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Desalination
Desalination
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Reverse osmosis desalination plant in Barcelona, Spain

Desalination is a process that removes mineral components from saline water. More generally, desalination is the removal of salts and minerals from a substance.[1] One example is soil desalination. This is important for agriculture. It is possible to desalinate saltwater, especially sea water, to produce water for human consumption or irrigation, producing brine as a by-product.[2] Many seagoing ships and submarines use desalination. Modern interest in desalination mostly focuses on cost-effective provision of fresh water for human use. Along with recycled wastewater, it is one of the few water resources independent of rainfall.[3]

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.[4][5][6] Desalination processes are using either thermal methods (in the case of distillation) or membrane-based methods (e.g. in the case of reverse osmosis).[7][8]: 24 

An estimate in 2018 found that "18,426 desalination plants are in operation in over 150 countries. They produce 87 million cubic meters of clean water each day and supply over 300 million people."[8]: 24  The energy intensity has improved: It is now about 3 kWh/m3 (in 2018), down by a factor of 10 from 20–30 kWh/m3 in 1970.[8]: 24  Nevertheless, desalination represented about 25% of the energy consumed by the water sector in 2016.[8]: 24 

History

[edit]

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 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.[9]

At the same time the desalination of seawater was recorded in China. Both the Classic of Mountains and Water Seas in the Period of the Warring States and the Theory of the Same Year in the Eastern Han Dynasty mentioned that people found that the bamboo mats used for steaming rice would form a thin outer layer after long use. The as-formed thin film had adsorption and ion exchange functions, which could adsorb salt.[10]

Numerous examples of experimentation in desalination appeared throughout Antiquity and the Middle Ages,[11] but desalination became feasible on a large scale only in the modern era.[12] A good example of this experimentation comes from Leonardo da Vinci (Florence, 1452), who realized that distilled water could be made cheaply in large quantities by adapting a still to a cookstove.[13] During the Middle Ages elsewhere in Central Europe, work continued on distillation refinements, although not necessarily directed towards desalination.[14]

The first major land-based desalination plant may have been installed under emergency conditions on an island off the coast of Tunisia in 1560.[14][15] It is believed that a garrison of 700 Spanish soldiers was besieged by the Turkish army and that, during the siege, the captain in charge fabricated a still capable of producing 40 barrels of fresh water per day, though details of the device have not been reported.[15]

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 that he had been able to supply his men with fresh water by means of shipboard distillation.[16] Additionally, during the early 1600s, several prominent figures of the era such as Francis Bacon and Walter Raleigh published reports on desalination.[15][17] These reports and others,[18] set the climate for the first patent dispute concerning desalination apparatus. The two first patents regarding water desalination were approved in 1675 and 1683 (patents No. 184[19] and No. 226,[20] published by William Walcot and Robert Fitzgerald (and others), respectively). Nevertheless, neither of the two inventions entered service as a consequence of scale-up difficulties.[14] No significant improvements to the basic seawater distillation process were made during the 150 years from the mid-1600s until 1800.

When the frigate Protector was sold to Denmark in the 1780s (as the ship Hussaren) its still was studied and recorded in great detail.[21] In the 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 reverse side of sailing clearance permits.[22][23]

Beginning about 1800, things started changing as a consequence of the appearance of the steam engine and the so-called age of steam.[14] Knowledge of the thermodynamics of steam processes[24] and the need for a pure water source for its use in boilers[25] 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.[14]

In parallel with the development and improvement of systems using steam (multiple-effect evaporators), these types of devices quickly demonstrated their desalination potential.[14] In 1852, Alphonse René le Mire de Normandy was issued a British patent for a vertical tube seawater distilling unit that, thanks to its simplicity of design and ease of construction, gained popularity for shipboard use.[14] Land-based units did not significantly appear until the latter half of the nineteenth century.[26] 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.[14][26][27] Another land-based plant was installed at Suakin during the 1880s that provided freshwater to the British troops there. It consisted of six-effect distillers with a capacity of 350 tons/day.[14][26]

After World War II, many technologies were developed or improved such as Multi Effect Flash desalination (MEF) and Multi Stage Flash desalination (MSF). Another notable technology is freeze-thaw desalination.[28] Freeze-thaw desalination, (cryo-desalination or FD), excludes dissolved minerals from saline water through crystallization.[29]

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.[5][30] This act was motivated by a water shortage in California and inland western United States. The Department of the Interior allocated resources including research grants, expert personnel, patent data, and land for experiments to further advancements.[31]

The results of these efforts included the construction of over 200 electrodialysis and distillation plants globally, reverse osmosis (RO) research, and international cooperation (for example, the First International Water Desalination Symposium and Exposition in 1965).[32] The Office of Saline Water merged into the Office of Water Resources Research in 1974.[30]

The first industrial desalination plant in the United States opened in Freeport, Texas in 1961 after a decade of regional drought.[5]

By the late 1960s and the early 1970s, RO started to show promising results to replace traditional thermal desalination units. Research took place at state universities in California, at the Dow Chemical Company and DuPont.[33] Many studies focus on ways to optimize desalination systems.[34][35] The first commercial RO plant, the Coalinga desalination plant, was inaugurated in California in 1965 for brackish water.[36] Dr. Sidney Loeb, in conjunction with staff at UCLA, designed a large pilot plant to gather data on RO, but was successful enough to provide freshwater to the residents of Coalinga. This was a milestone in desalination technology, as it proved the feasibility of RO and its advantages compared to existing technologies (efficiency, no phase change required, ambient temperature operation, scalability, and ease of standardization).[37] A few years later, in 1975, the first sea water reverse osmosis desalination plant came into operation.

As of 2000, more than 2000 plants were operated. The largest are in Saudi Arabia, Israel, and the UAE; and the biggest plant with a volume of 1,401,000 m3/d is in Saudi Arabia (Ras Al Khair).[38]

This decade also saw progress in integrating renewable energy sources, such as solar and wind power, into desalination systems. Though initially in early stages, these efforts paved the way for more environmentally sustainable desalination practices.[39]

The 2010s and 2020s marked the emergence of next-generation membranes, including graphene-based membranes, aquaporin-inspired biomimetic membranes, ceramic membranes, and nanocomposites. These materials significantly improved water permeability, selectivity, and fouling resistance.[40]

As of 2021 22,000 plants were in operation[38] In 2024 the Catalan government installed a floating offshore plant near the port of Barcelona and purchased 12 mobile desalination units for the northern region of the Costa Brava to combat the severe drought.[41]

In 2012, cost averaged $0.75 per cubic meter. By 2022, that had declined (before inflation) to $0.41. Desalinated supplies are growing at a 10%+ compound rate, doubling in abundance every seven years.[42]

Between 2024 and 2025, Spain has recently announced a €340 million investment to build Africa's largest desalination plant in Casablanca, demonstrating the growing importance of large-scale desalination infrastructure.[43]

Applications

[edit]
External audio
audio icon "Making the Deserts Bloom: Harnessing nature to deliver us from drought", Distillations Podcast and transcript, Episode 239, March 19, 2019, Science History Institute
Schematic of a multistage flash desalinator
A – steam in     B – seawater in     C – potable water out
D – brine out (waste)     E – condensate out     F – heat exchange    G – condensation collection (desalinated water)
H – brine heater
The pressure vessel acts as a countercurrent heat exchanger. A vacuum pump lowers the pressure in the vessel to facilitate the evaporation of the heated seawater (brine) which enters the vessel from the right side (darker shades indicate lower temperature). The steam condenses on the pipes on top of the vessel in which the fresh sea water moves from the left to the right.

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 Power and Desalination Plant) with a capacity of 1,401,000 cubic meters per day.[44]

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.[45] 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[46] or California.[47][48] The most extensive use is in the Persian Gulf.[49]

While noting costs are falling, and generally positive about the technology for affluent areas in proximity to oceans, a 2005 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 the 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."[50]

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.[51] After desalination at Jubail, Saudi Arabia, water is pumped 320 km inland to Riyadh.[52] For coastal cities, desalination is increasingly viewed as a competitive choice.

In 2023, Israel was using desalination to replenish the Sea of Galilee's water supply.[53]

Not everyone is convinced that desalination is or will be economically viable or environmentally sustainable for the foreseeable future. Debbie Cook wrote in 2011 that desalination plants can be energy intensive and costly. Therefore, water-stressed regions might do better to focus on conservation or other water supply solutions than invest in desalination plants.[54]

Technologies

[edit]
Water desalination
Methods

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.[55]

There are several methods.[56] 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.[2] The traditional process of desalination is distillation (i.e., boiling and re-condensation of seawater to leave salt and impurities behind).[57]

There are currently two technologies with a large majority of the world's desalination capacity: multi-stage flash distillation and reverse osmosis.

Distillation

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Solar distillation

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Solar distillation mimics the natural water cycle, in which the sun heats sea water enough for evaporation to occur.[58] After evaporation, the water vapor is condensed onto a cool surface.[58] There are two types of solar desalination. The first type uses photovoltaic cells to convert solar energy to electrical energy to power desalination. The second type converts solar energy to heat, and is known as solar thermal powered desalination.

Natural evaporation

[edit]

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.[citation needed]

Vacuum distillation

[edit]

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

[edit]

Water is evaporated and separated from sea water through multi-stage flash distillation, which is a series of flash evaporations.[58] Each subsequent flash process uses energy released from the condensation of the water vapor from the previous step.[58]

Multiple-effect distillation

[edit]

Multiple-effect distillation (MED) works through a series of steps called "effects".[58] 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.[58] To increase efficiency, the steam used to heat the sea water can be taken from nearby power plants.[58] Although this method is the most thermodynamically efficient among methods powered by heat,[59] a few limitations exist such as a max temperature and max number of effects.[60]

Vapor-compression distillation

[edit]

Vapor-compression evaporation involves using either a mechanical compressor or a jet stream to compress the vapor present above the liquid.[59] The compressed vapor is then used to provide the heat needed for the evaporation of the rest of the sea water.[58] Since this system only requires power, it is more cost effective if kept at a small scale.[58]

Membrane distillation

[edit]

Membrane distillation uses a temperature difference across a membrane to evaporate vapor from a brine solution and condense pure water on the colder side.[61] The design of the membrane can have a significant effect on efficiency and durability. A study found that a membrane created via co-axial electrospinning of PVDF-HFP and silica aerogel was able to filter 99.99% of salt after continuous 30-day usage.[62]

Osmosis

[edit]

Reverse osmosis

[edit]
Schematic representation of a typical desalination plant using reverse osmosis. Hybrid desalination plants using liquid nitrogen freeze thaw in conjunction with reverse osmosis have been found to improve efficiency.[63]

The leading process for desalination in terms of installed capacity and yearly growth is reverse osmosis (RO).[64] 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.[59] 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,[65] reduction in plant footprint, improvements to plant operation and optimization, more effective feed pretreatment, and lower cost energy sources.[66]

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.[67] A 2021 study found that the water permeability is primarily governed by the internal nanoscale mass distribution of the polyamide active layer.[68]

The reverse osmosis process requires maintenance. Various factors interfere with efficiency: ionic contamination (calcium, magnesium etc.); dissolved organic carbon (DOC); bacteria; viruses; colloids and insoluble particulates; biofouling and scaling, and membrane destruction in extreme cases. 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.[69][70]

Off-grid solar-powered desalination units use solar energy to fill a buffer tank on a hill with seawater.[71] 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.[72][73][74] Nano-tubes are also used for the same function (i.e., Reverse Osmosis).

Deep sea reverse osmosis (DSRO) installs equipment on the seabed to force water through RO membranes using the ocean's naturally occurring water pressure.[75] A 2021 study suggested DSRO could improve energy efficiency compared to standard RO by up to 50%.[76] The concept of DSRO has long been known, but has only recently become feasible due to technological advances from the deep sea oil and gas industry, drawing early-stage investments in DSRO startups.[75]

Forward osmosis

[edit]

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 as a "draw" solution of high concentration.[2]

Freeze–thaw

[edit]

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.[77]

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

[edit]

Electrodialysis uses electric potential to move the salts through pairs of charged membranes, which trap salt in alternating channels.[78] Several variances of electrodialysis exist such as conventional electrodialysis, electrodialysis reversal.[2]

Electrodialysis can simultaneously remove salt and carbonic acid from seawater.[79] Preliminary estimates suggest that the cost of such carbon removal can be paid for in large part if not entirely from the sale of the desalinated water produced as a byproduct.[80]

Microbial desalination

[edit]

Microbial desalination cells are biological electrochemical systems that implements the use of electro-active bacteria to power desalination of water in situ, resourcing the natural anode and cathode gradient of the electro-active bacteria and thus creating an internal supercapacitor.[4]

Wave-powered desalination

[edit]

Wave powered desalination systems generally convert mechanical wave motion directly to hydraulic power for reverse osmosis.[81] Such systems aim to maximize efficiency and reduce costs by avoiding conversion to electricity, minimizing excess pressurization above the osmotic pressure, and innovating on hydraulic and wave power components.[82] One such approach is desalinating using submerged buoys, a wave power approach done by CETO[83] and Oneka.[84] Wave-powered desalination plants began operating by CETO on Garden Island in Western Australia in 2013[85] and in Perth in 2015,[86] and Oneka has installations in Chile, Florida, California, and the Caribbean.[84]

Wind-powered desalination

[edit]

Wind energy can also be coupled to desalination. Similar to wave power, a direct conversion of mechanical energy to hydraulic power can reduce components and losses in powering reverse osmosis.[87] Wind power has also been considered for coupling with thermal desalination technologies.[88]

Desalination by thermophoresis

[edit]

In April 2024 [89], researchers from the Australian National University published experimental results of a novel technique for desalination. This technique, thermodiffusive desalination, passes saline water through a channel that is exposed to a temperature gradient. Due to thermophoresis, species migrate under this temperature gradient, orthogonal to the fluid flow. Researchers then separated the water into fractions. After multiple passes through the single channel, the researchers were able to achieve a NaCl concentration drop of 1000 ppm with a recovery rate (the desalination stream volume versus the original feedwater volume) of 6.2%. To achieve larger concentration drop while maintaining a reasonablely high recovery rate, they proposed using a multi-channel structure named the Burgers cascade, previously shown to enhance thermodiffusive separation in gases[90]. They show with modelling that Burgers cascade can achieve significant concentration drop that is useful for desalination. In 2025, the researchers from the Australian National University experimentally demonstrated thermodiffusive desalination through the Burgers cascade[91]. With the device of the same footprint area as the single channel device in 2004, they achieved 2000 ppm concentration drop with much higher recovery rate. More importantly, they identified various improvements that could be implemented to the Burgers cascade structure and the operation that will result in 40 times more energy-efficient separation compared to the published experimental results. Importantly, they identified one unique feature of the thermodiffusion-based desalination methods: the process is more efficient for treating hypersaline brine. This implies opportunities in brine treatment (minimal- or zero- liquid discharge), resource recovery from brine.

Design aspects

[edit]

Energy consumption

[edit]

The desalination process's energy consumption depends on the water's salinity. Brackish water desalination requires less energy than seawater desalination.[92]

The energy intensity of seawater desalination has improved: It is now about 3 kWh/m3 (in 2018), down by a factor of 10 from 20-30 kWh/m3 in 1970.[8]: 24  This is similar to the energy consumption of other freshwater supplies transported over large distances,[93] but much higher than local fresh water supplies that use 0.2 kWh/m3 or less.[94]

A minimum energy consumption for seawater desalination of around 1 kWh/m3 has been determined,[92][95][96] excluding prefiltering and intake/outfall pumping. Under 2 kWh/m3[97] 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.[92]

Supplying all US domestic water by desalination would increase domestic energy consumption by around 10%, about the amount of energy used by domestic refrigerators.[98] Domestic consumption is a relatively small fraction of the total water usage.[99]

Energy consumption of seawater desalination methods (kWh/m3)[100]
Desalination Method ⇨ Multi-stage
Flash
"MSF"
Multi-Effect
Distillation
"MED"
Mechanical Vapor
Compression
"MVC"
Reverse
Osmosis
"RO"
Energy ⇩
Electrical energy 4–6 1.5–2.5 7–12 3–5.5
Thermal energy 50–110 60–110 none none
Electrical equivalent of thermal energy 9.5–19.5 5–8.5 none none
Total equivalent electrical energy 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 an appropriate turbine generator. These calculations do not include the energy required to construct or refurbish items consumed.

Given the energy-intensive nature of desalination and the associated economic and environmental costs, desalination is generally considered a last resort after water conservation. But this is changing as prices continue to fall.

Cogeneration

[edit]

Cogeneration is generating useful heat energy and electricity 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.[101][102]

The Shevchenko BN-350, a former nuclear-heated desalination unit in Kazakhstan

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.[103]

A typical supercarrier in the US military is capable of using nuclear power to desalinate 1,500,000 L (330,000 imp gal; 400,000 US gal) of water per day.[104]

Alternatives to desalination

[edit]

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.[105] Wastewater reclamation provides multiple benefits over desalination of saline water,[106] although it typically uses desalination membranes.[107] Urban runoff and storm water capture also provide benefits in treating, restoring and recharging groundwater.[108]

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.[109]

The California Department of Water Resources and the California State Water Resources Control Board submitted a report to the state legislature recommending that urban water suppliers achieve an indoor water use efficiency standard of 55 US gallons (210 litres) per capita per day by 2023, declining to 47 US gallons (180 litres) per day by 2025, and 42 US gallons (160 litres) by 2030 and beyond.[110][111][112]

Costs

[edit]

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 only sometimes 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 costs, and since energy prices are very volatile, actual costs can vary substantially.[113]

The cost of untreated fresh water in the developing world can reach US$5/cubic metre.[114]

Since 1975, desalination technology has seen significant advancements, decreasing the average cost of producing one cubic meter of freshwater from seawater from $1.10 in 2000 to approximately $0.50 today. Improved desalination efficiency is a primary factor contributing to this reduction. Energy consumption remains a significant cost component, accounting for up to half the total cost of the desalination process.[115]

Desalination can significantly burden energy grids, especially in regions with limited energy resources. For instance, in the island nation of Cyprus, desalination accounts for approximately 5% of the country's total power consumption.[115]

The global desalination market was valued at $20 billion in 2023. With growing populations in arid coastal regions, this market is projected to double by 2032. In 2023, global desalination capacity reached 99 million cubic meters per day, a significant increase from 27 million cubic meters per day in 2003.[115]

Cost Comparison of Desalination Methods
Method Cost (US$/liter)
Passive solar (30.42% energy efficient)[116] 0.034
Passive solar (improved single-slope, India)[116] 0.024
Passive solar (improved double slope, India)[116] 0.007
Multi Stage Flash (MSF)[117] < 0.001
Reverse Osmosis (Concentrated solar power)[118] 0.0008
Reverse Osmosis (Photovoltaic power)[119] 0.000825
Average water consumption and cost of supply by seawater desalination at US$1 per cubic metre (±50%)
Area Consumption
Litre/person/day
Desalinated Water Cost
US$/person/day
US 378 0.38
Europe 189 0.19
Africa 57 0.06
UN recommended minimum 49 0.05

Desalination stills control pressure, temperature and brine concentrations to optimize efficiency. Nuclear-powered desalination might be economical on a large scale.[120][121]

In 2014, the Israeli facilities of Hadera, Palmahim, Ashkelon, and Sorek were desalinizing water for less than US$0.40 per cubic meter.[122] As of 2006, Singapore was desalinating water for US$0.49 per cubic meter.[123]

Environmental concerns

[edit]

Intake

[edit]

In the United States, cooling water intake structures are regulated by the Environmental Protection Agency (EPA). These structures can have the same impacts on 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.[124] Alternative intake types that mitigate these impacts include beach wells, but they require more energy and higher costs.[125]

The Kwinana Desalination Plant opened in the Australian city of 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.[126]

Outflow

[edit]

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).[127][128] 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.[129]

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.[127][130]

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.[131][132]

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 it 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.[133][134]

Energy use

[edit]

The energy demand for desalination in the Middle East, driven by severe water scarcity, is expected to double by 2030. Currently, this process primarily uses fossil fuels, comprising over 95% of its energy source. In 2023, desalination consumed nearly half of the residential sector's energy in the region.[135]

Other issues

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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.[136] In the case of a plant built inland, pipes have to be laid into the ground to allow for easy intake and outtake.[136] However, once the pipes are laid into the ground, they have a possibility of leaking into and contaminating nearby aquifers.[136] Aside from environmental risks, the noise generated by certain types of desalination plants can be loud.[136]

Health aspects

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Iodine deficiency

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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,[137] finding iodine deficits among adults exposed to iodine-poor water[138] concurrently with an increasing proportion of their area's drinking water from seawater reverse osmosis (SWRO).[139] They later found probable iodine deficiency disorders in a population reliant on desalinated seawater.[140] A possible link of heavy desalinated water use and national iodine deficiency was suggested by Israeli researchers.[141] 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.[142] 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.[143] 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.[144]

Experimental techniques

[edit]

Other desalination techniques include:

Waste heat

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Thermally-driven desalination technologies are frequently suggested for use with low-temperature waste heat sources, as the low temperatures are not useful for process heat needed in many industrial processes, but ideal for the lower temperatures needed for desalination.[59] 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.[145][146]

Low-temperature thermal

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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 (14–18 °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.[147]

Experiments were conducted in the US and Japan to test the approach. In Japan, a spray-flash evaporation system was tested by Saga University.[148] 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 (36 °F) 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).[149] 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.[147][150][151]

Thermoionic process

[edit]

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.[152]

Evaporation and condensation for crops

[edit]

The Seawater greenhouse uses natural evaporation and condensation processes inside a greenhouse powered by solar energy to grow crops in arid coastal land.

Ion concentration polarisation (ICP)

[edit]

In 2022, using a technique that used multiple stages of ion concentration polarisation followed by a single stage of electrodialysis, researchers from MIT manage to create a filterless portable desalination unit, capable of removing both dissolved salts and suspended solids.[153] Designed for use by non-experts in remote areas or natural disasters, as well as on military operations, the prototype is the size of a suitcase, measuring 42 × 33.5 × 19 cm3 and weighing 9.25 kg.[153] The process is fully automated, notifying the user when the water is safe to drink, and can be controlled by a single button or smartphone app. As it does not require a high pressure pump the process is highly energy efficient, consuming only 20 watt-hours per liter of drinking water produced, making it capable of being powered by common portable solar panels. Using a filterless design at low pressures or replaceable filters significantly reduces maintenance requirements, while the device itself is self cleaning.[154] However, the device is limited to producing 0.33 liters of drinking water per minute.[153] There are also concerns that fouling will impact the long-term reliability, especially in water with high turbidity. The researchers are working to increase the efficiency and production rate with the intent to commercialise the product in the future, however a significant limitation is the reliance on expensive materials in the current design.[154]

Other approaches

[edit]

Adsorption-based desalination (AD) relies on the moisture absorption properties of certain materials such as Silica Gel.[155]

Forward osmosis

[edit]

One process was commercialized by Modern Water PLC using forward osmosis, with a number of plants reported to be in operation.[156][157][158]

Hydrogel based desalination

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Scheme of the desalination machine: the desalination box of volume contains a gel of volume which is separated by a sieve from the outer solution volume . The box is connected to two big tanks with high and low salinity by two taps which can be opened and closed as desired. The chain of buckets expresses the fresh water consumption followed by refilling the low-salinity reservoir by salt water.[159]

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.[159]

Small-scale solar

[edit]

The United States, France and the United Arab Emirates are working to develop practical solar desalination.[160] 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.[161] 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.[162]

Energy-Based Desalination

[edit]

Integrating renewable energy into desalination processes is a key strategy to relieve the high demand for energy and environmental impact of conventional desalination. While most of today's desalination plants are powered mainly by fossil fuels, some use solar, wind, geothermal and wave. These systems are especially appealing in sparsely populated and remote regions in which grid access is lacking, but renewable resources abound. [163]

Solar-Powered Desalination

[edit]

There are two types of solar-powered desalination; solar thermal-based and PV-based. Solar thermal desalination uses concentrated solar power (CSP) or solar collectors to produce heat for applications like multi-effect distillation (MED), multi-stage flash distillation (MSF) or membrane distillation (MD). In comparison, PV-driven systems use sunlight to produce energy to run reverse osmosis (RO) or electrodialysis units. Phase change materials, nanofluids and modern thermal storage technologies have been widely utilized to improve efficiency of small-scale solar stills and hybrid systems (Ghaffour, 2016). For example, modular solar distillation devices have been introduced in coastal villages in North Africa and the Middle East, delivering up to 5,000 liters of clean water per day with no greenhouse gas (GHG) emissions (IRENA, 2022).[164]

Systems Powered by Wind and Hybrid

[edit]

Wind-driven desalination employs mechanical or electrical power from wind turbines to operate RO units or pressurize feedwater. Wind-solar hybrid systems are under test under different weather conditions to avoid erratic conditions. In Spain, an integrated wind–PV desalination facility has been in the Canary Islands, and has seen a 40% reduction in operating expenses when compared to grid-based desalination systems due to the deployment in 2019 (Al-Karaghouli & Kazmerski, 2013).[165]

Application of Geothermal and Waste Heat Treatment

[edit]

Geothermal resources at low temperatures and industrial waste heat can feed thermal energy to desalination systems to enhance the efficiency of desalination systems for water recovery and production processes. Geothermal desalination has been introduced in Iceland and Turkey where subsurface heat is used to power MED or low temperature distillation units (Narayan, 2019). Also, waste heat from diesel generators or manufacturing plants or industrial sources can be part of a membrane distillation system that is also stored in the processing process on site that is inherently energy free (Gude, 2016).[166]

Technological Innovations

[edit]

Materials science is also transforming the paradigms of renewables. Nanostructured membranes, with enhanced permeability and salt rejection to overcome the high energy demand for solar-driven RO, have been proposed (Shen et al., 2021). Furthermore, solar-driven capacitive deionization (CDI) or photothermal membrane distillation employing sunlight-absorbing materials for locally heating at the membrane surface, significantly enhancing vapor flux but reducing fouling, is being investigated (Shatat et al., 2014).[167]

Economic and Environmental Implications

[edit]

The capital costs which renewable desalination requires are relatively high but the energy production is variable. But life-cycle analysis finds that the environmental footprint of solar- or wind-powered desalination systems is much lower than that of fossil-based processes. According to IRENA (2022), compared to conventional methods, renewable desalination is capable of lowering carbon emissions by up to 80%. In several coastal regions, the levelized price of water from PV–RO hybrid systems is falling below $1 per cubic meter and approaching grid-driven desalination.[168]

Applications in Social and Regional Contexts

[edit]

In humanitarian and off-grid applications, renewable desalination is an important tool. Portable solar desalination units are already being developed for disaster relief and military use. They will get them drinking water from either seawater or brackish water and would require very little maintenance. National Institute of Ocean Technology (NIOT) has successfully started solar-assisted desalination units in island territories in India, while pilot projects in California use concentrated solar energy to treat agricultural runoff (United Nations, 2023).[169] [170]

Future Outlook

[edit]

The world as a whole demonstrates a huge potential of renewable desalination as countries work towards sustainable solutions to overcome water scarcity. As new technologies such as energy storage, Artificial Intelligence for process optimization, and graphene membranes are developed, it is anticipated that even better efficiency will be achieved. While the technology of desalination continues to evolve, the International Desalination Association estimates a 20% new desalination capacity should come from renewable sources by 2035 (IRENA, 2022). In spite of a series of challenges, such as cost, intermittency, and the need to scale the implementation of renewables, integrating renewables is viewed as one of the most viable approaches to sustainable water harvesting in the new century.[171]

Passarell

[edit]

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.[172]

Geothermal

[edit]

Geothermal energy can drive desalination. In most locations, geothermal desalination beats using scarce groundwater or surface water, environmentally and economically.[citation needed]

Nanotechnology

[edit]

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.[173]

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.[174][175][176]

Biomimesis

[edit]

Biomimetic membranes are another approach.[177]

Electrochemical

[edit]

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.[178] As of 2012 a demonstration plant was operating in Singapore.[179] Researchers at the University of Texas at Austin and the University of Marburg are developing more efficient methods of electrochemically mediated seawater desalination.[180]

Electrokinetic shocks

[edit]

A process employing electrokinetic shock waves can be used to accomplish membraneless desalination at ambient temperature and pressure.[181] 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

[edit]

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.[182] 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.[183]

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.

Wave energy

[edit]

A small-scale offshore system uses wave energy to desalinate 30–50 m3/day. The system operates with no external power, and is constructed of recycled plastic bottles.[184]

Plants

[edit]

Trade Arabia claims Saudi Arabia is producing 7.9 million cubic meters of desalinated water daily, or 22% of world total, as of 2021 year's end.[185]

As new technological innovations continue to reduce the capital cost of desalination, more countries are building desalination plants as a small element in addressing their water scarcity problems.[193]

  • Israel desalinizes water for a cost of 53 cents per cubic meter[194]
  • Singapore desalinizes water for 49 cents per cubic meter[195] and also treats sewage with reverse osmosis for industrial and potable use (NEWater).
  • China and India, the world's two most populous countries, are turning to desalination to provide a small part of their water needs[196][197]
  • In 2007 Pakistan announced plans to use desalination[198]
  • All Australian capital cities (except Canberra, Darwin, Northern Territory and Hobart) are either in the process of building desalination plants, or are already using them. In late 2011, Melbourne will begin using Australia's largest desalination plant, the Wonthaggi desalination plant to raise low reservoir levels.
  • In 2007 Bermuda signed a contract to purchase a desalination plant[199]
  • Before 2015, the largest desalination plant in the United States was at Tampa Bay, Florida, which began desalinizing 25 million gallons (95000 m3) of water per day in December 2007.[200] In the United States, the cost of desalination is $3.06 for 1,000 gallons, or 81 cents per cubic meter.[201] In the United States, California, Arizona, Texas, and Florida use desalination for a very small part of their water supply.[202][203][204] Since 2015, the Claude "Bud" Lewis Carlsbad Desalination Plant has been producing 50 million gallons of drinking water daily.[205]
  • After being desalinized at Jubail, Saudi Arabia, water is pumped 200 miles (320 km) inland though a pipeline to the capital city of Riyadh.[206]

As of 2008, "World-wide, 13,080 desalination plants produce more than 12 billion gallons of water a day, according to the International Desalination Association."[207] An estimate in 2009 found that the worldwide desalinated water supply will triple between 2008 and 2020.[208]

One of the world's largest desalination hubs is the Jebel Ali Power Generation and Water Production Complex in the United Arab Emirates. It is a site featuring multiple plants using different desalination technologies and is capable of producing 2.2 million cubic meters of water per day.[209]

A typical aircraft carrier in the U.S. military uses nuclear power to desalinize 400,000 US gallons (1,500,000 L) of water per day.[210]

In nature

[edit]
Mangrove leaf with salt crystals

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.[211][212]

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.

Willow trees and reeds absorb salt and other contaminants, effectively desalinating the water. This is used in artificial constructed wetlands, for treating sewage.[213]

Society and culture

[edit]

Despite the issues associated with desalination processes, public support for its development can be very high.[214][215] One survey of a Southern California community saw 71.9% of all respondents being in support of desalination plant development in their community.[215] 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.[215]

See also

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References

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[edit]
Revisions and contributorsEdit on WikipediaRead on Wikipedia
from Grokipedia
Desalination (/ˌdiː.sæl.ɪˈneɪ.ʃən/ dee-sal-i-NAY-shun in British English; /diːˌsæl.əˈneɪ.ʃən/ dee-sal-uh-NAY-shun in American English, with primary stress on the 'nay' syllable) is the process of removing salts and other minerals from , such as or brackish , to produce freshwater suitable for human consumption, , or industrial applications. The technology addresses in arid regions by converting abundant —covering over 70% of Earth's surface—into usable resources, though it requires substantial energy input primarily to overcome or evaporate . Modern desalination predominantly employs , a membrane-based method that forces through semi-permeable barriers under to separate salts, accounting for the majority of global capacity due to its efficiency over thermal techniques like multi-stage flash evaporation. While ancient methods date back thousands of years, large-scale implementation began in the early with the first multi-effect plant in 1928, followed by rapid advancements post-1975 that halved production costs through improved membranes and systems. Today, mega-plants in nations like , , and emerging facilities in and produce hundreds of millions of liters daily, enabling self-sufficiency in hyper-arid environments but at the expense of high operational costs—often 50-70% attributed to energy—and environmental drawbacks including hypersaline discharge that harms marine ecosystems and significant when powered by fuels. Controversies center on these ecological impacts, such as larval mortality from structures and localized dead zones from , alongside debates over scalability amid rising global demand projected to double by 2030, underscoring the trade-offs between and .

Fundamentals

Definition and Basic Principles

Desalination refers to the physical processes used to remove dissolved salts, minerals, and other impurities from sources, primarily or brackish , yielding freshwater suitable for , , or industrial applications. typically contains 35,000 mg/L of (TDS), while brackish water ranges from 1,000 to 10,000 mg/L; desalination reduces TDS to below 500 mg/L for potable standards. Approximately 97 percent of Earth's is saline, making desalination a potential supplement to limited freshwater resources. The fundamental principle involves separating from ionic solutes through methods that leverage differences in volatility, solubility, or molecular size. Thermal distillation exploits the of : saline feedwater is heated to evaporate pure , which condenses separately, leaving non-volatile salts in the residue; this requires equivalent to at least 2,257 kJ per kg of evaporated under ideal conditions. Membrane processes, such as , apply hydraulic pressure exceeding the —often 50-80 bar for —to drive through semi-permeable membranes that reject hydrated ions due to size exclusion and charge repulsion. Every desalination system generates two streams: a low-salinity product (permeate or distillate) comprising 30-50 percent of the feed volume, and a concentrated reject requiring disposal. These principles are governed by and laws, where minimum energy demands arise from the of mixing—approximately 1-2 kWh per cubic meter for —but real processes incur inefficiencies from irreversibilities like heat losses or pressure drops. Pretreatment, such as to remove particulates, and post-treatment, including remineralization and disinfection, address and ensure product quality.

Role in Addressing Water Scarcity

Desalination serves as a critical supplement to conventional freshwater sources in regions facing acute , producing potable water from and brackish where natural supplies are insufficient due to arid climates, , or population pressures. Globally, over 20,000 desalination plants in more than 150 countries generate approximately 150 million cubic meters of freshwater per day as of 2025, supplying to around 300 million people and mitigating shortages in coastal areas with limited rainfall or river access. In water-stressed nations like , desalination accounts for 55-75% of domestic , enabling the country to achieve water surplus through large-scale facilities such as Sorek and , which have reversed decades of scarcity-driven rationing. Similarly, Saudi Arabia relies on desalination for about 50% of its municipal needs, with the Saline Water Conversion Corporation operating plants that produce over 5 million cubic meters daily to support urban and industrial demands in the Arabian Peninsula's hyper-arid environment. The technology's efficacy stems from its ability to tap into the vast oceanic salt water resource—covering 71% of Earth's surface—bypassing hydrological constraints like depletion or disputes, as evidenced by Israel's export of desalinated water expertise to neighbors and its role in stabilizing regional water balances. Advances in energy efficiency, particularly in , have reduced consumption to 3 kWh per cubic meter, making it viable when paired with low-cost or renewables, though thermal methods remain higher at 10-15 kWh per cubic meter. This has enabled scalability in Gulf states, where desalination now constitutes up to 90% of public water in some emirates, demonstrating causal links between plant deployment and reduced scarcity indices. Despite these contributions, desalination's role remains constrained by high capital and operational costs—often $0.50-1.00 per cubic meter—and environmental externalities, including brine discharge that can hypersaline local ecosystems and elevate marine salinity by up to 50% near outfalls if unmanaged. demands, equivalent to 3-6% of a nation's in heavy users like , limit broader adoption without grid expansions or solar integration, while pretreatment chemical use and intake entrainment of add ecological costs not always quantified in feasibility studies. Thus, while desalination addresses immediate in affluent coastal zones, it functions best as a complementary strategy alongside conservation, wastewater reuse, and reforms, rather than a standalone for global freshwater deficits projected to affect 5 billion people by 2050.

Historical Development

Pre-20th Century Attempts

Early attempts at desalination relied primarily on simple , where was heated to evaporate vapor for , or rudimentary methods, though these were small-scale and labor-intensive, suitable mainly for maritime or isolated uses rather than widespread application. Archaeological and textual evidence suggests such practices date to the , with Minoan sailors in (ca. 3200–1100 BC) employing boiling techniques during Mediterranean voyages to produce potable water from . Similarly, in the Persian Empire around 1250 BC, infrastructure at in included water treatment systems that diverted and processed saline sources into reservoirs, indicating early organized efforts to manage . In , philosophical observations laid conceptual groundwork: (ca. 610–547 BC) noted water's evaporation and recycling in the hydrological cycle, while (384–322 BC) explicitly described desalting by boiling it in a vessel and collecting condensate via a sponge, as recorded in Meteorologica. Greek sailors routinely applied on ships, using basic apparatus to separate vapor from . Roman practices advanced , employing clay vessels to trap salts and combining heating with or gravel layers for purification, though these methods yielded low volumes and were adjuncts to aqueduct systems rather than primary solutions for . (AD 23–79) documented land-based techniques like passing through fleeces or wax-impregnated balls to capture distillate. During the medieval period, Arab scholars refined amid arid environments, experimenting with alembics and solar concentration via mirrors to heat , as evidenced in alchemical texts; these innovations stemmed from necessities in the Islamic world, where saline groundwater was common. In , texts from the (ca. 475–221 BC) and later (ca. 200 BC) describe using bamboo mats or sheeting in steamers to adsorb salts from boiled brines, applied to both and concentrated solutions. By the 4th century AD, accounts like St. Basil's post-shipwreck narrative highlight sponges positioned over boiling pots to condense vapor, a portable method echoed in traditions. Nineteenth-century efforts marked a transition toward semi-industrial scales, with the first documented land-based seawater distillation plant constructed around 1560 on an island off Tunisia's coast, likely for military or colonial needs, though details on capacity remain sparse. The British established a distillation facility at Aden, Yemen, in the mid-19th century to provision ships at the Red Sea port, relying on steam-powered evaporation. By 1898, Russia operated an early multi-effect evaporation plant on land, producing modest daily outputs of fresh water through sequential boiling stages, foreshadowing 20th-century thermal methods but still constrained by high fuel demands. These pre-20th century endeavors, while innovative, were hampered by energy inefficiencies and material limitations, producing negligible quantities compared to modern capacities—typically liters per day for shipboard use or cubic meters for rare land setups.

20th Century Advancements

The 20th century marked a pivotal shift in desalination from small-scale, energy-intensive distillation to scalable thermal and membrane processes, driven by post-World War II water scarcity and government investments. In 1955, the U.S. Department of the Interior established the Office of Saline Water to fund research, leading to the first U.S. desalination plant in Freeport, Texas, in 1961. Concurrently, multi-stage flash (MSF) distillation emerged as a breakthrough thermal method; developed in the 1950s by Weirs of Cathcart in Scotland, it was first installed on the U.S. Navy aircraft carrier Independence in 1954 with four 5-stage units producing 50,000 gallons per day each, and scaled to 500,000 imperial gallons per day units in Kuwait by 1956. MSF's efficiency stemmed from flashing brine in successive low-pressure stages, reducing energy needs compared to prior multi-effect distillation. Membrane technologies advanced rapidly mid-century, with commercialized in the 1950s for treatment using ion-selective membranes under electric fields. (RO) gained traction after 1959 demonstrations by Breton and Reid using films, culminating in the first synthetic RO membrane in 1960 at the . In 1962, Sidney Loeb and Srinivasa Sourirajan developed the asymmetric membrane at UCLA, enabling higher flux and salt rejection, followed by the first practical spiral-wound module in 1963 by . The inaugural commercial RO plant opened in , in 1965, treating at 1 million gallons per day. By the 1970s, seawater applications proliferated; the first seawater RO plant operated in in 1974, and a large facility in , , in 1975 employed interfacial composite membranes. Innovations included DuPont's hollow-fiber module in 1967 and John Cadotte's fully aromatic thin-film composite (FT-30) membrane in 1978, which offered superior durability and performance, patented as a three-layer TFC in 1981. Thermal methods like MSF dominated large-scale production in the , with plants exceeding 10 million gallons per day by the late , while RO costs declined due to membrane improvements, setting the stage for broader adoption. Low-pressure nanofiltration membranes emerged in 1986, further enhancing efficiency for partial demineralization. These developments reduced specific energy consumption from over 10 kWh/m³ in early thermal plants to lower figures, enabling economic viability for arid regions.

Post-2000 Expansion and Scaling

Global desalination capacity expanded dramatically after 2000, increasing fivefold from approximately 20 million cubic meters per day (m³/d) around the to over 100 million m³/d by the late 2010s, driven primarily by (SWRO) technology. This growth reflected annual capacity additions of 6-12%, with cumulative contracted capacity reaching 99.8 million m³/d by 2017, supported by over 16,000 operational plants worldwide by the early . The , particularly (GCC) nations like and the , accounted for the majority of this scaling, where desalination supplies over 70% of municipal water in arid regions facing chronic scarcity. SWRO's dominance post-2000 stemmed from its lower energy requirements compared to thermal methods, enabling exponential plant proliferation while thermal distillation saw only marginal gains. Over 90% of new capacity added since 2000 utilized RO membranes, which force seawater through semi-permeable barriers under high pressure, achieving energy efficiencies that reduced specific consumption to 3-4 kWh/m³ for large-scale plants. This shift was facilitated by membrane material advancements and pretreatment innovations, such as , which minimized and extended operational life, allowing for mega-plants exceeding 1 million m³/d capacity. Iconic scaling projects exemplified this era's ambitions: Saudi Arabia's Ras Al-Khair plant, commissioned in 2014 with 1.036 million m³/d output, became the world's largest SWRO facility, integrating co-generation for efficiency. Similarly, the UAE's Taweelah plant (909,200 m³/d) and Israel's Sorek facility (624,000 m³/d, operational 2013) demonstrated modular scaling, where plants are built in phases to match demand while optimizing capital costs. Outside the Middle East, and the expanded brackish and RO, with Carlsbad in (189,300 m³/d, 2015) addressing coastal shortages amid regulatory hurdles. Cost declines further propelled adoption, with levelized costs for SWRO dropping from $0.50-1.00/m³ in the early 2000s to $0.40-0.70/m³ by 2020, attributable to , energy price hedging, and process optimizations like devices achieving 95% efficiency. Despite persistent challenges such as discharge and high upfront investments, these trends positioned desalination as a viable supplement to traditional supplies, with projections for continued growth to meet rising global demand projected at 7% annually through the .

Core Technologies

Thermal Distillation Methods

Thermal distillation methods evaporate using heat, separating pure vapor from concentrated , which is then condensed to produce . These processes leverage the of vaporization, requiring to boil water at or near or under to lower boiling points and reduce scaling risks. Unlike membrane-based techniques, thermal distillation achieves near-total rejection of non-volatile solutes, yielding distillate with conductivity below 10 μS/cm and minimal biological contaminants, provided feedwater pretreatment addresses particulates and organics. Principal applications include large-scale desalination integrated with steam-cycle power plants, where offsets energy costs, and smaller systems for high-purity needs like . Core variants encompass multi-stage flash (MSF) distillation, multiple-effect distillation (MED), and vapor compression (VC) systems. In MSF, preheated enters successive chambers at reducing s, inducing in each stage; vapor condenses on tubes carrying incoming feed, preheating it while recovering . MED operates evaporators in series, where vapor from one effect heats the next at lower temperature and , achieving higher through multi-stage heat reuse; typical configurations use 4-16 effects at top temperatures of 60-70°C to minimize . VC methods, including mechanical (MVC) and thermal (TVC), compress low-pressure vapor to superheat it for duties, suitable for capacities under 10,000 m³/day with electrical or steam-driven compressors. Energy metrics highlight trade-offs: MSF plants exhibit gain output ratios (GOR) of 8-16 (kg distillate per kg ), translating to inputs of 80-120 kWh/m³ and electrical use of 1.5-4 kWh/m³, dominated by pumping and vacuum maintenance. MED offers GOR up to 14 with demands around 50-100 kWh/m³ at lower temperatures, reducing scaling but requiring careful concentration control below 1.5-2 times feed . VC variants achieve GOR of 10-20 in MVC via efficient compressors, though total (mostly electrical) ranges 7-15 kWh/m³ equivalent, favoring standalone or hybrid operation over MSF/MED's scale dependency. Overall, thermal methods' viability hinges on cheap heat sources, with yielding levelized costs of $0.50-1.00/m³ for at 35,000 ppm TDS, versus higher standalone figures due to sensitivity. Challenges include antiscalant dosing, acid cleaning for CaSO₄ , and from Cl⁻ in stainless or , necessitating robust materials.

Multi-Stage Flash and Multiple-Effect Distillation

Multi-stage flash (MSF) distillation involves heating to a high and then introducing it into a series of chambers with progressively lower pressures, causing portions of the water to "flash" into vapor at each stage; the vapor condenses on cooler tubes, producing while the remaining moves to the next stage. This process typically operates with 10 to 25 stages and relies on steam from power plants for heating, achieving a gain output ratio () of 8 to 16, where GOR measures kilograms of distillate produced per kilogram of steam input. MSF plants consume substantial , around 80–120 kWh per cubic meter of distillate, plus 1.5–4 kWh of , making it energy-intensive compared to methods. The first commercial MSF plant was commissioned in 1962 in Qatar's Ras Abu Aboud with a capacity of 6,800 cubic meters per day, marking the start of widespread adoption in the Middle East due to abundant low-cost energy from oil. MSF's robustness suits high-salinity feeds and large-scale operations, but disadvantages include severe scaling and corrosion from temperatures up to 110°C, necessitating acid dosing and exotic materials, which elevate capital costs to $1,000–2,000 per cubic meter of daily capacity. By 2012, MSF accounted for 26.8% of global desalination capacity, though its share has declined with the rise of reverse osmosis due to higher energy demands. Multiple-effect distillation (MED) evaporates in a sequence of effects, where vapor from one effect condenses to the in the next at lower temperature and pressure, typically using 4 to 16 effects and operating at 60–70°C to minimize scaling. This serial reuse of yields a higher GOR of 10–18, improving over MSF, with use around 1.5–2.5 kWh per cubic meter. MED variants like multiple-effect evaporation with vapor compression further boost by compressing non-condensable vapors. Early MED plants emerged in the 1930s, with a 60 cubic meters per day facility installed on an island in 1928 and adopting it by the early 1930s for coastal operations. Modern examples include hybrid plants in the UAE, such as those with capacities up to 100,000 cubic meters per day, often paired with gas turbines for . MED offers advantages like higher coefficients and lower risk than MSF, enabling operation with poorer water quality, but it produces smaller plant sizes (typically under 50,000 cubic meters per day) and requires precise control to avoid issues. Globally, MED holds about 7% as of 2019, favored in regions with variable prices. Compared to MSF, MED provides better energy efficiency and reduced pretreatment needs due to lower temperatures, avoiding flash evaporation's streams that concentrate non-condensables; however, MSF remains prevalent in hypersaline areas for its tolerance to impurities. Both methods excel in settings, where waste heat from power generation offsets high thermal inputs, but face challenges from discharge and environmental impacts not fully mitigated by current designs.

Vapor-Compression and Other Variants

Vapor-compression desalination recycles by compressing evaporated to increase its and , allowing the superheated vapor to condense while providing for further of saline feedwater. This single- or multi-effect process contrasts with multi-stage flash by relying on mechanical or thermal compression rather than pressure reduction for flashing, achieving higher through heat recovery. Systems typically operate under to lower boiling points, with occurring at 50–70°C to minimize scaling. Mechanical vapor compression (MVC) uses an electric-driven compressor, such as a centrifugal or turbocompressor, to elevate vapor pressure, making it independent of external steam sources and suitable for small- to medium-capacity plants (up to 10,000 m³/day). MVC excels in treating brackish water (1,000–10,000 ppm TDS) due to lower energy penalties from lower osmotic pressures, with electrical energy consumption of 7–18 kWh/m³ and gained output ratios (GOR) of 10–20, outperforming standalone multi-effect distillation in electricity-limited settings. Commercial examples include IDE Technologies' four MVC units in Israel, each producing 2,560 m³/day since the early 2000s, demonstrating reliability in continuous operation for ultrapure water production. Thermal vapor compression (TVC), often paired with (MED-TVC), employs a steam-jet ejector using high-pressure motive (from turbines) to entrain and compress low-pressure vapor, reducing electrical demand to primarily pumping (2–5 kWh/m³ total equivalent). This variant suits large-scale desalination (capacities exceeding 50,000 m³/day), yielding GORs of 8–16 by leveraging , though it requires at 1–3 bar absolute. MED-TVC plants, prevalent in the , achieve distillate purities below 10 ppm TDS but face higher capital costs from ejector complexity. Other variants include absorption and adsorption compression, which use chemical sorbents (e.g., solutions or silica gels) driven by heat rather than electricity, targeting remote or solar-integrated applications with theoretical efficiencies rivaling MVC but limited commercial deployment due to material corrosion and cycle complexity. Hybrid MVC-MED systems combine effects for capacities up to 20,000 m³/day, minimizing volumes and integrating with renewables for off-grid use, as modeled in recent simulations showing 15–25% savings over pure methods.

Membrane-Based Processes


Membrane-based desalination processes separate dissolved salts from using semi-permeable membranes that allow water passage while rejecting ions and solutes. These methods encompass pressure-driven techniques like and nanofiltration, electrically-driven , and osmotically-driven , each leveraging distinct physical principles to achieve demineralization without phase change. Operating at ambient temperatures, membrane processes demand primarily electrical or to overcome osmotic resistance, contrasting with thermal distillation's heat-intensive . This isothermal operation yields lower overall energy use, typically 2.5–4.0 kWh/m³ for seawater , compared to thermal equivalents exceeding 10 kWh/m³ in alone.
Advancements in polymer membrane synthesis, such as thin-film composites with enhanced selectivity and , have reduced specific energy consumption by over 80% since the 1970s through improved rejection rates exceeding 99% for monovalent ions and integration of devices like pressure exchangers. Membrane systems achieve water recoveries of 40–50% for and up to 85% for brackish sources, with pretreatment via or chemical dosing mitigating fouling from organics, scales, and bio-growth that can halve without intervention. Concentrated discharge poses environmental risks, including hypersalinity and chemical residuals, prompting innovations in zero-liquid discharge configurations using evaporators or crystallizers. Electrodialysis employs alternating cation- and anion-exchange membranes stacked between electrodes, where direct current drives selective ion migration, concentrating salts in alternate compartments; it excels for monovalent ions in brackish waters under 5,000 mg/L TDS, with energy needs scaling quadratically with salt concentration. Forward osmosis draws water across the membrane via an osmotic gradient from a high-salinity draw solution, avoiding high pressures but requiring regeneration steps that currently limit scalability, though pilot recoveries reach 90% with reduced fouling propensity. Hybrid membrane-thermal setups, such as membrane distillation, combine vapor permeation through hydrophobic pores with low-grade heat, bridging the two paradigms for fouling-resistant operation. Overall, membrane technologies now account for over 60% of global desalination capacity, driven by modular scalability and cost declines to $0.40–0.70/m³ for large seawater plants.

Reverse Osmosis Dominance

(RO) has emerged as the dominant desalination technology, accounting for approximately 85% of operational plants worldwide as of 2025. This prevalence stems from its superior energy efficiency compared to methods, with modern seawater RO systems achieving specific energy consumption as low as 2-3 kWh per cubic meter of product , versus 10-16 kWh/m³ for multi-stage flash . Advancements in thin-film composite membranes since the have enabled higher flux rates and salt rejection exceeding 99.5%, while energy recovery devices like pressure exchangers recapture up to 95% of hydraulic energy from streams, drastically reducing operational costs. The technology's modularity allows for scalable plant designs, from small units to gigaliter-scale facilities, facilitating rapid deployment in water-stressed regions such as the and . RO overtook thermal processes in new capacity additions around the early , driven by post-1970s oil price volatility that highlighted thermal methods' vulnerability to costs, alongside cost reductions from $10/m² in the 1980s to under $1/m² by 2010. By 2024, RO held a commanding share of global desalination capacity, estimated at 69-85% depending on metrics of installed versus operational volume. Within membrane-based processes, RO eclipses alternatives like , which is less viable for high-salinity due to higher energy demands (5-10 kWh/m³) and fouling issues, confining electrodialysis primarily to lower-salinity brackish sources. Ongoing innovations, including anti-fouling coatings and high-pressure modules tolerant of osmotic pressures up to 100 bar, continue to solidify RO's position, though challenges like disposal and pretreatment for persist.

Electrodialysis and Forward Osmosis

(ED) is a membrane-based desalination process that employs an to drive ions through selective ion-exchange , separating salt from in alternating cation- and anion-selective compartments. In ED systems, a voltage applied across a stack of membranes creates ion migration, concentrating in alternate channels while producing desalinated in others; this process is particularly effective for with salinities up to 3 g/L, where it achieves salt removal efficiencies of 70-90% depending on membrane properties and . for ED typically ranges from 0.7 to 2.5 kWh/m³ for brackish feeds, influenced by factors such as feed , recovery rate (often 50-90%), and stack design, with recent advancements in ion-exchange membranes reducing resistance and improving overall to over 30% in optimized setups. Compared to (RO), ED demonstrates lower energy use and operational costs for low-salinity desalination, as it avoids high-pressure pumping and is less prone to from particulates, though it requires pretreatment for scaling ions like calcium and magnesium. Applications include treatment and industrial reuse, with commercial plants operational since the 1960s, such as those in and the processing up to 10,000 m³/day; however, ED's scalability for (high >35 g/L) is limited due to exponential energy increase with ion concentration, making it non-competitive with RO for such feeds. Hybrid ED-RO systems have emerged to pretreat high-salinity brines, enhancing overall plant recovery and reducing waste disposal challenges. Forward osmosis (FO) utilizes an gradient across a , where a high-osmolarity draw solution pulls from the saline feed, avoiding the high hydraulic pressures of RO and reducing risks by up to 50% in some configurations. The process requires subsequent draw solute recovery, often via thermal methods, nanofiltration, or , which can add 1-2 kWh/m³ to total energy; standalone FO desalination yields fluxes of 5-20 L/m²/h with feeds, achieving 40-60% recovery when paired with draw agents like 2-methyl-1,3-propanediol or . Energy efficiency in FO-RO hybrids ranges from 1.5 to 3.5 kWh/m³ for , potentially lower than standalone RO's 2-4 kWh/m³ due to FO's pretreatment role in mitigating scaling, though internal limits flux and requires thin-channel designs for optimization. FO's primary applications target desalination and impaired water reuse, with pilot-scale demonstrations since 2010 showing promise in zero-liquid discharge scenarios; for instance, hybrid systems have treated from oilfields, recovering 80% of volume while concentrating contaminants. Despite lower propensity and potential for renewable integration via low-grade heat for draw recovery, FO remains emerging due to membrane durability issues and the need for recyclable, low-cost draw solutes, with commercial adoption lagging behind RO—fewer than 10 large-scale plants worldwide as of 2023, mostly in for niche high-fouling feeds. In comparisons, FO excels in energy savings for dilute feeds or when hybridized, but its viability hinges on advancing draw regeneration to compete economically with ED or RO in broad desalination contexts.

Alternative and Hybrid Approaches

Freeze-thaw desalination, also known as freeze crystallization, exploits the lower freezing point of pure water compared to saline solutions by cooling to induce formation, which inherently rejects salts due to differences in lattice structure. The process typically involves direct or indirect contact freezing, followed by mechanical separation of from concentrated and subsequent melting of the purified . Energy requirements are notably lower than thermal distillation methods, with reported consumptions as low as 0.09 kWh/m³ for progressive freeze concentration under optimized conditions, primarily for , though total system energy including separation can reach 1.5–3 kWh/m³. Advantages include minimal scaling and risks at low temperatures and potential for high-purity output exceeding 99% salt rejection, but challenges persist in salt entrapment within matrices and eutectic freezing points limiting recovery rates to 70–80% without hybrid enhancements. Pilot studies, such as those integrating slurry pressing, have demonstrated feasibility for treatment, with energy use around 54 kWh/m³ for reject streams, though commercial scalability remains limited by costs and process complexity. Ion exchange desalination employs to selectively bind and exchange salt ions (e.g., Na⁺ for H⁺ and Cl⁻ for OH⁻), producing demineralized via subsequent neutralization. While effective for low-total-dissolved-solids feeds like softening or polishing treated effluents, its application to desalination is constrained by resin capacity saturation—typically 1–2 equivalents per kg of —necessitating massive volumes and frequent regeneration with strong acids and bases, which generates and elevates costs beyond 10–20 USD/m³. Limitations include incomplete removal of all ions in complex matrices, sensitivity to organic fouling, and uneconomic scaling for high-salinity sources (>35 g/L TDS), rendering it supplementary rather than standalone; for instance, it complements for trace contaminant removal but not bulk desalination. Hybrid approaches integrate freeze-thaw or with dominant methods like to leverage synergies, such as pre-concentrating via freezing to reduce downstream or energy needs. One configuration places freeze concentration upstream of RO, achieving up to 50% volume reduction with total energy under 5 kWh/m³ in lab trials, mitigating limits in high- feeds. Electrochemical-ion exchange hybrids further enhance selectivity for specific ions, though overall adoption lags due to integration complexities and variable performance in real-world fluctuations. Renewable-powered variants adapt desalination to intermittent clean energy sources, prioritizing off-grid or remote applications where grid electricity is costly or unavailable. Solar-driven systems, including passive stills yielding 2–5 L/m²/day via evaporation-condensation or active thermal collectors for multi-effect , achieve levelized costs of 0.5–2 USD/m³ in sunny regions but suffer low productivity (e.g., <10 m³/day per unit) and dependence on direct normal irradiance. Wind-powered reverse osmosis, as in hybrid turbines-RO setups on islands like Gran Canaria since the 2000s, delivers stable output by buffering storage, with capacities up to 1 MW and efficiencies improved 20–30% via predictive controls, though turbine intermittency requires 20–50% overcapacity. Wave energy converters, such as oscillating water columns coupled to desalination, harness coastal kinetics for mechanical pumping, with prototypes like those in Portugal generating 100–500 kW for small plants, but high capital costs (3–5 times onshore renewables) and site-specific wave patterns limit deployment to <1% of global capacity as of 2023. Hybrid solar-wind-wave platforms, while promising for diversified output, face engineering hurdles in offshore durability and energy conversion losses exceeding 40%, with desalination integration still largely experimental. These variants reduce fossil fuel reliance—cutting emissions by 80–90% versus diesel backups—but economic viability hinges on subsidies and storage advancements, with payback periods of 5–10 years in high-resource locales.

Freeze-Thaw and Ion Exchange

Freeze-thaw desalination, also known as freeze desalination, exploits the principle that ice crystals formed from seawater exclude dissolved salts, producing purer water upon separation and melting. The process typically involves cooling seawater to below 0°C to nucleate ice formation, followed by growth of ice crystals, mechanical or hydraulic separation of ice from concentrated brine, and washing or thawing the ice to yield fresh water. This method leverages the lower latent heat of fusion (334 kJ/kg) compared to vaporization (2260 kJ/kg) in thermal distillation, potentially reducing energy requirements by up to 50% for the phase change step. Advantages include minimal scaling and corrosion due to operation at low temperatures, high tolerance to feedwater variations in salinity or impurities, and production of very pure ice with salt rejection rates exceeding 99%. However, challenges persist in efficient ice-brine separation, prevention of salt entrapment during crystal growth, and the energy needed for refrigeration, which historically has limited scalability. Pilot plants, such as those tested in the 1960s and 1970s under U.S. Bureau of Reclamation programs, demonstrated feasibility but faced economic hurdles from incomplete desalination in single stages and high capital costs for multi-stage systems. As of 2023, commercial deployment remains absent, confined to laboratory and small-scale pilots, with ongoing research exploring hybrid vacuum-assisted or eutectic freezing to improve efficiency. Ion exchange desalination employs synthetic resins to selectively swap undesirable ions in seawater, such as sodium and chloride, for hydrogen or hydroxide ions, effectively demineralizing the water through neutralization to form pure H₂O. The process requires periodic resin regeneration using acids or bases, generating concentrated waste streams. While efficient for brackish water or polishing low-salinity effluents, direct application to seawater is impractical due to the high ionic load (approximately 35,000 ppm TDS), necessitating massive resin volumes and frequent, costly regenerations that produce brine volumes exceeding those of reverse osmosis. In hybrid configurations, ion exchange serves as a post-treatment to remove residual hardness or specific contaminants like boron after primary desalination via reverse osmosis, enhancing overall purity without standalone seawater feasibility. Energy consumption is lower than thermal methods for targeted ion removal, but total costs for seawater remain prohibitive, with studies indicating regeneration inefficiencies and environmental concerns from chemical wastes. Recent innovations, such as continuous electrodeionization or resin-integrated flow systems, aim to mitigate saturation issues but have not achieved commercial viability for full-scale seawater desalination as of 2024.

Renewable-Powered Variants (Solar, Wind, Wave)

Renewable-powered desalination systems integrate solar, wind, or wave energy to drive processes like reverse osmosis (RO) or thermal distillation, reducing reliance on fossil fuels and grid electricity while addressing intermittency through storage or hybrid designs. These variants are particularly suited for remote or coastal regions with abundant renewables but limited infrastructure, though scalability remains constrained by energy variability and higher upfront costs compared to conventional plants. Peer-reviewed analyses indicate that solar-thermal methods often outperform photovoltaics for thermal desalination due to lower storage needs, while wind and wave systems excel in direct mechanical energy transfer for RO. Solar-powered desalination employs photovoltaic (PV) panels to generate electricity for RO pumps or solar-thermal collectors for evaporation-based methods like multi-effect distillation. A 2022 MIT-developed system achieves efficiencies exceeding 5 liters per hour per square meter under sunlight, rejecting salt concentrations up to five times seawater levels without additional energy input, at projected costs below $0.50 per cubic meter in sunny climates. In practice, hybrid solar-RO plants in the Middle East, such as Saudi Arabia's Al-Khafji facility operational since 2017, produce 60,000 cubic meters daily using concentrated solar power (CSP) cogeneration, cutting energy costs by 30-50% versus diesel alternatives. Solar-thermal variants, reviewed in 2023 studies, yield levelized costs of $0.72-1.50 per cubic meter, influenced by insolation rates above 5 kWh/m²/day and minimal battery requirements for thermal storage. Wind-powered systems typically couple turbines to RO units, leveraging steady coastal winds for baseload-like operation. A notable case is the Gran Canaria plant in Spain, where an 850 kW turbine powers a 4,500 m³/day RO facility since the early 2000s, achieving specific energy consumption of 3-4 kWh/m³ through grid-tied operation that offsets up to 80% of electricity needs. Parametric studies on direct wind-RO integration show optimal performance at wind speeds of 8-12 m/s, with permeate fluxes increasing 20-30% under variable loading, though output drops below 6 m/s without backups. Reviews of island deployments highlight hybrid wind-diesel setups reducing operational costs by 40% in sites like the Aegean Sea, where wind resources exceed 7 m/s annually. Wave-powered desalination harnesses oscillatory ocean motion via buoys or oscillating water columns to drive pumps or pressure exchangers, bypassing electrical conversion losses. The U.S. National Renewable Energy Laboratory's (NREL) Hybrid Energy Response in Ocean Waves (HERO) device, tested off North Carolina since 2023, generates pressures up to 70 bar for RO membranes using wave amplitudes of 1-2 meters, producing freshwater at rates scalable to 10-20 m³/day per unit without external power. Emerging floating systems, such as those prototyped in 2023, convert wave energy into mechanical forces yielding 25% recovery rates from seawater, with modular designs targeting $0.50-1.00 per cubic meter in high-wave regimes like the Atlantic coasts. Technology reviews note wave methods' potential for off-grid viability but cite challenges in survivability during storms, with commercial pilots limited to capacities under 1,000 m³/day as of 2024.

Engineering and Operations

Energy Consumption and Efficiency Metrics

Desalination processes exhibit significant variation in energy requirements, with membrane-based methods like reverse osmosis (RO) generally achieving lower specific energy consumption (SEC) compared to thermal distillation techniques such as multi-stage flash (MSF). SEC is typically measured in kilowatt-hours per cubic meter (kWh/m³) of produced water, encompassing electrical energy for pumping and, in thermal processes, equivalent thermal energy inputs. Modern RO systems for seawater desalination operate at 2.5–4.0 kWh/m³, benefiting from energy recovery devices that recapture pressure energy from brine reject streams, reducing net consumption by up to 60% compared to systems without such devices. In contrast, thermal methods like MSF require 80–120 kWh/m³ of thermal energy plus 1.5–4 kWh/m³ electrical, though cogeneration with power plants can offset some costs by utilizing waste heat. Efficiency improvements in RO have driven SEC reductions from approximately 6–10 kWh/m³ in early implementations to current levels, attributed to advancements in high-pressure pumps, low-friction membranes, and optimized recovery rates of 40–50%. For instance, optimized models achieve 3.65 kWh/m³ at 60–65% recovery, approaching the practical thermodynamic minimum of about 1.6 kWh/m³ limited by osmotic pressure. Thermal processes employ metrics like gain output ratio (GOR), defined as kilograms of distillate per kilogram of steam input; MSF typically yields GOR values of 8–12, while multiple-effect distillation (MED) reaches 10–16, reflecting multi-stage heat reuse but still higher overall energy intensity than RO due to latent heat demands.
MethodPrimary Energy TypeTypical SEC (kWh/m³)Key Efficiency MetricNotes
Reverse Osmosis (Seawater)Electrical2.5–4.0Recovery rate: 40–50%Energy recovery devices reduce pumping needs; theoretical min. ~1.6 kWh/m³
Multi-Stage Flash (MSF)Thermal + ElectricalThermal: 80–120; Elec: 1.5–4GOR: 8–12High thermal input; suited for cogeneration
Multiple-Effect Distillation (MED)Thermal + ElectricalElec: 1.5–2.5GOR: 10–16Lower electrical than MSF; heat reuse enhances efficiency
Ongoing trends indicate further SEC declines, with RO energy use dropping roughly 80% since the 1980s through membrane innovations and system optimizations, though site-specific factors like feed salinity (e.g., 35–45 g/L for seawater) and temperature influence performance. Hybrid approaches integrating renewables or advanced pretreatment can yield additional gains, but electrical grid dependency remains a bottleneck for scalability in non-cogenerated setups. Empirical data from operational plants underscore that pretreatment energy (e.g., for fouling control) can add 0.5–1 kWh/m³ in RO, emphasizing holistic system design for minimal total consumption.

Plant Design: Intake, Pretreatment, and Brine Management

Desalination plant intake systems withdraw seawater while minimizing ecological disruption, primarily through control of impingement—organisms trapped on screens—and entrainment—organisms passing through to the plant. Open-ocean intakes, often featuring velocity caps or traveling screens, maintain approach velocities below 0.15 m/s to reduce fish and plankton intake, as recommended in Australian guidelines for environmental protection. In California, through-screen velocities are limited to 0.5 ft/s (approximately 0.15 m/s) to comply with state regulations aimed at safeguarding marine life. Subsurface alternatives, such as infiltration galleries or beach wells, leverage sediment filtration to achieve over 90% reduction in entrainment compared to surface intakes, though they require suitable geological conditions and higher capital costs. Pretreatment processes condition raw seawater to protect downstream reverse osmosis (RO) membranes from fouling, scaling, and biofouling, which can increase energy use by up to 50% if unchecked. Initial coarse screening removes debris larger than 10 mm, followed by fine screening at 1-3 mm to eliminate smaller particulates. Coagulation with ferric chloride or aluminum salts induces flocculation of colloids and organics, often paired with dissolved air flotation (DAF) for solids removal achieving 80-95% turbidity reduction. Advanced systems incorporate ultrafiltration (UF) membranes with pore sizes of 0.01-0.1 μm, providing consistent silt density index (SDI) below 3 for RO feed, superior to conventional multimedia filtration in handling variable seawater quality. Chemical dosing, including antiscalants to inhibit calcium sulfate precipitation and biocides for microbial control, is standard, with pH adjustment via sulfuric acid to mitigate carbonate scaling. Brine management addresses the hypersaline reject stream from RO processes, typically exhibiting a concentration factor of 1.8-2.0 times feed salinity—reaching 60-70 ppt total dissolved solids (TDS) at 40-50% recovery rates—posing risks of benthic habitat alteration and oxygen depletion if not dispersed properly. Ocean discharge remains predominant, utilizing multi-port diffusers to achieve dilution ratios of 20:1 or higher, limiting near-field salinity plumes to under 5% above ambient levels. For inland or environmentally sensitive sites, zero liquid discharge (ZLD) approaches employ evaporators and crystallizers to recover 95%+ of residual water while extracting salts for reuse, though at 2-5 times the energy cost of direct discharge. Emerging valorization techniques, such as selective precipitation for lithium or magnesium recovery, transform brine into resources, but scalability remains limited by economic viability and trace contaminant handling. Empirical monitoring at operational plants, like those in the Arabian Gulf, confirms that well-designed diffusers mitigate acute toxicity, with salinity gradients dissipating within 100-500 m.

Cogeneration and Renewable Integration

Cogeneration schemes couple desalination units, particularly thermal processes like multi-effect distillation (MED) and multi-stage flash (MSF) distillation, with power generation facilities to exploit waste heat from turbines or steam cycles, thereby reducing the net energy input per unit of water produced. In such dual-purpose plants, low-grade heat—typically from gas or steam turbines—drives evaporation, achieving overall plant efficiencies where desalination consumes only 2.5–3% of standard primary energy relative to standalone power production. This integration is prevalent in regions with high desalination demand, such as the Middle East, where combined cycle power plants extract steam for MED or MSF units, yielding desalinated water outputs of up to 2,181 kg/s in modeled hybrid MSF-RO configurations. Empirical assessments confirm that cogeneration lowers the primary energy allocation to water production compared to separate facilities, with exergy analyses showing optimized heat recovery minimizing losses in power-water schemes. Nuclear power plants exemplify advanced cogeneration, as seen in facilities like the BN-350 reactor in Kazakhstan, which has operated since 1973 to co-produce electricity and desalinated water via MSF, demonstrating reliable long-term integration without greenhouse gas emissions from the desalination step. Optimization studies for hybrid MSF-RO systems in cogeneration settings further indicate that thermodynamic coupling with combined-cycle plants can balance power and water demands, with case-specific models applied to Gulf region plants showing reduced levelized costs through shared infrastructure. However, efficiency gains depend on precise heat extraction to avoid compromising power output, as over-extraction can reduce turbine performance by 5–10% in steam-driven setups. Renewable energy integration mitigates desalination's carbon footprint by powering reverse osmosis (RO) or supplementing thermal processes with intermittent sources like solar photovoltaic (PV), wind, and solar thermal. RO plants, with their electrical loads of 3–5 kWh/m³, integrate readily with PV-wind hybrids, which stabilize supply through complementary generation profiles—solar peaking daytime and wind at night—reducing reliance on grid power and achieving up to 38% higher freshwater yields in solar-hybrid configurations via improved operational continuity. Wind-desalination systems, often battery-buffered, have been reviewed for topologies yielding capacities of 10–100 m³/day in off-grid setups, with levelized costs competitive in windy coastal areas like those in Europe and Australia. Solar thermal integration with MED units uses concentrating collectors to provide process heat, enabling standalone or hybrid operation with gains in efficiency to 18% and specific energy consumption as low as 1.76 kWh/m³ in advanced prototypes. Hybrid RES-desalination deployments, such as PV-wind-RO for brackish or seawater, enhance durability and cost-effectiveness through modular scaling, though intermittency necessitates storage—e.g., batteries or pumped hydro—adding 20–30% to capital costs but enabling near-zero emissions. Recent analyses project that such integrations could supply 10–20% of global desalination capacity by 2030 in sun- and wind-rich regions, prioritizing RO for its lower energy threshold over thermal methods. Challenges include site-specific variability, with economic viability hinging on subsidies or falling renewable costs, as unsubsidized hybrids remain 10–15% higher in levelized cost than fossil-fueled RO without cogeneration synergies.

Economic Analysis

Capital and Operational Costs

Capital costs for constructing seawater reverse osmosis (SWRO) desalination plants, which dominate modern installations, typically range from $1,900 to $2,100 per cubic meter of annual average daily capacity for large-scale facilities exceeding 100,000 m³/day, with medium-sized plants around 38,000 m³/day costing approximately $80 million total. These figures encompass core equipment such as high-pressure pumps, membranes, and energy recovery devices, but exclude site-specific intake structures ($130,000–$790,000 per 1,000 m³/day capacity) and pretreatment systems ($130,000–$400,000 per 1,000 m³/day capacity), which can increase overall capital expenditure by 20–50% depending on seawater quality, coastal geology, and regulatory requirements for environmental protection. Economies of scale reduce unit costs for mega-plants, as evidenced by the Carlsbad plant (capacity ~189,000 m³/day), where total capital reached ~$1 billion including ancillary infrastructure, yielding ~$5,300 per m³/day when factoring in extensive permitting and pipeline costs. Operational costs for SWRO plants average $0.53–$1.58 per cubic meter of produced water, with energy comprising 50–70% of expenses due to specific energy consumption of 2.5–4.0 kWh/m³ after energy recovery. Breakdowns from operational data of mid-sized plants (23,000–33,000 m³/day) in 2015–2018 show energy at $0.40–$0.66/m³, maintenance $0.07–$0.08/m³, chemicals/reagents ~0.02/m3,membranereplacements 0.02/m³, membrane replacements ~0.01/m³, and labor ~$0.04–$0.05/m³, totaling $0.55–$0.83/m³ (adjusted from EUR at historical rates).
Cost ComponentTypical Range (USD/m³)Percentage of OPEX
Energy0.40–0.6650–70%
Maintenance0.07–0.0810–15%
Chemicals~0.023–5%
Membranes~0.012–3%
Labor/Other0.04–0.055–10%
Thermal desalination methods like multi-stage flash (MSF) incur higher operational costs, often $1.00–$2.00/m³, due to thermal energy demands of 10–15 kWh/m³ equivalent, making SWRO 30–50% cheaper in regions with access to low-cost electricity or cogeneration. Actual costs vary by location; for instance, the Fujairah plant in the UAE achieves under $0.60/m³ through subsidized energy and scale, while Carlsbad exceeds $1.80/m³ amid stringent U.S. regulations and higher labor rates. Recent advancements in membrane efficiency and energy recovery have driven a 20–30% decline in unit costs since 2010, though brine management and financing risks can elevate effective expenses in water-scarce areas.

Levelized Cost Comparisons with Alternatives

The levelized cost of water (LCOW) metric standardizes comparisons by amortizing capital, operational, maintenance, and energy expenses over a facility's lifetime output, typically expressed in USD per cubic meter. For seawater reverse osmosis (SWRO) desalination, LCOW ranges from 0.41 to 1.00 USD/m³ in modern large-scale plants (capacity >100,000 m³/day), with costs trending downward due to , membrane efficiency gains, and energy price fluctuations; for instance, a 2021 bid in achieved 0.41 USD/m³ through optimized financing and low-interest loans. Brackish RO yields lower LCOW of 0.20–0.60 USD/m³, benefiting from reduced and pretreatment needs. Thermal desalination methods, such as multi-stage flash (MSF), incur higher LCOW of 0.80–2.00 USD/m³, primarily from elevated energy demands (3–5 kWh thermal equivalent per m³), rendering them less competitive except in with power plants. In comparison, conventional freshwater sources exhibit lower LCOW: treatment (coagulation, , disinfection) averages 0.10–0.40 USD/m³ in regions with established infrastructure, while extraction and basic treatment falls to 0.05–0.30 USD/m³ where aquifers are shallow and uncontaminated, though pumping from deep aquifers can elevate costs to 0.50 USD/m³ or more due to for lift. These figures exclude scarcity premiums; in water-stressed basins, the full economic cost of overexploited —including depletion externalities and conveyance—often exceeds 0.50 USD/m³, narrowing the gap with desalination. Distributed renewable-powered desalination can achieve LCOW below 0.50 USD/m³ for brackish sources, positioning it as competitive for in remote areas, though solar integration typically adds 20–50% to baseline costs without subsidies or recovery.
Water Source/MethodTypical LCOW (USD/m³)Key Drivers
Surface Water Treatment0.10–0.40Low energy (0.2–0.5 kWh/m³), established infrastructure
(Shallow)0.05–0.30Minimal treatment, variable pumping energy
SWRO Desalination0.41–1.00Energy (3–4 kWh/m³), membranes, brine disposal
Brackish RO0.20–0.60Lower salinity reduces energy (1–2 kWh/m³)
Thermal (MSF/MED)0.80–2.00High thermal energy, suitable for hybrid power
Electrodialysis (ED) offers LCOW parity with RO for low-salinity feeds (≤3 g/L TDS), at 0.30–0.70 USD/m³, but scales poorly for without pretreatment. Emerging hybrid systems, like with renewables, report LCOW as low as 0.50 USD/m³ in pilot scales, though commercialization lags due to draw solution regeneration costs. Desalination's higher LCOW versus alternatives stems largely from (40–50% of total), but advancements in variable-speed pumps and renewable integration have reduced it by 50% since 2000, per World Bank analyses.

Market Growth and Investment Returns

The global desalination market has demonstrated consistent expansion, propelled by escalating water demand in arid regions, , and advancements in efficiency. Valued at USD 21.74 billion in 2024, the market is projected to reach USD 24.26 billion in 2025 and grow to USD 58.38 billion by 2033, reflecting a (CAGR) of approximately 9.61%. Similarly, the water desalination segment stood at USD 18.36 billion in 2024, anticipated to hit USD 20.01 billion in 2025, with broader markets forecasting USD 46.18 billion in 2025 en route to USD 109.42 billion by 2034 at a 10.06% CAGR. Key drivers include chronic shortages in the , , and parts of the , where desalination now supplies over 50% of municipal in countries like and . Investment in desalination infrastructure yields variable but often stable returns, underpinned by long-term offtake agreements with governments or utilities that mitigate demand risk. Large-scale projects, such as the in —operational since 2015 with a capacity of 189,000 cubic meters per day—have exhibited robust financial health, evidenced by sustained debt service coverage ratios exceeding 1.40x through 2025, enabling debt upgrades to investment-grade ratings. Public-private partnerships (PPPs) dominate financing, with internal rates of return (IRRs) typically ranging from 5% to 10%, influenced by factors like energy costs (which comprise 30-50% of operational expenses) and disposal regulations. Declining —from USD 1,000-2,000 per cubic meter of daily capacity in the early to under USD 1,000 today due to modular designs—enhance viability, though upfront investments for megaplants often exceed USD 1 billion. Smaller or renewable-hybrid systems offer higher relative returns in niche applications. Solar-powered desalination units, for instance, achieve payback periods of 3-7 years in high-insolation areas, driven by zero-fuel offsets against conventional rates of USD 0.10-0.20 per kWh. A modeled 2-ton-per-hour plant illustrates potential: with initial costs around USD 480,000 and annual operational savings of USD 740,000 from displaced purchases at USD 1-2 per cubic meter, ROI can exceed 100% annually post-, though scaled commercial analogs adjust for and regulatory hurdles. Risks including environmental litigation and fluctuating prices temper optimism, as seen in delayed U.S. projects, yet global capacity additions—projected at 10-15 million cubic meters per day annually—signal sustained investor interest amid freshwater depletion rates outpacing supply in 2.4 billion people worldwide.

Environmental Considerations

Brine Discharge: Salinity and Toxicity Effects

Brine discharge from desalination plants, particularly (RO) facilities, consists of concentrated residual effluent with levels typically ranging from 45 to 80 grams per liter, compared to ambient of approximately 35 grams per liter, resulting from recovery rates of 40-50%. This hypersalinity, combined with elevated temperatures (often 3-5°C warmer than intake ) and residual process chemicals, poses risks to marine ecosystems upon discharge, which accounts for over 90% of global disposal. The denser tends to sink and spread along the , creating localized gradients that can exceed 5% above ambient levels within mixing zones if dilution is inadequate, as observed in regulatory assessments recommending 20:1 dilution ratios and 100-meter mixing zones to limit ecological stress. Salinity increases induce osmotic stress on benthic organisms, leading to reduced metabolic rates, smothering of sediments, and shifts in community structure; for instance, studies on polychaetes, amphipods, and foraminifera near discharge sites have documented decreased abundance and diversity, with hypersaline plumes altering benthic macrofauna assemblages over distances of tens to hundreds of meters. Seagrasses and corals exhibit particular vulnerability, with field experiments showing up to 50% mortality in Posidonia oceanica meadows exposed to salinity elevations of 3-5 ppt above ambient, disrupting photosynthesis and root systems due to salt accumulation in tissues. In semi-enclosed basins like the Persian Gulf, cumulative brine inputs from multiple plants have contributed to basin-wide salinity rises of 0.1-0.5 ppt per decade, exacerbating natural evaporation-driven hypersalinity and stressing thermotolerant species. While diffuser systems can mitigate plume persistence, empirical monitoring at sites like Carlsbad, California, revealed salinity exceedances beyond permitted thresholds, though direct benthic impacts were not always detectable due to site-specific hydrodynamics. Beyond , arises from antiscalants (e.g., phosphonates), biocides (e.g., or at 0.1-1 mg/L residuals), coagulants (e.g., ferric ), and trace metals leached during pretreatment, which persist in at concentrations 1.5-2 times higher than influent. Laboratory bioassays indicate to and crustaceans at effective concentrations as low as 10-100 mg/L for certain antiscalants, with chronic exposure causing sublethal effects like impaired reproduction in copepods and inhibited bacterial activity, though field validations remain limited and peer-reviewed studies highlight variability based on chemical dosing and degradation rates. Copper-based antifouling agents in some brines have been linked to finfish mortality and in sediments, prompting regulatory scrutiny, while overall is often compounded by , amplifying stress on osmoregulatory capacities of marine species. Recent reviews (2022-2024) emphasize that while no widespread regional has been conclusively tied to modern plants with advanced pretreatment, localized hotspots near poorly diffused outfalls demonstrate community-level disruptions, underscoring the need for chemical-specific monitoring over generalized metrics.

Overall Carbon Footprint and Resource Use

Desalination processes generate primarily through , with (RO) exhibiting the lowest carbon intensity among dominant technologies at 0.4–6.7 kg CO₂eq per cubic meter of produced water, compared to 7.01–17.6 kg CO₂eq/m³ for multi-effect (MED) and 9.41–25 kg CO₂eq/m³ for multi-stage flash (MSF) . RO achieves 80–86% lower emissions than thermal methods due to its reliance on rather than heat-intensive processes often powered by fuels. Actual footprints vary by grid carbon intensity; for instance, a Saudi Arabian plant reported 1.79 kg CO₂e/m³ in 2025 assessments, reflecting dominance. Energy sourcing critically determines emissions: fossil fuel-based grids yield higher outputs, while solar photovoltaic integration can reduce RO footprints to 0.4 kg CO₂eq/m³ by minimizing indirect emissions from electricity generation. Efficiency improvements, such as advanced membranes and energy recovery devices, further lower specific energy use to 2–4 kWh/m³ for modern RO plants, translating to reduced carbon if paired with low-emission power. Thermal desalination, prevalent in the Middle East, amplifies footprints through cogeneration with steam turbines, though waste heat utilization can offset some impacts. Beyond carbon, resource demands include seawater intake volumes of 2–3 m³ per m³ of product water in RO systems, achieving 40–50% recovery rates and generating concentrated that requires for . Chemical inputs, such as antiscalants, coagulants, and biocides, constitute about 4% of RO emissions but add operational burdens, with annual usage scaling to thousands of tons in large . Material resources for , including membranes and pumps, contribute upfront embodied carbon, estimated at tens of tons CO₂ per from alone, amortized over decades of output.
Desalination TechnologyTypical CO₂ Emissions (kg/m³)Primary Energy Driver
Reverse Osmosis (RO)0.4–6.7 (2–5 kWh/m³)
Multi-Effect Distillation (MED)7.01–17.6
Multi-Stage Flash (MSF)9.41–25

Empirical Mitigation and Long-Term Impacts

Empirical studies demonstrate that multiport diffusers significantly enhance dilution, with one field-validated model showing up to 1684% improvement in dispersion rates compared to single-port systems, reducing near-field gradients and minimizing benthic exposure. Regulatory frameworks, such as those in , recommend limiting excess to no more than 5% (approximately 1.7 ppt) at the mixing zone boundary—typically 100 m from the outfall—to protect sensitive habitats, based on reviewed field data indicating seagrass mortality thresholds above 1-5 ppt increases and benthic community shifts at 2-3 psu. Co-discharge with cooling water or achieves in-pipe dilution ratios of 20:1 or higher, further attenuating from antiscalants and biocides, though empirical validation remains site-specific due to variable hydrodynamics. Long-term monitoring at operational plants reveals localized effects but limited basin-scale persistence when is applied. In the Persian Gulf, where desalination contributes 22.6 million m³/day (2.3% of net ), modeling of hydrological balances estimates current increases below 0.1 psu, with projections to 120 million m³/day yielding 0.4-1 psu rises under conservative outflow scenarios—effects diluted by high (1000 million m³/day average) and circulation. Spanish case studies, including multi-year benthic surveys near high-output facilities, report stable community structures post-diffuser upgrades, with no chronic declines in diversity or abundance beyond initial mixing zones, attributing resilience to adaptive designs and ambient flushing. However, gaps persist in sublethal metrics like reproduction rates, underscoring needs for extended tracking; unmitigated discharges have induced sediment anoxia in low-flow sites, but engineered systems consistently show recovery within 1-2 years. Overall, global operational data indicate that while hypersalinity poses risks to hyper-sensitive taxa, proper plume confines impacts to <1% of discharge footprints, enabling equilibration without irreversible degradation.

Health and Water Quality

Produced Water Composition and Treatment

Desalinated water produced primarily through (RO) or thermal distillation processes exhibits very low (TDS), typically ranging from 20 to 50 mg/L, with minimal concentrations of salts, dissolved gases, and trace metals such as . In RO systems, the permeate often contains less than 5 mg/L calcium, under 1 mg/L magnesium, and negligible levels of other electrolytes like sodium and potassium, resulting from the semi-permeable membrane's rejection of over 99% of ions present in feed (average TDS ~35,000 mg/L). This demineralized profile contrasts sharply with natural freshwater sources, where TDS commonly exceeds 100 mg/L and includes essential minerals for human and pipe stability. Post-treatment is essential to address the aggressiveness of demineralized , which can distribution infrastructure due to low buffering capacity and values often below 6.5. Common remineralization techniques include dosing with (lime) to raise calcium levels to 30-50 mg/L and adjust to 7.5-8.5, followed by injection to form stable for control. Alternative methods involve contactors or blending with conventionally treated to achieve target hardness (e.g., 50-75 mg/L as CaCO3) and TDS of 200-400 mg/L, aligning with guidelines for potable stability and taste. Disinfection follows remineralization, typically via chlorination (0.5-1 mg/L free chlorine residual) or ultraviolet irradiation to eliminate residual microbes, as the low-nutrient environment in desalinated water limits bacterial regrowth but does not preclude post-process contamination. Boron removal, if needed (target <0.5 mg/L for health standards), may employ a second RO pass or , given its incomplete rejection in primary desalination (up to 70-90% passage in standard RO). These treatments ensure compliance with standards, mitigating risks of electrolyte imbalances from prolonged consumption of untreated demineralized water, such as or cardiovascular strain observed in epidemiological studies. Desalinated water, after post-treatment and disinfection, meets high safety standards for drinking and is safe for consumption. However, it may occasionally exhibit unpleasant odors, typically attributable to chlorination byproducts or maintenance issues in distribution tanks and pipes, rather than the desalination process itself.
ParameterUntreated RO Permeate (Typical)Post-Treated Potable Standard (Target)Source
TDS (mg/L)20-50200-400
Calcium (mg/L)<530-75
pH5.5-6.57.5-8.5
(as CaCO3, mg/L)<10100-200

Potential Deficiencies and Supplementation Needs

Desalinated water produced through or thermal methods typically exhibits very low (TDS), often ranging from 10 to 50 mg/L, which strips essential minerals including calcium, magnesium, , and . This demineralization disrupts natural balance, potentially leading to increased urinary excretion of sodium, , chloride, calcium, and magnesium upon consumption, thereby exacerbating deficiencies in populations reliant on such water as a . Empirical studies, including those from Israel's extensive desalination supplying over 70% of domestic since the , indicate that chronic low magnesium intake from desalinated sources correlates with elevated risks of ischemic , , , cardiac arrhythmias, and . In vulnerable groups, such as children and the elderly, prolonged consumption of low-mineral has been linked to impaired bone development, reduced bone mineral density, and higher osteoporosis risk due to insufficient calcium and magnesium absorption, with animal models demonstrating activation of and growth inhibition after multi-generational exposure. Additionally, low fluoride and calcium levels contribute to increased dental caries risk due to impaired enamel remineralization. Human cohort analyses further suggest associations with inhibition and lower height development in youth, though direct causation remains debated given dietary confounders; nonetheless, contributes 5-20% of daily intake in many regions, amplifying risks where diets are marginal. While some reviews find inconsistent links to cardiovascular mortality, the consensus from physiological data underscores magnesium's role in over 300 enzymatic reactions, rendering its deficiency causally plausible for metabolic disruptions independent of broader . To address these deficiencies, post-treatment remineralization is standard practice, involving the addition of calcium (via lime or dissolution) and magnesium (via dolomitic lime or ) to achieve target levels of 30-100 mg/L calcium and 10-30 mg/L magnesium for and stability. Blending with or adding electrolytes like can further restore balance, with regulations in desal-heavy nations like mandating minimum TDS of 100-250 mg/L to mitigate risks. These interventions, implemented in plants since the early , prevent pipe while approximating natural water compositions, though optimal formulations vary by local diet and require ongoing monitoring to avoid over-mineralization effects like scaling.

Innovations and Emerging Methods

Advanced Membrane and Electrochemical Techniques

Advanced membrane techniques in desalination extend beyond conventional by incorporating innovations such as (FO) and (MD), which leverage osmotic gradients or vapor-liquid equilibria to reduce demands and . In FO, water permeates a semi-permeable from a saline feed to a hypertonic draw solution, driven by rather than hydraulic pressure, achieving lower propensity and use of approximately 0.2-0.5 kWh/m³ for compared to 2-4 kWh/m³ for RO. Recent developments include thin, selective membranes enabling high flux rates up to 20-30 L/m²·h, as demonstrated in pilot systems combining FO with RO for draw solution recovery. A 2024 solar-powered FO plant by Trevi Systems in produces 500 m³/day with zero carbon emissions, highlighting scalability for remote applications. MD employs hydrophobic membranes to separate from saline feed under a thermal gradient, suitable for integrating with sources and achieving salt rejection exceeding 99.9%. Advances in membranes, incorporating materials like oxide or carbon nanotubes, have improved by 50-100% while mitigating issues, with interfacial photothermal heating reducing to 1-2 kWh/m³ equivalent. A 2025 review notes pulsed enhancements in MD hybrids, boosting efficiency for hypersaline brines where RO fails. , a membrane-based process, has seen membrane optimizations like PVA-crosslinked variants yielding fluxes of 5-10 kg/m²·h for desalination, particularly effective for low-temperature operations. Electrochemical methods, including (ED) and capacitive deionization (CDI), apply electric fields to migrate ions through selective membranes or electrodes, offering advantages in treatment with tunable selectivity. ED uses ion-exchange membranes and to concentrate salts, with energy consumption of 0.5-2 kWh/m³ for 1-5 g/L , outperforming RO at low salinities due to reduced limitations. Improvements like ion-capture ED, developed in 2021, achieve 90%+ salt removal while extracting toxic metals such as lead and , enhancing quality. Flexible batch electrodialysis reversal (EDR) systems, optimized for solar intermittency in 2024, maintain consistent output with energy use under 1 kWh/m³ by adapting to variable power inputs. CDI adsorbs ions electrostatically onto porous carbon electrodes during charging, with discharge regenerating the electrodes; membrane CDI (MCDI) variants reduce energy to 0.13-0.59 kWh/m³ for brackish feeds by preventing ion leakage. For seawater, CDI efficiencies lag at 5-10 kWh/m³ due to high voltage needs, but hybrid nanofiltration-CDI systems achieve 3.5 kWh/m³ while treating RO brine. Microfluidic CDI prototypes enhance ion transport, yielding charge efficiencies over 95% and salt adsorption capacities of 15-20 mg/g. These techniques collectively address RO limitations in energy recovery and selectivity, though scaling remains challenged by electrode/membrane durability in high-salinity environments.

Bio-Inspired and Nanotech Approaches

Bio-inspired desalination methods replicate natural biological processes to achieve selective water transport with minimal energy input. Aquaporins, membrane proteins that facilitate rapid diffusion while excluding ions, have inspired biomimetic membranes where these channels are embedded in synthetic supports. A 2024 advancement involved integrating aquaporins into anodic aluminum oxide substrates, yielding biomimetic membranes with water permeability exceeding conventional (RO) films by factors of up to 100 liters per square meter per hour per megapascal, alongside 99% salt rejection in lab tests. These membranes maintain functionality under varying pressures, as confirmed by simulations evaluating nanoscale mechanical stability in 2025 studies. However, scalability remains limited by aquaporin stability and production costs, with commercial pilots primarily in rather than direct seawater desalination. Mangrove-inspired systems emulate desalination via capillary tension from , generating negative pressures to pull pure against osmotic gradients. A 2020 synthetic mangrove prototype demonstrated 5.6 kg of per square meter per day from 3.5% using solar alone, with salt rejection via nanoscale xylem-like channels. Recent extensions include photothermal zwitterionic fibrous membranes that selectively evaporate while precipitating salts, achieving 1.85 kg per square meter per hour under one-sun illumination in 2025 experiments. Such passive systems reduce energy demands but face challenges in high- feeds and , necessitating hybrid designs for practical deployment. Nanotechnology enhances membrane precision through atomic-scale pores and surfaces. oxide (GO) laminates form interlayer nanochannels tunable for ion sieving, with 2024 modifications enabling 97-99% NaCl rejection at fluxes 2-5 times higher than commercial RO membranes under operational pressures. These advances address swelling-induced defects via cross-linking, improving durability in real . Two-dimensional materials like offer adjustable d-spacing for monovalent/divalent ion separation, with 2025 reviews highlighting their antifouling properties and potential in hybrid capacitive deionization-desalination setups. Supramolecular nanocrystalline films, assembled via nano-confined , exhibited desalination rates of 10-20 liters per square meter per hour in crossflow tests, outperforming polymeric analogs in selectivity. Despite lab successes, field-scale validation lags, with issues like nanomaterial aggregation and cost hindering widespread adoption beyond pilots.

Pilot-Scale and Scalable Prototypes (Post-2020)

OceanWell's subsea pods represent a scalable offshore prototype, with pilot testing commencing in March 2025 at Las Virgenes Municipal District in to validate submerged filtration efficacy. The 40-foot pods utilize deep-water hydrostatic pressure to drive , filtering while returning unharmed and discharging diluted to minimize ecological impact. This approach claims a 40% reduction in energy costs relative to onshore plants by pumping smaller volumes and leveraging natural pressure, with recovery rates of 5-15% producing benign brine concentrations. In August 2025, plans advanced for Water Farm 1, deploying 20-25 pods to yield 60 million gallons per day—sufficient for approximately 250,000 households—with full operations targeted for 2028 and potential expansion to additional sites in and internationally. A batch prototype incorporating a flexible for management was piloted at the Yuma Desalting Plant in during 2022, processing up to 5 m³/day of scaling-prone concentrate. Over 885 cycles spanning one week, it achieved 82.6% water recovery, producing 31.1 m³ of permeate with mean of 150 mg/L and no observed scaling despite conditions. consumption measured 3.3 kWh/m³ at pilot scale, with projections estimating 0.8-0.9 kWh/m³ upon scaling to 379 m³/day using optimized pumps, indicating feasibility for integration into larger treatment systems. Modular solar desalination prototypes have also progressed to pilot scale post-2020, exemplified by a non-intrusive system tested in , , which delivered 6.24 L/day·m² productivity in peak summer conditions and exceeded 99% salt removal via conductivity metrics. The design emphasizes simple assembly and adaptability for variable demand in remote or island settings, relying solely on solar input without external , thus supporting scalability through replication in high-insolation regions. Electrochemical approaches include a semi-industrial capacitive deionization pilot employing six cells to desalinate in two stages, reducing from 1 g/L to 0.5 g/L at 200 L/h output. Operating at voltages of 0.85-0.9 V, it recovered about 30% of cycle , with enhanced by proposed storage tanks to rinse and boost overall efficiency.

Global Implementation

Largest Plants and Capacities

The largest operational desalination plant is the Ras Al-Khair facility in , with a production capacity approaching 3 million cubic meters of desalinated water per day, utilizing a combination of multi-stage flash (MSF) and (RO) technologies powered by an adjacent 2,400 MW plant commissioned in phases starting 2014. This capacity reflects expansions and optimizations by the Saudi Water Authority, enabling it to supply significant portions of regional freshwater needs amid arid conditions. Other major follow, often hybrid systems leveraging low-cost fossil fuels for thermal processes, though RO dominates newer large-scale builds for energy efficiency.
Plant NameLocationCapacity (m³/day)Primary TechnologyCommission YearSource
Ras Al-Khair~3,000,000MSF + RO2014 (phased)
Taweelah ROUAE ()909,200RO2021 (full)
Al-Jubail 2948,000MED-TVC2010s
Shuaiba 3880,000MSF + RO2010s
Casablanca (Rabat-Salé-Kénitra)822,000RO (planned/partial)2024+
Sorek624,000RO2013
These capacities represent peak output under optimal conditions; actual yields vary with maintenance, feedwater , and energy availability, with Gulf states accounting for over half of global large-scale desalination due to subsidized energy and policy mandates for . RO plants like Taweelah exemplify shifts toward tech for lower consumption (around 3-4 kWh/m³ versus 10-15 for thermal), though thermal methods persist where from power generation reduces marginal costs. Emerging projects, such as expansions in targeting 8.5 million m³/day national capacity by 2025, underscore scaling driven by and integration rather than renewables alone.

Regional Case Studies: Successes and Adaptations

Israel's desalination program exemplifies successful adaptation to chronic in a semi-arid region, with five major seawater (SWRO) plants operational by 2023 producing nearly 600 million cubic meters annually, meeting over 70% of municipal and domestic demand. The Sorek plant, commissioned in 2013 with a capacity of 624,000 cubic meters per day, incorporates advanced energy recovery devices that achieve up to 4 kWh per cubic meter energy use, significantly lowering operational costs through efficient technology and grid integration with power. Adaptations include pretreatment innovations to handle high-salinity Mediterranean feedwater and post-treatment addition to mitigate risks from low-mineral output, enabling reliable supply amid exceeding 2% annually. In , Perth's response to declining rainfall—averaging 20% reduction since the —centered on the Kwinana Seawater Desalination Plant, opened in 2006 with an initial capacity of 143,000 cubic meters per day, later expanded to contribute nearly half of the city's 300 million cubic meters annual supply by 2017. The Southern Seawater Desalination Plant, added in 2011, further boosted output to over 140 million cubic meters yearly combined, using SWRO with brine dispersion systems adapted to minimize ecological impact on Cockburn Sound ecosystems through rigorous environmental monitoring and diffuser design. Success stems from public-private partnerships that scaled infrastructure ahead of demand, reducing reliance on distant mainland imports and stabilizing prices at approximately AUD 1.50 per cubic meter despite energy costs comprising 40% of operations. California's Carlsbad Desalination Plant, operational since December 2015, supplies up to 50 million U.S. gallons daily—about 10% of County's needs for 400,000 residents—delivering over 100 billion gallons by November 2022 and proving resilient during the 2012-2016 by diversifying from imported and State Water Project sources vulnerable to allocation cuts. Adaptations include co-location with the Encina power plant for utilization in pretreatment, advanced ceramic membrane for fouling resistance in variable Pacific inflows, and compliance with stringent ocean discharge standards via subsurface brine diffusers that achieve 99% dilution within 200 meters. Energy efficiency targets under 3.5 kWh per cubic meter were met through variable frequency drives and isobaric recovery systems, though high exceeding $1 billion reflect regulatory hurdles overcome via long-term offtake agreements. Singapore's urban-constrained environment prompted hybrid desalination adaptations, with the Desalination Plant (Phase 1 operational 2018, 136,000 cubic meters per day) and Keppel East Plant (2020, 30,000 cubic meters per day) integrating SWRO with co-generation from adjacent power facilities to cut energy use by 20% via shared . The latter's dual-mode capability switches between seawater and during wet seasons, optimizing for tropical variability and contributing to desalination fulfilling 30% of national demand by 2023 alongside recycled water. Pretreatment employs for algae-prone equatorial waters, achieving 99.99% pathogen removal, while brine management uses deep-sea outfalls tailored to the Johor Strait's currents, supporting Singapore's "Four National Taps" strategy without compromising . These facilities, backed by R&D investment exceeding SGD 100 million, demonstrate scalable integration in land-scarce settings, with costs stabilized at SGD 0.50-0.60 per cubic meter through technological .

Policy and Societal Dimensions

Regulatory Hurdles and Political Resistance

Desalination projects frequently encounter stringent environmental regulations governing discharge, systems, and , which can extend permitting timelines significantly. In the United States, compliance with the Clean Water Act and state-specific frameworks like 's Ocean Plan mandates detailed assessments of hypersaline 's potential to alter local salinity levels and harm marine ecosystems, often requiring diffuser systems or dilution technologies to mitigate impacts. For instance, the Carlsbad Desalination Plant in underwent a seven-year permitting process from 2003 to 2010, involving multiple federal and state agencies, before overcoming ten legal challenges related to fish impingement and dispersion. These requirements, while intended to protect , have been criticized for imposing high compliance costs and delays, with peer-reviewed analyses indicating that modern plants, when regulated appropriately, produce minimal ecological footprints through advanced monitoring and engineering. Political resistance often stems from environmental advocacy groups and local stakeholders prioritizing conservation measures over supply expansion, leading to lawsuits and project vetoes. In , the Huntington Beach desalination proposal, debated for over two decades, was rejected by the in May 2022 amid concerns over coastal habitat disruption and energy use, despite proponent arguments for drought resilience. Similarly, the project faced repeated litigation from water districts and communities, with a 2023 appellate court ruling upholding approvals but highlighting ongoing disputes under the (CEQA), which amplifies scrutiny through mandatory impact disclosures. Advocacy organizations such as Food & Water Watch have mobilized against projects citing toxicity and carbon emissions, influencing and regulatory decisions, though empirical data from operational plants like Carlsbad demonstrate effective mitigation without widespread ecological harm. Beyond , political opposition has resulted in outright cancellations, underscoring tensions between water security and localized environmental priorities. In September 2025, the Corpus Christi City Council in voted to terminate a $1.2 billion desalination contract after a decade of planning, driven by community concerns over bay discharge effects, financial risks, and alternatives like wastewater reuse, despite the city's vulnerability to shortages. Such resistance reflects broader geopolitical challenges, as seen in the Gulf region where inter-state cooperation on shared desalination infrastructure has faltered due to sovereignty issues and competing resource agendas. Regulatory frameworks in these cases often intersect with political dynamics, where activist litigation under acts like CEQA or equivalent statutes prolongs uncertainty, potentially deterring investment despite desalination's proven role in arid regions like , where streamlined policies have enabled rapid scaling without comparable blocks.

Debates on Scalability vs. Conservation Narratives

Advocates for desalination scalability argue that technological advancements have reduced costs and energy requirements, enabling large-scale deployment to meet growing demand independent of variable rainfall or aquifer depletion. In Israel, desalination supplies over 70% of municipal water as of 2023, contributing to water security amid population growth from 8.5 million in 2010 to 9.8 million in 2023, with per capita consumption stabilized at around 100 liters per day through combined supply expansion and efficiency measures. Similarly, Australia's Perth Seawater Desalination Plant, operational since 2006 and expanded to 144 million cubic meters annually by 2018, has buffered against droughts, demonstrating that modular reverse osmosis facilities can scale output by 20-50% with minimal additional infrastructure. Proponents, including engineers at IDE Technologies, contend that levelized costs have fallen to 0.500.50-1.00 per cubic meter in optimal conditions by 2022, competitive with imported water, and that brine management innovations mitigate environmental concerns, positioning desalination as a causal driver of resilience rather than a supplementary measure. Opponents, often from environmental organizations like Surfrider Foundation, prioritize conservation narratives, asserting that demand reduction through pricing, leaks repair, and behavioral changes yields lower costs and fewer ecological impacts than desalination's energy demands, estimated at 3-4 kWh per cubic meter for seawater . In , where urban per capita use dropped 25% from 2013 to 2022 via mandatory restrictions during droughts, critics argue that desalination plants like the proposed Huntington Beach facility—facing delays over $1.4 billion in costs and entrainment risks—represent inefficient supply-side fixes that overlook reuse potential, with only 13% of recycled compared to Israel's 85%. These views frame scalability as enabling unsustainable growth, with a 2022 analysis in highlighting that conservation and capture could address 80% of shortfalls in coastal cities at half the of desalination. Critiques of dominant conservation narratives emphasize their limitations in addressing inelastic demand from economic expansion and demographic shifts, where historical data shows rebound effects offsetting 10-30% of savings through increased usage. In arid regions, prolonged reliance on conservation alone has led to and agricultural cutbacks, as seen in Australia's Millennium Drought (1997-2009), resolved partly by desalination capacity additions exceeding 1 million cubic meters daily. Sources affiliated with industry and analysts, such as CalMatters contributors, note that while conservation achieves short-term reductions—e.g., California's 20% statewide cut in 2015—it fails to scale with projected 20% population growth by 2040, rendering desalination essential for baseline supply rather than optional. This tension manifests in regulatory battles, like California's 2016 Desalination Amendment imposing stringent intake rules, which delayed projects despite empirical evidence from Israel's low-impact open-ocean intakes showing minimal ecological disruption. Empirical assessments, including a 2023 Review, underscore that hybrid approaches integrating both strategies outperform conservation-centric policies, as pure risks economic stagnation without supply diversification.

Economic Incentives and Future Outlook

The economics of desalination are driven primarily by high capital expenditures for plant construction, typically ranging from $1,000 to $2,500 per cubic meter of daily capacity, and operational costs dominated by consumption, which accounts for 30-50% of total expenses in systems requiring 3-4 kWh per cubic meter produced. Overall production costs for desalination vary from $0.50 to $2.50 per cubic meter, exceeding those of conventional sources like (0.100.10-0.60/m³) or (0.300.30-1.00/m³), though efficiencies in large-scale plants in regions like the have narrowed this gap to 0.700.70-0.90/m³ when paired with low-cost . Government incentives play a key role in mitigating these barriers, particularly in water-stressed areas, through direct grants and subsidies that target planning, construction, and . In the United States, the Bureau of Reclamation's Desalination and Water Purification Research Program allocated $2.2 million in 2023 for advancing technologies, while California's Department of Water Resources offers grants for brackish and ocean projects, including $5 million in Proposition 1 funding in 2023 for local desalination initiatives. The U.S. Department of Energy has similarly awarded $9 million across 12 projects in recent years to integrate desalination with reuse, and specific infrastructure like the Carlsbad plant received $19.4 million in federal grants in 2024 for upgrades. These measures reflect a shift toward supply augmentation, countering reliance on demand-side conservation amid growing scarcity, though critics argue they subsidize energy-intensive processes without fully internalizing environmental externalities like brine disposal. Looking ahead, desalination's viability hinges on cost reductions projected at up to 50% by 2030 through membrane improvements and energy efficiency gains, bolstered by renewable integration such as solar photovoltaics, which can lower operational expenses by 20-24% in hybrid systems. The anticipates further declines as solar and wind costs fall, enabling off-grid plants in remote areas and reducing grid dependency. Global market projections underscore this optimism, with the water desalination equipment sector expected to expand from $18.36 billion in 2024 to $31.69 billion by 2030 at a of approximately 9%, driven by demand in arid regions facing population pressures and climate variability. Challenges persist, including financing for scaling in developing economies and regulatory hurdles for management, but empirical trends in operational plants indicate desalination could supply 25-50% of municipal in high-adoption areas like and the Gulf states by mid-century, contingent on sustained technological and policy support.

References

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