DESALINATION STATION USING A HEAT PUMP AND PHOTOVOLTAIC ENERGY Technical field

The present invention relates to a desalination station according to the characteristics of the pre-characterizing part of claim 1.

Definitions

In the present description and in the appended claims the following terms must be interpreted according to the definitions given in the following.

With the term "desalination" or "desalinization" a process is generically indicated, which is used to reduce the amount of solids dissolved in water.

With the terms "solids dissolved in water" one should not understand only dissolved salt, but also minerals and/or chemicals contained in not drinking water.

The term "saline water" or "salty water" must be understood as including water comprising medium or high concentrations of salts or anyway of solids dissolved in water.

Prior art

In the field of execution of desalination systems or plants to obtain desalinated water for drinking use various processes are known, each of which is used in different fields according to the concentrations of salts present:

- ion exchange desalination in which the water is made to pass between two electrodes maintained at a low potential difference;

- electrodialysis desalination in which the salts are separated from the water by ionic migration through membranes inserted in an electric field;

- reverse osmosis desalination in which the water is separated from the salts by filtering through membranes;

- distillation desalination in which the seawater is heated until producing vapour that condenses and is collected.

DE 102004033409 describes an automatic water desalination plant, based on evaporation using a solar collector and a heat pump or Peltier element, using countercurrent principle for partial energy recovery.

WO2004076359 describes a water desalination method comprising the steps of: supplying thermal energy to salt water in a vaporisation zone, removing water vapour from the vaporisation zone to a condensation zone, and at least partly condensing the water vapour into fresh water in the condensation zone. A heat pump is used to transfer at least part of the heat extracted from the water vapour in the condensation zone to the salt water in the vaporisation zone. WO2004076359 also describes an apparatus for use in water desalination comprising: a vaporization chamber for holding seawater, and having a water vapour outlet connected via a water vapour transfer conduit to a condensation chamber for condensation of air humidity into fresh water. The vaporization chamber has at least one heater arranged to supply thermal energy to the salt water in the vaporization chamber. A heat pump is used to transfer at least part of the heat from the water vapour in the condensation chamber to the heater.

CN201059804Y relates to a combined device of power generation and seawater desalination by means of a photovoltaic system. The device uses the electric power and the thermal energy generated by the generation of energy through the photovoltaic system and a heat pump that is the heat source supplied to a container of the vapour at a low temperature and seawater desalination device; at the same time, a power supply system is used, which uses a renewable energy source to carry out the desalination of seawater.

Problems of the prior art

Each of the systems of the prior art presents different problems that limit their applicability.

For example, as for ion exchange desalination, the system must be periodically cleaned from the salts making water pass in the opposite direction and, furthermore, it is not applicable in case of high salt concentrations.

As for electrodialysis desalination, the desalination costs are very high and require much energy insomuch as the electrodialysis desalination plants are generally operated at night when the electrical fares are lower and, moreover, this method is not applicable in case of high salt concentrations.

As for reverse osmosis desalination, problems of high cost are linked both to the cost of the membranes used and to the cost of the electric power necessary for the activation of the high pressure pumps insomuch as the electrodialysis desalination plants are generally operated at night when electric fares are lower. If one does not use expensive membranes with a high resistance to pressure this process is not usable for high salt concentrations. Moreover, the water must be previously filtered to eliminate particles that might damage the membrane itself, besides requiring the addition of chemical additives to control pH and minimize the deposit of salt on the surface of the membrane.

As for distillation desalination, it is cheaper than the previous ones, but it requires the presence of energy sources for heating all the same, insomuch as its use is generally limited to the cases in which either hot water is already present as a waste product of other processes or when low cost energy is available or in the cases in which energy and desalinated water can be produced simultaneously in a co- generation process. The large-scale distillation units use a process known as Multistage distillation flash, which requires very expensive and bulky equipment for the need to have a series of evaporation chambers, each at a pressure and temperature lower than the previous one.

Aim of the invention

The aim of the present invention is to provide a desalination station or plant that exploits in an efficient way the available energy resources and that is able to work autonomously with respect to external energy sources coming from power networks, gas, hydrocarbons or other fuels.

Concept of the invention

The aim is achieved with the characteristics of the main claim. The sub-claims represent advantageous solutions.

Advantageous effects of the invention

The solution in accordance with the present invention, by the considerable creative contribution the effect of which constitutes an immediate and not negligible technical progress, presents various advantages.

A very important advantage is that the desalination station or plant according to the present invention can work autonomously with respect to external energy sources coming from power networks, ensuring its applicability also in case of isolated areas, for example areas not served by power networks or in the absence of external energy sources such as electric generators powered by fuel, the desalination plant according to the present invention being anyway able to work autonomously with respect to external energy sources coming from power networks, gas, hydrocarbons or other fuels.

A further advantage of the present invention is an efficient exploitation of the available energy minimizing energy waste.

A further advantage of the present invention is that it is particularly compact, resulting of easy installation.

A further advantage of the present invention is that it finds advantageous application in an installation made directly at sea, avoiding a waste of ground.

A further advantage of the present invention is that it can also be made in relatively small scale to meet the needs of small residential centres, for example small isolated residential centres.

Description of the drawings

In the following an embodiment is described with reference to the enclosed drawings to be considered as a non-limiting example of the present invention in which: Fig. 1 represents a schematic side view of the desalination station made according to the present invention.

Fig. 2 represents a schematic plan view of the desalination station made according to the present invention.

Fig. 3 represents a schematic front view of the desalination station made according to the present invention.

Fig. 4 represents a schematic sectional view of the structure of the wall of the desalination station made according to the present invention.

Fig. 5 represents a schematic side view of the container of the desalination station made according to the present invention showing the components inside the container. Fig. 6 represents a schematic side view of the casing of the desalination station made according to the present invention showing the components inside the casing.

Fig. 7 represents a schematic view of the desalination station made according to the present invention showing the connection diagram of the components.

Fig. 8 represents a schematic view of the desalination station made according to the present invention showing the schematic diagram of the desalination station.

Fig. 9 represents a schematic view of the desalination station made according to the present invention in an illustrative installation solution.

Fig. 10 represents a schematic view of the desalination station made according to the present invention in an illustrative installation solution.

Description of the invention

The invention aims at reproducing the cycle of water that develops in nature making the most of solar energy only, providing a distillation desalination station or plant in which the seawater is heated until producing vapour that condenses and is collected, all this exploiting only solar energy in a high energetic efficiency station or plant.

The salient steps of the water desalination process by distillation are the evaporation and the condensation of the humidity with the consequent recovery of the condensed water with a low concentration of dissolved solids at a suitable temperature and pressure gradient.

The present invention finds advantageous application in the case of the treatment of salty or brackish waters, such as seawater, even if the invention is applicable in an advantageous way also for low concentrations of dissolved solids.

The solution according to the present invention allows to speed up the evaporation of salty or brackish water and the following condensation of damp air minimizing the dispersion of the energies necessary for the realization of the cycle.

The desalination station (1) according to the present invention (Figures 1 , 2, 3) consists of a casing (2) into which salty or brackish water is introduced and closed by a hood (3) inside which is the container (4) in which the condensation of fresh water occurs.

The energy necessary to obtain evaporation is provided by solar radiation using both the phenomenon of production of energy by photovoltaic principle and the thermal phenomenon to heat the water.

The current technologies allow to combine the photovoltaic solar panel (5) with a light metal structural section (56) able to convey a cooling liquid inside it. In the desalination station (1 ) according to the present invention this solution offers various advantages. First of all the presence of a particularly light supporting structure allows to carry out a movement of the solar panels (5) suitable to obtain at any time of the day the best exposure possible with respect to the position of the sun. Moreover, the cooling of the photovoltaic solar panel (5) allows to maintain a high photovoltaic efficiency of the cells. Finally, the use of a cooling liquid that removes the heat accumulated on the photovoltaic solar panel (5) also allows to transfer the heat developed by solar radiation to a second environment, in this case to the salty or brackish water to obtain its evaporation in order to carry out the distillation process.

As known, the process of evaporation is regulated by temperature and pressure conditions, which determine the necessary evaporation energy: the higher the temperature, the greater the evaporation and the lower the pressure the greater the evaporation.

The desalination station (1) according to the present invention exploits all the physical principles present in the cycles of the various components and in the natural cycles in order to obtain the greatest efficiency possible:

- the heat obtained by cooling the photovoltaic solar panels (5) to improve their efficiency is transferred to the brackish or salty water to increase its temperature;

- the heat obtained by cooling the water vapour by condensation is transferred to the brackish or salty water to increase its temperature;

- the air taken from the casing containing the brackish or salty water to create a depression favouring the process of evaporation is used to increase the pressure inside the condensation container to favour the condensation process itself;

- tides are exploited to obtain the replacement of the brackish or salty water.

With these solutions the energy necessary to carry out the process is reduced, making the desalination station (1 ) according to the present invention particularly efficient insomuch as to make it autonomous from the energy point of view and allowing its installation also in areas where other energy sources are not available. The need for other energy sources is often a big obstacle to the spread of the desalination systems.

In the embodiment described (Figures 1 , 2, 3) the desalination station (1) according to the present invention consists of a cylindrical casing (2) into which the salty or brackish water is introduced through a feeding connection (33) and closed by a frusto- conical hood (3) inside which is the container (4) in which the condensation of the fresh water occurs. An internal drawing connection (35) present on the container (4) is connected to a corresponding external drawing connection (34) for drawing the desalinated water. Advantageously the hood (3) is a separate body with respect to the casing (2) and it can be removed for maintenance or inspection operations. For example the hood (3) can be hinged to allow its opening by rotation on the horizontal plane or by lifting an end, or, still, it can be intended to be lifted vertically by means of the use of jacks, etc. As an alternative, the hood (3) can also be made in two parts, one of which is a fixed part and the other is a movable part the opening of which allows access into the casing (2). Advantageously the hood (3) is equipped with guides (29) on which the supporting structure of the solar panels (5) can move, thus allowing for the movement of the panels. In the embodiment shown the supporting structure of the solar panels (5) can rotate (Fig. 2) on the guides (29) of the hood (3) along an arc of 180° in order to have the maximum solar energy of the day. In this way maximum efficiency is obtained in the generation of the electric power by the solar panels (5) and an optimal energy balance is obtained for the whole day. Obviously the photovoltaic solar panel (5) can be mounted on a supporting structure movable on the guides (29), and the movement of the photovoltaic solar panel (5) can be controlled by a control board (42) both with regard to the sun elevation and with regard to the sun azimuth to obtain a corresponding change in inclination (62) and/or a change in orientation (63) of the photovoltaic solar panel (5). The movement is realized by means of at least one motor (28), which is supplied by means of the electric power produced by the solar panel (5). A solar exposure sensor (57) (Figures 7, 8) can provide the control board (42) with the instructions necessary to command the rotation of the solar panels (5) or the control can occur by the knowledge of the position of the installation, that is to say, knowing, for each period of the year and for each hour of the day, the corresponding data of sun elevation and azimuth. The signal of the solar exposure sensor (57) can also be a signal obtained from a corresponding signal coming from the same photovoltaic solar panel (5), without the need for an external exposure sensor (57).

As previously observed, to further increase efficiency in the generation of the electric power by the solar panels (5), they are cooled. In fact, as it is known, the efficiency of the conversion of solar energy into electric power tends to decrease as temperature increases. Since the solar panels (5) can be moved along the guides (29) of the hood (3), the cooling circuit is made by means of flexible connections, if necessary equipped with rapid connections to also allow a rapid unfastening of the structure of the hood (3) in case it is necessary to remove it from the casing (2) for maintenance or inspection operations. Therefore, the cooling circuit of the solar panels (5) will include (Figures 2, 3) outlet pipes (26) of the "hot" coolant coming from the solar panels (5) and return pipes (27) of the "cold" coolant that is sent again to the solar panels (5) for their cooling.

Advantageously, as previously explained, to increase the efficiency of the desalination station (1) according to the present invention, the heat removed from the solar panels (5) to improve their efficiency is not wasted, but, rather, it is reused to heat the brackish or salty water in the distillation process. For this purpose (Figures 7, 8) a coolant circulation pump (17) is provided, which sets in motion the coolant coming from the outlet pipes (26), sends it to a first heat exchanger (6) and afterwards sends the coolant to the solar panels (5) again by means of the return pipes (27) of the "cold" coolant. The first heat exchanger (6) allows the heat exchange between the coolant circulating in the cooling circuit of the solar panels (5) and the brackish or salty water present in the casing (2). In particular the first heat exchanger (6) is immersed in the brackish or salty water present in the casing (2). The coolant circulation pump (17) is supplied by the electric power produced by the photovoltaic solar panels (5).

Moreover, advantageously, as explained before, to increase the efficiency of the desalination station (1) according to the present invention, the heat removed from the container (4) where the condensation occurs is used to heat the brackish or salty water in the distillation process. For this purpose (Figures 5, 7, 8) a heat pump (16) is provided which allows to remove heat from the refrigerating plate (9) present in the container (4) to transfer it by means of the circuit (52) of the heat pump, through the throttle valve (12), to a second heat exchanger (7), which is immersed in the brackish or salty water present in the casing (2), so that the heat coming from the refrigerating plate (9) is used to heat the brackish or salty water in the distillation process. The heat pump (16) is supplied by the electric power produced by the photovoltaic solar panels (5).

Therefore, in short, (Figures 7, 8), in a structural casing (2) of realization of the desalination station (1), through the water inlet (18), by means of a feeding pump (13), the brackish or salty water is introduced up to a limit level of brackish or salty water (37) determined by an outlet corresponding to a too full connection (36) and controlled by a first level sensor (39). The feeding pump (13) is supplied by the electric power produced by the photovoltaic solar panels (5) and the respective circuit is provided with a first check valve (10). Inside the casing (2) is a container (4) enclosing the refrigerating plate (9) of a heat pump (16). Inside the container (4) the damp air condenses and the so desalinated water is collected inside the container (4) itself for use in anthropic activities, also food activities upon purification. The desalinated water can be purified for example by means of a purification block (55) for instance by filtering and/or disinfection, obtaining drinking water. The desalinated water is extracted from the container (4), by means of a drawing pump (1 ) the circuit of which includes a second check valve (1 1) and the desalinated water is made available at the water outlet (19). The drawing pump (14) can be for example controlled by a second level sensor (40) and a third level sensor (41 ) one of which checks the activation of the drawing pump (14) when the level of desalinated water (38) is higher than a given threshold and the other checks its switching off when the drawing pump (14) has sufficiently lowered the level of desalinated water. The drawing pump (14) is supplied by the electric power produced by the photovoltaic solar panels (5). An accumulation container (20) of the desalinated water can also be provided.

Furthermore, the efficiency of the desalination station (1 ) according to the present invention is improved by the change in the evaporation and condensation pressures. As previously observed, evaporation increases as pressure decreases and, in a similar way, the condensation of water vapour increases as pressure increases. Therefore, by sucking in some air and forcing it to pass at a certain depth in the liquid, both a depression and an increase in the equivalent surface of evaporation are obtained. This is realized by immersing an air diffuser (8) below the first level (37) of salty or brackish water and conveying the damp air drawn by the hood (3) towards the refrigerating plate (9). A damp air circulation pump (15) is installed inside the casing (2) and creates a depression in the hood (3) to favour water evaporation and an overpressure in the container (4) to favour vapour condensation.

As previously observed, the condensation temperature is determined by the heat pump (16), which returns the heat taken from the container (4) in favour of the evaporation in the casing (2).

The level of the diffuser (8) with respect to the level of brackish or salty water (37) determines the depression of stimulation of the evaporation while the characteristics of the damp air circulation pump (15) determine the pressure provided to favour the condensation to obtain the desalinated or fresh water.

The depression is given by the difference in height between the diffuser (8) and the level of brackish or salty water (37).

For example 35 cm of difference in height are equivalent to about -35 relative hPa (hectopascals); the damp air circulation pump (15) can give a pressure drop of 80 hPa with a flow of 60 m ³ /h absorbing about 200 electric Watts, giving a pressure for condensation of 45 hPa.

The damp air circulation pump (15) sucks in (Fig. 6) the damp air by means of a suction mouth (21) present in the hood (3) and has the characteristic of conveying the air on an damp air duct (22) at high speeds up to (Fig. 5) the damp air inlet (24): for a duct of 30mm of diameter the air volume given imposes a speed of about 24m/s to the atmospheric pressure, which is high to obtain a high humidity rate from the evaporation.

To obtain lower speeds, the air is conveyed (Fig. 5) from the dry air outlet (25) through (Fig. 6) the dry air duct (23) to a diffuser (8) that distributes it on a surface that indicatively can be two/three orders of magnitude greater (about 1m of diameter) or even more than the diameter of the duct, obtaining transit speeds on the thickness of the water for the evaporation lower than 1 m/s.

All the necessary energy is supplied by the photovoltaic solar panels (5), which, as previously observed, are maintained at room temperature to improve efficiency, the heat taken from the solar panels (5) being used to contribute towards heating the top part of the salty or brackish water favouring evaporation.

For example, a couple of high efficiency photovoltaic solar panels (5) can supply over 450W of electric power and over 2300 thermal Watts able to supply the necessary electrical appliances and provide evaporation with about 350cal (1260kcal/h).

In the container (4) where the condensation occurs the damp air arrives at a positive pressure delta and, consequently, at a positive temperature delta. The air is cooled by means of the circuit of the heat pump (16) obtaining the drying of the air. This dried air is sucked and sent to the diffuser to be humidified again.

The circuit of the heat pump (16) is required to take the damp air to dew temperature for the condensation of the humidity contained therein; this is obtained by cooling the inlet air from about 40°C to about 0°C by means of a heat pump (16) that absorbs about 200 electrical Watts.

On the top of the container (4) of condensation and above the dry air diffuser (8) are immersed both the first heat exchanger (6) relative to the cooling of the solar panels (5) and the second heat exchanger (7) relative to the circuit of the heat pump (16). The heat exchangers (6, 7) are immersed in salty or brackish water, in order to maintain the top of the salty or brackish water at a positive temperature delta contrasting the heat reduction caused by evaporation.

In this way the heat taken for the cooling of the solar panels (5) and the heat taken from the condensation of the vapour of the damp air are returned to the salty or brackish water to increase its temperature and favour its evaporation.

The amount of heat given to evaporation is equal to about 1500kcal/h such as to raise the temperature of the superficial mass of the salty or brackish water to about 35°C.

To limit energy contributing towards obtaining a desalination station autonomous and independent of external electrical connections, the orientation (rotation) of the solar panels (5) can occur for example on a hour basis while the activation of the damp air circulation pump (15) and of the heat pump (16) occurs thanks to the photovoltaic state of the panels.

Advantageously, the introduction of the salty or brackish water through the water inlet (18), with a relative re-balance of the salinity can be carried out in the night hours, while the extraction of the fresh water can be activated on threshold levels established by the level sensors (40, 41) as explained before.

In order to limit energy waste for the loading of seawater the desalination station (1) can be placed in correspondence of sea coasts and partially immersed in seawater in such a way that the changes in sea level due to changes in tide levels and/or wave motion contribute towards the necessary refilling. Alternatively, or in combination with this solution, one can resort to the feeding pump (13) which in the night hours can be supplied (Fig. 8) by means of a battery (43) that is recharged during the day by means of the photovoltaic solar panels (5) themselves. Obviously the battery (43) can be used both to provide the necessary electric power making up for the possible losses of the electric power generated by the photovoltaic solar panel (5) during temporary obscuration of the sun, and to provide the electric power necessary for the night replacement or the night replenishment of the water. The fact that the desalination station is partially immersed in seawater or anyway in the water to be treated, in addition to the advantage of being able to obtain a natural replacement of the water contained to be desalinated or from which remove the dissolved solids, also allows to avoid the installation of expensive ducts for the drawing of the water to be treated, with consequent benefits from the point of view of the system and of nature. In fact, besides avoiding the presence of the ducts, except for the one for the drawing of the water deriving from the desalination process, the desalination station (1 ) can be at least partially camouflaged by the sea level itself, reducing its visual impact.

For example (Figures 9, 10), the desalination station (1 ) can be mounted in correspondence of a coast (64) on a supporting structure (60) resting on the sea bed (59) or floating so that the desalination station (1 ) is partially immersed in correspondence of the sea level (58). The supporting structure (60) may also advantageously comprise an auxiliary room (61 ) for containing the previously described auxiliary devices external to the casing (2), such as the feeding pump (13), the drawing pump (14), the control board (42), the battery (43), etc. The feeding pump (13) supplied by the electric power generated by the photovoltaic solar panel (5) and/or by the battery (43), therefore, is suitable to contribute to the replacement and/or to the replenishment of the salty or brackish water or anyway water with dissolved solids contained in the casing (1) by drawing water from a water inlet (18). The change in tide levels and/or wave motion (schematically represented by the arrows in Figures 9, 10) will contribute to the water fill up of the casing (2), if necessary assisted by the action of the feeding pump (13).

An illustrative and non-limiting design of the desalination station (1) according to the present invention, for example, could correspond to a fresh water output capacity of about 50l/h in peak time and a typical daily output of over 300I, sufficient for the domestic uses of a family with annexed fixtures. Obviously, according to needs, greater sizes are also possible, respecting the proper correspondences for the energies necessary for operation.

The structure can be made (Fig. 4) completely of composite materials and, to further increase efficiency, it will preferably include an internal structure (30) and an external structure (31) between which there is an insulator (32). This applies both to the container (4) and to the casing (2). The structure realized will preferably be load- bearing, so that the installation is particularly simple without the need for particular additional works.

In conclusion, the desalination station (1) according to the present invention (Fig. 8) includes:

- a cold area (44) consisting of the container (4) in which the condensation of the water vapour occurs and comprising level sensors (40, 41) for the start and the end of the drawing phase on the basis of the level (38) of the desalinated water and further comprising the refrigerating plate (9) with a respective throttle valve (12);

- a hot area (45) defined by the casing (2) comprising the first heat exchanger (6), the second heat exchanger (7), the dry air diffuser (8) and the corresponding circulation pump (15) of the damp air with the respective ducts of damp air (22) and of dry air (23) and further comprising the first level sensor (39) for measuring the level (37) of the brackish or salty water;

- a feeding area (46) comprising the feeding pump (13) with the respective first check valve (10);

- a drawing area (47) comprising the drawing pump (14) with the respective second check valve (11);

- a power supply generation area (48) comprising the photovoltaic solar panels (5);

- a movement area (49) of the photovoltaic solar panels (5) comprising the motor (28) and the possible exposure sensor (57), the signal of which, as previously explained, can also be a signal obtained from a corresponding signal coming from the photovoltaic solar panel (5) itself, without the need for an external exposure sensor (57);

- a heating area (50) comprising the coolant circulation pump (17) of the solar panels (5) to transfer their heat to the hot area (45) by means of the respective outlet pipes (26) and return pipes (27) of the coolant;

- a control area (51) comprising the control board (42) and a possible rechargeable battery (43).

Finally, the desalination station (1) according to the present invention is of the distillation type and comprises a hot area (45) defined by a casing (2) and by a hood (3) containing water with dissolved solids that is caused to evaporate to generate water vapour, up to a first level (37), a cold area (44) consisting of a container (4) in which the condensation of the water vapour coming from the hot area (45) occurs with the formation of water without dissolved solids or fresh water up to a second level (38), at least one heat pump (16) that transfers heat from a refrigerating plate (9) present in the cold area (44) to a second heat exchanger (7) that gives heat to the water with dissolved solids causing the evaporation of the water contained in the casing (2) with the formation of water vapour in correspondence of the hood (3), transferring means (15) of the water vapour from the hood (3) to the refrigerating plate (9), a feeding area (46) of the water with dissolved solids towards the casing (2), a drawing area (47) of the condensed water and further comprises a power supply generation area (48) which comprises at least one photovoltaic solar panel (5) and a heating area (50), the photovoltaic solar panel (5) generating the electric power supply at least for the heat pump (16) and the transferring means (15) of the water vapour making said desalination station (1) autonomous from other external energy sources, the photovoltaic solar panel (5) being combined with a circulation system (56) of a cooling fluid that is put in circulation by a circulation pump ( 7) present in the heating area (50) supplied by said photovoltaic solar panel (5), the cooling fluid circulating in correspondence of the solar panel (5) and transferring heat from the solar panel (5) to the hot area (45) by means of a first heat exchanger (6) that gives heat to the water with dissolved solids contained in the casing (2) of the hot area (45).

Furthermore, the system preferably comprises other sensors, such as a first hood temperature sensor (53), a second container temperature sensor (54), which, together with the first level sensor (39), the second level sensor (40), the third level sensor (41) are connected to the control board (42) that carries out the corresponding control functions of the elements present, such as the motor (28) for moving the photovoltaic solar panels (5), the feeding pump (13), the drawing pump (14), the damp air circulation pump (15), the heat pump (16), the coolant circulation pump (17).

In a different embodiment, essentially assimilable to that schematically represented in Fig. 8, the container (4) can be not immersed in the casing (2), that is to say, not immersed in the salty or brackish water, but the container (4) can be placed under the casing (2). It will be obvious to those skilled in the art that the solar panels (5) can also be made up of one or more photovoltaic solar panels in combination with one or more thermal solar panels according to the total size of the system and to the performances required. Therefore, the photovoltaic solar panel (5) can be combined with one or more thermal solar panels to heat the water to be evaporated.

As previously observed, the desalination station (1 ) can include various sensor means, such as a hood temperature sensor (53) and/or a container temperature sensor (54) and/or a panel temperature sensor and/or an exposure sensor (57) and/or humidity measuring sensors and/or level sensors (39, 40, 41). Said control board (42) will preferably control the activation of the possible pumps present according to the embodiment of the present invention, such as the feeding pump (13) if present, the drawing pump (14) if present, the damp air circulation pump (15), the heat pump (16), the coolant circulation pump (17) and/or the activation of the possible motors (28) for moving the photovoltaic and/or thermal solar panels (5) depending on the measurements carried out by means of said sensor means. For example the control board (42) can control the coolant circulation pump (17) and/or the motors (28) for moving the photovoltaic and/or thermal solar panels (5) according to the signal provided by the exposure sensor (57) or to an equivalent signal coming from the solar panel (5) itself and/or according to the signal provided by the panel temperature sensor. In a similar way, the control board (42) can control the possible drawing pump (14) according to the signals provided by the level sensors (40, 41) or the possible feeding pump (13) according to the signal provided by the first level sensor (39). In a similar way, the control board (42) can control the activation of the heat pump (14) according to the signals provided by the humidity measuring sensors and/or according to the signal provided by the hood temperature sensor (53) and/or according to the signal provided by the container temperature sensor (54).

Therefore, in general, the desalination station (1 ) can comprise sensor means including a hood temperature sensor (53) and/or a container temperature sensor (54) and/or a panel temperature sensor and/or an exposure sensor (57) and/or humidity measuring sensors and/or level sensors (39, 40, 41), and the activation of the possible pumps (13, 14, 15, 16, 17) and/or of the possible motors (28) can be controlled by the control board (42) depending on the measurements carried out by means of the sensor means.

The description of the present invention has been made with reference to the enclosed figures in the form of a preferred embodiment, but it is evident that many possible alterations, changes and variants will be immediately clear to those skilled in the art in light of the previous description. Therefore, it should be pointed out that the invention is not limited by the previous description, but includes all the alterations, changes and variants in accordance with the appended claims.

Used nomenclature

With reference to the identification numbers reported in the enclosed figures, the following nomenclature was used:

1. Desalination station

2. Casing

3. Hood

4. Container

5. Solar panel

6. First heat exchanger

7. Second heat exchanger

8. Diffuser

9. Refrigerating plate

10. First valve

11. Second valve

12. Throttle valve

13. Feeding pump

14. Drawing pump 15. Damp air circulation pump or transferring means of the water vapour

16. Heat pump

17. Coolant circulation pump

18. Water inlet

19. Water outlet

20. Tank

21. Suction mouth

22. Damp air duct

23. Dry air duct

24. Damp air inlet

25. Dry air outlet

26. Hot coolant outlet pipe

27. Cold coolant return pipe

28. Motor

29. Guide

30. Internal structure

31. External structure

32. Insulator

33. Feeding connection

34. External drawing connection

35. Internal drawing connection

36. Too full connection

37. First level or level of brackish or salty water or water with dissolved solids

38. Second level or level of desalinated water or fresh water

39. First level sensor

40. Second level sensor

41. Third level sensor

42. Control board 43. Battery

44. Cold area

45. Hot area

46. Feeding area

47. Drawing area

48. Power supply generation area

49. Movement area

50. Heating area

51. Control area

52. Circuit of the heat pump

53. First hood temperature sensor

54. Second container temperature sensor

55. Purification block

56. Structural section or circulation system

57. Exposure sensor

58. Sea level

59. Sea bed

60. Supporting structure

61. Auxiliary room

62. Change in inclination

63. Change in orientation

64. Coast