• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    High thermal conductance device for multi-effect water desalination systems with improved thermal conductance through a point-to-point management of the fluids that are supplied and extracted in the evaporation and condensation surfaces and the ordering of the flow of liquids through spaces of capillary dimensions in the evaporators and condensers. (Machine-translation by Google Translate, not legally binding)
    公开号:ES2554550A1
    申请号:ES201430740
    申请日:2014-05-20
    公开日:2015-12-21
    发明作者:Juan Eusebio NOMEN CALVET；Dan Alexandru HANGANU
    申请人:ALEX HANGANU RES S L；ALEX HANGANU RESEARCH SL；
    IPC主号:
    专利说明:

    DESCRIPTION
    High thermal conductance device for multi-effect water desalination systems. Object
    A multi-effect distillation device that achieves high thermal conductance. Understanding thermal conductance watts per unit area and Kelvin degree transferred to 5 through the layers of material and fluids that separate two effects .. State of the art
    Current thermal desalination systems use the multi-effect technique to improve their thermal efficiency, that is, the water vapor produced in one effect provides thermal energy for evaporation in the next effect that is maintained at a lower pressure and temperature. to those of the first effect. They are systems in which each effect is maintained under conditions of controlled pressure and in which the dynamic equilibrium between the vapor phase and the water phase is used.
    In a way, each effect could be visualized as a large open caloduct, whose working fluid is salt water that is supplied in the evaporator zone, the excess brine is extracted and in the condenser zone the distilled water is extracted . But there is a big difference in thermal efficiency between a hot water pipeline as a working fluid and an effect of current multi-effect distillation systems, be it MED, Multi-Effect Distillation, or MSF, Multi-Stage Flash.
    The thermal conductance resulting from the passage of energy through the wall of the tubes or the 20 panels that separates the effects, plus the passage through the sheets of water that cover these surfaces is between 1,000 and 2,000 W / m2 / ºC , while there are commercial caloducts that use water as a working liquid whose thermal conductance resulting from the thermal flow through the walls of the caloduct and the porous structures that capillary channel the return of the working liquid, known technically as “wicks”, is located 25 around 60,000 W / m2 / ºC, a thermal conductance between 30 and 60 times higher. The lower thermal conductance of the current effects implies the need to use large exchange surfaces and / or use large temperature jumps per effect.
    The surface of heat exchange between effects, either in the form of a tube or a panel, is made of alloys of high thermal conductivity similar to those used for the preparation of the external walls of the caloducts. The thickness of the walls of the tubes or of the panels of the effects is not 30 times greater than the thickness of the external wall of the caloducts. In fact, they may have similar thicknesses. Therefore, the difference between the conductances of 2,000 W / m2 / ºC of the effects and the 60,000 / m2 / ºC of the heat is not only a function of the thermal properties of the energy exchange surfaces that separate the effects.
    The essential factor that explains the great difference between the thermal efficiency of the heat and the effects of the current multi-effect distillation systems is the difference in their current logistics of the fluids on the evaporation and condensation surfaces. It is known that the thermal conductivity of the caloducts is highly dependent on the structure and materials of the internal porous structures "wick" of the caloduct. This "wick" structure allows a controlled flow of fluids on the evaporation and condensation surfaces. Its capillary structure allows to increase the contact areas between the heat transmitting surface and the fluid, minimizes the sheets of water, the effects of the boundary layer and allows to improve other physical factors of complex modeling but that result in an improvement of the thermal conductance of the device .. It is known that the resulting thermal conductance between a surface and a water flow depends on many factors such as the speed of transit, the texture, the surface, the shape of this surface, its wettability and others
    factors with very complex effects and difficult to model and whose better understanding allows the permanent evolution in new internal structures of the caloducts that allow to improve their conductances.
    The placement of porous structures similar to the internal "wick" of the caduducts on the evaporation and condensation areas of the multi-effect desalination devices and the correct contribution and extraction of fluids in these areas will allow increasing the conductance of the effects to similar levels to the current thermal conductances of the caloducts. Thus, the capacity of production of distilled water per unit of energy provided in the heat source of the desalination device would be considerably increased, since the thermal jump differential could be reduced by effect and the energy exchange surfaces improved.
    The internal "wick" structures of a pipeline do not incorporate a brine evacuation system from the evaporator zone since the working fluid does not leave salts after evaporation. In the case of porous “wick” structures located on evaporators, the logistics of brine extraction will be included. fifteen Summary
    The present invention increases the thermal conductance of the multi-effect distillation devices by improving the management of the fluids that are supplied and extracted on the evaporation and condensation surfaces; namely, an effect, and the ordering of the flow of liquids through spaces of capillary dimensions in the evaporators and condensers. twenty
    A distillation device comprises at least one condensing zone, which acts as a condenser of an effect, a "wick" capillary structure being arranged on the condensing zone, which channels the fluids, which are supplied and extracted on the condensation surfaces, by spaces of capillary dimensions to reduce the boundary layer and the accumulation of a layer of distilled water in the condensing zone of the effect. 25
    The distillation device also comprises at least one evaporator zone, which acts as an evaporator of the effect, a "wick" capillary structure being arranged on the evaporator zone, which channels the fluids, which are supplied and extracted on the evaporation surfaces, by capillary dimensions spaces to reduce the boundary layer and the accumulation of a salt or brine layer in the evaporating zone of the effect. 30
    The desalination device is a high efficiency MED, HE-MED, comprising at least one wall of high thermal conductivity with at least one heat pipe on the outside of the portion of which it acts as an evaporator a "wick" capillary structure is placed so that the condensation of an effect occurs in said capillary structure.
    The desalination device is a high efficiency MED, HE-MED, comprising at least one wall of high thermal conductivity with at least one heat pipe on the outside of the portion of which it acts as a condenser a "wick" capillary structure of so that the evaporation of the following effect takes place in said capillary structure.
    The desalination device comprising the wall of high thermal conductivity is assembled with a distilled water extractor for each "wick" capillary structure that acts as a condenser of an effect; a brine extractor unit of the different "wick" capillary structure that acts as an evaporator and a salt water supply unit that controls the controlled salt water supply to the different "wick" capillary structure.
    The desalination device is a high efficiency MED, HE-MED, in which at least one heat pipe is reduced to a sandwich formed, in turn, by the union of two capillary structures 45 "wick", so that one structure "wick" capillary acts as a condenser of one effect and the other "wick" capillary structure acts as an evaporator of the following effect, the surface being
    of union of the two capillary structures "wick" impermeable to the passage of water and water vapor between effects.
    The desalination device is a high efficiency MED, HE-MED, the sandwich comprising a distilled water extractor for each "wick" capillary structure that acts as an effect condenser; a brine extractor unit of the different "wick" capillary structure and a salt water supply unit that controls the controlled salt water supply to the different "wick" capillary structure. Brief description of the figures
    A more detailed explanation of the device according to the embodiments of the invention is given in the following description based on the attached figures in which:
    Figure 1 shows a diagram of a wall of high thermal conductivity of a multi-effect distillation device MED of high efficiency HE-MED with a pipe with outer wick capillary structures that act as a condenser of an effect and as an evaporator of the next and with a liquid flow logistics system integrated in the wall with high thermal conductivity and that allows distilled water and brine streams to be extracted point by point and that allows to provide salt water in a controlled and point to point manner.
    Figure 2 shows a diagram of a wall of high thermal conductivity of a HE-MED device in which at least one heat pipe is reduced to a sandwich of two "wick" capillary structures that act as an effect condenser and as an evaporator of the following effect and with a liquid flow logistics system integrated in the wall of high thermal conductivity that allows point-to-point distilled water and brine flows to be extracted and that allows to provide salt water in a controlled and point-to-point manner . Description of an embodiment
    A portion of a high conductivity wall of a high efficiency MED device, HE-MED, is illustrated in Figure 1, in which the wall of high thermal conductivity (1) with at least one heat pipe (2) includes a capillary structure "wick" (4) on the outside of the portion of the pipeline that acts as an evaporator (6). This structure (4) has a structure similar to those used as internal capillary structures "wick" (3) of the caloducts.
    The water vapor (5) of an effect is captured and condensed on this capillary structure (4). The capillary structure (4) channels the fluids through spaces with capillary dimensions and will have a thermal efficiency similar to that achieved by the internal "wick" capillary structure (3) of the caloduct in its condensation zone (8). The distilled water resulting from the condensation within the structure (4) is channeled through the capillary structure to an extraction point (7) so that the logistics of the distilled water that is evacuated through internal canalizations of the wall is optimized instead of flow over the following condensation areas. 35
    A "wick" capillary structure (13) on the outside of the portion of the heat pipe that acts as a condenser (8). This structure (13) has a structure similar to those used as internal "wick" capillary structures (3) of the caloducts in their evaporation zone (6). Salt water (9) is provided on this structure (13), which is distributed neatly by the "wick" capillary structure (13) so that the thermal conductance is increased by reduction 40 of the boundary layer effects and the insulating effects of the water sheets, as is the case with the "wick" capillary structure in the internal evaporator (6) of the pipeline. Saltwater is supplied on the “wick” capillary structure (13) of each caloduct from a point of contribution (9) from conduits that circulate inside the wall, and the remaining brine is channeled through the capillary structure to a point extraction (12) that is evacuated by internal conduits 45 of the wall. In this way, salt water only flows through the exact evaporation point and within capillary structures.
    Inside the wall of high thermal conductivity PACT is added a system of intelligent logistics of contribution and extraction of liquids. This system provides salt water (9) on the outer capillary structure (13) of the heat pipe that acts as an evaporator of an effect, the contribution is made following a controlled flow according to the rate of evaporation (11) so that the salinity Brine does not exceed the desired level according to the operating conditions of the desalination plant and is extracted in a controlled manner (12). This system also extracts all distilled water (7) generated in each capillary structure (4). This extraction is channeled through ducts that circulate inside the PACT wall.
    A section of a high conductivity wall of a high efficiency MED device, HE-MED, in which at least one caloduct of the high thermal conductivity wall 10 is replaced by a sandwich created by joining is illustrated in FIG. or fusion (14) of two "wick" capillary structures. So one of these capillary structures "wick" (15) acts as a condenser of an effect and the other capillary structure "wick (16) acts as an evaporator of the next effect. The fluid logistics system described for Figure 1 can be applied to these capillary structures, with the salt water supply in the capillary structure (16) 15 acting as an evaporator and its subsequent brine extraction, as well as water extraction distilled from the "wick" capillary structure (15) that acts as a condenser. The integration of the two capillary structures (15) and (16) is carried out in such a way that at their point of attachment (14) the capillary spaces are eliminated, forming a continuous impermeable surface through which a liquid water molecule cannot pass or of water vapor. This junction point (14) does not require the shape of a wall with a certain thickness to withstand structural forces. Capillary structures can provide the necessary forces for the support of the sandwich and for the support of tensions due to pressure differences between effects. The internal structure of the PACT also provides the structural forces necessary to support each of these sandwiches between the two effects. 25
    For the optimization of fluid logistics in the evaporators and condensers of a distillation device using the multi-effect system, the following advances can be made:
    - First, the flow of the liquids in the evaporation and condensation zone of the desalination device is ordered by placing porous structures similar to the internal porous structures "wick" of the caloducts, so that the fluids are ordered in capillary dimensions spaces. Which allows to increase the heat transfer surface, allows to optimize the boundary layer of liquids, allows to reduce the sheets of water and other factors that allow to improve the resulting thermal conductance in the areas of evaporation and condensation of the effects of a device desalination 35 multi-effect.
    - Secondly, if the desalination device is a high efficiency MED, HE-MED, we will have a wall of high thermal conductivity (1) with at least one heat pipe (2), on which we can place a “wick” structure external to the evaporator of the heat pipe (4). This external structure will channel the water vapor through its pores allowing an efficient condensation in the effect and the channeling of the distilled water to a point of extraction of the distilled water (7), so that this water does not hinder the thermal transfer of other dew points of the separation wall between effects. We can also place a “wick” structure (13) on the external part of the condenser of the heat pipe. This external structure will channel the salt water from the evaporator of the effect, previously filtered so that it does not contain particles with a diameter greater than the capillary, which is provided in a controlled way from inside the wall (9). The capillary structure will order the salt water flow so that the boundary layers are reduced and the phase change to steam is facilitated (11). The remaining brine is removed in an orderly manner (12) from each effect evaporator through internal ducts of the separation wall. fifty
    - Thirdly, we can improve the thermal conductance of a HE-MED by reducing the figure of the pipeline to a sandwich of wick capillary structures (14) so that the contribution and liquid extraction components are maintained but only what would be equivalent is maintained. to a wall of the caloduct and a wick capillary structure (15) that acts as a condenser of an effect and the wick capillary structure (16) that instead of acting as an internal evaporator of the caloduct, acts as an evaporator of the following effect.
    The sandwich (14) of two capillary structures "wicks" represents a remarkable improvement in HE-MED devices that allows eliminating one of the faces of the heat transfer in the heat flow, which provides a simplification of the construction of the High thermal conductivity walls of the HE-MED and prevents the gain of entropy that involves a cycle of evaporation and condensation through a wall of heat pipe and its wick capillary structures.
    The sandwich (14) of two "wicks" capillary structures also makes it possible to apply all current knowledge of interior wicks of caduducts on the evaporation surface and on the condensation surface of the effects of a distillation device using the multi-effect system. This allows reducing the problems of the boundary layer and unnecessary thicknesses of liquid sheets on current evaporators and condensers.
    The logistics of liquids with a contribution and extraction of point-to-point liquids eliminates transits in areas of evaporation or condensation of liquids that may be necessary or resulting from previous or subsequent areas, but that are not necessary liquid flows 20 for a given evaporation or condensation zone. This allows to reduce unnecessary thicknesses of salt water circulating on the evaporators and unnecessary thicknesses of distilled water circulating on the condensers.
    Sandwiches (14) of "wick" structures can be made by fusing or joining two structures (15) (16) that adopt any of the known formats of interior capillary structures of caloducts such as so-called "wrap screen" screen wrappings; sintered metal, axial grooves, open annulus open rings, open artery open artery, integral artery integrated arteries or composite structures such as those known as composite composite screen, grooves covered by screen or sintered metal, composite slab ”, spiral artery, monoranura or double wall artery. 30
    The union or fusion of the two capillary structures is carried out in such a way that on their joint surface (14), the capillary spaces are eliminated, forming a continuous impermeable surface through which a water or water vapor molecule cannot pass.
    The internal "wick" structures of a pipeline can incorporate a composite structure that includes grooves or ducts called arteries through which the working liquid 35 flows more easily following the direction marked by the capillary tension. The “wick” structure placed on the evaporation surface of a desalination device must manage the evacuation of the brine, a problem that does not occur in the internal structures of the caloducts since in them the working fluid does not leave salts when evaporating . The "wick" structure placed on an evaporator of a desalination effect may incorporate a network of arteries through which salt water flows by gravity or by pressure to a network of arteries through which salt water flows by capillarity to a structure sintered or porous in which evaporation takes place. The resulting brine can be extracted through a network of "veins" in which the brine circulates by capillarity, by pressure difference or by gravity to an evacuation point. The "wick" structure 45 placed on a condenser of a desalination effect can incorporate a network of "veins" in which the distilled water circulates by capillarity, by pressure difference or by gravity to an evacuation point
    权利要求:
    Claims (8)
    [1]
    1. A multi-effect distillation device; characterized in that the distillation device comprises at least one condensing zone, which acts as a condenser of an effect, a "wick" capillary structure being arranged on the condensing zone, which channels the fluids, the water vapor that arrives and the distilled water that is generates, by spaces of 5 capillary dimensions to increase the heat transfer surface, optimize the boundary layer of liquids, reduce the sheets of water and other factors that improve the resulting thermal conductance.
    [2]
    2. Device according to claim 1; characterized in that the distillation device comprises at least one evaporating zone, which acts as an evaporator of an effect, with a "wick" capillary structure being arranged on the evaporating zone that channels the salt water supply, brine that is evacuated, and the steam of released water, by spaces of capillary dimensions to increase the heat transfer surface, optimize the boundary layer of liquids, reduce the sheets of water and other factors that allow to improve the resulting thermal conductance. fifteen
    [3]
    3. Device according to claim 2; characterized in that the desalination device is a high efficiency MED, HE-MED, comprising at least one heat pipe of a wall of high thermal conductivity, on the outer faces of which a "wick" capillary structure (4) is arranged on the area that acts as a condenser of an effect and a "wick" capillary structure (13) on the area that acts as an evaporator of the following effect, 20 to increase the heat transfer surface, optimize the boundary layer of liquids, reduce the sheets of water and other factors that improve the resulting thermal conductance.
    [4]
    4. Device according to claim 3; characterized in that a distilled water extractor (7) is assembled on the wall of high thermal conductivity for each "wick" capillary structure (4) that acts as a condenser of an effect; a brine extractor unit (12) of the different "wick" capillary structure (13) that acts as an evaporator and a salt water supply unit (9) that controls the supply of salt water to the different "wick" capillary structure (13 ).
    [5]
    5. Device according to claim 3; characterized in that at least one heat tube is reduced to a sandwich formed by the union or fusion (14) of two "wick" capillary structures, so that a "wick" capillary structure (15) acts as a condenser of an effect and the other "wick" capillary structure (16) acts as an evaporator of the following effect and so that the joint surface (14) of the two structures (15) (16) is impervious to the passage of water and water vapor between effects . 35
    [6]
    6. Device according to claim 5; characterized in that in the sandwich (14) a distilled water extractor is assembled for each "wick" capillary structure (15) that acts as an effect condenser; a brine extractor unit of the different "wick" capillary structure (16) that acts as an effect evaporator and a salt water supply unit that controls the supply of salt water to the different "wick" capillary structure 40 (16).
    [7]
    Device according to claim 1, 2, 3 or 5, characterized in that the wick capillary structure of the evaporator of a desalination effect incorporates an internal network of arteries through which the salt water flows by gravity or by pressure to a network of arteries through which salt water flows by capillarity to a sintered or porous structure in which evaporation takes place; and the brine resulting from evaporation is evacuated by a network of veins in which the brine circulates by capillarity, by pressure difference or by gravity to an evacuation point.
    [8]
    Device according to claim 1, 2, 3, 5 or 7, characterized in that the wick capillary structure of the condenser of a desalination effect incorporates a network of veins through which the distilled water circulates by capillarity, by pressure difference or by gravity to an evacuation point.
    类似技术:
    公开号 | 公开日 | 专利标题
    US4279294A|1981-07-21|Heat pipe bag system
    US20030136555A1|2003-07-24|Heat pipe loop with pump assistance
    US10648678B2|2020-05-12|Building-integrated solar energy system
    JP6587618B2|2019-10-09|Evaporation and absorption equipment
    US4339929A|1982-07-20|Heat pipe bag system
    NO343058B1|2018-10-22|Intermediate Fluid Type Vaporizer
    ES2554550B1|2016-09-28|High thermal conductance device for multi-effect water desalination systems
    US9052126B2|2015-06-09|Heat exchange circulatory system
    WO2016123996A1|2016-08-11|Sintered heat pipe and semiconductor cooling refrigerator having same
    WO2015107250A1|2015-07-23|Highly thermally conductive device for multiple-effect water-desalination systems
    JP2019032146A|2019-02-28|Joint assembly of vapor chambers
    NO20180844A1|2018-06-18|Intermediate Fluid Type Vaporizer
    JP2006010141A|2006-01-12|Double tube type heat pipe
    JP2005337336A|2005-12-08|Liquefied gas evaporating device
    US20130098582A1|2013-04-25|Method using heat pipes with multiple evaporator/condenser zones and heat exchangers using same
    JP2019132583A|2019-08-08|Heat exchanger
    ES2742869T3|2020-02-17|Heat exchanger with at least three fluids of improved efficiency
    TWM423819U|2012-03-01|Heat-pipe type heat exchanger structure
    JP2856246B2|1999-02-10|Heat recovery / supply device
    WO2019110861A1|2019-06-13|Arrangement for a latent-heat exchanger chamber
    US4745963A|1988-05-24|Heat exchanger and systems and methods for using the same
    Stefano et al.2021|Setting up of a cost-effective continuous desalination plant based on coupling solar and geothermal energy
    CN104654655B|2016-11-23|Sintered heat pipe and there is its semiconductor freezer
    US8261563B2|2012-09-11|External refrigerator condensing unit
    JP2006275423A|2006-10-12|Heat exchange system
    同族专利:
    公开号 | 公开日
    ES2554550B1|2016-09-28|
    ES2548106B1|2016-07-26|
    WO2015107251A1|2015-07-23|
    ES2473190B1|2015-06-11|
    ES2473190A1|2014-07-03|
    ES2548106A1|2015-10-13|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US6423187B1|1998-12-11|2002-07-23|Ovation Products Corporation|Heat exchanger mechanism using capillary wipers for a thin film distiller|
    WO2006002636A1|2004-07-06|2006-01-12|Idekontoret Aps|A layer and a module for a multiple effect distillation system|
    US20060260786A1|2005-05-23|2006-11-23|Faffe Limited|Composite wick structure of heat pipe|
    KR20120067028A|2010-12-15|2012-06-25|한국기계연구원|Ambient pressure type multi-effect distiller using solar thermal energy and waste heat|
    KR20130141841A|2012-06-18|2013-12-27|한국기계연구원|Multi effect distiller with transparent plate using solar thermal energy|
    US20140042009A1|2012-08-12|2014-02-13|Bin-Juine Huang|Muliti-effect distillation device|
    GB2417435A|2004-08-27|2006-03-01|O H D L Optimized Hybrid Desal|MSF desalination system|
    CN201367361Y|2009-03-13|2009-12-23|国家海洋局天津海水淡化与综合利用研究所|Integrated cabinet-type low-temperature multiple-effect distilled seawater desalting plant|CN107001088A|2014-12-03|2017-08-01|西尔万资源公司|The Water warfare of energy-conservation and desalination|
    法律状态:
    2016-09-28| FG2A| Definitive protection|Ref document number: 2554550 Country of ref document: ES Kind code of ref document: B1 Effective date: 20160928 |
    优先权:
    申请号 | 申请日 | 专利标题
    ESP201430054|2014-01-20|
    ES201430054A|ES2473190B1|2014-01-20|2014-01-20|Multi-Effect Distillation Device|
    ES201430329A|ES2548106B1|2014-01-20|2014-03-11|A high efficiency MED multi-effect distillation device HE-MED|
    ESP201430329|2014-03-11|PCT/ES2015/070032| WO2015107250A1|2014-01-20|2015-01-20|Highly thermally conductive device for multiple-effect water-desalination systems|
    [返回顶部]