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Desalination is a process that takes away mineral components from saline water. More generally, desalination refers to the removal of salts and minerals from a target substance, as in soil desalination, which is an issue for agriculture. Saltwater (especially sea water) is desalinated to produce water suitable for human consumption or irrigation. The by-product of the desalination process is brine. Desalination is used on many seagoing ships and submarines. Most of the modern interest in desalination is focused on cost-effective provision of fresh water for human use. Along with recycled wastewater, it is one of the few rainfall-independent water resources.
Due to its energy consumption, desalinating sea water is generally more costly than fresh water from surface water or groundwater, water recycling and water conservation. However, these alternatives are not always available and depletion of reserves is a critical problem worldwide. Desalination processes are usually driven by either thermal (in the case of distillation) or electrical (in the case of reverse osmosis) as the primary energy types.
|"Making the Deserts Bloom: Harnessing nature to deliver us from drought", Distillations Podcast and transcript, Episode 239, March 19, 2019, Science History Institute|
There are approximately 16,000 operational desalination plants, located across 177 countries, which generate an estimated 95 million m3/day of freshwater. Currently, desalination accounts for about one percent of the world's drinking water. Desalination is particularly prevalent in countries located in the Middle East and North Africa region, such as Saudi Arabia, the UAE, and Kuwait. Kuwait produces a higher proportion of its water through desalination than any other country. Desalination is also an important source of water in small island developing states.
There are now about 21,000 desalination plants in operation around the globe. The biggest ones are in the United Arab Emirates, Saudi Arabia and Israel. The world's largest desalination plant is located in Saudi Arabia (Ras Al Khair) with a capacity of 1,401,000 cubic meters per day.
Desalination is currently expensive compared to most alternative sources of water, and only a very small fraction of total human use is satisfied by desalination. It is usually only economically practical for high-valued uses (such as household and industrial uses) in arid areas. However, there is growth in desalination for agricultural use, and highly populated areas such as Singapore or California. The most extensive use is in the Persian Gulf.
While noting costs are falling, and generally positive about the technology for affluent areas in proximity to oceans, a 2004 study argued, "Desalinated water may be a solution for some water-stress regions, but not for places that are poor, deep in the interior of a continent, or at high elevation. Unfortunately, that includes some of the places with biggest water problems.", and, "Indeed, one needs to lift the water by 2000 m, or transport it over more than 1600 km to get transport costs equal to the desalination costs.
Thus, it may be more economical to transport fresh water from somewhere else than to desalinate it. In places far from the sea, like New Delhi, or in high places, like Mexico City, transport costs could match desalination costs. Desalinated water is also expensive in places that are both somewhat far from the sea and somewhat high, such as Riyadh and Harare. By contrast in other locations transport costs are much less, such as Beijing, Bangkok, Zaragoza, Phoenix, and, of course, coastal cities like Tripoli." After desalination at Jubail, Saudi Arabia, water is pumped 320 km inland to Riyadh. For coastal cities, desalination is increasingly viewed as a competitive choice.
|Water desalination |
Desalination is an artificial process by which saline water (generally sea water) is converted to fresh water. The most common desalination processes are distillation and reverse osmosis.
There are several methods. Each has advantages and disadvantages but all are useful. The methods can be divided into membrane-based (e.g., reverse osmosis) and thermal-based (e.g., multistage flash distillation) methods. The traditional process of desalination is distillation, i.e. boiling and re-condensation of seawater to leave salt and impurities behind.
Solar distillation mimics the natural water cycle, in which the sun heats sea water enough for evaporation to occur. After evaporation, the water vapor is condensed onto a cool surface. There are two types of solar desalination. The former one is using photovoltaic cells which converts solar energy to electrical energy to power the desalination process. The latter one utilises the solar energy in the heat form itself and is known as solar thermal powered desalination.
Water can evaporate through several other physical effects besides solar irradiation. These effects have been included in a multidisciplinary desalination methodology in the IBTS Greenhouse. The IBTS is an industrial desalination (power)plant on one side and a Greenhouse operating with the natural water cycle (scaled down 1:10) on the other side. The various processes of evaporation and condensation are hosted in low-tech utilities, partly underground and the architectural shape of the building itself. This integrated biotectural system is most suitable for large scale desert greening as it has a km2 footprint for the water distillation and the same for landscape transformation in desert greening, respectively the regeneration of natural fresh water cycles.
In vacuum distillation atmospheric pressure is reduced, thus lowering the temperature required to evaporate the water. Liquids boil when the vapor pressure equals the ambient pressure and vapor pressure increases with temperature. Effectively, liquids boil at a lower temperature, when the ambient atmospheric pressure is less than usual atmospheric pressure. Thus, because of the reduced pressure, low-temperature "waste" heat from electrical power generation or industrial processes can be employed.
Multi-stage flash distillation
Water is evaporated and separated from sea water through multi-stage flash distillation, which is a series of flash evaporations. Each subsequent flash process utilizes energy released from the condensation of the water vapor from the previous step.
Multiple-effect distillation (MED) works through a series of steps called "effects". Incoming water is sprayed onto pipes which are then heated to generate steam. The steam is then used to heat the next batch of incoming sea water. To increase efficiency, the steam used to heat the sea water can be taken from nearby power plants. Although this method is the most thermodynamically efficient among methods powered by heat, a few limitations exist such as a max temperature and max number of effects.
Vapor-compression evaporation involves using either a mechanical compressor or a jet stream to compress the vapor present above the liquid. The compressed vapor is then used to provide the heat needed for the evaporation of the rest of the sea water. Since this system only requires power, it is more cost effective if kept at a small scale.
The leading process for desalination in terms of installed capacity and yearly growth is reverse osmosis (RO). The RO membrane processes use semipermeable membranes and applied pressure (on the membrane feed side) to preferentially induce water permeation through the membrane while rejecting salts. Reverse osmosis plant membrane systems typically use less energy than thermal desalination processes. Energy cost in desalination processes varies considerably depending on water salinity, plant size and process type. At present the cost of seawater desalination, for example, is higher than traditional water sources, but it is expected that costs will continue to decrease with technology improvements that include, but are not limited to, improved efficiency, reduction in plants footprint, improvements to plant operation and optimization, more effective feed pretreatment, and lower cost energy sources.
Reverse osmosis uses a thin-film composite membrane, which comprises an ultra-thin, aromatic polyamide thin-film. This polyamide film gives the membrane its transport properties, whereas the remainder of the thin-film composite membrane provides mechanical support. The polyamide film is a dense, void-free polymer with a high surface area, allowing for its high water permeability. A recent study has found that the water permeability is primarily governed by the internal nanoscale mass distribution of the polyamide active layer.
The reverse osmosis process is not maintenance free. Various factors interfere with efficiency: ionic contamination (calcium, magnesium etc.); DOC; bacteria; viruses; colloids and insoluble particulates; biofouling and scaling. In extreme cases, the RO membranes are destroyed. To mitigate damage, various pretreatment stages are introduced. Anti-scaling inhibitors include acids and other agents such as the organic polymers polyacrylamide and polymaleic acid, phosphonates and polyphosphates. Inhibitors for fouling are biocides (as oxidants against bacteria and viruses), such as chlorine, ozone, sodium or calcium hypochlorite. At regular intervals, depending on the membrane contamination; fluctuating seawater conditions; or when prompted by monitoring processes, the membranes need to be cleaned, known as emergency or shock-flushing. Flushing is done with inhibitors in a fresh water solution and the system must go offline. This procedure is environmentally risky, since contaminated water is diverted into the ocean without treatment. Sensitive marine habitats can be irreversibly damaged.
Off-grid solar-powered desalination units use solar energy to fill a buffer tank on a hill with seawater. The reverse osmosis process receives its pressurized seawater feed in non-sunlight hours by gravity, resulting in sustainable drinking water production without the need for fossil fuels, an electricity grid or batteries. Nano-tubes are also used for the same function (i.e., Reverse Osmosis).
Freeze–thaw desalination (or freezing desalination) uses freezing to remove fresh water from salt water. Salt water is sprayed during freezing conditions into a pad where an ice-pile builds up. When seasonal conditions warm, naturally desalinated melt water is recovered. This technique relies on extended periods of natural sub-freezing conditions.
A different freeze–thaw method, not weather dependent and invented by Alexander Zarchin, freezes seawater in a vacuum. Under vacuum conditions the ice, desalinated, is melted and diverted for collection and the salt is collected.
Electrodialysis utilizes electric potential to move the salts through pairs of charged membranes, which trap salt in alternating channels. Several variances of electrodialysis exist such as conventional electrodialysis, electrodialysis reversal.
Forward osmosis uses a semi-permeable membrane to effect separation of water from dissolved solutes. The driving force for this separation is an osmotic pressure gradient, such that a "draw" solution of high concentration.
CETO is a wave power technology that desalinates seawater using submerged buoys. Wave-powered desalination plants began operating on Garden Island in Western Australia in 2013 and in Perth in 2015.
The energy consumption of the desalination process depends on the salinity of the water. Brackish water desalination requires less energy than the seawater desalination. Energy consumption of seawater desalination has reached as low as 3 kWh/m³ including pre-filtering and ancillaries, similar to the energy consumption of other fresh water supplies transported over large distances, but much higher than local fresh water supplies that use 0.2 kWh/m3 or less.
A minimum energy consumption for seawater desalination of around 1 kWh/m3 has been determined, excluding prefiltering and intake/outfall pumping. Under 2 kWh/m3 has been achieved with reverse osmosis membrane technology, leaving limited scope for further energy reductions as the reverse osmosis energy consumption in the 1970s was 16 kWh/m3.
Supplying all US domestic water by desalination would increase domestic energy consumption by around 10%, about the amount of energy used by domestic refrigerators. Domestic consumption is a relatively small fraction of the total water usage.
|Desalination Method >>||Multi-stage Flash MSF||Multi-Effect Distillation MED||Mechanical Vapor Compression MVC||Reverse Osmosis RO|
|Electrical energy (kWh/m3)||4–6||1.5–2.5||7–12||3–5.5|
|Thermal energy (kWh/m3)||50–110||60–110||None||None|
|Electrical equivalent of thermal energy (kWh/m3)||9.5–19.5||5–8.5||None||None|
|Total equivalent electrical energy (kWh/m3)||13.5–25.5||6.5–11||7–12||3–5.5|
Note: "Electrical equivalent" refers to the amount of electrical energy that could be generated using a given quantity of thermal energy and appropriate turbine generator. These calculations do not include the energy required to construct or refurbish items consumed in the process.
Cogeneration is generating excess heat and electricity generation from a single process. Cogeneration can provide usable heat for desalination in an integrated, or "dual-purpose", facility where a power plant provides the energy for desalination. Alternatively, the facility's energy production may be dedicated to the production of potable water (a stand-alone facility), or excess energy may be produced and incorporated into the energy grid. Cogeneration takes various forms, and theoretically any form of energy production could be used. However, the majority of current and planned cogeneration desalination plants use either fossil fuels or nuclear power as their source of energy. Most plants are located in the Middle East or North Africa, which use their petroleum resources to offset limited water resources. The advantage of dual-purpose facilities is they can be more efficient in energy consumption, thus making desalination more viable.
The current trend in dual-purpose facilities is hybrid configurations, in which the permeate from reverse osmosis desalination is mixed with distillate from thermal desalination. Basically, two or more desalination processes are combined along with power production. Such facilities have been implemented in Saudi Arabia at Jeddah and Yanbu.
Alternatives to desalination
Increased water conservation and efficiency remain the most cost-effective approaches in areas with a large potential to improve the efficiency of water use practices. Wastewater reclamation provides multiple benefits over desalination. Urban runoff and storm water capture also provide benefits in treating, restoring and recharging groundwater.
A proposed alternative to desalination in the American Southwest is the commercial importation of bulk water from water-rich areas either by oil tankers converted to water carriers, or pipelines. The idea is politically unpopular in Canada, where governments imposed trade barriers to bulk water exports as a result of a North American Free Trade Agreement (NAFTA) claim.
Factors that determine the costs for desalination include capacity and type of facility, location, feed water, labor, energy, financing and concentrate disposal. Costs of desalinating sea water (infrastructure, energy, and maintenance) are generally higher than fresh water from rivers or groundwater, water recycling, and water conservation, but alternatives are not always available. Desalination costs in 2013 ranged from US$0.45 to US$1.00/m3. More than half of the cost comes directly from energy cost, and since energy prices are very volatile, actual costs can vary substantially.
The cost of untreated fresh water in the developing world can reach US$5/cubic metre.
|Passive solar ( 30.42% energy efficient)||0.034|
|Passive solar (improved single-slope, India)||0.024|
|Passive solar (improved double slope, India)||0.007|
|Multi Stage Flash (MSF)||< 0.001|
|Reverse Osmosis (Concentrated solar power)||0.0008|
|Reverse Osmosis (Photovoltaic power)||0.000825|
|Desalinated Water Cost|
|UN recommended minimum||49||0.05|
In 2014, the Israeli facilities of Hadera, Palmahim, Ashkelon, and Sorek were desalinizing water for less than US$0.40 per cubic meter. As of 2006, Singapore was desalinating water for US$0.49 per cubic meter.
In the United States, cooling water intake structures are regulated by the Environmental Protection Agency (EPA). These structures can have the same impacts to the environment as desalination facility intakes. According to EPA, water intake structures cause adverse environmental impact by sucking fish and shellfish or their eggs into an industrial system. There, the organisms may be killed or injured by heat, physical stress, or chemicals. Larger organisms may be killed or injured when they become trapped against screens at the front of an intake structure. Alternative intake types that mitigate these impacts include beach wells, but they require more energy and higher costs.
The Kwinana Desalination Plant opened in Perth in 2007. Water there and at Queensland's Gold Coast Desalination Plant and Sydney's Kurnell Desalination Plant is withdrawn at 0.1 m/s (0.33 ft/s), which is slow enough to let fish escape. The plant provides nearly 140,000 m3 (4,900,000 cu ft) of clean water per day.
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Desalination processes produce large quantities of brine, possibly at above ambient temperature, and contain residues of pretreatment and cleaning chemicals, their reaction byproducts and heavy metals due to corrosion (especially in thermal-based plants). Chemical pretreatment and cleaning are a necessity in most desalination plants, which typically includes prevention of biofouling, scaling, foaming and corrosion in thermal plants, and of biofouling, suspended solids and scale deposits in membrane plants.
To limit the environmental impact of returning the brine to the ocean, it can be diluted with another stream of water entering the ocean, such as the outfall of a wastewater treatment or power plant. With medium to large power plant and desalination plants, the power plant's cooling water flow is likely to be several times larger than that of the desalination plant, reducing the salinity of the combination. Another method to dilute the brine is to mix it via a diffuser in a mixing zone. For example, once a pipeline containing the brine reaches the sea floor, it can split into many branches, each releasing brine gradually through small holes along its length. Mixing can be combined with power plant or wastewater plant dilution. Furthermore, zero liquid discharge systems can be adopted to treat brine before disposal.
Another possibility is making the desalination plant movable, thus avoiding that the brine builds up into a single location (as it keeps being produced by the desalination plant). Some such movable (ship-connected) desalination plants have been constructed.
Brine is denser than seawater and therefore sinks to the ocean bottom and can damage the ecosystem. Brine plumes have been seen to diminish over time to a diluted concentration, to where there was little to no effect on the surrounding environment. However studies have shown the dilution can be misleading due to the depth at which it occurred. If the dilution was observed during the summer season, there is possibility that there could have been a seasonal thermocline event that could have prevented the concentrated brine to sink to sea floor. This has the potential to not disrupt the sea floor ecosystem and instead the waters above it. Brine dispersal from the desalination plants has been seen to travel several kilometers away, meaning that is has the potential to cause harm to ecosystems far away from the plants. Careful reintroduction with appropriate measures and environmental studies can minimize this problem.
Due to the nature of the process, there is a need to place the plants on approximately 25 acres of land on or near the shoreline. In the case a plant is built inland, pipes have to be laid into the ground to allow for easy intake and outtake. However, once the pipes are laid into the ground, they have a possibility of leaking into and contaminating nearby aquifers. Aside from environmental risks, the noise generated by certain types of desalination plants can be loud.
Desalination removes iodine from water and could increase the risk of iodine deficiency disorders. Israeli researchers claimed a possible link between seawater desalination and iodine deficiency, finding iodine deficits among adults exposed to iodine-poor water concurrently with an increasing proportion of their area's drinking water from seawater reverse osmosis (SWRO). They later found probable iodine deficiency disorders in a population reliant on desalinated seawater. A possible link of heavy desalinated water use and national iodine deficiency was suggested by Israeli researchers. They found a high burden of iodine deficiency in the general population of Israel: 62% of school-age children and 85% of pregnant women fall below the WHO's adequacy range. They also pointed out the national reliance on iodine-depleted desalinated water, the absence of a universal salt iodization program and reports of increased use of thyroid medication in Israel as a possible reasons that the population's iodine intake is low. In the year that the survey was conducted, the amount of water produced from the desalination plants constitutes about 50% of the quantity of fresh water supplied for all needs and about 80% of the water supplied for domestic and industrial needs in Israel.
Other desalination techniques include:
Thermally-driven desalination technologies are frequently suggested for use with low-temperature waste heat sources, as the low temperatures are not useful for many industrial processes, but ideal for the lower temperatures found in desalination. In fact, such pairing with waste heat can even improve electrical process: Diesel generators commonly provide electricity in remote areas. About 40–50% of the energy output is low-grade heat that leaves the engine via the exhaust. Connecting a thermal desalination technology such as membrane distillation system to the diesel engine exhaust repurposes this low-grade heat for desalination. The system actively cools the diesel generator, improving its efficiency and increasing its electricity output. This results in an energy-neutral desalination solution. An example plant was commissioned by Dutch company Aquaver in March 2014 for Gulhi, Maldives.
Originally stemming from ocean thermal energy conversion research, low-temperature thermal desalination (LTTD) takes advantage of water boiling at low pressure, even at ambient temperature. The system uses pumps to create a low-pressure, low-temperature environment in which water boils at a temperature gradient of 8–10 °C (46–50 °F) between two volumes of water. Cool ocean water is supplied from depths of up to 600 m (2,000 ft). This water is pumped through coils to condense the water vapor. The resulting condensate is purified water. LTTD may take advantage of the temperature gradient available at power plants, where large quantities of warm wastewater are discharged from the plant, reducing the energy input needed to create a temperature gradient.
Experiments were conducted in the US and Japan to test the approach. In Japan, a spray-flash evaporation system was tested by Saga University. In Hawaii, the National Energy Laboratory tested an open-cycle OTEC plant with fresh water and power production using a temperature difference of 20 C° between surface water and water at a depth of around 500 m (1,600 ft). LTTD was studied by India's National Institute of Ocean Technology (NIOT) in 2004. Their first LTTD plant opened in 2005 at Kavaratti in the Lakshadweep islands. The plant's capacity is 100,000 L (22,000 imp gal; 26,000 US gal)/day, at a capital cost of INR 50 million (€922,000). The plant uses deep water at a temperature of 10 to 12 °C (50 to 54 °F). In 2007, NIOT opened an experimental, floating LTTD plant off the coast of Chennai, with a capacity of 1,000,000 L (220,000 imp gal; 260,000 US gal)/day. A smaller plant was established in 2009 at the North Chennai Thermal Power Station to prove the LTTD application where power plant cooling water is available.
In October 2009, Saltworks Technologies announced a process that uses solar or other thermal heat to drive an ionic current that removes all sodium and chlorine ions from the water using ion-exchange membranes.
Evaporation and condensation for crops
Adsorption-based desalination (AD) relies on the moisture absorption properties of certain materials such as Silica Gel.
Hydrogel based desalination
The idea of the method is in the fact that when the hydrogel is put into contact with aqueous salt solution, it swells absorbing a solution with the ion composition different from the original one. This solution can be easily squeezed out from the gel by means of sieve or microfiltration membrane. The compression of the gel in closed system lead to change in salt concentration, whereas the compression in open system, while the gel is exchanging ions with bulk, lead to the change in the number of ions. The consequence of the compression and swelling in open and closed system conditions mimics the reverse Carnot Cycle of refrigerator machine. The only difference is that instead of heat this cycle transfers salt ions from the bulk of low salinity to a bulk of high salinity. Similarly to the Carnot cycle this cycle is fully reversible, so can in principle work with an ideal thermodynamic efficiency. Because the method is free from the use of osmotic membranes it can compete with reverse osmosis method. In addition, unlike the reverse osmosis, the approach is not sensitive to the quality of feed water and its seasonal changes, and allows the production of water of any desired concentration.
The United States, France and the United Arab Emirates are working to develop practical solar desalination. AquaDania's WaterStillar has been installed at Dahab, Egypt, and in Playa del Carmen, Mexico. In this approach, a solar thermal collector measuring two square metres can distill from 40 to 60 litres per day from any local water source – five times more than conventional stills. It eliminates the need for plastic PET bottles or energy-consuming water transport. In Central California, a startup company WaterFX is developing a solar-powered method of desalination that can enable the use of local water, including runoff water that can be treated and used again. Salty groundwater in the region would be treated to become freshwater, and in areas near the ocean, seawater could be treated.
The Passarell process uses reduced atmospheric pressure rather than heat to drive evaporative desalination. The pure water vapor generated by distillation is then compressed and condensed using an advanced compressor. The compression process improves distillation efficiency by creating the reduced pressure in the evaporation chamber. The compressor centrifuges the pure water vapor after it is drawn through a demister (removing residual impurities) causing it to compress against tubes in the collection chamber. The compression of the vapor increases its temperature. The heat is transferred to the input water falling in the tubes, vaporizing the water in the tubes. Water vapor condenses on the outside of the tubes as product water. By combining several physical processes, Passarell enables most of the system's energy to be recycled through its evaporation, demisting, vapor compression, condensation, and water movement processes.
Nanotube membranes of higher permeability than current generation of membranes may lead to eventual reduction in the footprint of RO desalination plants. It has also been suggested that the use of such membranes will lead to reduction in the energy needed for desalination.
Hermetic, sulphonated nano-composite membranes have shown to be capable of removing various contaminants to the parts per billion level, and have little or no susceptibility to high salt concentration levels.
In 2008, Siemens Water Technologies announced technology that applied electric fields to desalinate one cubic meter of water while using only a purported 1.5 kWh of energy. If accurate, this process would consume one-half the energy of other processes. As of 2012 a demonstration plant was operating in Singapore. Researchers at the University of Texas at Austin and the University of Marburg are developing more efficient methods of electrochemically mediated seawater desalination.
A process employing electrokinetic shocks waves can be used to accomplish membraneless desalination at ambient temperature and pressure. In this process, anions and cations in salt water are exchanged for carbonate anions and calcium cations, respectively using electrokinetic shockwaves. Calcium and carbonate ions react to form calcium carbonate, which precipitates, leaving fresh water. The theoretical energy efficiency of this method is on par with electrodialysis and reverse osmosis.
Temperature swing solvent extraction
Temperature Swing Solvent Extraction (TSSE) uses a solvent instead of a membrane or high temperatures.
Solvent extraction is a common technique in chemical engineering. It can be activated by low-grade heat (less than 70 °C (158 °F), which may not require active heating. In a study, TSSE removed up to 98.4 percent of the salt in brine. A solvent whose solubility varies with temperature is added to saltwater. At room temperature the solvent draws water molecules away from the salt. The water-laden solvent is then heated, causing the solvent to release the now salt-free water.
It can desalinate extremely salty brine up to seven times as salty as the ocean. For comparison, the current methods can only handle brine twice as salty.
- Perth began operating a reverse osmosis seawater desalination plant in 2006. The Perth desalination plant is powered partially by renewable energy from the Emu Downs Wind Farm.
- A desalination plant now operates in Sydney, and the Wonthaggi desalination plant was under construction in Wonthaggi, Victoria. A wind farm at Bungendore in New South Wales was purpose-built to generate enough renewable energy to offset the Sydney plant's energy use, mitigating concerns about harmful greenhouse gas emissions.
- A January 17, 2008, article in The Wall Street Journal stated, "In November, Connecticut-based Poseidon Resources Corp. won a key regulatory approval to build the $300 million water-desalination plant in Carlsbad, north of San Diego. The facility would produce 190,000 cubic metres of drinking water per day, enough to supply about 100,000 homes. As of June 2012, the cost for the desalinated water had risen to $2,329 per acre-foot. Each $1,000 per acre-foot works out to $3.06 for 1,000 gallons, or $0.81 per cubic meter.
Evaporation of water over the oceans in the water cycle is a natural desalination process.
The formation of sea ice produces ice with little salt, much lower than in seawater.
Seabirds distill seawater using countercurrent exchange in a gland with a rete mirabile. The gland secretes highly concentrated brine stored near the nostrils above the beak. The bird then "sneezes" the brine out. As freshwater is not usually available in their environments, some seabirds, such as pelicans, petrels, albatrosses, gulls and terns, possess this gland, which allows them to drink the salty water from their environments while they are far from land.
Mangrove trees grow in seawater; they secrete salt by trapping it in parts of the root, which are then eaten by animals (usually crabs). Additional salt is removed by storing it in leaves that fall off. Some types of mangroves have glands on their leaves, which work in a similar way to the seabird desalination gland. Salt is extracted to the leaf exterior as small crystals, which then fall off the leaf.
Desalination has been known to history for millennia as both a concept, and later practice, though in a limited form. The ancient Greek philosopher Aristotle observed in his work Meteorology that "salt water, when it turns into vapour, becomes sweet and the vapour does not form salt water again when it condenses," and also noticed that a fine wax vessel would hold potable water after being submerged long enough in seawater, having acted as a membrane to filter the salt. There are numerous other examples of experimentation in desalination throughout Antiquity and the Middle Ages, but desalination was never feasible on a large scale until the modern era. A good example of this experimentation are the observations by Leonardo da Vinci (Florence, 1452), who realized that distilled water could be made cheaply in large quantities by adapting a still to a cookstove. During the Middle Ages elsewhere in Central Europe, work continued on refinements in distillation, although not necessarily directed towards desalination.
However, it is possible that the first major land-based desalination plant may have been installed under emergency conditions on an island off the coast of Tunisia in 1560. It is believed that a garrison of 700 Spanish soldiers was besieged by a large number of Turks and that, during the siege, the captain in charge fabricated a still capable of producing 40 barrels of fresh water per day, even though details of the device have not been reported.
Before the Industrial Revolution, desalination was primarily of concern to oceangoing ships, which otherwise needed to keep on board supplies of fresh water. Sir Richard Hawkins (1562-1622), who made extensive travels in the South Seas, reported in his return that he had been able to supply his men with fresh water by means of shipboard distillation. Additionally, during the early 1600s, several prominent figures of the era such as Francis Bacon or Walter Raleigh published reports on water desalination. These reports and others, set the climate for the first patent dispute concerning desalination apparatus. The two first patents regarding water desalination date back to 1675 and 1683 (patents No.184 and No. 226, published by Mr. William Walcot and Mr. Robert Fitzgerald (and others), respectively). Nevertheless, neither of the two inventions was really put into service as a consequence of technical problems derived from scale-up difficulties. No significant improvements to the basic seawater distillation process were made for some time during the 150 years from mid-1600s until 1800.
When the frigate Protector was sold to Denmark in the 1780s (as the ship Hussaren) the desalination plant was studied and recorded in great detail. In the newly formed United States, Thomas Jefferson catalogued heat-based methods going back to the 1500s, and formulated practical advice that was publicized to all U.S. ships on the backs of sailing clearance permits.
Beginning about 1800, things started changing very rapidly as consequence of the appearance of the steam engine and the so-called age of steam. The development of a knowledge of the thermodynamics of steam processes  and the need for a pure water source for its use in boilers, generated a positive effect regarding distilling systems. Additionally, the spread of European colonialism induced a need for freshwater in remote parts of the world, thus creating the appropriate climate for water desalination.
In parallel with the development and improvement systems using steam (multiple-effect evaporators), this type of devices quickly demonstrated its potential in the field of desalination. In 1852, Alphonse René le Mire de Normandy, was issued a British patent for a vertical tube seawater distilling unit which thanks to its simplicity of design and ease of construction, very quickly gained popularity for shipboard use. Land-based desalting units did not significantly appear until the later half of the nineteenth century. In the 1860s, the US Army purchased three Normandy evaporators, each rated at 7000 gallons/day and installed them on the islands of Key West and Dry Tortugas. Another important land-based desalter plant was installed at Suakin during the 1980s which was able to provide freshwater to the British troops placed there. It consisted of six-effect distillers with a capacity of 350 tons/day.
Significant research into improved desalination methods occurred in the United States after World War II. The Office of Saline Water was created in the United States Department of the Interior in 1955 in accordance with the Saline Water Conversion Act of 1952. It was merged into the Office of Water Resources Research in 1974.
The first industrial desalination plant in the United States opened in Freeport, Texas in 1961 with the hope of bringing water security to the region after a decade of drought. Vice-president Lyndon B. Johnson attended the plant's opening on June 21, 1961. President John F. Kennedy recorded a speech from the White House, describing desalination as "a work that in many ways is more important than any other scientific enterprise in which this country is now engaged."
The first commercial reverse osmosis desalination plant, Coalinga desalination plant, was inaugurated in California in 1965 for brackish water. A few years later, in 1975, the first sea water reverse osmosis desalination plant came into operation.
Society and culture
Despite the issues associated with desalination processes, public support for its development can be very high. One survey of a Southern California community saw 71.9% of all respondents being in support of desalination plant development in their community. In many cases, high freshwater scarcity corresponds to higher public support for desalination development whereas areas with low water scarcity tend to have less public support for its development.
- "Desalination" (definition), The American Heritage Science Dictionary, via dictionary.com. Retrieved August 19, 2007.
- "Australia Aids China In Water Management Project."[permanent dead link] People's Daily Online, 2001-08-03, via english.people.com.cn. Retrieved August 19, 2007.
- Panagopoulos, Argyris; Haralambous, Katherine-Joanne; Loizidou, Maria (November 25, 2019). "Desalination brine disposal methods and treatment technologies - A review". The Science of the Total Environment. 693: 133545. Bibcode:2019ScTEn.693m3545P. doi:10.1016/j.scitotenv.2019.07.351. ISSN 1879-1026. PMID 31374511.
- Fischetti, Mark (September 2007). "Fresh from the Sea". Scientific American. 297 (3): 118–119. Bibcode:2007SciAm.297c.118F. doi:10.1038/scientificamerican0907-118. PMID 17784633.
- Ebrahimi, Atieh; Najafpour, Ghasem D; Yousefi Kebria, Daryoush (2019). "Performance of microbial desalination cell for salt removal and energy generation using different catholyte solutions". Desalination. 432: 1. doi:10.1016/j.desal.2018.01.002.
- "Making the Deserts Bloom: Harnessing nature to deliver us from drought, Distillations Podcast and transcript, Episode 239". Science History Institute. March 19, 2019. Retrieved August 27, 2019.
- Jones, Edward; Qadir, Manzoor; van Vliet, Michelle T. H.; Smakhtin, Vladimir; Kang, Seong-mu (March 20, 2019). "The state of desalination and brine production: A global outlook". Science of the Total Environment. 657: 1343–1356. Bibcode:2019ScTEn.657.1343J. doi:10.1016/j.scitotenv.2018.12.076. ISSN 0048-9697. PMID 30677901.
- Ahmadi, Esmaeil; McLellan, Benjamin; Mohammadi-Ivatloo, Behnam; Tezuka, Tetsuo (2020). "The Role of Renewable Energy Resources in Sustainability of Water Desalination as a Potential Fresh-Water Source: An Updated Review". Sustainability. 12 (13): 5233. doi:10.3390/su12135233.
- Laurene Veale (August 19, 2015) "Seawater desalination: A solution or an environmental disaster?". MIT Technology News. Archived from the original on February 2, 2017. Retrieved January 25, 2017.
- "Largest water desalination plant". Guinness World Records. Retrieved August 21, 2020.
- Yuan Zhou and Richard S.J. Tol. "Evaluating the costs of desalination and water transport" (PDF) (Working paper). Hamburg University. December 9, 2004. Archived from the original (PDF) on March 25, 2009. Retrieved August 20, 2007.
- Desalination is the Solution to Water Shortages, redOrbit, May 2, 2008
- "2.2 Desalination by distillation". www.oas.org.
- Khawaji, Akili D.; Kutubkhanah, Ibrahim K.; Wie, Jong-Mihn (March 2008). "Advances in seawater desalination technologies". Desalination. 221 (1–3): 47–69. doi:10.1016/j.desal.2007.01.067.
- Warsinger, David M.; Mistry, Karan H.; Nayar, Kishor G.; Chung, Hyung Won; Lienhard V, John H. (2015). "Entropy Generation of Desalination Powered by Variable Temperature Waste Heat" (PDF). Entropy. 17 (12): 7530–7566. Bibcode:2015Entrp..17.7530W. doi:10.3390/e17117530.
- Al-Shammiri, M.; Safar, M. (November 1999). "Multi-effect distillation plants: state of the art". Desalination. 126 (1–3): 45–59. doi:10.1016/S0011-9164(99)00154-X.
- Fritzmann, C; Lowenberg, J; Wintgens, T; Melin, T (2007). "alination". Desalination. 216 (1–3): 1–76. doi:10.1016/j.desal.2006.12.009.
- Warsinger, David M.; Tow, Emily W.; Nayar, Kishor G.; Maswadeh, Laith A.; Lienhard V, John H. (2016). "Energy efficiency of batch and semi-batch (CCRO) reverse osmosis desalination" (PDF). Water Research. 106: 272–282. doi:10.1016/j.watres.2016.09.029. hdl:1721.1/105441. PMID 27728821.
- Thiel, Gregory P. (June 1, 2015). "Salty solutions". Physics Today. 68 (6): 66–67. Bibcode:2015PhT....68f..66T. doi:10.1063/PT.3.2828. ISSN 0031-9228.
- Culp, T.E. (2018). "Electron tomography reveals details of the internal microstructure of desalination membranes". Proceedings of the National Academy of Sciences of the United States of America. 115 (35): 8694–8699. Bibcode:2018PNAS..115.8694C. doi:10.1073/pnas.1804708115. PMC 6126755. PMID 30104388.
- Culp, Tyler E.; Khara, Biswajit; Brickey, Kaitlyn P.; Geitner, Michael; Zimudzi, Tawanda J.; Wilbur, Jeffrey D.; Jons, Steven D.; Roy, Abhishek; Paul, Mou; Ganapathysubramanian, Baskar; Zydney, Andrew L. (January 1, 2021). "Nanoscale control of internal inhomogeneity enhances water transport in desalination membranes". Science. 371 (6524): 72–75. Bibcode:2021Sci...371...72C. doi:10.1126/science.abb8518. ISSN 0036-8075. PMID 33384374. S2CID 229935140.
- Rautenbach, Melin (2007). Membranverfahren – Grundlagen der Modul und Anlagenauslegung. Germany: Springer Verlag Berlin. ISBN 978-3540000716.
- Seawater Desalination – Impacts of Brine and Chemical Discharge on the Marine Environment. Sabine Lattemann, Thomas Höppner. January 1, 2003. ISBN 978-0866890625.
- "Access to sustainable water by unlimited resources | Climate innovation window". climateinnovationwindow.eu.
- "Solving fresh water scarcity, using only the sea, sun, earth & wind". www.glispa.org.
- "From Plentiful Seawater to Precious Drinking Water". SIDS Global Business Network.
- "HH Sheikh Maktoum bin Mohammed bin Rashid Al Maktoum honours 10 winners from 8 countries at Mohammed bin Rashid Al Maktoum Global Water Award". Suqia.
- Boysen, John E.; Stevens, Bradley G. (August 2002). "Demonstration of the Natural Freeze-Thaw Process for the Desalination of Water From The Devils Lake Chain to Provide Water for the City of Devils Lake" (PDF).
- Van der Bruggen, Bart; Vandecasteele, Carlo (June 2002). "Distillation vs. membrane filtration: overview of process evolutions in seawater desalination". Desalination. 143 (3): 207–218. doi:10.1016/S0011-9164(02)00259-X.
- Warsinger, David M.; Tow, Emily W.; Swaminathan, Jaichander; Lienhard V, John H. (2017). "Theoretical framework for predicting inorganic fouling in membrane distillation and experimental validation with calcium sulfate" (PDF). Journal of Membrane Science. 528: 381–390. doi:10.1016/j.memsci.2017.01.031.
- "Perth Wave Energy Project". Australian Renewable Energy Agency. Commonwealth of Australia. February 2015. Archived from the original on February 1, 2016. Retrieved January 26, 2016.
This project is the world's first commercial-scale wave energy array that is connected to the grid and has the ability to produce desalinated water.
- Wave-powered Desalination Riding High in Australia – WaterWorld
- "World's first wave-powered desalination plant now operational in Perth". www.engineersaustralia.org.au.
- Panagopoulos, Argyris (December 1, 2020). "A comparative study on minimum and actual energy consumption for the treatment of desalination brine". Energy. 212: 118733. doi:10.1016/j.energy.2020.118733. ISSN 0360-5442.
- Wilkinson, Robert C. (March 2007) "Analysis of the Energy Intensity of Water Supplies for West Basin Municipal Water District" Archived December 20, 2012, at the Wayback Machine, Table on p. 4
- "U.S. Electricity Consumption for Water Supply & Treatment" Archived June 17, 2013, at the Wayback Machine, pp. 1–4 Table 1-1, Electric Power Research Institute (EPRI) Water & Sustainability (Volume 4), 2000
- Elimelech, Menachem (2012) "Seawater Desalination" Archived February 23, 2014, at the Wayback Machine, p. 12 ff
- Semiat, R. (2008). "Energy Issues in Desalination Processes". Environmental Science & Technology. 42 (22): 8193–201. Bibcode:2008EnST...42.8193S. doi:10.1021/es801330u. PMID 19068794.
- "Optimizing Lower Energy Seawater Desalination", p. 6 figure 1.2, Stephen Dundorf at the IDA World Congress November 2009
- "Membrane Desalination Power Usage Put In Perspective" Archived April 24, 2014, at the Wayback Machine, American Membrane Technology Association (AMTA) April 2009
-  Total Water Use in the United States
- "Energy Requirements of Desalination Processes", Encyclopedia of Desalination and Water Resources (DESWARE). Retrieved June 24, 2013
- Hamed, O. A. (2005). "Overview of hybrid desalination systems – current status and future prospects". Desalination. 186 (1–3): 207. CiteSeerX 10.1.1.514.4201. doi:10.1016/j.desal.2005.03.095.
- Misra, B. M.; Kupitz, J. (2004). "The role of nuclear desalination in meeting the potable water needs in water scarce areas in the next decades". Desalination. 166: 1. doi:10.1016/j.desal.2004.06.053.
- Ludwig, H. (2004). "Hybrid systems in seawater desalination – practical design aspects, present status and development perspectives". Desalination. 164: 1. doi:10.1016/S0011-9164(04)00151-1.
- Tom Harris (August 29, 2002) How Aircraft Carriers Work. Howstuffworks.com. Retrieved May 29, 2011.
- Gleick, Peter H., Dana Haasz, Christine Henges-Jeck, Veena Srinivasan, Gary Wolff, Katherine Kao Cushing, and Amardip Mann. (November 2003.) "Waste not, want not: The potential for urban water conservation in California." (Website). Pacific Institute. Retrieved September 20, 2007.
- Cooley, Heather, Peter H. Gleick, and Gary Wolff. (June 2006.) Pacific Institute. Retrieved September 20, 2007.
- Gleick, Peter H., Heather Cooley, David Groves (September 2005). "California water 2030: An efficient future.". Pacific Institute. Retrieved September 20, 2007.
- Sun Belt Inc. Legal Documents. Sunbeltwater.com. Retrieved May 29, 2011.
- Zhang, S.X.; V. Babovic (2012). "A real options approach to the design and architecture of water supply systems using innovative water technologies under uncertainty". Journal of Hydroinformatics. 14: 13–29. doi:10.2166/hydro.2011.078.
- "Finding Water in Mogadishu"IPS news item 2008
- Tiwari, Anil Kr.; Tiwari, G. N. (January 1, 2006). "Evaluating the Performance of Single Slope Passive Solar Still for Different Slope of Cover and Water Depths by Thermal Modeling: In Moderate Climatic Condition". Solar Energy. ASMEDC: 545–553. doi:10.1115/isec2006-99057. ISBN 0-7918-4745-4.
- Andrew Burger (June 20, 2019). "No Batteries Needed: Can Low-Cost Solar Desalination System "Green" Namibia's Desert Coast?". Solar Magazine. Retrieved April 5, 2020.
- "How the world could have 100 percent solar desalination". EurekAlert!. Retrieved April 5, 2020.
- Alsheghri, Ammar; Sharief, Saad Asadullah; Rabbani, Shahid; Aitzhan, Nurzhan Z. (August 1, 2015). "Design and Cost Analysis of a Solar Photovoltaic Powered Reverse Osmosis Plant for Masdar Institute". Energy Procedia. Clean, Efficient and Affordable Energy for a Sustainable Future: The 7th International Conference on Applied Energy (ICAE2015). 75: 319–324. doi:10.1016/j.egypro.2015.07.365. ISSN 1876-6102.
- "Nuclear Desalination". World Nuclear Association. January 2010. Retrieved February 1, 2010.
- Barlow, Maude, and Tony Clarke, "Who Owns Water?" The Nation, 2002-09-02, via thenation.com. Retrieved August 20, 2007.
- Over and drought: Why the end of Israel's water shortage is a secret, Haaretz, January 24, 2014
- "Black & Veatch-Designed Desalination Plant Wins Global Water Distinction," Archived March 24, 2010, at the Wayback Machine (Press release). Black & Veatch Ltd., via edie.net, May 4, 2006. Retrieved August 20, 2007.
- Water: Cooling Water Intakes (316b). water.epa.gov.
- Cooley, Heather; Gleick, Peter H. and Wolff, Gary (2006) Desalination, With a Grain of Salt. A California Perspective, Pacific Institute for Studies in Development, Environment, and Security. ISBN 1-893790-13-4
- Sullivan, Michael (June 18, 2007) "Australia Turns to Desalination Amid Water Shortage". NPR.
- Panagopoulos, Argyris; Haralambous, Katherine-Joanne (October 1, 2020). "Minimal Liquid Discharge (MLD) and Zero Liquid Discharge (ZLD) strategies for wastewater management and resource recovery – Analysis, challenges and prospects". Journal of Environmental Chemical Engineering. 8 (5): 104418. doi:10.1016/j.jece.2020.104418. ISSN 2213-3437.
- Greenberg, Joel (March 20, 2014) "Israel no longer worried about its water supply, thanks to desalination plants" Archived March 24, 2014, at the Wayback Machine, McClatchy DC
- Lattemann, Sabine; Höpner, Thomas (2008). "Environmental impact and impact assessment of seawater desalination". Desalination. 220 (1–3): 1. doi:10.1016/j.desal.2007.03.009.
- "Innovative floating desalination system". www.theexplorer.no.
- "Oisann Engineering". Oisann Engineering.
- Yolanda Fernández-Torquemada (March 16, 2009). "Dispersion of brine discharge from seawater reverse osmosis desalination plants". Desalination and Water Treatment. 5 (1–3): 137–145. doi:10.5004/dwt.2009.576. hdl:10045/11309.
- Panagopoulos, Argyris; Haralambous, Katherine-Joanne (December 1, 2020). "Environmental impacts of desalination and brine treatment - Challenges and mitigation measures". Marine Pollution Bulletin. 161 (Pt B): 111773. doi:10.1016/j.marpolbul.2020.111773. ISSN 0025-326X. PMID 33128985.
- "מידעון הפקולטה". מידעון הפקולטה לחקלאות מזון וסביבה עש רוברט ה סמית. agri.huji.ac.il. July 2014
- Yaniv Ovadia. "Estimated iodine intake and status in adults exposed to iodine-poor water". ResearchGate.
- Ovadia YS, Troen AM, Gefel D (August 2013). "Seawater desalination and iodine deficiency: is there a link?" (PDF). IDD Newsletter.
- Ovadia, Yaniv S; Gefel, Dov; Aharoni, Dorit; Turkot, Svetlana; Fytlovich, Shlomo; Troen, Aron M (October 2016). "Can desalinated seawater contribute to iodine-deficiency disorders? An observation and hypothesis". Public Health Nutrition. 19 (15): 2808–2817. doi:10.1017/S1368980016000951. PMID 27149907.
- "Millions of Israeli children said at risk of stunted development, possibly from desalinated water". jta.org. March 27, 2017. Retrieved October 22, 2017.
- "High burden of Iodine deficiency found in Israel's first national survey – האוניברסיטה העברית בירושלים – The Hebrew University of Jerusalem". new.huji.ac.il. Retrieved October 22, 2017.
- "Israeli Water Authority". water.gov.il. Retrieved October 22, 2017.
- "Desalination plant powered by waste heat opens in Maldives" European Innovation Partnerships (EIP) news. Retrieved March 18, 2014
- "Island finally gets its own water supply" Archived March 18, 2014, at the Wayback Machine, Global Water Intelligence, February 24, 2014. Retrieved March 18, 2014
- Sistla, Phanikumar V.S.; et al. "Low Temperature Thermal DesalinbationPLants" (PDF). Proceedings of the Eighth (2009) ISOPE Ocean Mining Symposium, Chennai, India, September 20–24, 2009. International Society of Offshore and Polar Engineers. Archived from the original (PDF) on October 4, 2011. Retrieved June 22, 2010.
- Haruo Uehara and Tsutomu Nakaoka Development and Prospective of Ocean Thermal Energy Conversion and Spray Flash Evaporator Desalination Archived March 22, 2012, at the Wayback Machine. ioes.saga-u.ac.jp
- Indian Scientists Develop World's First Low Temperature Thermal Desalination Plant. Retrieved January 1, 2019.
- Floating plant, India Archived August 27, 2008, at the Wayback Machine. Headlinesindia.com (April 18, 2007). Retrieved May 29, 2011.
- Tamil Nadu / Chennai News : Low temperature thermal desalination plants mooted. The Hindu (April 21, 2007). Retrieved March 20, 2011.
- Current thinking, The Economist, October 29, 2009
- "A Study of Silica Gel Adsorption Desalination System" (PDF). Jun Wei WU. Retrieved November 3, 2016.
- "FO plant completes 1-year of operation" (PDF). Water Desalination Report: 2–3. November 15, 2010. Retrieved May 28, 2011.[permanent dead link]
- "Modern Water taps demand in Middle East" (PDF). The Independent. November 23, 2009. Retrieved May 28, 2011.[permanent dead link]
- Thompson N.A.; Nicoll P.G. (September 2011). "Forward Osmosis Desalination: A Commercial Reality" (PDF). Proceedings of the IDA World Congress. Perth, Western Australia: International Desalination Association.
- Rud, Oleg; Borisov, Oleg; Košovan, Peter (2018). "Thermodynamic model for a reversible desalination cycle using weak polyelectrolyte hydrogels". Desalination. 442: 32. doi:10.1016/j.desal.2018.05.002.
- UAE & France Announce Partnership To Jointly Fund Renewable Energy Projects, Clean Technica, January 25, 2015
- Tapping the Market, CNBC European Business, October 1, 2008
- Peters, Adele (February 10, 2014). "Can This Solar Desalination Startup Solve California Water Woes?". Fast Company. Retrieved February 24, 2015.
- The "Passarell" Process. Waterdesalination.com (November 16, 2004). Retrieved May 14, 2012.
- "Nanotube membranes offer possibility of cheaper desalination" (Press release). Lawrence Livermore National Laboratory Public Affairs. May 18, 2006. Archived from the original on October 1, 2006. Retrieved September 7, 2007.
- Cao, Liwei. "Patent US8222346 – Block copolymers and method for making same". Retrieved July 9, 2013.
- Wnek, Gary. "Patent US6383391 – Water-and ion-conducting membranes and uses thereof". Retrieved July 9, 2013.
- Cao, Liwei (June 5, 2013). "Dais Analytic Corporation Announces Product Sale to Asia, Functional Waste Water Treatment Pilot, and Key Infrastructure Appointments". PR Newswire. Retrieved July 9, 2013.
- "Sandia National Labs: Desalination and Water Purification: Research and Development". sandia.gov. 2007. Retrieved July 9, 2013.
- Team wins $4m grant for breakthrough technology in seawater desalination Archived April 14, 2009, at the Wayback Machine, The Straits Times, June 23, 2008
- "New desalination process uses 50% less energy | MINING.com". MINING.com. September 6, 2012. Retrieved June 11, 2016.
- "Chemists Work to Desalinate the Ocean for Drinking Water, One Nanoliter at a Time". Science Daily. June 27, 2013. Retrieved June 29, 2013.
- Shkolnikov, Viktor; Bahga, Supreet S.; Santiago, Juan G. (April 5, 2012). "Desalination and hydrogen, chlorine, and sodium hydroxide production via electrophoretic ion exchange and precipitation" (PDF). Stanford Microfluidics Laboratory. 14 (32): 11534–45. Bibcode:2012PCCP...1411534S. doi:10.1039/c2cp42121f. PMID 22806549. Retrieved July 9, 2013.
- Reilly, Claire. "Scientists discover a game-changing way to remove salt from water". CNET.
- Ramirez, Vanessa Bates (June 18, 2019). "Inching Towards Abundant Water: New Progress in Desalination Tech". Singularity Hub. Retrieved June 19, 2019.
- Perth Seawater Desalination Plant, Seawater Reverse Osmosis (SWRO), Kwinana. Water Technology. Retrieved March 20, 2011.
- PX Pressure Exchanger energy recovery devices from Energy Recovery Inc. An Environmentally Green Plant Design Archived March 27, 2009, at the Wayback Machine. Morning Edition, NPR, June 18, 2007
- "Sydney desalination plant to double in size," Australian Broadcasting Corporation, June 25, 2007. Retrieved August 20, 2007.
- Fact sheets, Sydney Water
- Kranhold, Kathryn. (January 17, 2008) Water, Water, Everywhere... The Wall Street Journal. Retrieved March 20, 2011.
- Mike Lee. "Carlsbad desal plant, pipe costs near $1 billion". U-T San Diego.
- Sweet, Phoebe (March 21, 2008) Desalination gets a serious look. Las Vegas Sun.
- Proctor, Noble S.; Lynch, Patrick J. (1993). Manual of Ornithology. Yale University Press. ISBN 978-0300076196.
- Ritchison, Gary. "Avian osmoregulation". Retrieved April 16, 2011. including images of the gland and its function
- "Enhancement Marshes". Arcata's Wastewater Treatment Plant & The Arcata Marsh and Wildlife Sanctuary. Archived from the original on August 8, 2011. Retrieved April 5, 2018.
- Aristotle with E.W. Webster, trans., Meteorologica, in: Ross, W. D., ed., The Works of Aristotle, vol. 3, (Oxford, England: Clarendon Press, 1931), Book III, §358: 16–18 and §359: 1–5.
- Joseph Needham, Ho Ping-Yu, Lu Gwei-Djen, Nathan Sivin, Science and Civilisation in China: Volume 5, Chemistry and Chemical Technology (Cambridge, England: Cambridge University Press, 1980), p. 60.
- Alexander of Aphrodisias (fl. 200 A.D.) wrote, in his commentary on Aristotle's Meteorology, that if a lid is placed on a boiling pot of seawater, fresh water will condense on the lid.
- In his Hexaemeron, Homily IV, § 7, St. Basil of Caesarea (c. 329–379 AD) mentioned that sailors produced fresh water via distillation. Saint Basil with Sister Agnes Clare Way, trans., Saint Basil Exegetic Homilies (Washington, DC: The Catholic University of America Press, 1963), p. 65. From p. 65: "Moreover, it is possible to see the water of the sea boiled by sailors, who, catching the vapors in sponges, relieve their thirst fairly well in times of need."
- "Sample" (PDF). www.desware.net.
- J. R. Partington, History of Chemistry, Vol. 2-3, Macmillan, London, 1962.
- Birkett, James D. (January 1, 1984). "A brief illustrated history of desalination: From the bible to 1940". Desalination. 50: 17–52. doi:10.1016/0011-9164(84)85014-6. ISSN 0011-9164.
- Nebbia, G.; Menozzi, G.N. (1966). "Aspetti storici della dissalazione". Acqua Ind. 41–42: 3–20.
- Haarhoff, Johannes (February 1, 2009). "The Distillation of Seawater on Ships in the 17th and 18th Centuries". Heat Transfer Engineering. 30 (3): 237–250. Bibcode:2009HTrEn..30..237H. doi:10.1080/01457630701266413. ISSN 0145-7632. S2CID 121765890.
- Baker, M.N. (1981). "Quest for Pure Water". Am. Water Works Assoc. 2nd Ed. 1.
- Cleveland, J. (1754). "Universal Magazine": 44. Cite journal requires
- W. Walcot, Purifying Water, Britain No. 184, 1675
- R. Fitzgerald et al, Purifying Salt Water, Britain No. 226, 1683.
- "Enkel Søgning". www.orlogsbasen.dk.
- Thomas Jefferson (November 21, 1791). "Report on Desalination of Sea Water".
- "Desalination of Sea Water | Thomas Jefferson's Monticello". www.monticello.org.
- O. Lyle, Efficient Use of Steam, His Majesty's Stationery Office, London, 1947.
- A. Fraser-MacDonald, Our Ocean Railways, Chapman and Hall, London 1893.
- James D. Birkett. History, development and management of water resources – Vol. I. The history of desalination before large-scale use. EOLSS Publications, (2010).
- Birkett J. D. The 1861 de Normandy desalting unit at Key West. International Desalination & Water Reuse Quarterly 7(3), 53-57
- "Records of the office of Saline Water". August 15, 2016.
- Roberts, Jacob; Jaehnig, Kenton G. (November 12, 2018). "Nor Any Drop to Drink". Distillations. Science History Institute. 4 (3): 8–13. Retrieved February 10, 2020.
- David Talbot (November 23, 2015). "Bankrolling the 10 Breakthrough Technologies: Megascale Desalination". Archived from the original on October 3, 2016. Retrieved October 3, 2016.
- Singleton, M.; et., al. (2011). "Optimization of ramified absorber networks doing desalination". Phys. Rev. E. 83 (1): 016308. Bibcode:2011PhRvE..83a6308S. doi:10.1103/PhysRevE.83.016308. PMID 21405775.
- Koutroulis, E.; et., al. (2010). "Design optimization of desalination systems power-supplied by PV and W/G energy sources". Desalination. 258 (1–3): 171. doi:10.1016/j.desal.2010.03.018.
- Heck, N.; Paytan, A.; Potts, D.C.; Haddad, B. (2016). "Predictors of local support for a seawater desalination plant in a small coastal community". Environmental Science and Policy. 66: 101–111. doi:10.1016/j.envsci.2016.08.009.
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- International Desalination Association
- European Desalination Society
- Working principles in desalination systems
- Classification of Desalination Technologies (CDT)
- SOLAR TOWER Project – Clean Electricity Generation for Desalination.
- Desalination bibliography Library of Congress
- Encyclopedia of Desalination and water and Water Resources