Saline treatment system and method

A treatment system and brine technology, applied in the field of water treatment, can solve the problems of low evaporation efficiency, small steam output, environmental hazards, etc., and achieve the effects of improving evaporation efficiency, reducing equipment investment, and increasing water yield.

Inactive Publication Date: 2012-02-01
陶欣 +1
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Such as the solar compressed air distillation seawater desalination device disclosed in the Chinese patent of publication number CN101723476A, the difference between this device and the Chinese patent of the above-mentioned publication number CN101591042A is that the heat pump is cancelled, the solar energy is transmitted to the seawater through the heat exchanger, and the steam evaporated from the seawater is compressed by a fan ;The device passes the low-temperature seawater heated by solar energy into the negative pressure evaporation chamber to vaporize itself, and then uses the latent heat of steam condensation to heat the seawater in the evaporation chamber, so there are still disadvantages of low evaporation efficiency, low fresh water yield, and impossibility of industrialization
Another example is the seawater desalination low-temperature multi-effect device disclosed in the Chinese patent of Notification No. CN2934211Y. This device wants to use solar energy to generate steam to evaporate seawater, but obviously the efficiency of directly generating steam with solar energy is very low (steam output is small), and it is difficult to continue the evaporation of seawater. need
Another example is the solar desalination equipment disclosed by the Chinese patent of Publication No. CN1417132A. This equipment uses the heat exchanger to generate steam from the working medium heated by the solar energy, and then uses the steam to evaporate seawater through a multi-effect distillation device to obtain fresh water; when the equipment distills seawater, it needs The steam consumption is large, which requires a large-scale investment in solar heaters to meet, so the evaporation efficiency is still low (that is, the fresh water yield is low), and it is difficult to industrialize production
[0006] There is also a common defect in the prior art of each patent illustrated above: since solar energy cannot continuously provide energy, only solar heat collectors cannot guarantee continuous operation of seawater distillation or desalination devices.
[0007] In addition, the concentrated brine produced by the above-mentioned prior art is generally directly discharged (such as discharged into the sea), which not only causes harm to the environment (such as causing changes in the local ecology of the ocean), but also does not fully utilize the salt in the concentrated brine

Method used

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Experimental program
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Effect test

Embodiment 1

[0051] The brine treatment system of the present embodiment is as figure 1 As shown, it includes a concentrating solar heater 1, a steam generator 2, a vacuum multi-effect distillation device 3, a steam pipeline, a brine pool 4, a brine pipeline, a first brine pump 5-1, a fresh water pool 6, and a fresh water pipe road and fresh water pump7. The steam generator 2 contains a fresh water tank, a first heat exchanger 8 placed in the fresh water tank and a steam chamber, and the water inlet of the fresh water tank (that is, the water inlet of the steam generator 2) is connected to the fresh water tank through a fresh water pipeline and a fresh water pump 7 6 outlets. The vacuum multi-effect distillation device 3 is mainly composed of the same three distillation units connected in series, and each distillation unit includes a shower head 9, a heat exchange evaporator, a distillation chamber, a first brine tank and a second brine pump 5-2, The brine outlet of the vacuum multiple-e...

Embodiment 2

[0061] The brine treatment system of the present embodiment is an improvement on the basis of the first brine treatment system, such as figure 2 As shown, except that it is the same as Embodiment 1, the difference is that it also includes an energy storage oil pool 16 and an energy storage oil pump 17, and the oil outlet of the energy storage oil pool 16 is respectively connected to the first oil pump through the oil pipeline and the energy storage oil pump 17. The oil inlet of the heat exchanger 8 and the second heat exchanger 15, the oil inlet of the energy storage oil pool 16 are connected to the oil outlet of the concentrating solar heater 1 through the oil pipeline.

[0062] The salt water treatment method of this embodiment is an improvement on the basis of the salt water treatment method of Embodiment 1, except that it is the same as Embodiment 1. The difference is: using the salt water treatment system of this embodiment, in step 1), when When the concentrating solar ...

Embodiment 3

[0064] The brine treatment system of the present embodiment is an improvement on the basis of the first brine treatment system, such as image 3 As shown, except that it is the same as Embodiment 1, the difference is: it also includes a vacuum spray evaporation device 18, and the vacuum spray evaporation device 18 contains a spray nozzle 19, an evaporator 20, an evaporation chamber, the third brine tank and the fourth brine pump 5 -4. The steam outlet of the steam chamber of the steam generator 2 is connected to the steam inlet of the evaporator 20 through a steam pipeline, and the steam outlet of the evaporator 20 is connected to the inlet of the first steam-water separator 14-1 through a steam pipeline. Steam port, the steam outlet of the evaporation chamber of the vacuum spray evaporation device 18 is connected to the steam inlet of the first heat exchange evaporator 10-1 of the vacuum multiple-effect distillation device 3 through a steam pipeline; the brine outlet of the th...

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Abstract

The invention relates to a saline treatment system and method belonging to the technical field of water treatment. A concentrating type solar heater, a steam generator, a vacuum multi-effect distillation device, a saline pump, a fresh water pump, a saline heater, an oil pool, an oil pump and a gas and water separator are used in the system and method. High-temperature heat conducting oil generated by the concentrating type solar heater is respectively conveyed to the steam generator and the saline heater, saline pumped in the saline heater is heated to high-temperature saline and then conveyed to the vacuum multi-effect distillation device, and fresh water pumped in the steam generator is heated to steam and then conveyed to the vacuum multi-effect distillation device. Strong saline is finally discharged. As the saline is heated by the high-temperature heat conducting oil generated by solar energy so as to generate the high-temperature saline, and the cycling utilization fo the steam is formed by utilizing gas and water separation, the steam quantity required by a heat exchange evaporator of the vacuum multi-effect distillation device can be greatly reduced. Furthermore, the evaporation efficiency of the saline can be greatly increased, and equipment investment can be reduced.

Description

technical field [0001] The invention relates to a brine treatment system and a brine treatment method, belonging to the technical field of water treatment. Background technique [0002] In recent years, the shortage of water resources in my country has become very serious. It has become a trend to use salt water (such as sea water or industrial wastewater) to obtain fresh water through desalination. Commonly used methods for desalination of industrial brine are divided into two categories, thermal method (multi-stage flash evaporation, low-temperature multi-effect distillation) and membrane method (reverse osmosis). The thermal method is to use heat energy to cause phase change of brine, evaporate water, and obtain fresh water through condensation. Thermal desalination needs to use steam as a heat source, and a steam generating device (usually a large coal-fired, gas-fired or oil-fired boiler) must be configured, which requires large investment, high cost and high energy co...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/04C02F1/12C02F1/14C01D3/06
CPCY02A20/212Y02P20/133Y02W10/37
Inventor 陶欣
Owner 陶欣
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