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Reverse Osmosis Water Purification Systems
Reverse Osmosis is common water purification process for large filtration systems. Often, commercial and industrial water filtration systems will utilise a reverse osmosis process to ensure high compliance with water testing. Reverse osmosis can be a difficult process to understand, this page will cover of what the process entails, how it works, and the areas where reverse osmosis is most effective. We have also included a list of common terminology as well.
What is Osmosis
Osmosis is a process common in biological systems. It results in water from a dilute solution that passes through a semi-permeable membrane into a more concentrated solution on the other side. Energy is released in the process. This is counterproductive to the requirements of desalination where we require the reverse to occur, i.e., we need fresh water to pass out of the concentrated solution and to accumulate on the other side of the membrane where we may collect and utilise it. A reversed process needs the input of energy. The process is called reverse osmosis, commonly abbreviated to R.O.
Reverse osmosis achieves separation of dissolved salts and impurities from water solutions using pressure exerted on a semi-permeable membrane. The passage of dissolved materials (solutes) through the membrane is resisted. The membrane materials� chemical structure though, allows the potable water to permeate through relatively easily. Salts along with other impurities that build up on the feed side of the membrane are continuously flushed away. This is a more concentrated solution called the Concentrate or Reject. The purified water called the Permeate is meanwhile drawn off for use.
The diagram below shows a vessel with two compartments separated by a semipermeable membrane. On one side of the membrane, we have potable water or a very dilute solution. A more concentrated salt solution is on the other side.
Through the semi permeable membrane, water will pass into the concentrated solution from the purer solution. The level will increase on the right and fall on the left.
You place a limp lettuce leaf into cold water to make it crisp. The fresh water from the outside permeates through the leaf cell�s natural semi-permeable membrane into the slightly salty solution inside the cell. The pressure in each tiny cell makes it taut and the leaf becomes crisp once again.
Let us consider the situation where seawater, containing 36,000 ppm of salts, is in the right hand compartment and potable water in the left. In a short time, a pressure of about 2600 kPa (i.e. about 360 psi) would be registered on the gauge. It may be hard to visualise, but this pressure would in fact develop spontaneously in the apparatus shown, and so we say that the osmotic pressure of seawater is about 2600 kPa. If we wanted to produce fresh water from the seawater in this apparatus, we could mechanically apply in excess of 2600 kPa to the right hand chamber to push the fresh water out of the seawater through the membrane. In fact, a typical reverse osmosis seawater desalinator uses 5-7000 kPa (i.e. up to 1000 psi) to do just this. Excess pressure over the osmotic pressure is used to overcome the membrane�s natural flow resistance.
Practically, the osmotic pressure of salt water may be regarded as directly proportional to the salt concentration. It means if the seawater in the above illustration was diluted 50/50 with fresh water, the osmotic pressure would fall to 1300 kPa, or half that of undiluted seawater. Conversely, the osmotic pressure doubles when the concentration of salt doubles. Therefore the lower the salt content of the water, the easier it is (i.e., the lower the pressure required) to desalinate it.
Configuration of Practical Reverse Osmosis Systems
General Flow Schematic
The process described previously would not be a practical proposition, as the salt concentration would quickly rise in the right hand chamber (see fig. 3) as a result of the fresh water passing out to the left and leaving the salt behind. This would lead to higher osmotic pressure to be overcome by the piston to sustain the flow. The process would quickly stop when the osmotic pressure reached the applied pressure.
One could stop the process, empty out the concentrated seawater and replace it with more untreated seawater before repeating the procedure. This would be a cumbersome process and in practice, reverse osmosis is conducted as in figure 4.
Salt water is supplied to the high-pressure pump as Feed Water (F). From here, it is forced through the chamber (C) and out through the let-down value (L) which is set to maintain the necessary operating pressure of the system. In the case of seawater desalination, this valve would be adjusted to maintain about 6000 kPa in the chamber C.
When passing along the chamber (C), some of the water goes through the membrane into the chamber (P) as desalinated product (permeate). This leaves the salt behind. The salt concentration of the feed water increases as it passes from (F) to (L) from where it is continuously directed to waste. It carries the concentrated salts and impurities with it. This flow is called either the Concentrate or Reject.
The actual proportion of fresh water removed from the salt water feed depends on the design of the machine. The type and quality of the salt water being processed are also factors. Recovery Ratio is the ratio of the permeate flow rate to the feed flow rate. It varies from about 20% to 80%.
Some Important Terms
Before proceeding, you should become familiar with the following terms, which are used fairly consistently throughout the industry:
PERMEATE The desalinated water is called the permeate, because it has permeated through the membrane. Also called PRODUCT.
CONCENTRATE The discharge to waste is called the concentrate because it has been concentrated as it passes along the chamber (C). This discharge is also called the REJECT.
FEED The flow entering the membrane from the high pressure pump is called the feed.
SYSTEM PRESSURE The operating pressure of the system, the pressure inside chamber (C), is called the system pressure. It is also sometimes called the feed pressure but this is confusing as feed pressure is more commonly applied to the pressure BEFORE the high-pressure pump.
LETDOWN VALVE The valve (L) is called the letdown valve because it is here that the system pressure is "let down" to atmospheric pressure again.
RECOVERY RATIO The ratio of permeate flow rate to feed flow rate is called the recovery ratio because it denotes the proportion of product water recovered from the feed. It is usually expressed as a percentage.
REJECTION RATIO This is the percentage reduction of salt in the permeate with respect to the feed supply. For example, a permeate of TDS 200 from a feed supply of TDS 10,000 would be referred to as a rejection of 98%. It is dependent on both the membrane itself and the RO system design in general.
The first question that may spring to mind is, how does the thin semi-permeable membrane withstand the high pressures that we have been considering? A number of different techniques have been used to do this, but at this stage we will consider in detail only the most common configuration presently used, the Spiral Wound configuration.
It is perhaps easiest to visualise the spiral wound configuration by considering the membrane material as a sheet having been made into a bag, similar to an ordinary plastic bag but with a lip like a letter envelope. Consider now a sheet of thick, porous fabric inserted into the bag and the lip sealed around a tube that contains a number of small holes drilled in it as in fig. 5.
Imagine the entire representation depicted in fig. 5b now being placed into a pressure resistant closed box with the ends of the permeate tube protruding from and sealed into the box wall. If we were to now pump salt water into this box, we can see that the water would exert equal pressures on both sides of the membrane bag so that it would be evenly supported. Permeate would pass through the membrane into the porous permeate carrier and flow through the carrier to the permeate tube. It would then pass through the perforations in the tube and out of the box through the permeate tube itself.
Because such a configuration would require a lot of space and a large pressure vessel, the representation of fig. 5b is rolled into a spiral something like a Swiss roll so that a cylindrical pressure vessel can be used, which is compact and relatively cheap. A sheet of coarse mesh is rolled up with it to act as a spacer and prevent the two membrane surfaces from coming into contact and restricting water flow. The result is depicted in figure 6; the space between the membranes in which the mesh spacer lies constitutes the schematically represented chamber (C) in figure 4.
The concentrate spacer also acts to promote turbulence in the feed flow which in turn tends to discourage the deposition of scale and other fouling materials on the membrane surface.
Turbulent flow over the membrane is also important for another reason. As we have seen, removal of the fresh water from the feed results in a concentration of the salts in the remaining solution. This concentration is most pronounced at the membrane surface, as this is the area where the desalination process takes place. This means that the membrane is called upon to desalinate water of higher salinity than is necessary. Turbulence helps to disperse this concentrated layer into the more dilute bulk of the feed flow.
Using this general configuration, large surface areas of the membrane can be formed relatively cheaply into the membrane elements. Several of these elements can be fitted into a pressure vessel made of fibreglass pipe, which is corrosion resistant and strong. The most common size for these elements is 4 inches diam. and 40 inches long. They are also available in 2.5, 6, 8 and 11-inch diameter sizes.