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    • 专利摘要:
    Underwater desalination plant that operates on the seabed, connected to the coast, which takes advantage of the hydrostatic pressure generated by the submergence, without requiring intake or discharge works. Integrated into a constructive unit, it emerges by injecting air under pressure. At sufficient depths, a feed flow enters through the filter (5), sucked by a pump (1) located in a concentrate duct, then evacuated by a chimney (16). At lower depths, the pump (1) sucks the feed flow through the chimney (16), driving it at a pressure which, added to the hydrostatics, allows the reverse osmosis process to be operated, inverting the flow direction. The permeate, poured into a pitcher (3) connected to the surface by means of a vent (8), is driven and transported by pipes (20) or tankers to the coast. Arranged as a roof with two slopes, with the membrane tubes (13) flanged to the pitcher (3), the desalination plant rests on a closed structure. (Machine-translation by Google Translate, not legally binding)
    公开号:ES2680904A1
    申请号:ES201700175
    申请日:2017-03-06
    公开日:2018-09-11
    发明作者:Manuel Lahuerta Romeo
    申请人:Manuel Lahuerta Romeo；
    IPC主号:
    专利说明:

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    DESCRIPTION
    Underwater desalination plant.
    Object of the invention
    The present invention, as expressed in the description of this specification, refers to an underwater desalination plant that provides essential novelty characteristics and notable advantages over other desalination plants of the current state of the art.
    More particularly, the invention relates to a seawater desalination plant that connected to the coast works submerged in the marine environment at a depth that, by submergence and naturally, achieves the necessary pressure to obtain drinking water from a Reverse osmosis process through membranes.
    Field of application of the invention
    The field of application of the present invention is within the sector of drinking water supply to coastal areas, although due to its low energy cost, speed of implementation and transportability, it can be easily found within other sectors of the technique, such as for water supply even to irrigation facilities in agriculture with high added value.
    Background of the invention
    Reverse osmosis is a process of obtaining potable water from sea or brackish water, very widespread and known, with a large number of large companies, distributed throughout the world, operating within this activity.
    In general, existing facilities have an open outlet or coastal wells to capture the raw water to be treated. These shots represent large civil works executed on the coast.
    After a collection and filtration process, the raw water is energized at pressures of the order of 55-60 bar to feed the pressure tubes containing the membranes. With conversion rates of 40-45%, two flows are obtained, namely, one of permeated water (without pressure) and another of rejection, which represents 60-65% very charged with salts (brine) that is poured back into the sea through a conduction (emissary) that takes it away from the coast. As this flow (brine) is pressurized, a part of its energy is recovered by turbines or other similar devices that reduce the energy demand of the process. At present, this energy demand is of the order of 3.4-3.9 KWh / m3 depending on the salinity of the raw water, the quality sought and the design of the mechanical components (pumps and turbines) used in the process.
    It should be noted that in July 2015 the same author of the present invention filed an International Patent application with the PCT No. ES20150370379, relating to "procedure and means to dilute or concentrate solutions applied to water desalination processes", in the that an osmosis plant is located at the bottom of a coastal well obtaining very important energy advantages. This procedure supposes the previous execution of a work of taking, consisting of a well of great depth (400-450 m) of great diameter, since inside it, in its bottom, the own osmosis plant is installed.
    It also requires the extraction of the flow of concentrate, through the mouth of the well, and then pour it into the sea, through an emissary, which represents new works. These requirements
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    they limit and condition the size of the plants and their possibilities of expansion, especially in geologically difficult areas to drill, of low permeability or of high seismic activity.
    The invention described in said International patent application transfers the procedure to the seabed by installing the suspended wells from a floating platform anchored to the bottom, operating in accordance with the principles claimed in it.
    Explanation of the invention.
    The final objective pursued by this type of facilities is to have potable water on the coast, where the greatest demand is based. Therefore, it is sought to install these desalination plants closest to the coast, where the raw material is inexhaustible and of quality, provided that the necessary conditions are achieved for the osmosis process to work. The desalination plant recommended by the present invention has set other important additional objectives, including the following:
    As ecological objectives we can specifically mention two:
    - Avoid long and expensive works derived from the shots for the collection and discharge of emissaries that violate the coastal ecosystem.
    - Pour less concentrated brines easily diffused in the marine environment, minimizing the harmful effect on the ecosystem.
    Another environmental objective is to achieve the energy sustainability of the process. Thanks to the depth at which it operates, the pressure necessary for the reverse osmosis process can be obtained naturally. Well, for the process to work it is necessary, in principle, to force water flows through tubes containing filters and membranes, and then force the permeate to the coast. To force these flows it is necessary to have pumps that consume energy, although the needs in the specified circumstances, are of the order of half that in the traditional procedures, using 20% in generating the flow of feeding through the tubes that they contain filters and membranes and 80% in extracting the permeate to the coast. This lower energy consumption and the fact that the pressure remains constant naturally, allows more easily the support of renewable energy to the process, achieving greater energy sustainability.
    Another objective of the present invention is to obtain drinking water immediately. As the plant operates submerged in the marine environment, the zero civil work to be carried out allows to reduce the installation and commissioning times of the plant. From a provisional generator set and the installation of pipelines or tankers that evacuate the permeate, the plant resting on the bottom of the sea can begin to operate.
    The invention described herein dispenses with any floating platform, as well as the installation of two wells suspended from said platform and improves the installation and operation procedure since, being the plant resting on the seabed, it takes full advantage of the maximum pressure Hydrostatic available. It is a structural design of its own, being energetically fed from the ground, the plant being designed so that it can emerge when injecting compressed air. Advantages that denote clear differences in both its design and operation with respect to other alternatives.
    The present invention achieves the aforementioned objectives by providing a better solution to the problems of supplying drinking water to coastal areas immediately and sustainably, and it should be noted that the applicant does not have
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    knowledge of the existence of any other invention that has similar characteristics.
    As is known, coastal desalination plants work with a raw material that is seawater. Having seawater in uniform quantity and quality is the first point to solve. A good water intake (raw water) must be inexhaustible and unalterable in its quality, in addition to agreeing that it is at a constant temperature. Therefore, any desalination project must start from that premise, that is, by designing a good raw water intake. Deep intakes, conveniently off the coast, better meet these requirements. The present invention has taken these considerations into account.
    Thus, in the installation proposed by the present invention, a reverse osmosis process begins by adding to the water flow to treat a pressure higher than the osmotic (23 bar for seawater) that is called net pressure, this being of the order of 50% higher than osmotic, to obtain acceptable qualities and productions with low conversion rates. The submarine desalination plant described herein, when operating on the seabed has no limits in the collection of water to be treated, being of uniform quality and temperature in addition to having pressure naturally. This makes it possible to operate with low conversion rates, requiring less net pressure to permeate, and which in turn causes the concentrate flows to be less charged, thus being able to operate closer to the coast. The discharges of the concentrate flow must be diluted at points away from those of the intake, so that an evacuation chimney has been arranged that, while standing upright and flexible, is oriented in the direction of the sea current to avoid its feedback.
    The submarine desalination plant developed in the present invention, designed to operate supported by the seabed, takes the water from its lower part, where the pressure is higher, entering the free end of the tubes that house filters and membranes, where it is fragmented into two flows: permeate and concentrate.
    The permeate (15/30%) is collected inside the pitcher, a cylindrical receptacle that is subjected to the pressure caused by the submerged outside, but that its interior remains at atmospheric pressure when connected by a vent with the surface. Inside the pitcher there is a motor pump that drives the permeate and that by means of pipes or tankers, is transported to the coast for consumption. The concentrate (85/70%) is sucked through manifolds, by low pressure pump, only defeating losses in tubes, filters and membranes to end up being expelled to the marine environment by means of a chimney as a flexible, armed sleeve by floating hoops that keep it upright, which serves as an evacuation duct (emissary) and that is capable of tilting slightly in favor of the sea current, thus separating both areas to avoid feedback between flows.
    The project begins once the quantities and qualities to be delivered in a given area have been defined.
    With the available information on the seabed mapping (see Navionics system), the points closest to the coast that meet the required depth conditions are searched, then making a transverse profile of the seabed to the coast where the pipes for extracting permeate and submarine cables that will supply the plant with energy.
    Since the osmotic pressure of seawater is of the order of 23 bar, it is necessary to exceed this pressure threshold for the reverse osmosis process to begin. At this pressure we will have to
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    add the net pressure, responsible for the quality and quantity of the permeate that will be of the order of 50% more (23 x 1.5 = 34.5 bar) to operate with conversion rates of 15% to 20%.
    Since the density of seawater is 1032 kg / m3, and since 1 bar equals 10.2 m of water column of 1000 kg / m3 density, 9.88 meters of column of seawater are needed to get 1 bar of pressure. In the calculations that follow, the approximation of 1 bar = 10 meters of submergence has been adopted.
    Operating with the Q + Projection program available for download at www.nanoh2o.com you get that:
     Water to the imentada-Aqua de Mar  Ppm 32,000
     Temperature, ° C  25
     PH  * 7.8
     Membrane Year  3
     Flow Rate  m3 / h 11
     Recovery  % fifteen
     Membrane Model  L.GSW4 4 OES
    Operating for 1 tube with 3 membranes in series, with permeate back pressure of 0.2 bar (maximum level of +2 mca inside the pitcher), the following data are obtained, among others:
     Permeate Flow  1.65 mVh
     Permeate TDS  269.72 ppm
     Container Pressure Drop  1.1 bar
     Supply Pressure R0  33.51 bar
     Concentrate Flow  9.35 mVh
     TDS Concentrate  37,537 ppm
    To provide the desalination plant of the present invention with these requirements demanded by the results of the program, it will be enough to achieve a pressure of 33.51 bar from a depth of 335 m, and generate a flow of 11 m3 / h of feed per three membrane tube, by means of a pump capable of overcoming the pressure loss of 1.1 bar, equivalent to 11 mca, plus the pressure losses associated with this flow in filters and ducts («1.2 mea) resulting in a pressure to overcome of: 11 + 1.2 = 12.2 mca, so that for this application a power is required (per tube of three membranes) of:
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    80% pump performance in all cases:
    11 x 12.2
    CV ---------------- 0, 621 fe 0, 457 kW
    3.6 x 75 x 0.8
    resulting in a specific consumption for this concept of:
    0, 457
    --------- = 0.277 kWh / m3
    1.65
    15% of the feed flow is converted to the permeate flow (269 ppm) that drains into a sealed container (pitcher) whose interior is at atmospheric pressure because it is connected through a vent with the surface. This vessel or pitcher houses inside the motor pump responsible for extracting the permeate to the coast, overcoming the height due to the depth plus the losses of load of the transport pipes that for a speed of 0.65 m / s, are encrypted at 1 m / km. A multi-stage vertical motor pump, of the type used in deep well extraction, in which the motor is submerged, of IP68 protection with balanced mechanical seals to seal its axis, and special housing capable of withstanding external pressures of 35 bar is preferred that could occur in the event of a power failure and poor closure of the non-return valve, due to the withdrawal of the supply water to the coast.
    The power absorbed in this process of driving the permeate through the 5 km of transport pipe:
    image 1
    Therefore, the total power of the process will be the sum of the two pumps (feed + permeate), that is, kW = 0.457 + 1.91 = 2.367 kW per 3-membrane tube, resulting in a global specific consumption of:
    2,367
    ---------- - 1,434 kWh / m3
    1, 65
    of permeate (2.5 to 3 times smaller than traditional).
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    Due to the in-line arrangement of the permeate drive pump with the concentrate suction pump since both pumps can operate associated to the same axis and, therefore, to the same number of revolutions, it is preferred to use a single motor to drive both pumps, whose power is the sum of the two. This coaxial arrangement of both pumps also has an additional advantage, which is that their respective axial thrusts (trust) are arranged to be in the opposite direction and therefore partially compensated, as is convenient for a longer engine life. The feed flow generating pump is preferably propeller, with 4 adjustable blades to adjust its draft and obtain the necessary flow to achieve the desired conversion ratio.
    When there is a circumstance that the available depth near the coast is less and does not compensate for moving far from the coast, it will be necessary to pressurize the feed flow to achieve, along with the submergence, the appropriate pressure (33.5 bar) necessary for the reverse osmotic process. In this case, there will be a residual pressure in the concentrate flow from which its energy can be recovered. Ideally, with this energy, recovered by means of a turbine, it is possible, either to pump the feed flow, or to boost the permeate flow to the coast, thus avoiding the use of the submersible motor pump inside the tank, being :
    Q1 = feed flow (100%) pressurized to P1.
    Q2 = concentrate flow (85%) pressurized to P2.
    Q3 = permeate flow (15%) pressurized to P3 (pressure to transport to shore).
    If it is fulfilled that [0.69 (Q2xP2)> Q3xP3], the permeate can be extracted by turbine the concentrate, for turbine yields of 0.85 and pump performance of 0.82 attainable with a suitable design whenever it is a question of permeate flow rates Q3> 0.1 m3 / s. Therefore, it will be necessary to pressurize the feed flow Q1, sucking it through the chimney, so that after passing through filters and membranes, it is evacuated by means of a collector that leads it to the waste pressure recovery turbine, so that will reverse the direction of flow.
    When there is the circumstance of desalination of brackish or salty waters driven from the mainland, the deep desalination plant will provide hydrostatic pressure, reducing energy consumption and will serve as an emissary.
    Because they are low conversion plants, which cause low concentration brines, they are diluted in the marine environment, affecting the ecosystem less. This argument, together with the fact that it does not require tapping or emissary works and low energy consumption, are key aspects in the evaluation of the environmental impact and therefore the underwater desalination plant of the present invention responds to the concept of environment-friendly desalination plants. environment and more sustainable.
    Other advantages provided by the underwater desalination plant of the present invention and which should be mentioned, derived from this application, include those mentioned below:
    The membranes, the heart of the osmosis system, work in this application at low pressure (33.5 bar), almost a third of the pressure they can withstand. In addition, because they are static natural pressure, without peaks or vibrations, they are less fatigued without risks of collapse. The last membrane (3a) of the tube works with low concentration and therefore without risk of crystallization. As a consequence of all this, the typical washings that precede the stops are not necessary.
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    The desalination plant of the present invention is controlled by means of a series of sensors, some on land and others in the underwater plant itself. From ground, the flow rates and qualities of the permeate are controlled, as well as ensuring that energy consumption is within the expected rates.
    In the dimensioning of pipes and transport cables, special attention is paid to the fact that the assembly has a lower weight of its own so that they are floating during the installation process, and that once they are located in the vertical of their future location they are easily collapsible by simply introducing water into the pipes.
    The desalination plant disclosed herein is able to integrate in a single construction unit the collection, filtration, feed pump, osmosis plant, permeate pitcher and dilution of rejection with a total weight of 11 Tm dry, for a plant of 50 1 / s or 4320 m3 / day, which allows the installation to be defined as a light and portable plant. The weight of the plant when submerged is 6.5 Tm, because it is made of low density materials that allow the use of the tank as a float because it has a greater displacement, so that by injecting compressed air from the outside, through the vent, the water is discharged from the inside through the backflow valve located at the bottom, the plant emerging to facilitate maintenance operations, especially the replacement of filter cartridges and membranes.
    The stability of the underwater plant against sea currents is guaranteed by offering low cross-section and its inclined shape, which causes reactions whose directions tend downwards adding to the weight and increasing its stability.
    Thus, duly explained the submarine desalination plant proposed by the present invention, any expert will appreciate that it represents an innovative solution with characteristics and operation far superior to those offered by the plants of the current technique, reasons that together with its practical utility endow it of sufficient foundation to obtain the privilege of exclusivity that is requested.
    Description of the drawings
    To complete the description that is being made and in order to facilitate its understanding, a set of drawings is attached, in which the following has been represented by way of illustration and not limitation:
    Figure 1 is an illustrative chart of the symbols used in the following figures, with explanation of each one of the symbols.
    Figures 2.1 to 2.3 are schematic illustrations of examples of desalination plants located at different depths.
    Figure 3 represents an example of an underwater desalination plant where the main elements of the plant are arranged as a roof with eaves on two slopes.
    Figure 4 is a graphic, schematic representation of an example of a practical embodiment of a desalination plant according to the present invention.
    Preferred Embodiment of the Invention
    In the following, a detailed description of an illustrative, non-limiting example of the object of the invention will be made, with reference to the representations shown schematically in the accompanying drawings. So, attending first
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    Instead of the explanatory table shown in Figure 1, it can be seen that there are only graphic symbols identifying the devices, mechanisms or instruments involved in the schematic representations contained in Figures 2 to 4, together with the designation, composition and / or operational characteristics of the devices associated with some of said symbols. Figure 1 is therefore included for informational purposes only.
    If the representation of Figure 2 is now taken into account, it can be seen that it shows three application schemes at different depths, identified as Figures 2.1 to 2.3. In such schemes, the striped part represents the marine environment.
    Figure 2.1 represents a scheme of an underwater desalination plant according to the invention, installed at a depth sufficient to operate as described. The raw water (4.a) comes under pressure through the inlet (7) located on the seabed, passes through the filter (5), entering the membranes (4) under pressure due to the suction caused by the motor pump (1) placed in the duct (4.b) of the concentrate. The same engine, located in the tank (3) 15 drives the permeate drive pump (1) to the coast. The tank (3) has at its bottom a non-return valve (6) to evacuate the permeate (4c) when compressed air is injected through the vent (8) to emerge. The vent (8) keeps the pitcher (3) at atmospheric pressure in normal operation.
    Figure 2.2 is a schematic representation of an example of positioning an underwater desalination plant at an insufficient depth to operate. The raw water (4.a) is pressurized by the intake (7) sucked by the motor pump (1) where it is energized by adding pressure, until reaching the necessary to operate the reverse osmosis process. After passing through the filters (5) and membranes (4), the rejection flow (4.b) is turbinated to pump the permeate flow (4.c) collected in the tank (3), through the turbo- pump (2) to the coast.
    Referring now to Figure 2.3, there is a schematic representation of a submarine desalination plant fed from the ground, with water previously raised, pumped or not by means of a motor pump (1) at a pressure that added to that obtained by submergence, allows the process to operate With lower energy cost. In this case, the permeate flow (4.c), collected in the tank (3) is driven to the coast by means of a turbo pump (2) taking advantage of the residual energy of the concentrate flow (4.b).
    In the three schematic representations of Figures 2.1 - 2.3, the underwater desalination plant provides or adds natural pressure to facilitate the reverse osmosis process.
    With reference to Figure 3, according to a profile view, the arrangement of the main elements of an underwater desalination plant according to the invention, arranged as a roof with two-sided eaves, is shown. On its cusp is the pitcher (3) on which the concentrate collectors (11) are fixed on both sides, forming the ridge. Crossing the concentrate manifolds (11) and communicating directly with the pitcher (3), the permeate ducts (12) that are self-bleeding through the pitcher (3) are located because they are inclined. Membrane holder tubes (13) are flanged to the collectors (11) housing the membranes (4), filters (5), adapters (14) and suction diffusers (15) through which raw water enters treat (4.a).
    With reference to Figure 4, a perspective of an underwater desalination plant is shown in which a chimney (16) can be seen, which by way of a flexible hose is held up by floating hoops (17) that assemble it, serving as an evacuation duct or suction separating both zones to avoid feedback between feed and concentrate flows.
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    The pitcher (3) located in the central part as a ridge has the concentrator manifolds (11) attached on both sides where the membrane carrier tubes (13) are flanged.
    The concentrate collectors (11) flow into two tubes (18) which, in the form of a loop, serve as a feed pipe to the pump (1) that energizes the flow of the concentrate (4.b) before being evacuated through the diffuser ( 19) towards the fireplace (16).
    Inside the tank (3) is located the motor pump (1) that drives the flow of the permeate (4.c) through pipes (20) weighed down to the coast. A vent (8) runs parallel to the supply pipes (20) to the coast causing the inside of the tank (3) to be at atmospheric pressure. Electric power supply cables run parallel to the pipes described above, supported by the openings that form the double half-shells (22) for joining and ballasting the pipes.
    The set rests on an enclosed structure (21), integrating into a single unit.
    In view of the aforementioned figures and in accordance with the numbering adopted, it can be seen that the representation of Figure 4 is an example of a preferred practical application of the invention, which integrated into a unit, comprises the parts and elements indicated and describe later.
    In the practical example considered, it is about designing an underwater desalination plant capable of supplying 132 m3 / h equivalent to 3168 m3 / day, with quality less than or equal to 320 ppm destined to be installed for the supply of the residential core of San Rosario- La Paz, Baja California, Mexico. Consulting the Navionics program, it can be seen that the coastal bathymetry indicates for that area various points with depths of 350 m at a distance of about 3 km from the coast. The equidistance of the contour lines assumes a uniform slope without special complications for the location of the transport pipes. Therefore we have a model of installation whose scheme corresponds to that of Figure 2.1.
    From the results obtained in the "summary explanation of the invention" section, with the membrane program www.nanoh2o.com it is observed that each tube (13) of 3 membranes (4) will permeate 1.65 m3 / h when fed (4.a) with 11 m3 / h at a pressure of 33.51 bar, pressure that is obtained by submerging the plant at a depth equal to or greater than 335 m since the plant is projected for a conversion rate of 15%.
    To achieve the 132 m3 / h of permeate (4.c), use 132/1, 65 = 80 tubes (13) with three membranes (4) inside, preceded by the installation of a filter (5) of 10 microns
    The feed flow (4.a) will be generated by the suction of the pump (1) placed in the concentrate pipeline (4. b), taking advantage of the principle of the communicating vessels. Suctioning 85% (concentrate flow 4.b), 100% will be aspirated (feed flow 4.a), overcoming the pressure losses of the three membranes (4) that represent 1.1 bar, plus the losses in tubes ( 13), filters (5), collectors (11) and chimney of evacuation (16) that suppose 0.12 bar, requiring a power for a performance of 80% of the pump of:
    image2
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    Therefore, this pump is capable of sucking a flow rate of:
    0.85 x 11 x 80 = 748 m3 / h = 0.2077 m3 / s
    overcoming a height of 11 + 1.2 = 12.2 m, driven by the shaft of a submerged electric motor of 2 poles at 50 Hz, which will rotate at 2950 rpm, and will have a specific speed given by the formula:
    image3
    specific speed corresponding to an axial flow pump with a four-blade propeller impeller, which according to: 1.5.3 pages 39 to 42 of the book ISBN978-3-8343-3293-6 Willi Bohl - Editorial Vogel, must have a propeller diameter Da = 0.2 m with bushing Di = 0.1 m causing an axial thrust (thrust) of 3,959 N in the stretching direction of the shaft.
    For its part, the permeate flow (4.c) of 1.65 x 80 = 132 m3 / h, will pass through the collectors (11) through the ducts (12) pouring into the interior of the pit (3) from where a motor pump (1) drives it through the pipes (20) of 3 km in length to the coast, overcoming the height due to the depth (335 m) plus the pressure losses in the pipes at a rate of 1 m / km, resulting a height to overcome of 335 + 3 = 338 m. Preferably, a 17-stage motor pump is used in series, model SP125-17 (Grundfos) with a yield of 80% and will need a power on its axis of:
    image4
    generating an axial thrust on the 22,000 N motor in the direction of compressing the shaft.
    Since the permeate pump (1) and the concentrate pump (1) rotate in solidarity with the same motor axis, and their respective thrust thrusts in the opposite direction, these will be compensated by reducing the load on the motor and resulting in a final axial thrust of 22,000 - 3,939 = 18,068 N.
    The axial thrust and the power absorbed by both pumps constitute a conditioner for the selection of the submerged electric motor, having chosen for this example practical application a Franklin motor of 12 ", 220 kW, two poles, capable of supporting an axial thrust of 60,000 N.
    As can be seen in Figure 2.1, the motor pump (1) of the permeate (4.c) that will absorb 83% of the total power and has a length of 4.5 m, is located inside the tank (3) . On the contrary, the propeller pump (1) that will absorb the remaining 17% of the power is located in the concentrate duct (4.b), separated by two partitions crossed by the shaft and sealed by double balanced seal. The flow of concentrate will be evacuated by the propeller pump (1) through the chimney (16) that will act as an emissary. The pitcher (3), with
    a diameter of 1.2 m and 7 m in length, displaces a volume of about 8 m3, which allows it to become a large float by dislodging the volume of water inside it through the non-return valve (6) located at its bottom, by the injection of compressed air through the vent (8), coming from outside.
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    The permeate (4.c) is supplied to the coast by two pipes (20) in parallel, joined by double half-shells (22), which in turn serve as cradles for the power and control cables and the vent (8 ). The pipes are, for example, made of PE-100 with a diameter of 225 mm, with a thickness of 13.4 mm of a 10-atmosphere ring where the permeate flow 10 (4. c) will run at a speed of 0.6 m / s, and that for a friction coefficient of 0.008 will generate a load loss of 1 m / km. The pipes are expected to flow into a casket at the foot of the coast from where the water will be pumped to the general water distribution network.
    15 Describing sufficiently the nature of the invention and its details of operation and implementation, it is not considered necessary to broaden its explanation so that any person skilled in the art understands its scope and the advantages derived therefrom, making to state that, within its essentiality, it may be implemented in other forms of realization to which the protection now sought will be achieved, provided that its fundamental principles are not altered or modified.
    权利要求:
    Claims (4)
    [1]
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    1. - Underwater desalination plant, specifically designed to obtain drinking water from seawater through a process of reverse osmosis through membranes, characterized by operating on the seabed and connected to the coast, taking advantage of the hydrostatic pressure generated by submerging, without requiring tapping or emissary works, integrated into a single construction unit, capable of emerging when pressurized air is injected from the outside, and the desalination plant is designed so that, when installed at depths sufficient to operating admits the entry of a feed flow (4.a) through the filter (5), so that when it is sucked through a pump (1) placed in a concentrate duct (4.b), it reaches a chimney (16 ) far from the outlet (7), so that the permeate flow (4.c) is collected in a pitcher (3), connected to the surface by a vent (8), from where it is driven by means of a motob omba (1) housed inside the pitcher (3), to be transported by means of pipes (20) or tankers to the coast, and where the two pumps (1) are driven simultaneously by a single engine.
    [2]
    2. - Underwater desalination plant according to claim 1, characterized in that when the desalination plant is installed at insufficient depths to operate, the pump (1) aspirates the feed flow (4.a) through the chimney (16), reversing the direction of the flow, and impelling it to a pressure such that added to the hydrostatic pressure, it is capable of operating the process, and the residual energy of the concentrate flow (4.b) being recovered by means of a turbo-pump (2) to boost the flow feed or permeate (4.c) by pipes (20) or tankers to the coast.
    [3]
    3. - Underwater desalination plant according to claim 1, characterized in that, applied to brackish and / or salty water desalination processes, driven by a height accumulator or motor pump (1) from the coast, the underwater desalination plant is capable of providing hydrostatic pressure to the flow of food (4.a), reducing energy consumption and serving as an emissary.
    [4]
    4. - Underwater desalination plant according to claim 1, characterized in that it adopts a two-slope roof-like configuration in which the membrane carrier tubes (13) are inclined to facilitate their bleeding, embedded on the collectors (11) attached to the pitcher (3), which as a ridge collects the permeate (4.c) from where it is pumped through pipes (20) or tanker to the coast, the chimney (16) being built as a flexible armed sleeve by floating hoops (17) that keep it upright, capable of serving as an evacuation or aspiration pipeline, separating both zones to avoid interference between feed (4.a) and concentrate (4.b) flows, resting all the set on an enclosed structure (21) that stabilizes the plant and from which split handles for its mooring.
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    同族专利:
    公开号 | 公开日
    ES2680904B1|2020-01-23|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    JPS5599379A|1979-01-24|1980-07-29|Riichi Fujii|Deep sea reverse osmotic pressure water making method|
    EP0709130A1|1994-10-12|1996-05-01|Toray Industries, Inc.|Apparatus and method for multistage reverse osmosis separation|
    ZA962680B|1995-04-07|1996-12-04|Vazquez Figueroa Rial|Plant to desalinate sea water by reverse osmosis by natural pressure and method to desalinate sea water by reverse osmosis by natural pressure|
    ES1070065U|2008-12-04|2009-06-08|Juan Reyes Florido|Unit of desalation and pumping of marine water |
    WO2016036125A1|2014-09-02|2016-03-10|현대건설주식회사|Hybrid cnt-ro membrane pressure vessel|
    WO2016180993A1|2015-05-12|2016-11-17|Tempero 2000 S L|Method and means for diluting or concentrating solutions, applied to processes for the desalination of water|ES2786876A1|2019-04-12|2020-10-13|M Torres Disenos Ind S A|SUBMARINE DESALINATION PLANT FOR DESALINATION OF MARINE WATER BY REVERSE OSMOSIS AND DISPOSAL PROCEDURE OF THE SUBMARINE DESALINATION PLANT ON THE SEA BOTTOM |
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