applications for FT-30 membrane have appeared in all reverse osmosis fields from seawater desalination to home tapwater systems operating on line pressure. At this date, it is the only commercial reverse osmosis membrane other than cellulose acetate that has specific FDA approval for food contact usage.63 Versions of this membrane, manufactured under license to FilmTec, are available in tubular form (ZF-99, Patterson Candy International) and plate-and-frame design (HR-95, HR-98, De Danske Sukkerfabrikker).64 65... 

Figure 5.16, adapted from Kurihara,79 80 shows a comparison of several types of commercial reverse osmosis membranes in terms of salt rejection and permeate flow rate under seawater test conditions (35,000 ppm, 800 psi, 25°C). This chart emphasizes the capability of PEC-1000 to provide complete single-stage seawater desalting. In a test at Toray s Ehime desalination test facility on 42,000 ppm seawater (equivalent to Red Sea salinity), PEC-1000 spiral elements operated at 35% recovery produced a permeate having an average salinity of only 220 ppm, well below WHO standards. Average salt rejection was 99.5%. 

V. Murugan, K. Rajanbabu, S.A. Tiwari, C. Balasubramanian, M.K. Yadav, A.Y. Dangore, S. Prabhakar, P.K.Tewari, Fouling and cleaning of seawater reverse osmosis membranes in Kalpakkam nuclear desalination plant, Int. J. Nucl. Desal. 2,2006,172-178. 

J.E. Cadotte, R.J. Petersen, R.E. Larson, E. E. Erickson, A new thin-film composite seawater reverse osmosis membrane. Desalination 32 (1980) 25. 

Kim SG, Hyeon DH, Chun JH, Chun BH, Kim SH. Nanocomposite poly(arylene ether sulfone) reverse osmosis membrane containing functional zeolite nanoparticles for seawater desalination. J Membr Sci 2013 443 10-8. 

Vial D and Doussau G (2002), The use of microfiltration membranes for seawater pre-treatment prior to reverse osmosis membranes , Desalination, 153, 141-147. 

One immediate drawback of desalination is that the process requires huge amounts of energy. Desalination expenses are about five times that of filtering freshwater. The techniques that have been tried include heat distillation, chemical (ion exchange) or electrical (ion removal) procedures, freezing, solar humidification, and reverse osmosis (forcing seawater through a semipermeable membrane). 

The mixture seems to be suitable to produce reverse osmosis membranes for seawater desalination. 

Cellulose acetate membranes developed by Loeb and Sourirajan for the purpose of seawater desalination continue to be useful in various membrane applications, despite the development of new membrane materials and new membrane preparation techniques. Because of its historical importance, the casting method of the first successful reverse osmosis membrane is described below in detail. 

Matin, Asif, Z. Khan, S. M. J. Zaidi, and M. C. Boyce, Biofouling in Reverse Osmosis Membranes for Seawater Desahnation Phenomena and Prevention, Desalination, 281,1-16,2011. 

Fadhillah, F. Application of polyelectrolyte multilayer reverse osmosis membrane in seawater desalination. PhD thesis. King Fahd University of Petroleum and Minerals (2012)... 

Hiro, A., and Hirose, M. (2000). Development of the high boron removal reverse osmosis membrane element for seawater desalination. Nitto Giho 40, 36. 

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