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Seawater atomization cyclone desalination equipment system and method

An atomization device and cyclone technology, which is applied in chemical instruments and methods, seawater treatment, general water supply saving, etc., can solve the problems of high engineering investment, high operation cost, high water production cost, and achieve good process controllability, The effect of low operating costs and low water quality requirements

Pending Publication Date: 2020-12-08
长沙紫宸科技开发有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0010] (1) Low-temperature multiple-effect distillation technology (LT-MED): Fresh water is produced by multiple low-temperature distillation and condensation of seawater, but the outer wall of the heat exchange tube is prone to fouling, and the improvement of thermal efficiency is limited by low temperature (≤70°C). Huge, relatively high investment
[0011] (2) Multi-stage flash technology (MSF): Seawater is condensed after pretreatment and disinfection and multi-stage flash evaporation by steam heating to produce fresh water. High, high project investment, low operating flexibility of equipment, difficult to adapt to projects with large changes in water production, and will cause thermal pollution to the marine environment
[0012] (3) Compressed steam distillation (VC): The steam generated by hot seawater is pressurized twice and condensed into fresh water. This system has high requirements for sealing and seawater pretreatment. It is easy to scale and consumes heat and electricity. High, the equipment volume is also large, the operating cost is high, and it will cause thermal pollution to the marine environment
This method has high requirements for seawater pretreatment, large loss of membrane modules, and the membrane flux is sensitive to temperature. It needs to be equipped with a large number of high-quality corrosion-resistant auxiliary materials (stainless steel pipes, plates and titanium metal pipes), and the cost of fresh water treatment is relatively high.
[0015] (2) Electrodialysis technology (ED): uses potential difference to move and separate salt and water in a directional way, and its operating energy consumption is relatively high (generally 17-20kW·h / m 3 ), and it is difficult to remove salts with low dissociation degree, non-dissociated substances and bacteria, etc., and the product water quality is poor
[0024] The fifth category is oil separation and desalination method, such as mixing coconut oil and seawater to heat up, condensing and separating to remove salt, but the efficiency is low and it is easy to cause secondary pollution
Secondly, due to the addition of various chemicals in the desalination process of the concentrated brine generated by the existing seawater desalination project, there are no corresponding comprehensive utilization and disposal measures in the follow-up, and the concentrated brine is directly discharged into the ocean, which has a great impact on the ecological environment of the ocean.
[0025] Obviously, the existing seawater desalination technologies all suffer from high engineering cost, large equipment footprint, high seawater pretreatment requirements, complicated process, high energy consumption, high water production cost, low freshwater separation efficiency, or freshwater effluent. Technical problems such as low quality
Moreover, in the existing technology, the concentrated seawater is directly discharged into the ocean, which affects the marine ecological environment. It is still necessary to consider the extraction and deep processing of chemical resources from the concentrated seawater after seawater desalination, so as to form an industrial chain for comprehensive utilization of seawater, and the development of circular economy is also imminent.
[0026] On the other hand, the current process of directly extracting salt or potassium salt from seawater or salt lake brine is complex and requires a large investment, and is almost limited to salt or potassium salt extraction, and does not involve seawater desalination treatment

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  • Seawater atomization cyclone desalination equipment system and method
  • Seawater atomization cyclone desalination equipment system and method
  • Seawater atomization cyclone desalination equipment system and method

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Embodiment 1

[0061] refer to figure 1 and figure 2 , this embodiment includes an atomization and desalination tower 1, a first tank body 101, a first atomization device 102, a first brine chamber 103, a first fan 104, a parallel multi-tube vortex cyclone condensation device 105, and a fiber screen water condensation device 106, gas preheating device 2, solar heat source gas preheating device 201, waste heat heat source gas preheating device 203, first seawater pumping device 3, first brine discharge device 4, first hot air blowing device 7, first Hot air injection device 10. The first seawater pumping device 3 communicates with the first atomizing device 102 with pipelines, and the heat source outlet of the gas preheating device 2 with solar energy as the heat source is respectively connected with the first hot blast blowing device 7 and the first hot blast injection device 10 with pipelines The first hot air blowing device 7 communicates with the first atomizing device 102 through pipe...

Embodiment 2

[0068] refer to image 3 and Figure 4 , this embodiment includes an atomization and desalination tower 1, a first tank body 101, a first atomization device 102, a first brine chamber 103, a first fan 104, a parallel multi-tube vortex cyclone condensation device 105, and a fiber screen water condensation device 106, electric heat source gas preheating device 204, first seawater pumping device 3, first brine discharge device 4, impurity removal device 5, dosing mechanism 501, impurity removal reaction mechanism 502, impurity removal and filtration mechanism 503, spray Drying device 6, spray drying tower 601, bag filter 603, centrifugal fan 604, first hot air blowing device 7, magnesium hydroxide extraction device 8, modifier adding mechanism 801, magnesium extraction reaction mechanism 802, magnesium extraction Filtration mechanism 803 , strontium salt extraction device 9 , precipitant addition mechanism 901 , strontium extraction reaction mechanism 902 , strontium extraction ...

Embodiment 3

[0075] refer to Figure 5 and Figure 6, this embodiment includes two sets of parallel atomization and desalination systems, mainly including the atomization and desalination tower 1, the first tank body 101 and the second tank body 101', the first atomization device 102 and the second atomization device 102', The first brine chamber 103 and the second brine chamber 103', the first blower fan 104 and the second blower fan 104', the parallel multi-pipe vortex cyclone condensation device 105, the fiber screen water condensation device 106, the fuel combustion heat energy gas preheating device 202, Waste heat heat source gas preheating device 203, first seawater pumping device 3 and second seawater pumping device 3', first brine discharge device 4 and second brine discharge device 4', impurity removal device 5, dosing mechanism 501, impurity removal reaction mechanism 502, impurity removal and filtration mechanism 503, spray drying device 6, spray drying tower 601, cyclone separ...

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Abstract

The invention relates to a seawater atomization cyclone desalination equipment system and method. The seawater atomization cyclone desalination equipment system comprises an atomization desalination tower, an atomization device arranged in the atomization desalination tower and used for atomizing and spraying high temperature seawater, and a brine chamber arranged at the bottom of the atomizationdesalination tower, wherein the atomization device is connected with a gas preheating device arranged outside a tank body; and the upper part of the tank body is provided with a water condensing device and a fan which are used for sucking atomized fresh water out of the tank body by utilizing a negative pressure principle and collecting the fresh water, wherein the water condensing device is connected with the fan, and the brine chamber is connected with a salt extracting device. The invention also comprises a method for desalinating seawater by using the seawater atomization cyclone desalination equipment system. The equipment system is low in investment, simple in structure, small in occupied area, low in operation energy consumption (less than 4kW.h per m<3>of fresh water), high in water yield, low in seawater desalination cost and easy to popularize.

Description

technical field [0001] The invention relates to the technical field of seawater desalination, in particular to an equipment system and method for seawater atomization cyclone desalination. Background technique [0002] At present, China's fresh water reserves are about 2.8 trillion tons, accounting for about 6% of the world's total water resources. The per capita fresh water accounts for less than 2300 tons of water, which is less than 1 / 4 of the world's per capita water. It is the country with the poorest per capita water resources in the world. one. The huge population base has exacerbated the contradiction between supply and demand of water resources. [0003] At the same time, the spatial distribution of my country's water resources is extremely uneven, forming an obvious pattern of more in the east and less in the west, and more in the south and less in the north. About two-thirds of the major cities in the country are short of water, and nearly one-fifth of the citie...

Claims

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Application Information

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IPC IPC(8): C02F1/14C02F1/16C02F1/04C01D3/06C01F5/14C01F11/00C02F103/08
CPCC02F1/14C02F1/16C02F1/04C01D3/06C01F5/14C01F11/00C02F2103/08Y02A20/142Y02A20/124Y02A20/212
Inventor 尹小林黄波
Owner 长沙紫宸科技开发有限公司