Membranes reverse osmotic

Reverse Osmosis. Osmosis is the flow of solvent through a semipermeable membrane, from a dilute solution to a concentrated solution. This flow results from the driving force created by the difference in pressure between the two solutions. Osmotic pressure is the pressure that must be added to the concentrated solution side to stop the solvent flow through the membrane. Reverse osmosis is the process of reversing the flow, forcing water through a membrane from a concentrated solution to a dilute solution to produce pure water. Figure 2 illustrates the processes of osmosis and reverse osmosis. 

Electron Microscopy of Cellulose Acetate Reverse-Osmotic Membranes by Means of the Improved Replication Method... 

It is the rate of separation rather than the efficiency of salt retention that is the primary practical issue in the development of reverse osmosis desalination. In addition to a variety of other factors, the rate of reverse osmotic flow depends on the excess pressure across the membrane. Therefore the problem of rapid flow is tied into the technology of developing membranes capable of withstanding high pressures. The osmotic pressure of sea water at 25 °C is about 25 atm. This means that no reverse osmosis will occur until the applied pressure exceeds this value. This corresponds to a water column about 840-ft high at this temperature. 

P. Meares, On the Mechanism of Desalination by Reversed Osmotic Flow Through Cellulose Acetate Membrane, Eur. Polym. J. 2, 241 (1966). 

Osmosis involves the transfer, by a concentration gradient, of a solvent through a membrane into a mixture of solute and solvent. The membrane is almost non-permeable to the solute. In reverse osmosis, transport of solvent in the opposite direction is effected by imposing a pressure, higher than the osmotic pressure, on the feed side. Using a non-porous membrane, reverse osmosis successfully desalts water. 

Concentration polarization caused by macromolecules, which may induce a reversible osmotic pressure that disappears after the filtration pressure is released, and the adsorption on the membrane pores of solid materials or inside the membrane pores of solid materials, which are rid of by rinsing the membrane after the filtration process, are occurrences that both contribute to the reversible resistance to permeation, 7 rev On the other hand, the solids that are deposited on the membrane surface or inside the pores, which are removed only by chemical cleaning of the membrane, constitute the irreversible fouling, Rmev-... 

Reverse osmosis (RO) is a membrane-based process that is used to remove solutes of relatively low molecular weight that are in solution. As an example, almost pure water can be obtained from sea water by using RO, which will filter out molecules of NaCl and other salts. The driving potential for water permeation is the difference in hydraulic pressure. A pressure that is higher than the osmotic pressure of the solution (which itself could be quite high if the molecular weights of the solutes are small) must be applied to the solution side of the membrane. Reverse osmosis also involves the concentration polarization of solute molecules. 

The flow of water through a reverse osmosis membrane is primarily dependent on the applied pressure differential and the osmotic pressure differential across the membrane. The osmotic pressure is directly dependent on the salt concentration of the process stream. As a rule of thumb, each 100 mg/ of dissolved solids is roughly equivalent to one psi of osmotic pressure. Since the product stream usually has a very low salt content, the osmotic pressure of that stream is negligible. In addition, the product stream normally leaves the reverse osmosis pressure vessels at near atmospheric pressure so that the applied pressure differential is the feed pressure. Consequently, the term "net applied pressure" has come to mean the applied pressure minus the feed osmotic pressure. 

Reverse osmosis is the inverse of natural osmosis under pressure. Osmosis is the solvent flow from a more dilute solution toward a more concentrated one through a semi-permeable membrane. The process is driven by the osmotic pressure of the concentrated solution, which depends on the chemical identities of the solvent and the dissolved substance, as well as on their ratio. If the external pressure acting on the more concentrated solution is higher than its osmotic pressure, reverse osmosis, i.e. a solvent flow toward the more diluted solution happens through the membrane. Reverse osmosis is most commonly known for its use in drinking water purification from seawater, removing the salt and other effluent materials from the water molecules. 

When a solution containing solutes and only one solvent is set up across a semipermeable membrane, an osmotic pressure occurs. When a higher pressure than this osmotic pressure is applied on the side of the solution, only the solvent in the solution can be permeated from the solution side to the solvent through the semipermeable membrane and a solute in the solution can be rejected by the semipermeable membrane, as shown in Figure 34.3. This membrane-separation technique is called reverse osmosis and is applied for the desalination of seawater and brackish water. 

Here z is the electrochemical valence, F is the Faraday constant, Q is the feed solution flow rate, Ac is the difference in concentration between the feed and product solution, and is the current utilization factor. The current utilization factor is always less than 100% because of losses in the stack. Because the membranes are not perfectly semipermeable, some co-ions diffuse across the membrane. Some water is also transferred across the membrane by osmotic flow. Finally, some current flows through the stack manifold and is dissipated as electrical heating. Nonetheless, electrodialysis uses significantly less energy than competitive processes such as evaporation or reverse osmosis, especially for low concentration feed solutions. 

Arai, S. and Akiya, F. (1978). Desalination reverse osmotic membranes and their preparation, U.S. Patent, 4111810. 

In open fibers the fiber wall may be a permselective membrane, and uses include dialysis, ultrafiltration, reverse osmosis, Dorman exchange (dialysis), osmotic pumping, pervaporation, gaseous separation, and stream filtration. Alternatively, the fiber wall may act as a catalytic reactor and immobilization of catalyst and enzyme in the wall entity may occur. Loaded fibers are used as sorbents, and in ion exchange and controlled release. Special uses of hoUow fibers include tissue-culture growth, heat exchangers, and others. 

The pressure difference between the high and low pressure sides of the membrane is denoted as AP the osmotic pressure difference across the membrane is defined as Att the net driving force for water transport across the membrane is AP — (tAtt, where O is the Staverman reflection coefficient and a = 1 means 100% solute rejection. The standardized terminology recommended for use to describe pressure-driven membrane processes, including that for reverse osmosis, has been reviewed (24). 

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). 

Concentration of Seawater by ED. In terms of membrane area, concentration of seawater is the second largest use. Warm seawater is concentrated by ED to 18 to 20% dissolved soHds using membranes with monovalent-ion-selective skins. The EDR process is not used. The osmotic pressure difference between about 19% NaCl solution and partially depleted seawater is about 20,000 kPa (200 atm) at 25°C, which is well beyond the range of reverse osmosis. Salt is produced from the brine by evaporation and crystallisa tion at seven plants in Japan and one each in South Korea, Taiwan, and Kuwait. A second plant is soon to be built in South Korea. None of the plants are justified on economic grounds compared to imported solar or mined salt. 

Membrane Pervaporation Since 1987, membrane pei vapora-tion has become widely accepted in the CPI as an effective means of separation and recovery of liquid-phase process streams. It is most commonly used to dehydrate hquid hydrocarbons to yield a high-purity ethanol, isopropanol, and ethylene glycol product. The method basically consists of a selec tively-permeable membrane layer separating a liquid feed stream and a gas phase permeate stream as shown in Fig. 25-19. The permeation rate and selectivity is governed bv the physicochemical composition of the membrane. Pei vaporation differs From reverse osmosis systems in that the permeate rate is not a function of osmotic pressure, since the permeate is maintained at saturation pressure (Ref. 24). 

You should remember that RO uses a semi-permeable membrane. As such, the membrane is permeable to only very light molecules like water. Under atmospheric condirtions the fresh water flows into the solution which is called osmotic flow. But for purification purposes, this is no use, and hence we employ the reverse of osmotic flow. For this to happen, we need to apply external pressure in excess of osmotic pressure. The osmotic pressure is given by ... 

Reverse Osmosis. The process of osmosis is used by plants to obtain food and moisture from the soil. The density of the sap in the roots of the plant is greater than that of the soil water surrounding it. The root wall provides a semipermeable membrane, and the difference in suction across it is the osmotic pressure. 

In reverse osmosis, the osmotic pressure is increased manually to get the water to flow from a high-density area through a semipermeable membrane to the lower-density weaker solution. The water will pass through the membrane and leave the solids behind. A pressure of about 2.76 MPa will extract 90% or more of the dissolved absorbed solids further refinement may be achieved through a base exchange process. 

The most important application of semi-permeable membranes is in separations based on reverse osmosis. These membranes generally have pores smaller than 1 nm. The pressure across the semi-permeable membranes for reverse osmosis is generally much larger than those for ultrafiltration, for example. This is because reverse osmosis is usually used for small molecules which have a much higher osmotic pressure, because of the higher number density, than the colloids separated in ultrafiltration. As a result reverse osmosis membranes have to be much more robust than ultrafiltration membranes. Since the focus of our discussion in this chapter will be on reverse osmosis based separations, we will describe these membranes in greater detail. 

The semi-permeable membrane is the heart of the reverse osmosis separation process. Semi-permeable membranes for reverse osmosis are broadly divided into two types. The earhest practical membrane was of the asymmetric type [3-6]. It consisted of an osmotically active surface layer with very small pores (less than 1 nm) with a thickness of 30-100 nm. This layer was physically supported on a porous substructure, whose porosity increased with distance from the surface layer. In such a membrane, the... 

An alternative method of purifying water is by reverse osmosis. Under normal conditions, if an aqueous solution is separated by a semi-permeable membrane from pure water, osmosis will lead to water entering the solution to dilute it. If, however, sufficient pressure is applied to the solution, i.e. a pressure in excess of its osmotic pressure, then water will flow through the membrane from the solution the process of reverse osmosis is taking place. This principle has been... 

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