The purpose of this study is to explore the architecture and functioning of hybrid solar desalination systems and investigate their potential as a sustainable solution for water purification. The study reveals that solar-powered desalination systems offer a remarkable alternative to traditional methods, as they rely on clean solar energy and produce no noise or sound pollution. In addition, they have demonstrated cost-effectiveness in generating drinking water, especially in desert regions and inaccessible areas. Furthermore, the research highlights the significance of incorporating waste heat energy into the desalination process. Also shows that utilizing waste heat energy can significantly reduce expenses and enhance the overall effectiveness of water desalination. Through an in-depth analysis of the fundamental principles and real-world applications, this study underscores the importance and rationale for implementing hybrid solar desalination systems. By effectively utilizing solar energy, these systems provide a sustainable approach to address water scarcity and ensure the efficient management of water and energy resources. This study emphasizes the fundamental importance of the structure of hybrid solar desalination systems fueled by solar energy in the efficient management of water resources. By combining technological innovations with renewable energy sources, these systems pave the way for a sustainable future.

  • Hybrid solar desalination systems, which rely on solar energy as their major power source for purifying water.

  • This review paper explores the architecture and functioning of hybrid solar desalination systems.

  • This review paper emphasizes the significance and rationale for utilizing hybrid solar desalination systems that rely on solar energy to efficiently handle water and energy resources.

Water, the essential and primary element that sustains life, plays a fundamental role in the advancement of human societies (He et al. 2020). Consequently, locating and accessing water sources is a paramount concern for humanity (Nejatian et al. 2023). Even explorers venturing beyond Earth's confines are actively seeking planets harboring water sources, recognizing its utmost importance for sustaining human life in extraterrestrial environments (Nejatian et al. 2023). The Earth's surface is composed of around 71% water and 29% land. However, due primarily to the high salinity of seawater and the limited availability of freshwater supplies, countries are currently experiencing a serious water crisis. Merely 2.5% of the entire water amount is comprised of fresh water, a significant portion of which is inaccessible to humans as it is stored in polar ice and subsurface reservoirs (Jahanshahi et al. 2017). Figure 1 depicts the regional distribution of water on the planet's land.
Figure 1

Total global water and fresh water resources.

Figure 1

Total global water and fresh water resources.

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Water, a resource that is challenging to purify, costly to transport, and irreplaceable, is the sole ingredient essential for the creation of food, economic progress, and the survival of life (Kong et al. 2023). The new United Nations Commission for Sustainable Development, in mid-1993, highlighted the significance of water in human health and well-being by prioritizing the improvement of water quality as a key aspect of technology transfer from developed to developing countries (Khajvand et al. 2022). Currently, the global average indicates that over one in six individuals lack sufficient access to potable water, while over two in six individuals lack adequate sewage disposal facilities (Kheskwani & Ahammed 2023). Insufficient availability of potable water and proper sanitation facilities results in the affliction and mortality of millions of individuals annually (see Figure 2). Due to population expansion and rising worldwide demand, the available sources of fresh water are diminishing. By 2025, a scarcity of potable water is expected to affect over 50% of the global community (Van der Leeden et al. 1990).
Figure 2

Predicted water stress until 2040 (Luo et al. 2015).

Figure 2

Predicted water stress until 2040 (Luo et al. 2015).

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The water dilemma is interconnected with climate change, food supply, agriculture, energy, and economically challenging businesses. Efficient management of water resources is a viable solution for addressing societal issues such as inequality and poverty reduction. Establishing sustainable and reliable sources of potable water is crucial for sustaining the economic development of nations globally (Connor 2015). Agriculture and industries are the primary water consumers globally, while the proportion of water allocated for drinking and personal use in society is relatively smaller. Throughout history, humanity has employed many methods to desalinate water, thereby ensuring a reliable supply of fresh water (Angelakis et al. 2021). Water desalination, sometimes known as desalination, encompasses all methods of extracting salt from water. This procedure is extensively utilized in urban, industrial, and commercial settings, and its efficacy has been enhanced with the progress of the industry. Simultaneously, the decline in the groundwater level and the desiccation of rivers have rendered other means of providing potable water arduous and costly. The field of water desalination is regarded as a relatively recent scientific discipline that has made significant advancements throughout the latter half of the 20th century, with ongoing efforts to enhance its technology. Based on Kalogirou's calculations, a continuous production of 1,000 m3 of water/day requires an annual production and extraction of 10,000 metric tonnes of oil (Kalogirou 2004). Green energy-driven desalination devices can be classified into three categories: wind, solar (photovoltaic (PV) or solar collector), and geothermal energy (Taner & Demirci 2014). Water can be produced by using these sustainable energy sources in distillation or thermal membrane desalination equipment (Carpes et al. 2023). The selection of the optimal energy source should be predicated upon economic, environmental, and safety factors (Jaspal et al. 2023). Many individuals argue that solar energy, with its environmental benefits and superior safety profile, should be prioritized over fossil fuel energy, even if it results in somewhat higher expenses for the company (Taner 2019). Utilizing solar energy for the sweetening process is an exemplary use of sustainable energy sources. Concentrating on solar-powered desalination is ideal for application in remote regions, given the expansive nature of desert and arid areas, the existence of dispersed and thinly populated areas on the periphery of these deserts, and the pressing demand for the production of potable water for both human consumption and agricultural purposes. Solar desalination plants exhibit superior dependability in comparison to existing conventional systems. Moreover, their utilization of novel and environmentally friendly energy sources positions them as one of the most effective and eco-friendly alternatives for addressing the global water crisis (Taner 2018a). The solar energy radiation levels vary throughout different regions of the world, with the largest concentration found in the solar belt of the Earth (see Figure 3) (Obotey Ezugbe & Rathilal 2020).
Figure 3

Global distribution of annual average solar irradiation over the Earth's surface. The average is calculated over a 3-year period, taking into account both nighttime and cloud coverage. Placing solar cells with a conversion efficiency of 8% in the designated locations marked by the six discs on the map would yield an average electrical power output of 18 TW (Schrenker 2021).

Figure 3

Global distribution of annual average solar irradiation over the Earth's surface. The average is calculated over a 3-year period, taking into account both nighttime and cloud coverage. Placing solar cells with a conversion efficiency of 8% in the designated locations marked by the six discs on the map would yield an average electrical power output of 18 TW (Schrenker 2021).

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Currently, the expense associated with water production through desalination systems utilizing conventional energy sources is significantly lower than that of renewable energy-powered systems (Taner & Sivrioglu 2017). Overall, the price of potable water has declined in the past few years because of technological developments and research advancements. Utilizing renewable energy sources results in significantly elevated expenses. However, the environmental benefits can balance out the costs. In scenarios where desalination systems use both conventional and renewable sources of energy, Figure 4 shows the cost of fresh water, expressed in dollars per cubic meter ($/m3) (Shatat et al. 2013).
Figure 4

The cost of water desalination with different energy sources.

Figure 4

The cost of water desalination with different energy sources.

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As stated in Abdelkareem et al. (2018), the global desalination capacity is 86.5 million m3/day. About 60% of its capacity comes from seawater. The most common desalination technologies are RO (66%) and MSF (21%) (Henthorne 2011). The Middle East possesses the greatest amount of installed desalination capacity (Greenlee et al. 2009), with countries such as Saudi Arabia contributing 21% of the global total (about 5 million m3/day) (Radhwan & Fath 2005). However, nearly 90% of the desalination systems in this region utilize multi-stage flash (MSF) technology due to their heavy dependence on fossil fuels (Greenlee et al. 2009). Several desalination methods have achieved significant progress in recent years and are expected to continue progressing in the future, taking into account their energy, efficiency, and economic aspects. The thermal desalination methods that incorporate a phase-change mechanism encompass MSF, VC, multi-effect evaporation, and humidification–dehumidification (HDH) desalination techniques (Li et al. 2013). The energy performance of desalination plants is assessed by metrics such as specific energy or heat consumption, gained output ratio (GOR), second law efficiency, and exergy efficiency (Altmann et al. 2019). The future of desalination is experiencing a rising trajectory, primarily propelled by factors like continuously expanding industrialization, population growth, and the deterioration of current water resources (Henthorne 2011). Nevertheless, these systems require a substantial quantity of energy, ranging from 2.5 to 12 kWh/m3 (Byrne et al. 2015), and the majority of them rely on fossil fuels. In 2012, fossil fuels accounted for 81.7% of the worldwide main energy source and 67.9% of electricity production, resulting in approximately 99.5% of the overall emissions of greenhouse gases (Dincer & Acar 2015). Nevertheless, these energy sources are depleting. Hence, it is essential to employ renewable energy sources to produce environmentally benign (non-polluting) electricity, which is vital for achieving stability. The process is widely referred to as greenization, with the aim of improving efficiency, decreasing gas pollution, recovering losses, and generating numerous outputs. Therefore, the shift toward renewable energies is inevitable in order to improve human well-being and promote economic advancement (Environment America 2009). As stated in Lindeman (2015), over 1.3 billion individuals are now deprived of access to electricity, with 95.7% of this population residing in developing nations in Asia and sub-Saharan Africa. The processes of industrialization and population growth emphasize the significance of addressing the rising energy demands of society (Li & Lin 2015). The connection between energy and water is mutually dependent, as energy is essential for the production of water through any desalination process, while power-generating units are reliant on water (IEA International Energy Agency 2016). Owing to the dwindling accessibility of fossil fuels, green energies have garnered substantial popularity and affordability, courtesy of recent technical advancements. Different types of renewable energy, including solar, geothermal, etc., have been used for desalination. Solar energy is a highly abundant and dependable source compared to other forms of renewable energy (Al Suleimani & Nair 2000; Gorjian & Ghobadian 2015). On a bright sunny day, the solar radiation that reaches the Earth's surface is about 1 kW/m2. This is only a tiny portion roughly 1/1,000th of the total energy the sun has released (Lovegrove & Luzzi 2003). Therefore, it can effectively tackle issues related to energy security and environmental concerns. Furthermore, numerous dry regions experiencing water scarcity and requiring sustainable food production are situated in areas with significant solar radiation levels, often ranging from 4 to 6 kWh/m2 (Chaibi 2013). Therefore, solar-powered desalination is a highly appealing alternative and accounts for nearly 57% of the desalination market (Eltawil et al. 2009). The article offers a thorough examination of current and developing methods designed to decrease energy usage in greenhouses. The review encompasses several subjects, such as experimental and analytical models pertaining to heating, the cooling process, and tactics for climatic control. Furthermore, it investigates the most efficient form and alignment of greenhouses. Prior research has investigated the utilization of solar energy in greenhouses for many functions, including heating, cooling, lighting, and irrigation. However, in terms of irrigation, the research has primarily concentrated on solar-powered irrigation pumps. Alternatively, utilizing solar-powered desalination systems for greenhouses is a viable method to tackle the interconnected issues of water, energy, and food. These methods have been implemented in many nations globally and analyzed in multiple papers. These technologies can enable the operation of greenhouses in rural locations that lack connection to the energy grid, commonly known as off-grid greenhouses. In 2020, Coppitters et al. conducted an assessment of the thermal and economic efficiency of a hybrid solar and microturbine system that incorporates a desalination unit. According to their research findings, the production cost of fresh water in this power plant ranges from 1.78 to 1.92 dollars per production cubic meter, which is lower than the cost of solar water desalination (Coppitters et al. 2020). The purpose of this study is to investigate the architecture and functioning of hybrid solar desalination systems. These systems utilize solar energy to perform water purification through evaporation and condensation mechanisms. The study aims to explore the advantages of solar-powered desalination systems as a preferable alternative to traditional methods, highlighting their use of clean energy and absence of noise or sound pollution. Additionally, the cost-effectiveness of solar desalination systems for generating drinking water, particularly in desert regions and inaccessible areas, is examined. The study also emphasizes the significance of utilizing waste heat energy to lower expenses and improve the effectiveness of water desalination processes. The findings underscore the importance and rationale for implementing hybrid solar desalination systems, which rely on solar energy to efficiently handle water and energy resources.

Desalination is the extraction of freshwater from seawater or other saline water sources. Currently, a range of techniques are employed to extract salt from water. The process of choosing a desalination method is contingent on variables such as the salinity of the water, the expenses associated with production, the economic circumstances of the region, the desired quality of the resulting freshwater, the existing engineering capabilities, the availability of suitable technology, and the accessibility of energy sources. These mechanisms operate according to the principles illustrated in Figure 5.
Figure 5

Working principles of desalination processes.

Figure 5

Working principles of desalination processes.

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Figure 6 provides a comprehensive overview of the categorization of desalination methods.
Figure 6

Different desalination systems.

Figure 6

Different desalination systems.

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MSF distillation is commonly referred to as MSF. The construction and operation of MSF distillation systems began in the late 1950s (Morris 1993). The operational principles of MSF distillation entail the application of heat to saltwater until it reaches a certain temperature, followed by its introduction into a chamber with a lower pressure compared to that of saturated water vapor. Some of this water rapidly evaporates, converting it into steam (Al-Ghamdi 2009). The water vapor that is suddenly produced is free from salt and other contaminants. The steam is initially routed through a dust collector and then subjected to distillation on an external plate consisting of heat transfer tubes. The desalinated water is collected in a container. The open circulation current utilizes heat transfer between the tube walls to absorb the latent heat of steam distillation (Bazargan & Salgado 2022). By implementing this approach, the circulating saline solution is heated in advance until it reaches the highest temperature at which the process may operate, and the energy derived from the steam is also recovered. To reach its highest attainable operating temperature, the preheated saline solution is then further heated using a heater or an external heat source (Nigim 2017). Figure 7 depicts the process of multi-stage flash distillation.
Figure 7

Schematic of MSF (Rabiee et al. 2019).

The adoption of multiple-effect distillation (MED) technology occurred in the late 1950s and later 1960s. Utilizing a variety of conduits and channels, a series of sequential processes carry out distillation (Long & Lee 2017). These ducts are well-known for their effectiveness, utilizing the processes of evaporation and distillation at reduced pressures to achieve their functionality (Al-Mutaz 2022). Water vapor is delivered into a series of pipes from the heater or other heat sources in these systems. The cooling and distillation process takes place when the water enters the pipes and makes contact with their surface. In contrast, the steam loses heat through heat transfer, which the feed water spraying over the pipe then absorbs, leading to its vaporization (Sayed et al. 2023). The vaporized saline solution then moves on to the next stage, delivering its thermal energy to a portion of the water, raising its temperature and causing it to evaporate (Alzafiri 2012). The procedure entails a series of chilling and evaporation phases to achieve full completion. Figure 8 illustrates the schematic of a multi-effect distillation process.
Figure 8

Schematic of MSF (Micari et al. 2019).

HDH desiccants are classified according to the arrangement of their components, the manner in which water and air circulate, and the heating of each stream (Rahimi-Ahar et al. 2020). This method is employed for the purification of water on a small scale, specifically in remote and sparsely populated areas (Fouda et al. 2018). Figure 9 illustrates one of the techniques used for desalination. The salt water traverses an open cycle by initially entering the dehumidification chamber, where it functions as a cooling flow in the heat exchanger. Subsequently, it enters the humidity chamber where it experiences the process of humidification and makes direct contact with the surrounding air (Xu et al. 2022a).
Figure 9

Schematic of HDH (open water and natural air circulation).

Figure 9

Schematic of HDH (open water and natural air circulation).

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Ultimately, it emerges from the humidity chamber. The warm air first enters the dehumidifier chamber, where it takes in moisture from the hot water. Subsequently, it moves to the dehumidifier chamber, where a fraction of the collected moisture is condensed while the remaining fraction is discharged into the surrounding atmosphere. Reverse osmosis (RO) is a procedure where water molecules travel through a semi-permeable membrane in the opposite direction of natural osmosis, leading to the removal of pollutants and the creation of pure water (Faroon et al. 2023). The commercial application of RO began in the 1970s, primarily for the purpose of desalinating saline water (Dhakal et al. 2022). RO uses pressure as a driving force to remove salt from water. The aim of this strategy is to attain an applied pressure that surpasses the threshold at which water no longer passes through the walls. The pressure that is referred to in this context is known as osmotic pressure (Helfer et al. 2014). A difference in concentration drives the phenomenon of osmosis, which involves the ingestion of dissolved substances through a selectively permeable membrane (Jiang et al. 2016). This process uses a semi-permeable membrane to separate water and finished product from concentrated water (Ruiz-García et al. 2017). The primary factor driving water movement across this barrier is the difference in concentration and pressure. Figure 10 depicts the RO process (Lovegrove & Luzzi 2003).
Figure 10

Schematic of RO (Chen et al. 2011).

Electrodialysis (ED) is an electrochemical technique employed for the purpose of desalination. This method removes dissolved ions using semi-permeable membranes and an electric field (Valero et al. 2011). A direct current voltage energizes a pair of electrodes, resulting in the production of an electric field. Ions possess an electrical charge, which can be either positive or negative. The strength of the electric field and the charge of the ion both influence the electric force applied to each ion. The anode demonstrates preferential cation absorption, primarily targeting positively charged ions such as sodium ions and calcium ions, whereas the cathode demonstrates selective anion absorption, especially targeting negatively charged ions such as chlorine ions. The process of installing anionic and cationic semi-permeable membranes alternately takes place within the area situated between two electrodes (Shahmirzadi et al. 2018). The first allows for the transportation of anions, which are negatively charged ions, while the second allows for the transportation of cations, which are positively charged ions. Semi-permeable membranes selectively hinder the movement of ions produced by the electric field. For example, a cation with a positive charge can traverse the membrane in the direction of a positively charged electrode (positioned on the left side of the image), but it is unable to cross the membrane with a negative charge. As a result, the anionic membrane prevents the positive charges from moving rightward and reaching the electrode when the electric field is present. In a similar manner, positively charged membranes impede the mobility of negatively charged ions as they travel toward the electrode with a positive charge. Consequently, the ions are confined to the salt water channels and expelled through the fresh water channels. The first commercial ED units appeared in the early 1970s (see Figure 11) (Curto et al. 2021).
Figure 11

Working principles of an electrodialysis desalination unit (Curto et al. 2021).

Figure 11

Working principles of an electrodialysis desalination unit (Curto et al. 2021).

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Hydration-based desalination (HY) produces gas hydrates. Crystalline solids consist of water and gas molecules such as nitrogen, CO2, and methane. Under normal circumstances, the process of extracting 1 m3 of hydrate results in the production of 0.8 of water and 164 of gas (Lv et al. 2019). The process of hydrate formation requires lower thermodynamic parameters (temperature below 20 °C and pressure above 30 bar) compared to other methods of phase-change desalination (Taner 2018b, 2021). HY desalination is a process that involves creating hydrates and then separating the gas and water components. Following the first cooling process, seawater is then combined with a blend of propane and carbon dioxide within the reactor. The mixture is moved to the crystallizer, where the formation of hydrate occurs because of the combination of low temperature and high pressure (see Figure 12). The aqueous mixture containing the hydrate is isolated from the saline solution and sent to a decomposer. When exposed to heat, hydrates undergo a transformation into both fresh water and gas. The final one is reclaimed for subsequent use in the synthesis of hydrate (Li et al. 2022). This technology exhibits lower energy consumption in comparison to both MSF and RO.
Figure 12

Hydration system (Curto et al. 2021).

The membrane distillation (MD) technique is a relatively new approach that is being employed to a limited extent in seawater desalination. This technology combines RO with distillation. During the purification process, water vapor particles pass through a semi-permeable membrane while the solutes in the water stay in the water flow around the unit (see Figure 13). This approach necessitates a reduced level of pressure compared to the RO technique and utilizes a smaller amount of thermal energy in comparison to the distillation method. These two benefits are associated with the MD method. However, in comparison to RO, the MD method requires more room for unit construction. Additionally, when compared to distillation, the MD method is considered to have a drawback due to the necessity of pre-treating water. It is important to acknowledge that MD was initially developed for the purpose of desalinating seawater. However, it has since expanded its use to include the purification of water with low levels of salinity (Kujawa et al. 2017).
Figure 13

Types of functional MD structures (Curto et al. 2021).

Figure 13

Types of functional MD structures (Curto et al. 2021).

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As can be seen in Figure 14, the solar distillation (SSD) can be achieved by utilizing a tank that is coated in black to enhance the absorption of solar radiation (Sharon & Reddy 2015). This tank is filled with a mixture of salt, water, and air. The device is encased in glass that is angled (Nagendrababu et al. 2023).

Thus, solar radiation heats the system and promotes fresh water evaporation. Condensation occurs on the glass surface due to the lower temperature of this area, causing internal moisture to turn into liquid droplets. Ultimately, the condensate is gathered and pure water is acquired. The graphic below displays the schematic of this system. An optimal yield of superior condensate is achieved at a rate of around 2–3 L/m2 on a daily basis. Consequently, this system is limited to small-scale applications (Curto et al. 2021). Solar water desalination system performance depends on system design, operational and environmental circumstances, and technical competency. Water depth, inlet water temperature, tilt angle, glass thickness, additional condensers, reflectors, phase-change materials, flat plate and evacuated tube collector (ETC) collectors, and nanofluids affect the thermal performance of the solar desalination system. Freshwater productivity depends on system design and technical expertise. Water depth, basin materials, transparent glass angle, water-glass temperature difference, and absorber area affect solar still productivity (Boukhriss et al. 2023). Desalination is the process of removing salt and minerals from saline water to produce freshwater. There are several methods of desalination, including thermal methods such as MSF distillation, MED, vapor-compression (VC), and membrane-based methods such as RO, nanofiltration (NF), MD, and forward osmosis (FO). Thermal methods such as MSF, MED, and VC involve heating saltwater until it reaches a certain temperature, followed by its introduction into a chamber with lower pressure compared to that of saturated water vapor. The sudden drop in pressure causes some of the water to evaporate, leaving behind salt and other contaminants. The steam produced is then condensed to produce freshwater. Membrane-based methods such as RO, NF, MD, and FO use semi-permeable membranes to separate salt and other contaminants from water. In RO, water molecules travel through a semi-permeable membrane in the opposite direction of natural osmosis, leading to the removal of pollutants and the creation of pure water. In NF, the membrane has smaller pores than in RO, allowing for the removal of smaller ions and molecules. In MD, water vapor particles pass through a semi-permeable membrane while the solutes in the water stay in the water flow around the unit. In FO, an osmotic pressure gradient drives the movement of water from a low-concentration solution to a high-concentration solution. Other methods of desalination include ED, which removes dissolved ions using semi-permeable membranes and an electric field, and HDH, which is employed for the purification of water on a small scale, specifically in remote and sparsely populated areas. Finally, hydration-based desalination (HY) produces gas hydrates, which are crystalline solids consisting of water and gas molecules such as nitrogen, CO2, and methane. The cost of producing water varies depending on the desalination method used. According to a study conducted by the International Desalination Association, the cost of producing water using RO ranges from $0.50 to $2.00/m3, while the cost of producing water using thermal methods such as MSF distillation and MED ranges from $1.00 to $3.00/m3. The cost of producing water using ED is estimated to be between $0.50 and $2.00/m3. The cost of producing water using HDH is estimated to be between $1.00 and $2.00/m3. The cost of producing water using hydration-based desalination (HY) is estimated to be between $1.00 and $2.00/m3. The cost of producing water using MD is estimated to be between $0.50 and $2.00/m3. It is important to note that the cost of water production depends on various factors such as the salinity of the water, the cost of energy, the quality of the resulting freshwater, and the availability of suitable technology and energy sources (Ziolkowska 2015; Tiwari et al. 2023).

The integration of thermal and membrane water production techniques allows for the creation of a hybrid water desalination plant. The ratio of RO desalination plants to thermal desalination plants (MED) is only affected by things like the building's conditions, changes in how much electricity and water are used, the power generation unit's utilization factor, and the presence of a water transmission network. The evaluation and calculation of the capacity ratio should be performed individually for each building, taking into account the specific circumstances of each situation. Thermal desalination facilities in tropical and temperate climates have a challenge due to the variation in water consumption throughout the year, with a rise in summer and a decline in winter. Meanwhile, the demand for water remains relatively stable. Therefore, when the burden of the power generation unit is reduced, the production of thermal desalinated water (MED) is also dropped accordingly. These situations also arise when the power-generating unit is temporarily removed for periodic maintenance and repairs. Hence, a RO desalination facility is presently being built. Furthermore, thermal desalination (MED) has the capacity to improve the flexibility of water and energy production.

Hybrid power plants have the advantage of reducing water production costs. For water made using the hybrid RO technique, the TDS measurement indicates that the water quality level is between 300 and 500 parts per million (ppm). On the other hand, water obtained using the multi-effect distillation method has an exceptionally low total dissolved solids (TDS) level that is less than 10 parts per million (ppm). Therefore, combining water produced through the multi-effect distillation method with water generated through RO reduces the need for adding extra chemicals and leads to a drop in the costs associated with water production. If the power plant is used, it would be wise to use a single-path design in RO. This would result in enhanced water quality in the output of the RO process. The RO system gradually improves the quality of the water it produces. Hybrid power plants utilize the thermal technology known as MED to generate water of exceptional purity. As a consequence, there are longer time intervals between replacing the membrane, which ultimately leads to decreased operational expenses. Furthermore, another advantage of the hybrid method is that the product water and concentrated water (brine) generated by the thermal process usually have a relatively high temperature, requiring cooling for environmental purposes. The lower temperatures of the product and RO-concentrated water lower the temperature when combined. An important limitation of RO systems is the high concentration of concentrated water. Releasing a substantial quantity of water back into the ocean can result in ecological problems. Nevertheless, the combination of condensed water from thermal systems and the low concentration of hybrid power plants yields a satisfactory quality of output water that may be safely discharged into the sea. Table 1 presents a comprehensive summary of various research studies conducted in the field of hybrid desalination.

Table 1

Hybrid desalination technologies

RowYearResearcherConducted researchResults
2012 Shakib Simulating and thermodynamically optimizing a multi-effect distilled water desalination system that utilizes thermal steam condensation paired with a gas turbine cycle and a heat recovery boiler. The findings of this study indicate that the particle swarm optimization (PSO) algorithm achieves a superior minimum value for the objective function, despite exhibiting higher efficiency (Shakib et al. 2012). 
2014 Najafi An energy, exergy, and environmental economic analysis of a solid oxide fuel cell for gas turbine and water desalination is done. The exergetic efficiency of this optimal strategy is 46.7%, and the investment return period is 8 years (Najafi et al. 2014). 
2015 Palenzuela Technical economic analysis – combined production of electricity and freshwater in the Mediterranean and MENA Region Enhancing energy efficiency and exergy to ultimately boost the productivity factor (Palenzuela et al. 2015). 
2017 Almutairi Integrating a 100 MW gas turbine with a reverse osmosis (RO) unit to establish a power station. The combined cycle of simultaneous production is more efficient than the separate mode (Almutairi et al. 2017). 
2017 Shahzad The integration of an absorption chiller and RO system in the Persian Gulf, utilizing thermal and solar energy sources. The system achieves a remarkable efficiency of 18% and consumes only 1.76 kWh/m3 of energy (Shahzad et al. 2017). 
2017 Mohammadi A Kalina cycle and RO desalination system generate power, heating, refrigeration, and fresh water. This system has the capacity to generate 46.77 kW of power, provide 451 kW of heating, 52 kW of cooling, and produce 0.79 kg/s of fresh water (Mohammadi & Mehrpooya 2017). 
2017 Mata-Torres Examining the feasibility of utilizing solar power facilities to generate both electricity and potable water in Venezuela and Chile. A power plant with a power capacity of 50 MW has the ability to supply electricity and fresh water to a population of 85,000 individuals (Mata-Torres et al. 2017). 
2018 Lai An evaluation of the Stirling Alpha engine coupler including RO and electrochemical discharge machining (EDM). The maximum productivity estimate is 3% (Lai et al. 2018). 
2018 Hafdhi Exploring the solar desalination system utilizing solar collectors and phase-change materials. The quantity of freshwater generated is directly proportional to the rise in surrounding temperature and the rate of circulation of hot water (Hafdhi et al. 2018). 
10 2018 Sadri Developing a mathematical representation of a hybrid desalination unit that incorporates an absorption cooling system, focusing on analyzing its efficiency and cost-effectiveness using exergy and economic principles. The quantity of freshwater generated in this situation exceeded twice the original amount (Sadri et al. 2018). 
11 2018 Ghorbani The utilization of flat plate collectors for power and fresh water generation in an industrial town situated in Asalouye. The capacity to generate 1,864 kW of electricity, 65,154 kW of thermal energy, and 83.22 kg/s of potable water concurrently (Ghorbani et al. 2018). 
12 2020 Elsaid Analysis of current advancements in utilizing waste heat for the purpose of desalination. Utilizing WH yields substantial economic and environmental advantages, resulting in decreased desalination expenses and associated GHG emissions (Elsaid et al. 2020). 
13 2020 Abd Elbar This article presents empirical research on improving the effectiveness of a hybrid solar desalination system. The system consists of a combined solar panel and desalination chamber, which are reinforced by the utilization of porous materials and preheating of salt water. Raising the temperature of the incoming water by 50, 40, and 60% leads to an associated enhancement in desalination efficiency by 10.4, 20.9, and 15.5%, respectively, along with an elevation in energy efficiency of 8.2, 13, and 20% (Abd Elbar & Hassan 2020). 
14 2021 Wang An investigation of the efficiency of a new concentrated solar energy and desalination system that utilizes the Brayton cycle and MSF technology. The economic feasibility of the concentrated solar-driven power and desalination (CSPD) system was acknowledged (Wang et al. 2021). 
15 2021 Malik An exergoeconomic study and multi-objective optimization were conducted on a solar desalination system that utilizes paraffin as a phase-change material. The exergy efficiency improved by approximately 1.47%, and the annual production of distilled water increased by 4.35% compared to the suboptimal system (Malik et al. 2021). 
16 2021 Sanna Analyzed the technical aspects of a decentralized salt water RO desalination unit that operates using photovoltaic (PV) technology and pumped storage. The utilization of a high-pressure pump in the battery system exhibits a notable enhancement of 2.4% in overall efficiency when compared to current designs of Brackish Water RO systems that depend on photovoltaic PV and battery technologies (Sanna et al. 2021). 
17 2021 Xu Exploring methods to decrease salt content in solar-powered desalination systems. The text discusses the categorization of ways for reducing salt content using photothermal evaporation configurations. It also explores the fundamental mechanism behind salt reduction and the creation of photothermal materials for this purpose (Xu et al. 2021). 
18 2021 Li Advanced technology for using sunlight energy to produce sustainable solar water. Efficient, energy-conserving, and affordable procedures can be employed to convert different alternative water sources, such as seawater, atmospheric water, and sewage, into fresh water (Li et al. 2021). 
19 2021 Gao Utilizing solar energy to drive a membrane distillation process for water generation. Guidelines for the material and system design of photothermal membrane distillation (PMD) systems are given to facilitate the advancement of portable water provision in both large-scale and decentralized systems (Gao et al. 2021). 
RowYearResearcherConducted researchResults
2012 Shakib Simulating and thermodynamically optimizing a multi-effect distilled water desalination system that utilizes thermal steam condensation paired with a gas turbine cycle and a heat recovery boiler. The findings of this study indicate that the particle swarm optimization (PSO) algorithm achieves a superior minimum value for the objective function, despite exhibiting higher efficiency (Shakib et al. 2012). 
2014 Najafi An energy, exergy, and environmental economic analysis of a solid oxide fuel cell for gas turbine and water desalination is done. The exergetic efficiency of this optimal strategy is 46.7%, and the investment return period is 8 years (Najafi et al. 2014). 
2015 Palenzuela Technical economic analysis – combined production of electricity and freshwater in the Mediterranean and MENA Region Enhancing energy efficiency and exergy to ultimately boost the productivity factor (Palenzuela et al. 2015). 
2017 Almutairi Integrating a 100 MW gas turbine with a reverse osmosis (RO) unit to establish a power station. The combined cycle of simultaneous production is more efficient than the separate mode (Almutairi et al. 2017). 
2017 Shahzad The integration of an absorption chiller and RO system in the Persian Gulf, utilizing thermal and solar energy sources. The system achieves a remarkable efficiency of 18% and consumes only 1.76 kWh/m3 of energy (Shahzad et al. 2017). 
2017 Mohammadi A Kalina cycle and RO desalination system generate power, heating, refrigeration, and fresh water. This system has the capacity to generate 46.77 kW of power, provide 451 kW of heating, 52 kW of cooling, and produce 0.79 kg/s of fresh water (Mohammadi & Mehrpooya 2017). 
2017 Mata-Torres Examining the feasibility of utilizing solar power facilities to generate both electricity and potable water in Venezuela and Chile. A power plant with a power capacity of 50 MW has the ability to supply electricity and fresh water to a population of 85,000 individuals (Mata-Torres et al. 2017). 
2018 Lai An evaluation of the Stirling Alpha engine coupler including RO and electrochemical discharge machining (EDM). The maximum productivity estimate is 3% (Lai et al. 2018). 
2018 Hafdhi Exploring the solar desalination system utilizing solar collectors and phase-change materials. The quantity of freshwater generated is directly proportional to the rise in surrounding temperature and the rate of circulation of hot water (Hafdhi et al. 2018). 
10 2018 Sadri Developing a mathematical representation of a hybrid desalination unit that incorporates an absorption cooling system, focusing on analyzing its efficiency and cost-effectiveness using exergy and economic principles. The quantity of freshwater generated in this situation exceeded twice the original amount (Sadri et al. 2018). 
11 2018 Ghorbani The utilization of flat plate collectors for power and fresh water generation in an industrial town situated in Asalouye. The capacity to generate 1,864 kW of electricity, 65,154 kW of thermal energy, and 83.22 kg/s of potable water concurrently (Ghorbani et al. 2018). 
12 2020 Elsaid Analysis of current advancements in utilizing waste heat for the purpose of desalination. Utilizing WH yields substantial economic and environmental advantages, resulting in decreased desalination expenses and associated GHG emissions (Elsaid et al. 2020). 
13 2020 Abd Elbar This article presents empirical research on improving the effectiveness of a hybrid solar desalination system. The system consists of a combined solar panel and desalination chamber, which are reinforced by the utilization of porous materials and preheating of salt water. Raising the temperature of the incoming water by 50, 40, and 60% leads to an associated enhancement in desalination efficiency by 10.4, 20.9, and 15.5%, respectively, along with an elevation in energy efficiency of 8.2, 13, and 20% (Abd Elbar & Hassan 2020). 
14 2021 Wang An investigation of the efficiency of a new concentrated solar energy and desalination system that utilizes the Brayton cycle and MSF technology. The economic feasibility of the concentrated solar-driven power and desalination (CSPD) system was acknowledged (Wang et al. 2021). 
15 2021 Malik An exergoeconomic study and multi-objective optimization were conducted on a solar desalination system that utilizes paraffin as a phase-change material. The exergy efficiency improved by approximately 1.47%, and the annual production of distilled water increased by 4.35% compared to the suboptimal system (Malik et al. 2021). 
16 2021 Sanna Analyzed the technical aspects of a decentralized salt water RO desalination unit that operates using photovoltaic (PV) technology and pumped storage. The utilization of a high-pressure pump in the battery system exhibits a notable enhancement of 2.4% in overall efficiency when compared to current designs of Brackish Water RO systems that depend on photovoltaic PV and battery technologies (Sanna et al. 2021). 
17 2021 Xu Exploring methods to decrease salt content in solar-powered desalination systems. The text discusses the categorization of ways for reducing salt content using photothermal evaporation configurations. It also explores the fundamental mechanism behind salt reduction and the creation of photothermal materials for this purpose (Xu et al. 2021). 
18 2021 Li Advanced technology for using sunlight energy to produce sustainable solar water. Efficient, energy-conserving, and affordable procedures can be employed to convert different alternative water sources, such as seawater, atmospheric water, and sewage, into fresh water (Li et al. 2021). 
19 2021 Gao Utilizing solar energy to drive a membrane distillation process for water generation. Guidelines for the material and system design of photothermal membrane distillation (PMD) systems are given to facilitate the advancement of portable water provision in both large-scale and decentralized systems (Gao et al. 2021). 

The basic driver of heat desalination is heat. Integrating these units with power generation plants to create water and power simultaneously is a viable way to achieve competitive economics. Traditional electricity generation requires continual water sources, while water desalination requires constant energy. Hybrid systems that produce electricity and fresh water simultaneously are needed due to their dependency. Using the power plant's condensation heat to power the water desalination unit increases the thermal efficiency (Shakouri et al. 2021). Cost reductions can be attained by using shared infrastructure equipment across plants, such as the power plant condenser as a salt water heater in the desalination plant, and employing the same inlet and outlet openings (Rezk et al. 2019). Waste can be reduced by optimizing energy transmission and cutting costs. In addition, we may improve land utilization and reduce industrial maintenance and repair labor. Figure 15 shows a hybrid system with a RO fuel cell. This arrangement heats saline feed water with fuel cell chimney waste heat (Rezk et al. 2019). A drop in pressure reduces desalination energy usage by 8–10% when the drinking water temperature rises from 20 to 28 °C, according to research. Enhanced efficiency reduces the number of membrane elements needed to obtain the same water flow rate, lowering capital and operating expenses. The dissolved ion content in the water produced is a minor drawback. Due to osmotic pressure, product water quality diminishes with temperature. Compared to water, ions require more activation energy to flow across the membrane (Singh 2008).
Figure 15

RO and fuel cell hybrid desalination system (Singh 2008).

Figure 15

RO and fuel cell hybrid desalination system (Singh 2008).

Close modal

An important benefit of a fuel cell RO desalination plant is its low water requirement for fuel cell operation, as opposed to the significant water usage of conventional power plants (CPP) for cooling purposes. Fuel cell plants also help to alleviate or eliminate harmful environmental effects on aquatic ecosystems. In integrated membrane desalination (CPP) power plant systems, thermal energy discharge into the oceans is a major issue (Shakouri et al. 2021).

RO water desalination with PV devices is a promising renewable energy desalination method (Delgado-Torres et al. 2020), especially efficient when used in remote areas. As a result, there has been considerable enthusiasm for employing small-scale PV–RO systems in recent times, leading to the development of several demonstration systems (Al-Karaghouli & Kazmerski 2013). The market offers PV dilute and concentrated RO desalination systems (PV/brackish water reverse osmosis (BWRO) and PV/seawater reverse osmosis (SWRO)). The process of desalinating salt water requires minimal pressure, leading to a low usage of electricity (Delgado-Torres et al. 2020). Across the world, a multitude of solar and RO initiatives have been successfully executed. Some of these projects have integrated battery systems or energy backup mechanisms to guarantee uninterrupted functionality. Consequently, the expense of water production is elevated. Figure 16 depicts a PV/RO schematic.
Figure 16

RO and photovoltaic hybrid desalination system (Al-Karaghouli & Kazmerski 2013).

Figure 16

RO and photovoltaic hybrid desalination system (Al-Karaghouli & Kazmerski 2013).

Close modal
Solar thermal energy systems use sunshine to generate extreme heat, which is used to generate electricity using steam turbines, gas turbines, or stirling engines. The devices use glass mirrors to track the sun to improve concentration. The flat collector, Fresnel mirror reflector, power tower, and dish motor are significant CSP technologies (Iaquaniello et al. 2014). The main purpose of CSP installations is to generate energy. The CSP can be combined with other desalination methods. MED and RO are best for CSP desalination (Mohammadi et al. 2019). An MED system can use the parabolic arrangement to use high-temperature steam (more than 380 °C) in a turbine and then for desalination (Iaquaniello et al. 2014). The usual steam temperature for the MED system is 70 °C, ensuring enough energy for electricity production before usage. In recent years, this method has grown significantly (Mohammadi et al. 2019). Its economic competitiveness compared to other desalination systems is limited and requires further development. Figure 17 shows the hybrid (CSP/MED) system (Al-Karaghouli & Kazmerski 2013).
Figure 17

CSP/MED combination schematic (Al-Karaghouli & Kazmerski 2013).

The concentrated solar power (CSP) plant can harness thermal energy to provide the required electrical power for operating the RO pumps (Iaquaniello et al. 2014). Combining CSP with MED for desalination has benefits. First, CSP can provide reliable and sustainable energy for desalination, reducing fossil fuel use and greenhouse gas (GHG) emissions. Second, by storing extra energy in thermal storage systems, CSP can power the desalination process even when the sun is not shining. Third, CSP can offer energy and heat for desalination, improving system efficiency. Finally, CSP can power remote MED systems without expensive transmission lines or infrastructure (Liu et al. 2024). Combining CSP and MED reduces the energy needed to produce freshwater, improving desalination efficiency. Compared to standard thermal desalination methods, combining CSP with MED can lower energy consumption by up to 50%, according to a Berkeley study (Xu et al. 2022b). Engineers have concluded, via experiments, that coupling CSP with RO is more efficient and consumes less energy than coupling CSP with CSP/MED. Figure 18 depicts a schematic illustration of the CSP/RO combination (Al-Karaghouli & Kazmerski 2013).
Figure 18

CSP/RO combination schematic (Al-Karaghouli & Kazmerski 2013).

The Stirling water desalination system consists of two components: a power generation component and a water desalination component (Al-Karaghouli & Kazmerski 2013). A diagram of the proposed system is shown in Figure 19. The Stirling engine design is specifically designed for power generation and acts as the initial component to provide the required heat for the subsequent multi-effect water desalination system (Shakouri et al. 2021). This configuration allows for the simultaneous production of electricity and drinkable water for a small community living in remote and secluded areas (Karambasti et al. 2022).
Figure 19

Stirling/MED desalination system.

Figure 19

Stirling/MED desalination system.

Close modal
A combined power, heating, and cooling (CCHP) system, MED unit with thermal vapor compression (TVC), solar energy recovery (SER), and heat exchanger make up the hybrid system (Moghimi et al. 2018). Primary power generation uses a hybrid power cycle with a solid oxide fuel cell (SOFC) and micro gas turbine (MG). A thermocompressor-equipped water desalination unit, Rankine organic cycle with an ejector cooling cycle, and heat exchanger are used to generate fresh water, chill district power, and heat dwellings. Figure 20 shows the suggested system schematic (Moghimi et al. 2018). The high-efficiency SOFC system uses an inverter, afterburner (AB), gas microturbine, air compressor, and fuel compressor. In the lower cycle, the water softener-thermocompressor unit can use the waste heat from the gas microturbine-SOFC hybrid power cycle to make drinking water. This heat can be collected in the heat recovery boiler (WHB) (Ghamari et al. 2022). The heat recovery boiler consists of an evaporator, an economizer 1, and an evaporator 2. The economizer and evaporator 1 have the capability to produce steam (38) that is used to power the desalination unit – thermocompressor, yielding the generation of potable water (Ghamari et al. 2022).
Figure 20

MED/CCHP/heat exchanger combination schematic (You et al. 2020).

Figure 20

MED/CCHP/heat exchanger combination schematic (You et al. 2020).

Close modal
The solar desalination hybrid system schematic is shown in Figure 21. The HDH solar unit has two vertically aligned ducts linked above and below to form a closed air loop and an open water loop (Easa et al. 2023). The dehumidifier gathers condensed water from its condenser, while the evaporator transfers hot water to a separate tank for desalination in the solar desalination unit. This procedure enables the uninterrupted generation of potable water, which can take place around the clock (Sharshir et al. 2016).
Figure 21

Solar water heater and HDH combination schematic (Sharshir et al. 2016).

Figure 21

Solar water heater and HDH combination schematic (Sharshir et al. 2016).

Close modal
To tackle the issue of limited power and water resources, it is customary to integrate thermal desalination facilities with power plants, forming a dual-purpose system that concurrently generates electricity and provides freshwater (Sharshir et al. 2016). The combined MED–RO system may simultaneously provide potable water while utilizing the gas turbine (GT) for power generation. The hybrid method depicted in Figure 22 has the following advantages: improved adaptability and readiness in water production during times of electrical sector disruption due to repairs or insufficient demand in the network (Mokhtari & Sepahvand 2016). Combining the water from the RO system with the water from the distilled water (MED) system can significantly lower desalination costs. Lower the temperatures of water and wastewater produced in RO systems compared to MED systems and utilize additional grid electricity during periods of high demand for water production (Mokhtari & Sepahvand 2016; Khouya 2023).
Figure 22

Schematic diagram of reverse osmosis hybrid system, multi-stage distillation, and modeled gas turbine (Mokhtari & Sepahvand 2016).

Figure 22

Schematic diagram of reverse osmosis hybrid system, multi-stage distillation, and modeled gas turbine (Mokhtari & Sepahvand 2016).

Close modal
The power plant uses a GT SOFC hybrid system and a triple-pressure steam recovery generator (HRSG) for waste heat recovery (Yadav & Singh 2022). Figure 23(a) and 23(b) show the schematic design of the SOFC-GT integrated system (Vojdani et al. 2021).
Figure 23

(a) SOFC-GT integrated with WHR and (b) MED–TVC schematic (Vojdani et al. 2021).

Figure 23

(a) SOFC-GT integrated with WHR and (b) MED–TVC schematic (Vojdani et al. 2021).

Close modal

Figure 23(a) shows how the triple-pressure HRSG gets heat for the double-pressure steam turbine cycle (Yadav & Singh 2022). In addition, the heat that is recovered from the low-pressure HRSG is used as steam to improve the efficiency of the Med/TVC desalination plant. To get the required operating pressure for the SOFC system, the fuel–air combination containing methane and the water needed are individually pressurized using a compressor and a water pump, respectively (Wang et al. 2023). Before entering the chimney, each of these three currents is heated separately to the designated input temperature of the chimney (SOFC) (Azhar et al. 2023). Preheated fuel and steam are mixed in the mixing unit to make gas. At point 1, the mixture enters the SOFC. The gas mixture is then modified and transferred into the anode electrode to form hydrogen for electrochemistry. The cathode electrode receives equally distributed preheated air for an electrochemical process that produces energy and heat (Azhar et al. 2023). For SOFC cooling, the canal cathode uses most of the air. In addition, an inverter converts direct electricity into grid-quality alternating current. Fuel cell heat is used for adjustment and to raise the output current temperature (Wang et al. 2023). The high-temperature gas mixture and exhaust gases from the anode and cathode of the fuel cell are, respectively, routed to the rear, where the fuels (methane, hydrogen, and carbon) do not undergo a reaction with surplus air. The high-temperature combustion gases are harnessed to produce additional power for the compressors as they flow through the GT. The GT exhaust is channeled toward point two of three pre-heater sets to elevate the temperature of the incoming flow for the SOFC (Vojdani et al. 2021).

The remaining pre-heater gases still contain a lot of energy that must be used. Before being released into the environment, exhaust gases enter the triple pressure (HRSG) system, which generates steam in three subsystems. Each subsystem has 10 heat transfer phases (Azhar et al. 2023). The heat exchangers are strategically located to create high pressure (HP), intermediate pressure (IP), and low pressure (LP) at 33, 36, and 37. MED/TVC unit details, including parallel feed, are shown in Figure 23(b). Figure 23 shows steam cycle ejector, evaporation, and condenser. These data show that steam from the latter phase of evaporation warms seawater first. A large amount of the condenser (MED) warmed seawater is used as cooling water. As seawater feed, the residue is equally distributed during evaporation. It is important to remember that MED systems transfer steam from high-pressure to low-pressure units during evaporation. Therefore, an ejector steam cycle is used to offset the pressure drop between the beginning and final stages. The HRSG's low-pressure stage sends saturated steam into the ejector steam cycle to remove some of the final evaporation steam. In the initial evaporation phase tube heat exchanger, pressurized steam from the ejector steam cycle condenses completely (Ghaedi et al. 2022). In this process, feed water is sprayed to absorb thermal energy and evaporate (Ghaedi et al. 2022). Seawater supplied into the shell side of the initial evaporation process is heated to the first effect's boiling point. Thus, some seawater evaporates and flows toward the pipe as a heat supply (Shakib et al. 2021). The residual feed saltwater, with high dissolved chemical content and boiling temperature, is pumped into the following stage. Every hit sends steam and concentrated brine through the next to evaporate evenly sprayed feed water into potable water (Shakib et al. 2021). Evaporating the maximal seawater concentration back into the ocean is the final result. The suggested cogeneration system is evaluated, focusing on mathematical models and assumptions. This evaluation analyzes the system's energy, exergy, economics, and environmental performance, considering all important factors. Figure 24 displays an initial examination of a new hybrid power plant that can produce 10 MW of electricity to fulfill the power and fresh water needs of Kish Island in Iran (Sadeghi & Askari 2022).
Figure 24

Multiple hybrid system based on power and fresh water production (Sadeghi & Askari 2022).

Figure 24

Multiple hybrid system based on power and fresh water production (Sadeghi & Askari 2022).

Close modal

The system includes a molten carbonate fuel cell (MCFC), GT, steam Rankine cycle (SRC), solar tower (ST), organic Rankine cycle (ORC), and MED/RO desalination units. In Figure 24, the solar cell tower and natural gas boiler (NGB) are heating the MCFC reactants. Methane (CH4), air, and water react. The NGB raises the solar field temperature from 570 to 935 °C. MCFC preheaters need this greater temperature. Higher temperatures are needed to elevate the MCFC intake to 550 °C. The reactants from the MCFC's power generation are sent to the AB, where the exhaust stack fuel is used to raise the GT input temperature to 909 °C. Combustion will occur. Power comes from AB exhaust gases supplied into the GT. The HRSG converts combustion byproducts from the GT into steam for the 545 °C SRC. After leaving the heat recovery steam generator, the reactants enter the organic Rankine cycle at 152 °C to heat the organic fluid and generate electricity. Finally, the RO desalination plant uses organic Rankine cycle power to produce fresh water. Figure 24 shows the SRC condenser replaced by a multi-stage distillation desalination device to produce fresh water. In order to summarize the stated content, it can be said that solar desalination systems have the potential to provide a sustainable and reliable source of freshwater in areas with limited access to freshwater resources. However, there are several challenges that need to be addressed to make solar desalination systems more efficient and cost-effective. One of the main challenges of solar desalination systems is their low efficiency compared to conventional desalination methods. Solar desalination systems require a large amount of energy to produce freshwater, which can be expensive and inefficient. Additionally, solar desalination systems are highly dependent on weather conditions, which can affect their performance and productivity. Another challenge of solar desalination systems is their high capital and maintenance costs. Solar desalination systems require a significant investment in infrastructure and equipment, which can be a barrier to their widespread adoption. Additionally, solar desalination systems require regular maintenance and cleaning to ensure their optimal performance, which can be time-consuming and expensive. Despite these challenges, solar desalination systems have several advantages and prospects for the future. Solar desalination systems can provide a sustainable and reliable source of freshwater in areas with limited access to freshwater resources. Additionally, solar desalination systems can reduce dependence on fossil fuels and lower GHG emissions. Furthermore, advances in technology and materials science are expected to improve the efficiency and cost-effectiveness of solar desalination systems in the future. In conclusion, solar desalination systems have several challenges and prospects for the future. While there are several challenges that need to be addressed to make solar desalination systems more efficient and cost-effective, advances in technology and materials science are expected to improve the efficiency and cost-effectiveness of solar desalination systems in the future.

Through a comprehensive analysis of the fundamental principles and real-world applications, this study emphasizes the importance of hybrid solar desalination systems in addressing water scarcity and ensuring efficient water and energy resource management. By combining technological innovations with renewable energy sources, these systems pave the way for a sustainable future and provide access to clean water in diverse and challenging environments. This study on hybrid solar desalination systems has shed light on their innovative structure and impressive performance in addressing the pressing challenge of water purification. By harnessing abundant solar energy, these systems efficiently convert saline water into fresh drinking water through evaporation and condensation mechanisms. The research findings demonstrate that solar-powered desalination systems offer a remarkable alternative to traditional methods, as they rely on clean energy sources, produce no noise pollution, and have shown cost-effectiveness, particularly in desert regions and inaccessible areas. Furthermore, the incorporation of waste heat energy into the desalination process has been highlighted as a significant breakthrough. The utilization of waste heat energy not only reduces expenses but also enhances the overall effectiveness of water desalination. This innovation holds great promise for improving the efficiency and sustainability of hybrid solar desalination systems. The study's analysis of the fundamental principles and real-world applications emphasizes the importance and rationale for implementing hybrid solar desalination systems. The combination of renewable energy sources, technological innovations, and efficient water management paves the way for a sustainable future. These systems not only contribute to water security but also align with global sustainability goals and efforts to mitigate climate change. In conclusion, the innovative structure and impressive performance of hybrid solar desalination systems showcased in this study offer a promising solution to the global water crisis. Continued research and investment in this field will further drive advancements, making these systems even more efficient, affordable, and widely accessible. With their potential to provide clean water in a sustainable manner, hybrid solar desalination systems represent a significant step toward a more water-secure and environmentally conscious future.

The author extends his appreciation to the deanship of scientific research at Shaqra University for supporting this research work.

The authors give their full consent for the publication of this manuscript.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

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