CN108314121B - Brackish water desalination device and brackish water desalination method - Google Patents

Brackish water desalination device and brackish water desalination method Download PDF

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CN108314121B
CN108314121B CN201810346527.8A CN201810346527A CN108314121B CN 108314121 B CN108314121 B CN 108314121B CN 201810346527 A CN201810346527 A CN 201810346527A CN 108314121 B CN108314121 B CN 108314121B
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谭垚
韩德梁
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Beautiful Land Beijing Ecological Environment Engineering Technology Research Institute Co ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/14Treatment of water, waste water, or sewage by heating by distillation or evaporation using solar energy
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/043Details
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/04Flow arrangements
    • C02F2301/046Recirculation with an external loop
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/138Water desalination using renewable energy
    • Y02A20/142Solar thermal; Photovoltaics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/208Off-grid powered water treatment
    • Y02A20/212Solar-powered wastewater sewage treatment, e.g. spray evaporation

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Abstract

本发明涉及苦咸水淡化技术领域,尤其是涉及一种苦咸水淡化装置及苦咸水淡化方法。该苦咸水淡化装置包括内循环结构和外循环结构,内循环结构和外循环结构形成双层结构;内循环结构形成用于淡化苦咸水的第一水循环网络,外循环结构形成用于淡化苦咸水第二水循环网络;内循环结构包括有太阳能集热器,用于白天收集热量并蓄存于第一水循环网络;苦咸水在第一水循环网络流通过程中通过蒸发冷凝形成淡化水并将热量传递到第二水循环网络实现热量积蓄;待到夜晚,第二水循环网络凝结形成淡化水。该苦咸水淡化装置夜晚利用白天积蓄的热量实现昼夜连续的苦咸水蒸馏,成倍提高淡化效率;并且利用自然冷热源,节省成本。

Figure 201810346527

The invention relates to the field of brackish water desalination technology, in particular to a brackish water desalination device and a brackish water desalination method. The brackish water desalination device includes an inner circulation structure and an outer circulation structure, the inner circulation structure and the outer circulation structure form a double-layer structure; the inner circulation structure forms the first water circulation network for desalination of the brackish water, and the outer circulation structure forms the first water circulation network for desalination The second water circulation network of brackish water; the internal circulation structure includes a solar collector, which is used to collect heat during the day and store it in the first water circulation network; the brackish water forms desalinated water through evaporation and condensation during the circulation of the first water circulation network. The heat is transferred to the second water circulation network to realize heat storage; at night, the second water circulation network condenses to form desalinated water. The brackish water desalination device uses the heat accumulated during the day to realize diurnal continuous brackish water distillation at night, which doubles the desalination efficiency; and uses natural cold and heat sources to save costs.

Figure 201810346527

Description

苦咸水淡化装置及苦咸水淡化方法Brackish water desalination device and brackish water desalination method

技术领域technical field

本发明涉及苦咸水淡化技术领域,尤其是涉及一种苦咸水淡化装置及苦咸水淡化方法。The invention relates to the field of brackish water desalination technology, in particular to a brackish water desalination device and a brackish water desalination method.

背景技术Background technique

世界上第一个大型的太阳能海水淡化装置是由瑞典工程师Wilson于1872年建造于智利北部的顶棚式太阳能蒸馏装置,总集热面积4700m2,晴天每天可生产淡水23t,其结构简单,类似于一个温室,但占地面积大,日产水率一般为2~4kg/m2,热效率只能达到35%~45%。太阳能蒸馏器在传统的顶棚式(池式)之后又出现了倾斜幕芯式、倾斜盘式、充气式、吸液芯式等多种形式。在这些基本形式的基础上,为了提高热利用效率,又逐渐由单级结构发展到多级结构。目前,人们研究得最多、技术上最为成熟的仍是盘式太阳能蒸馏器,这种装置因结构简单和取材方便而易于推广应用。然而,盘式太阳能蒸馏器具有效率不高的严重缺陷,一般而言,它的年产率仅为1000kg/m2左右,不能满足用户的要求。理论和实践均已证明,如果在系统运行过程中,水蒸气的冷凝潜热能被重复利用,蒸发过程所需的热能将被显著降低。在多效蒸馏系统中可实现上述要求,其主要优点在于成功地将水蒸气的凝结潜热和热盐水的显热再循环加以利用,用之预热进入的海水。但是,它们的结构通常都很复杂,运行成本及固定资本的投入相对较高。The world's first large-scale solar desalination device was built by Swedish engineer Wilson in 1872. It is a roof-type solar distillation device in northern Chile. The total heat collection area is 4700m 2 , and it can produce 23t of fresh water per day in sunny days. Its structure is simple, similar to A greenhouse, but covers a large area, the daily water production rate is generally 2-4kg/m 2 , and the thermal efficiency can only reach 35%-45%. After the traditional ceiling type (pool type), solar stills have appeared in various forms such as inclined curtain core type, inclined plate type, inflatable type, and liquid-absorbing core type. On the basis of these basic forms, in order to improve the heat utilization efficiency, it has gradually developed from a single-level structure to a multi-level structure. At present, the most researched and the most mature technology is still the disc solar still, which is easy to popularize and apply because of its simple structure and convenient materials. However, the disc-type solar distiller has a serious defect of low efficiency. Generally speaking, its annual production rate is only about 1000kg/m 2 , which cannot meet the requirements of users. Both theory and practice have proved that if the latent heat of condensation of water vapor is reused during the operation of the system, the heat energy required for the evaporation process will be significantly reduced. The above requirements can be achieved in a multiple effect distillation system, the main advantage of which is the successful use of the latent heat of condensation of water vapor and the sensible heat of hot brine to recycle to preheat the incoming seawater. However, their structures are usually complex, and the operating costs and fixed capital investment are relatively high.

可见,现有技术中的太阳能蒸馏海水或苦咸水的淡化装置只能白天蒸馏收集淡化水,产能低且成本高。It can be seen that the solar-powered desalination devices for distilling seawater or brackish water in the prior art can only distill and collect desalinated water during the day, which has low production capacity and high cost.

公开于该背景技术部分的信息仅仅旨在加深对本发明的总体背景技术的理解,而不应当被视为承认或以任何形式暗示该信息构成已为本领域技术人员所公知的现有技术。The information disclosed in this background section is only intended to enhance the understanding of the general background of the present invention, and should not be considered as an acknowledgment or any form of suggestion that the information constitutes the prior art that is already known to those skilled in the art.

发明内容Contents of the invention

本发明的目的在于提供一种苦咸水淡化装置及苦咸水淡化方法,缓解了现有技术中的太阳能蒸馏海水或苦咸水的淡化装置产能低且成本高的技术问题。The object of the present invention is to provide a brackish water desalination device and a brackish water desalination method, which alleviates the technical problems of low production capacity and high cost of solar distilled seawater or brackish water desalination devices in the prior art.

本发明提供的一种苦咸水淡化装置,包括:内循环结构和外循环结构,所述内循环结构和所述外循环结构形成双层结构;A brackish water desalination device provided by the present invention comprises: an inner circulation structure and an outer circulation structure, wherein the inner circulation structure and the outer circulation structure form a double-layer structure;

所述内循环结构形成用于淡化苦咸水的第一水循环网络,所述外循环结构形成用于淡化苦咸水第二水循环网络;The inner circulation structure forms a first water circulation network for desalination of brackish water, and the outer circulation structure forms a second water circulation network for desalination of brackish water;

所述内循环结构包括有太阳能集热器,用于白天收集热量并蓄存于所述第一水循环网络;苦咸水在所述第一水循环网络流通过程中通过蒸发冷凝形成淡化水并将热量传递到所述第二水循环网络,使得所述第二水循环网络得到热量并蓄存;待到夜晚,所述第一水循环网络和所述第二水循环网络积蓄的热量释放,使得苦咸水在所述第二水循环网络流通过程中冷凝形成淡化水。The internal circulation structure includes a solar collector, which is used to collect heat during the day and store it in the first water circulation network; the brackish water forms desalinated water through evaporation and condensation during the circulation of the first water circulation network and transfers heat transfer to the second water circulation network, so that the second water circulation network gets heat and stores it; at night, the heat stored in the first water circulation network and the second water circulation network is released, so that the brackish water Desalinated water is condensed during circulation in the second water circulation network.

作为一种进一步的技术方案,所述内循环结构包括内层蓄热水池、内层顶盖;所述内层顶盖罩设于所述内层蓄热水池上;所述太阳能集热器的进水口与所述内层蓄热水池连通,出水口穿过所述内层顶盖的顶部连通,以使苦咸水回到所述内层蓄热水池;As a further technical solution, the internal circulation structure includes an inner heat storage pool and an inner roof; the inner roof cover is arranged on the inner heat storage pool; the solar heat collector The water inlet communicates with the inner heat storage pool, and the water outlet communicates through the top of the inner roof so that the brackish water returns to the inner heat storage pool;

所述外循环结构包括外层蓄热水池、外层顶盖;所述外层顶盖罩设于所述外层蓄热水池上;所述外层蓄热水池与所述外层顶盖的顶部连通,以使所述外层蓄热水池中的苦咸水进入所述外层顶盖与所述内层顶盖之间并沿所述内层顶盖的外表面回到所述外层蓄热水池。The outer circulation structure includes an outer heat storage pool and an outer top cover; the outer top cover is set on the outer heat storage pool; the outer heat storage pool and the outer top cover The top is connected, so that the brackish water in the outer layer heat storage tank enters between the outer layer roof and the inner layer roof and returns to the outer layer along the outer surface of the inner layer roof Thermal storage pool.

作为一种进一步的技术方案,所述内层顶盖的内侧设置有第一集水槽,用于收集所述第一水循环网络中的淡化水;As a further technical solution, the inner side of the inner roof is provided with a first water collection tank for collecting the desalinated water in the first water circulation network;

所述外层顶盖的内侧设置有第二集水槽,用于收集所述第二水循环网络中的淡化水。The inner side of the outer top cover is provided with a second water collection tank for collecting the desalinated water in the second water circulation network.

作为一种进一步的技术方案,所述内循环结构还包括设置于所述内层顶盖顶部的布水喷头,所述布水喷头与所述太阳能集热器的出水口相连通,用于将苦咸水喷洒落入所述内层蓄热水池。As a further technical solution, the internal circulation structure also includes a water distribution nozzle arranged on the top of the inner roof, and the water distribution nozzle communicates with the water outlet of the solar heat collector for The brackish water spray falls into the inner water storage tank.

作为一种进一步的技术方案,所述内层蓄热水池通过第一管道与所述太阳能集热器的进水口相连通,所述第一管道上设置有第一循环泵。As a further technical solution, the inner heat storage pool is connected to the water inlet of the solar heat collector through a first pipeline, and a first circulating pump is arranged on the first pipeline.

作为一种进一步的技术方案,所述外循环结构还包括设置于所述外层顶盖顶部的布水槽,所述布水槽与所述外层蓄热水池连通,用于将苦咸水导入所述外层顶盖与所述内层顶盖之间并沿所述内层顶盖的外表面回到所述外层蓄热水池。As a further technical solution, the outer circulation structure also includes a water distribution tank arranged on the top of the outer layer top cover, the water distribution tank communicates with the outer heat storage pool, and is used to introduce brackish water into the between the outer roof and the inner roof and along the outer surface of the inner roof back to the outer heat storage pool.

作为一种进一步的技术方案,所述外层蓄热水池通过第二管道与所述布水槽相连通,所述第二管道上设置有第二循环泵。As a further technical solution, the outer heat storage pool is connected to the water distribution tank through a second pipeline, and a second circulating pump is arranged on the second pipeline.

作为一种进一步的技术方案,所述外层蓄热水池连通有导入苦咸水的补水管道,且所述补水管道用于连接所述外层蓄热水池的端口设置有第二浮球阀;所述外层蓄热水池与所述内层蓄热水池连通,且二者连通处设置有第一浮球阀。As a further technical solution, the outer heat storage pool is connected with a replenishment pipe for introducing brackish water, and the port of the water replenishment pipe for connecting the outer heat storage pool is provided with a second float valve; The outer heat storage pool is in communication with the inner heat storage pool, and a first float valve is arranged at the connection between the two.

作为一种进一步的技术方案,所述外层蓄热水池与所述内层蓄热水池均采用地埋式设置。As a further technical solution, both the outer heat storage pool and the inner heat storage pool are buried underground.

本发明还提供一种苦咸水淡化方法,采用如上述技术方案提供的任一种所述的苦咸水淡化装置收集淡化水,包括以下步骤:The present invention also provides a brackish water desalination method, using the brackish water desalination device described in any one of the above technical solutions to collect desalinated water, including the following steps:

白昼循环淡化:所述内循环结构中的所述太阳能集热器收集太阳能,通过苦咸水在所述第一水循环网络中循环将热量蓄存于所述第一水循环网络中;苦咸水在所述第一水循环网络中循环时蒸发凝结形成淡化水,并释放汽化潜热,被所述第二水循环网络中的苦咸水吸收;所述第二水循环网络中的苦咸水通过循环将热量蓄存于所述第一水循环网络中;Diurnal cycle desalination: the solar heat collector in the internal circulation structure collects solar energy, and heat is stored in the first water circulation network by circulating the brackish water in the first water circulation network; the brackish water circulates in the first water circulation network; When circulating in the first water circulation network, evaporation and condensation form desalinated water, and release latent heat of vaporization, which is absorbed by the brackish water in the second water circulation network; the brackish water in the second water circulation network stores heat through circulation stored in said first water circulation network;

夜晚循环淡化:所述第一水循环网络和所述第二水循环网络积蓄的热量释放,使得所述第二水循环网络中循环的苦咸水冷凝形成淡化水。Circulating desalination at night: the heat stored in the first water circulation network and the second water circulation network is released, so that the brackish water circulating in the second water circulation network condenses to form desalinated water.

与现有技术相比,本发明所提供的苦咸水淡化装置及苦咸水淡化方法能够达到以下有益效果:Compared with the prior art, the brackish water desalination device and the brackish water desalination method provided by the present invention can achieve the following beneficial effects:

本发明提供一种苦咸水淡化装置,包括内循环结构和外循环结构,内循环结构和外循环结构形成双层结构;内循环结构形成用于淡化苦咸水的第一水循环网络,外循环结构形成用于淡化苦咸水第二水循环网络;内循环结构包括有太阳能集热器,用于白天收集热量并蓄存于第一水循环网络;苦咸水在第一水循环网络流通过程中通过蒸发冷凝形成淡化水并将热量传递到第二水循环网络,使得第二水循环网络得到热量并蓄存;待到夜晚,第一水循环网络和第二水循环网络积蓄的热量释放,使得苦咸水在第二水循环网络流通过程中冷凝形成淡化水。The invention provides a brackish water desalination device, which includes an inner circulation structure and an outer circulation structure, the inner circulation structure and the outer circulation structure form a double-layer structure; the inner circulation structure forms a first water circulation network for desalinating brackish water, and the outer circulation structure The structure forms the second water circulation network for desalinating the brackish water; the inner circulation structure includes a solar collector for collecting heat during the day and storing it in the first water circulation network; the brackish water passes through evaporation during the circulation of the first water circulation network Condensation forms desalinated water and transfers heat to the second water circulation network, so that the second water circulation network can obtain heat and store it; at night, the heat stored in the first water circulation network and the second water circulation network is released, making the brackish water in the second water circulation network Condensation forms desalinated water during the circulation of the water circulation network.

白天,苦咸水在内循环结构循环流通时,太阳能集热器收集热量不断提高苦咸水的温度,使得第一水循环网络循环中的苦咸水不断积蓄热量,同时,升温的苦咸水蒸发冷凝形成淡化水。在此过程中,冷凝过程释放的热量被第二水循环网络中的苦咸水收集,并随着苦咸水在第二水循环网络中的流通不断积蓄于第二水循环网络中。待到夜晚,第二水循环网络中的苦咸水在循环过程中随着温度降低不断冷凝形成淡化水。During the day, when the brackish water circulates in the internal circulation structure, the solar collector collects heat to continuously increase the temperature of the brackish water, so that the brackish water in the first water circulation network continuously accumulates heat, and at the same time, the heated brackish water evaporates Condensation forms desalinated water. During this process, the heat released during the condensation process is collected by the brackish water in the second water circulation network, and is continuously accumulated in the second water circulation network along with the circulation of the brackish water in the second water circulation network. At night, the brackish water in the second water circulation network condenses continuously as the temperature drops during the circulation process to form desalinated water.

可以看出,本发明提供的苦咸水淡化装置,利用自然的冷热源,采用两层水循环网络,内层直接利用太阳能蓄热,外层利用蒸发产生汽化潜热的二次热量蓄热,实现了热量的回收,夜晚利用白天积蓄的热量实现昼夜连续的苦咸水蒸馏,成倍提高淡化效率;并且利用自然冷热源,节省成本。It can be seen that the brackish water desalination device provided by the present invention utilizes natural cold and heat sources and adopts a two-layer water circulation network. The inner layer directly uses solar energy to store heat, and the outer layer uses evaporation to generate secondary heat heat storage of latent heat of vaporization to achieve With the recovery of heat, the heat accumulated during the day is used at night to realize continuous distilling of brackish water day and night, which doubles the desalination efficiency; and the use of natural cold and heat sources saves costs.

本发明提供的苦咸水淡化方法采用上述苦咸水淡化装置进行昼夜蒸馏淡化水,产能高且成本低廉。The brackish water desalination method provided by the present invention adopts the above-mentioned brackish water desalination device to distill desalinated water day and night, and has high production capacity and low cost.

本发明的其他特征和优点将在随后的说明书中阐述,并且,部分地从说明书中变得显而易见,或者通过实施本发明而了解。本发明的目的和其他优点在说明书、权利要求书以及附图中所特别指出的结构来实现和获得。Additional features and advantages of the invention will be set forth in the description which follows, and in part will be apparent from the description, or may be learned by practice of the invention. The objectives and other advantages of the invention will be realized and attained by the structure particularly pointed out in the written description and claims hereof as well as the appended drawings.

附图说明Description of drawings

为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the specific embodiments of the present invention or the technical solutions in the prior art, the following will briefly introduce the drawings that need to be used in the description of the specific embodiments or the prior art. Obviously, the accompanying drawings in the following description The drawings show some implementations of the present invention, and those skilled in the art can also obtain other drawings based on these drawings without creative work.

图1为本发明实施例提供的一种苦咸水淡化装置的结构示意图。Fig. 1 is a schematic structural diagram of a brackish water desalination device provided by an embodiment of the present invention.

图标:11-内层蓄热水池;12-内层顶盖;13-第一集水槽;14-布水喷头;15-太阳能集热器;16-第一管道;17-第一循环泵;18-第一浮球阀;19-检修门;21-外层蓄热水池;22-外层顶盖;23-第二集水槽;24-布水槽;25-第二管道;26-第二循环泵;27-第二浮球阀;28-水池盖板;3-补水管道。Icons: 11 - inner heat storage pool; 12 - inner roof; 13 - first water collection tank; 14 - water distribution nozzle; 15 - solar collector; 16 - first pipeline; 17 - first circulation pump; 18 - first float valve; 19 - inspection door; 21 - outer heat storage pool; 22 - outer top cover; 23 - second water collection tank; 24 - water distribution tank; 25 - second pipeline; 26 - second circulation Pump; 27-the second float valve; 28-cover plate of the pool; 3-water supply pipeline.

具体实施方式Detailed ways

下面将结合附图对本发明的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions of the present invention will be clearly and completely described below in conjunction with the accompanying drawings. Apparently, the described embodiments are part of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

在本发明的描述中,需要说明的是,术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。此外,术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer" etc. The indicated orientation or positional relationship is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, or in a specific orientation. construction and operation, therefore, should not be construed as limiting the invention. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and should not be construed as indicating or implying relative importance.

在本发明的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, it should be noted that unless otherwise specified and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection or a detachable connection. Connected, or integrally connected; it can be mechanically connected or electrically connected; it can be directly connected or indirectly connected through an intermediary, and it can be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present invention in specific situations.

以下结合附图对本发明的具体实施方式进行详细说明。应当理解的是,此处所描述的具体实施方式仅用于说明和解释本发明,并不用于限制本发明。Specific embodiments of the present invention will be described in detail below in conjunction with the accompanying drawings. It should be understood that the specific embodiments described here are only used to illustrate and explain the present invention, and are not intended to limit the present invention.

参照图1,本发明实施例提供一种苦咸水淡化装置,包括内循环结构和外循环结构,内循环结构设置于外循环结构内;内循环结构形成用于淡化苦咸水的第一水循环网络,外循环结构形成用于淡化苦咸水第二水循环网络;Referring to Fig. 1, an embodiment of the present invention provides a brackish water desalination device, including an inner circulation structure and an outer circulation structure, the inner circulation structure is arranged in the outer circulation structure; the inner circulation structure forms the first water circulation for desalination of brackish water network, the outer circulation structure forms a second water circulation network for desalination of brackish water;

内循环结构包括有太阳能集热器15,用于白天收集热量并蓄存于第一水循环网络;苦咸水在第一水循环网络流通过程中通过蒸发冷凝形成淡化水并将热量传递到第二水循环网络,使得第二水循环网络得到热量并蓄存;待到夜晚,第一水循环网络和第二水循环网络积蓄的热量释放,使得苦咸水在第二水循环网络流通过程中冷凝形成淡化水。The internal circulation structure includes a solar heat collector 15, which is used to collect heat during the day and store it in the first water circulation network; the brackish water forms desalinated water through evaporation and condensation during the circulation of the first water circulation network and transfers heat to the second water circulation Network, so that the second water circulation network gets heat and stores it; at night, the heat accumulated in the first water circulation network and the second water circulation network is released, so that the brackish water condenses during the circulation of the second water circulation network to form desalinated water.

传统太阳能蒸馏器产水量过低有三点原因:一是水蒸气的凝结潜热未被重新利用,而是通过盖板散失到大气中去了;二是传统太阳能蒸馏器中自然对流的换热模式,大大限制了蒸馏器热性能的提高;三是待蒸发的苦咸水热容量太大,限制了运行温度的提高,从而减弱了蒸发的驱动力。因此,要提高太阳能蒸馏系统的产水量,必须克服上述缺陷。There are three reasons for the low water production of traditional solar stills: first, the latent heat of condensation of water vapor is not reused, but is lost to the atmosphere through the cover plate; second, the heat transfer mode of natural convection in traditional solar stills, It greatly limits the improvement of the thermal performance of the distiller; the third is that the heat capacity of the brackish water to be evaporated is too large, which limits the increase of the operating temperature, thereby weakening the driving force of evaporation. Therefore, in order to increase the water yield of the solar distillation system, the above-mentioned defects must be overcome.

本发明实施例所提供的苦咸水淡化装置,白天,苦咸水在内循环结构循环流通时,太阳能集热器15收集热量不断提高苦咸水的温度,使得第一水循环网络循环中的苦咸水不断积蓄热量。同时,升温的苦咸水蒸发冷凝形成淡化水,冷凝过程释放热量被第二水循环网络中的苦咸水收集,并随着苦咸水在第二水循环网络中的流通不断积蓄于第二水循环网络中。待到夜晚,第一水循环网络中的水不断释放热量,第二水循环网络中的苦咸水在循环过程中不断冷凝形成淡化水。In the brackish water desalination device provided by the embodiment of the present invention, during the day, when the brackish water circulates in the internal circulation structure, the solar heat collector 15 collects heat to continuously increase the temperature of the brackish water, so that the brackish water in the first water circulation network circulation Salt water keeps accumulating heat. At the same time, the heated brackish water evaporates and condenses to form desalinated water. The heat released during the condensation process is collected by the brackish water in the second water circulation network, and is continuously accumulated in the second water circulation network as the brackish water circulates in the second water circulation network. middle. At night, the water in the first water circulation network continuously releases heat, and the brackish water in the second water circulation network continuously condenses to form desalinated water during the circulation process.

可以看出,本发明实施例提供的太阳能苦咸水淡化装置,利用自然的冷热源,采用两层水循环网络,内层直接利用太阳能蓄热,外层利用蒸发产生汽化潜热的二次热量蓄热,实现了热量的回收,夜晚利用白天积蓄的热量实现昼夜连续的苦咸水蒸馏,成倍提高淡化效率;并且利用自然冷热源,节省成本。It can be seen that the solar brackish water desalination device provided by the embodiment of the present invention utilizes natural cold and heat sources and adopts a two-layer water circulation network. The inner layer directly uses solar energy to store heat, and the outer layer uses evaporation to generate secondary heat storage of latent heat of vaporization. Heat recovery is realized, and at night, the heat accumulated during the day is used to realize continuous distillation of brackish water day and night, which doubles the desalination efficiency; and the use of natural cold and heat sources saves costs.

并且,当晚上温度降低,第一水循环网络中的苦咸水温度不断下降,当苦咸水中盐浓度达到一定值时析出盐晶体,省去苦咸水浓水晾晒的步骤,同时实现苦咸水利用最大化。Moreover, when the temperature drops at night, the temperature of the brackish water in the first water circulation network continues to drop. When the salt concentration in the brackish water reaches a certain value, salt crystals are precipitated, which saves the step of drying the brackish water concentrated water, and at the same time realizes the brackish water Take advantage of it.

其中,外层蓄热水池21连通有导入苦咸水的补水管道3,且补水管道3用于连接外层蓄热水池21的端口设置有第一浮球阀18;外层蓄热水池21与内层蓄热水池11连通,且二者连通处设置有第二浮球阀27。Wherein, the outer layer heat storage pool 21 is communicated with a replenishment pipeline 3 that introduces brackish water, and the port of the water replenishment pipeline 3 for connecting the outer layer heat storage pool 21 is provided with a first float valve 18; the outer layer heat storage pool 21 is connected with the inner layer The layer heat storage tanks 11 are connected, and a second float valve 27 is arranged at the connection point between the two.

外部的苦咸水通过补水管道3首先进入外层蓄热水池21中,并由第二浮球阀27进行液位调节。外层蓄热水池21中的苦咸水再进入内层蓄热水池11中,在二者连通处设置的第一浮球阀18能够调节进水量,使得内层蓄热水池11中的苦咸水保持一定的液位。The external brackish water first enters the outer heat storage tank 21 through the replenishment pipeline 3 , and the liquid level is adjusted by the second float valve 27 . The brackish water in the outer layer heat storage pool 21 enters the inner layer heat storage pool 11 again, and the first float valve 18 provided at the connection between the two can adjust the water intake, so that the brackish water in the inner layer heat storage pool 11 Maintain a certain fluid level.

苦咸水采用外部补水管道3-外层蓄热水池21-内层蓄热水池11依次补水的方式,保证外层蓄热水池21补水量大,蒸发量小,始终保持不饱和状态,减少由于盐析出或结垢产生的维护工作量。The brackish water adopts the method of replenishing water from the external water supply pipeline 3-the outer heat storage pool 21-the inner heat storage pool 11 in order to ensure that the outer heat storage pool 21 has a large amount of water replenishment and a small evaporation, and is always in an unsaturated state, reducing the Maintenance workload due to salt precipitation or scaling.

自然隔热保温功能需要说明的是,外层蓄热水池21与内层蓄热水池11均采用地埋式设置,双层蓄热水池具有自然隔热保温功能,有利于蓄热保温,并能降低建造成本。Natural heat insulation function It should be noted that both the outer layer heat storage pool 21 and the inner layer heat storage pool 11 are buried, and the double-layer heat storage pool has the function of natural heat insulation and heat preservation, which is beneficial to heat storage and heat preservation, and can Reduce construction costs.

具体地,内循环结构还包括内层蓄热水池11、内层顶盖12;内层顶盖12罩设于内层蓄热水池11上;太阳能集热器15的进水口与内层蓄热水池11连通,出水口穿过内层顶盖12的顶部连通,以使苦咸水回到内层蓄热水池11,以此形成第一水循环网络。Specifically, the internal circulation structure also includes an inner layer heat storage pool 11 and an inner layer top cover 12; the inner layer top cover 12 is covered on the inner layer heat storage pool 11; the water inlet of the solar collector 15 and the inner layer heat storage The water pool 11 is connected, and the water outlet is connected through the top of the inner layer top cover 12, so that the brackish water returns to the inner layer heat storage pool 11, thereby forming a first water circulation network.

具体地,内循环结构还包括设置于内层顶盖12顶部的布水喷头14,布水喷头14与太阳能集热器15的出水口相连通,用于将苦咸水喷洒落入内层蓄热水池11。Specifically, the internal circulation structure also includes a water distribution nozzle 14 arranged on the top of the inner layer top cover 12, and the water distribution nozzle 14 is connected with the water outlet of the solar collector 15 for spraying brackish water into the inner layer storage. Hot pool11.

此处,太阳能集热器15优选为真空玻璃管集热器,内层顶盖12优选使用0.3mm厚、型号为316的不锈钢板,可以获得比较理想的冷凝传热效果,同时保证耐腐蚀性能。Here, the solar heat collector 15 is preferably a vacuum glass tube heat collector, and the inner top cover 12 is preferably made of a 0.3 mm thick stainless steel plate of type 316, which can obtain a relatively ideal condensation heat transfer effect while ensuring corrosion resistance .

内层蓄热水池11通过第一管道16与太阳能集热器15的进水口相连通,第一管道16上设置有第一循环泵17。The inner heat storage pool 11 communicates with the water inlet of the solar heat collector 15 through a first pipe 16 , and a first circulation pump 17 is arranged on the first pipe 16 .

进一步地,在内层顶盖12的内侧设置有第一集水槽13,用于收集第一水循环网络中的淡化水。Further, a first water collection tank 13 is provided inside the inner roof 12 for collecting the desalinated water in the first water circulation network.

本发明至少一种实施例中,外循环结构包括外层蓄热水池21、外层顶盖22;外层顶盖22罩设于外层蓄热水池21上;外层蓄热水池21与外层顶盖22的顶部连通,以使外层蓄热水池21中的苦咸水进入外层顶盖22与内层顶盖12之间并沿内层顶盖12的外表面回到外层蓄热水池21,以此形成第二水循环网络。In at least one embodiment of the present invention, the outer circulation structure includes an outer heat storage pool 21 and an outer top cover 22; the outer top cover 22 is set on the outer heat storage pool 21; The top of the layer top cover 22 is connected, so that the brackish water in the outer layer heat storage pool 21 enters between the outer layer top cover 22 and the inner layer top cover 12 and returns to the outer layer storage along the outer surface of the inner layer top cover 12. The hot water pool 21 forms the second water circulation network.

具体地,外循环结构还包括设置于外层顶盖22顶部的布水槽24,布水槽24与外层蓄热水池21连通,用于将苦咸水导入外层顶盖22与内层顶盖12之间并沿内层顶盖12的外表面回到外层蓄热水池21。Specifically, the outer circulation structure also includes a water distribution tank 24 arranged on the top of the outer layer top cover 22, and the water distribution tank 24 communicates with the outer layer heat storage pool 21 for introducing brackish water into the outer layer top cover 22 and the inner layer top cover. 12 and return to the outer heat storage pool 21 along the outer surface of the inner roof 12.

此处,外层顶盖22优选使用透明白玻璃,可以最大限度的利用太阳能,同时起到隔热保温的作用。Here, the outer layer top cover 22 is preferably made of transparent white glass, which can maximize the use of solar energy and simultaneously play the role of heat insulation.

外层蓄热水池21通过第二管道25与布水槽24相连通,第二管道25上设置有第二循环泵26。The outer layer heat storage tank 21 is in communication with the water distribution tank 24 through the second pipeline 25, and the second circulation pump 26 is arranged on the second pipeline 25.

进一步地,外层顶盖22的内侧设置有第二集水槽23,用于收集第二水循环网络中的淡化水。Further, the inner side of the outer top cover 22 is provided with a second water collection tank 23 for collecting the desalinated water in the second water circulation network.

需要说明的是,第一循环泵17和第二循环泵26优选的使用塑料自吸泵或隔膜自吸泵,有利于设备的维护。It should be noted that the first circulation pump 17 and the second circulation pump 26 preferably use plastic self-priming pumps or diaphragm self-priming pumps, which is beneficial to equipment maintenance.

此外,本发明实施例所提供的苦咸水淡化装置还包括检修门19和水池盖板28,检修门19设置于内层顶盖12上,水池盖板28设置于外层蓄热水池21上。检修门19和水池盖板28分别用于内层蓄热水池11和外层蓄热水池21的清理和维护In addition, the brackish water desalination device provided by the embodiment of the present invention also includes an inspection door 19 and a pool cover 28, the inspection door 19 is arranged on the inner roof 12, and the water pool cover 28 is arranged on the outer heat storage tank 21 . The inspection door 19 and the pool cover 28 are used for cleaning and maintenance of the inner heat storage pool 11 and the outer heat storage pool 21 respectively

结合上述实施例提供的苦咸水淡化装置的具体结构,对该苦咸水淡化装置的工作过程做以详细描述。In combination with the specific structure of the brackish water desalination device provided in the above embodiments, the working process of the brackish water desalination device is described in detail.

白天,内层蓄热水池11中的苦咸水在第一循环泵17的驱动下沿第一管道16进入太阳能集热器15的进水口,并从太阳能集热器15的出水口流出,在此过程中,苦咸水吸收太阳能温度升高。由太阳能集热器15的出水口流出的苦咸水到达内层顶盖12的顶部,通过布水喷头14向下喷洒,苦咸水落入内层蓄热水池11。在苦咸水向下喷洒的过程中,由于苦咸水温度较高,部分苦咸水会蒸发为水蒸气,并凝结在内层顶盖12的内壁,这部分水蒸汽形成淡化水沿内层顶盖12的内壁向下流被第一集水槽13收集。依次循环,内层蓄热水池11中的苦咸水温度不断升高。需要说明的是,当苦咸水蒸发在内层顶盖12的内壁凝结,会释放汽化潜热。During the day, the brackish water in the inner heat storage tank 11 enters the water inlet of the solar heat collector 15 along the first pipeline 16 under the drive of the first circulation pump 17, and flows out from the water outlet of the solar heat collector 15. During this process, the brackish water absorbs solar energy and increases in temperature. The brackish water flowing out from the water outlet of the solar heat collector 15 reaches the top of the inner roof 12 , and is sprayed downwards by the water distribution nozzle 14 , and the brackish water falls into the inner layer heat storage pool 11 . In the process of spraying the brackish water downward, due to the high temperature of the brackish water, part of the brackish water will evaporate into water vapor and condense on the inner wall of the inner roof 12, and this part of the water vapor will form desalinated water along the inner layer. The inner wall of the top cover 12 flows downwards and is collected by the first sump 13 . Circulating successively, the temperature of the brackish water in the inner layer heat storage pool 11 continues to rise. It should be noted that when the brackish water evaporates and condenses on the inner wall of the inner roof 12, latent heat of vaporization will be released.

外层蓄热水池21中的苦咸水在第二循环泵26的驱动下沿第二管道25到达外层顶盖22顶部,并由布水槽24向下均匀布撒,由于内层顶盖12位于外层顶盖22内侧,布水槽24洒出的苦咸水进入外层顶盖22与内层顶盖12之间,并在重力的作用下落在内层顶盖12外表面,沿内层顶盖12的外表面向下流落入外层蓄热水池21。在苦咸水沿内层顶盖12的外表面向下流的过程中,凝结于内层顶盖12内侧的水蒸气所释放的汽化潜热被该部分苦咸水吸收。依次循环,外层蓄热水池21中的苦咸水温度不断升高。需要说明的是,当苦咸水沿内层顶盖12的外表面流的过程中,部分苦咸水蒸发凝结于外层顶盖22的内壁,这部分水蒸汽形成淡化水沿外层顶盖22的内壁向下流被第二集水槽23收集。The brackish water in the outer heat storage pool 21 is driven by the second circulation pump 26 to reach the top of the outer roof 22 along the second pipeline 25, and is evenly distributed downwards by the water distribution tank 24. Since the inner roof 12 is located Inside the outer roof 22, the brackish water spilled from the water distribution tank 24 enters between the outer roof 22 and the inner roof 12, and falls on the outer surface of the inner roof 12 under the action of gravity, along the inner roof. The outer surface of the cover 12 flows down into the outer heat storage tank 21 . During the process of the brackish water flowing downward along the outer surface of the inner roof 12 , the latent heat of vaporization released by the water vapor condensed on the inner side of the inner roof 12 is absorbed by the part of the brackish water. Circulating successively, the temperature of the brackish water in the outer layer heat storage pool 21 continues to rise. It should be noted that, when the brackish water flows along the outer surface of the inner roof 12, part of the brackish water evaporates and condenses on the inner wall of the outer roof 22, and this part of water vapor forms desalinated water along the outer roof. The inner wall of 22 flows down and is collected by the second sump 23.

夜晚或者太阳落山,太阳能集热器15不再集热,内层蓄热水池11中的苦咸水蓄热停止,在第一水循环网络中的苦咸水的不断循环中,内层蓄热水池11中的苦咸水温度不断下降,当苦咸水中盐浓度达到一定值时析出盐晶体。At night or when the sun sets, the solar heat collector 15 no longer collects heat, and the heat storage of the brackish water in the inner heat storage tank 11 stops. In the continuous circulation of the brackish water in the first water circulation network, the inner heat storage tank The temperature of the brackish water in 11 keeps dropping, and when the salt concentration in the brackish water reaches a certain value, salt crystals are precipitated.

随着夜晚降临,环境温度不断降低,外层蓄热水池21中的苦咸水,在第二水循环网络中的苦咸水的不断循环中,部分苦咸水在外层顶盖22的内壁凝结,凝结水汇集到第二集水槽23中,作为淡化水收集利用。As night falls, the ambient temperature continues to decrease, and the brackish water in the outer heat storage pool 21 is continuously circulated in the second water circulation network, part of the brackish water condenses on the inner wall of the outer roof 22, The condensed water is collected in the second water collection tank 23 and used as desalinated water.

本发明还提供一种苦咸水淡化方法,采用上述实施例提供的任一种苦咸水淡化装置收集淡化水,包括以下步骤:The present invention also provides a brackish water desalination method, using any brackish water desalination device provided in the above embodiments to collect desalinated water, including the following steps:

白昼循环淡化:内循环结构中的太阳能集热器15收集太阳能,通过苦咸水在第一水循环网络中循环将热量蓄存于第一水循环网络中;苦咸水在第一水循环网络中循环时蒸发凝结形成淡化水,并释放汽化潜热,被第二水循环网络中的苦咸水吸收;第二水循环网络中的苦咸水通过循环将热量蓄存于第二水循环网络中;Diurnal cycle desalination: the solar collector 15 in the internal circulation structure collects solar energy, and the heat is stored in the first water circulation network through the circulation of brackish water in the first water circulation network; when the brackish water circulates in the first water circulation network Evaporation and condensation form desalinated water, and release latent heat of vaporization, which is absorbed by the brackish water in the second water circulation network; the brackish water in the second water circulation network stores heat in the second water circulation network through circulation;

夜晚循环淡化:第一水循环网络和第二水循环网络积蓄的热量释放,使得第二水循环网络中循环的苦咸水冷凝形成淡化水。Night circulation desalination: the heat accumulated in the first water circulation network and the second water circulation network is released, so that the brackish water circulating in the second water circulation network condenses to form desalinated water.

综上,本发明实施例提供的苦咸水淡化装置及苦咸水淡化方法具有以下技术优势:In summary, the brackish water desalination device and the brackish water desalination method provided by the embodiments of the present invention have the following technical advantages:

1、采用双层蓄热水池设计和蒸发潜热二次利用的设计,内层直接利用太阳能蓄热,外层利用蒸发产生汽化潜热的二次热量蓄热,实现了热量的回收,夜晚利用白天积蓄的热量实现昼夜连续的苦咸水蒸馏,成倍提高淡化效率;1. It adopts the design of double-layer heat storage pool and the design of secondary utilization of evaporation latent heat. The inner layer directly uses solar energy to store heat, and the outer layer uses evaporation to generate secondary heat storage of latent heat of vaporization, which realizes heat recovery and utilizes the accumulated heat during the day at night. The heat realizes continuous distilling of brackish water day and night, and doubles the desalination efficiency;

2、利用自然冷热源,无需额外的复杂设备和动力,可以采用分布式就地实现苦咸水的淡化利用,节省成本;2. Utilizing natural cold and heat sources, without the need for additional complex equipment and power, distributed in-situ desalination and utilization of brackish water can be used to save costs;

3、苦咸水采用外部补水管道3-外层蓄热水池21-内层蓄热水池11依次补水的方式,保证外层蓄热水池21补水量大,蒸发量小,始终保持不饱和状态,内层蓄热水池11实现持续浓缩,省去苦咸水浓水晾晒的步骤,同时实现苦咸水利用最大化,减少由于盐析出或结垢产生的维护工作量;3. The brackish water adopts the method of replenishing water from the external water supply pipeline 3-outer heat storage pool 21-inner heat storage pool 11 in order to ensure that the outer heat storage pool 21 has a large amount of water replenishment, a small amount of evaporation, and is always in an unsaturated state. The inner hot water storage pool 11 realizes continuous concentration, saves the step of drying brackish water concentrated water, and at the same time maximizes the use of brackish water, reducing the maintenance workload due to salt precipitation or scaling;

4、整套装置采用地埋式双层结构,具有自然隔热保温功能;4. The whole device adopts the buried double-layer structure, which has the function of natural heat insulation;

5、用于我国缺水的中西部,可以充分利用丰富的太阳能资源以及昼夜温差较大的特点,满足中西部苦咸水淡化的巨大需求。5. It is used in the central and western regions where water is scarce in my country. It can make full use of the abundant solar energy resources and the characteristics of large temperature difference between day and night to meet the huge demand for desalination of brackish water in the central and western regions.

最后应说明的是:以上各实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述各实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention, rather than limiting them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: It is still possible to modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some or all of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the technical solutions of the various embodiments of the present invention. scope.

Claims (6)

1. A brackish water desalination apparatus, comprising: an inner circulation structure and an outer circulation structure, the inner circulation structure and the outer circulation structure forming a double-layer structure;
the inner circulation structure forms a first water circulation network for desalting the brackish water, and the outer circulation structure forms a second water circulation network for desalting the brackish water;
the internal circulation structure comprises a solar heat collector (15) for collecting heat in the daytime and storing the heat in the first water circulation network; the brackish water forms desalted water through evaporation and condensation in the circulation process of the first water circulation network and transfers heat to the second water circulation network, so that the second water circulation network obtains and stores the heat; when the night arrives, the heat accumulated by the first water circulation network and the second water circulation network is released, so that the brackish water is condensed to form desalted water in the circulation process of the second water circulation network;
the inner circulation structure comprises an inner layer heat storage water tank (11), an inner layer top cover (12) and a water distribution spray head (14) arranged at the top of the inner layer top cover (12); the inner layer top cover (12) is covered on the inner layer heat storage water tank (11); the water inlet of the solar heat collector (15) is communicated with the inner layer heat storage water tank (11), and the water outlet passes through the top of the inner layer top cover (12) and is communicated with the water distribution nozzle (14), so that brackish water returns to the inner layer heat storage water tank (11);
the external circulation structure comprises an external heat storage pool (21) and an external top cover (22); the outer layer top cover (22) is covered on the outer layer heat storage water tank (21); the outer layer heat storage water tank (21) is communicated with the top of the outer layer top cover (22) so that brackish water in the outer layer heat storage water tank (21) enters between the outer layer top cover (22) and the inner layer top cover (12) and returns to the outer layer heat storage water tank (21) along the outer surface of the inner layer top cover (12);
a first water collecting tank (13) is arranged on the inner side of the inner layer top cover (12) and is used for collecting desalted water in the first water circulation network;
a second water collecting tank (23) is arranged on the inner side of the outer layer top cover (22) and is used for collecting desalted water in the second water circulation network;
the outer layer heat storage water tank (21) is communicated with a water supplementing pipeline (3) for leading in brackish water, and a second ball float valve (27) is arranged at a port of the water supplementing pipeline (3) for connecting the outer layer heat storage water tank (21); the outer-layer heat storage water tank (21) is communicated with the inner-layer heat storage water tank (11), and a first ball float valve (18) is arranged at the communication position of the outer-layer heat storage water tank and the inner-layer heat storage water tank.
2. The brackish water desalination device according to claim 1, characterized in that the inner layer heat storage water tank (11) is communicated with the water inlet of the solar heat collector (15) through a first pipeline (16), and a first circulating pump (17) is arranged on the first pipeline (16).
3. The brackish water desalination plant according to claim 1, characterized in that the outer circulation structure further comprises a water distribution tank (24) arranged at the top of the outer layer top cover (22), the water distribution tank (24) being in communication with the outer layer heat storage water tank (21) for guiding brackish water between the outer layer top cover (22) and the inner layer top cover (12) and back to the outer layer heat storage water tank (21) along the outer surface of the inner layer top cover (12).
4. A brackish water desalination plant according to claim 3, wherein the outer heat storage water tank (21) is connected to the water distribution tank (24) through a second pipe (25), and a second circulation pump (26) is arranged on the second pipe (25).
5. The brackish water desalination device according to claim 1, wherein the outer layer heat storage water tank (21) and the inner layer heat storage water tank (11) are both arranged in a buried manner.
6. A method for desalinating brackish water, characterized in that the method for collecting desalinated water by using the brackish water desalination apparatus according to any one of claims 1 to 5 comprises the steps of:
day cycle desalination: the solar heat collector (15) in the internal circulation structure collects solar energy, and heat is stored in the first water circulation network through the circulation of brackish water in the first water circulation network; evaporating and condensing brackish water to form desalted water when the brackish water circulates in the first water circulation network, releasing vaporization latent heat, and absorbing the brackish water in the second water circulation network; the brackish water in the second water circulation network stores heat in the second water circulation network through circulation;
and (3) circularly desalting at night: and releasing heat accumulated by the first water circulation network and the second water circulation network, so that brackish water circulating in the second water circulation network is condensed to form desalted water.
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