Salt separation and purification recovery method for salt-containing wastewater

A technology for salt-containing wastewater and salt separation, applied in chemical instruments and methods, general water supply conservation, multi-stage water treatment, etc., can solve the problem of increasing the operating cost of evaporative crystallization technology, increasing unit steam consumption, and increasing equipment heat transfer resistance. and other problems, to achieve significant economic and social benefits, reduce energy consumption, and not easily corrode equipment.

Active Publication Date: 2017-06-13
SYNFUELS CHINA INNER MONGOLIA CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Evaporation crystallization is mainly to use heat source to heat water into steam and separate concentrated brine mother liquor. Although multi-effect evaporation or mechanical steam recompression utilizes steam waste heat to reduce energy consumption, the energy consumption of evaporation crystallization due to the thermal limitation of water vapor phase change is still relatively high. high
The second is that evaporation and crystallization lead to corrosion and scaling of equipment and pipelines
Due to high-temperature heating, the corrosiveness of the concentrated brine increases, and as the evaporation proceeds, the concentration of the mother liquor of the concentrated brine continues to increase, which further enhances the corrosiveness. Therefore, corrosion-resistant materials must be used in the material selection of evaporation crystallization equipment, which also increases equipment Investment cost; and evaporator fouling also leads to increased heat transfer resistance of equipment and increased unit steam consumption, thereby increasing the operating cost of evaporation and crystallization technology

Method used

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  • Salt separation and purification recovery method for salt-containing wastewater
  • Salt separation and purification recovery method for salt-containing wastewater
  • Salt separation and purification recovery method for salt-containing wastewater

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0065] according to figure 1 In the process shown, the high-salt wastewater 101 from the upstream unit passes through the pretreatment unit 1 to obtain the pretreated saline wastewater 102, and after entering the advanced oxidation unit 2, the high-salt wastewater 103 from which organic matter is removed is obtained.

[0066] The saline waste water 103 from which organic matter has been removed enters the desalination purification unit 3 to obtain desalted product water 104 and concentrated water 105 ; the concentrated water 105 passes through the secondary softening unit 4 to obtain softened concentrated water 106 .

[0067] The softened concentrated water 106 enters the deep concentration unit 5 to obtain deep concentrated product water 107 and deep concentrated concentrated water 108; the deep concentrated product water 107 returns to the desalination purification unit 3 for further processing.

[0068] The deeply concentrated concentrated water passes through the freeze cr...

Embodiment 2

[0078] according to figure 2 In the process shown, the high-salt wastewater 106 from the upstream unit enters the deep concentration unit 5 and is concentrated by the ED membrane to obtain the deep concentrated product water 107 and the deep concentrated concentrated water 108; the deep concentrated product water 107 is desalted and purified again Reuse, deeply concentrated concentrated water 108 enters the freeze crystallization unit 6, and the temperature of the freeze crystallization unit 6 is -8°C to obtain Na 2 SO 4 Crystal 109 and frozen crystal concentrated water 110; Na 2 SO 4 Crystal 109 was dried to obtain Na 2 SO 4 Solid, frozen and crystallized concentrated water 110 passes through the freeze-concentration unit 7 to obtain freeze-concentrated product water 111 and freeze-concentrated concentrated water 112; the heat exchanger temperature of the freeze-concentration unit is -35°C, the temperature of the crystallizer is -22°C, and the pressure of the cleaning to...

Embodiment 3

[0083] according to image 3 In the process shown, the high-salt wastewater 101 from the upstream unit enters the freezing crystallization unit 6, and the temperature of the freezing crystallization unit 6 is -8°C to obtain Na 2 SO 4 Crystal 109 and frozen crystal concentrated water 110; Na 2 SO 4 Crystal 109 Na after drying 2 SO 4 Solid, frozen and crystallized concentrated water 110 passes through the freeze-concentration unit 7 to obtain freeze-concentrated product water 111 and freeze-concentrated concentrated water 112; the heat exchanger temperature of the freeze-concentration unit is -35°C, the temperature of the crystallizer is -23°C, and the pressure of the cleaning tower is 6 bar; the freeze-concentrated product water is reused after desalination and purification, and the freeze-concentrated concentrated water 112 is further dried 8 to obtain NaCl solid 113.

[0084] Each logistics mass flow rate, water quality index and crystalline salt purity in table 4 embodi...

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Abstract

The invention discloses a salt separation and purification recovery method for salt-containing wastewater. The method comprises the following steps: performing advanced oxidation treatment on pretreated salt-containing wastewater so as to obtain salt-containing wastewater in which organic matters are removed; desalting and purifying the salt-containing wastewater in which organic matters are removed so as to obtain desalted produced water and desalted concentrated water, performing secondary softening treatment on the desalted concentrated water so as to obtain softened concentrated water; performing deep concentration on the softened concentrated water so as to obtain deeply concentrated produced water and deeply-concentrated concentrated water; performing freezing crystallization on the deeply-concentrated concentrated water so as to obtain sodium sulfate crystals and freezing crystallized concentrated water; performing freezing crystallization on the freezing crystallized concentrated water for at least one time so as to obtain freezing crystallized produced water and freezing crystallized concentrated water; and evaporating or drying the freezing crystallized concentrated water, thereby obtaining the sodium chloride crystal. The traditional evaporative crystallization process is replaced with the freezing crystallization, the process is implemented under low temperature and normal pressure, the equipment is difficultly corroded, the operation is safe and reliable, the energy consumption is effectively reduced, the pipeline is difficultly blocked, and the investment and operating cost can be reduced.

Description

technical field [0001] The invention relates to a salt separation and purification recovery method of saline waste water. Background technique [0002] Coal chemical industry uses coal as raw material and converts coal into gas, liquid and solid products through chemical processing. However, because the coal chemical industry needs to consume and by-produce a large amount of water, the problems of water resource recycling and environmental protection are becoming increasingly prominent. Coal chemical wastewater mainly includes coking wastewater, coal gasification wastewater, coal direct / indirect liquefaction wastewater, and wastewater generated during the preparation of synthesis gas conversion catalysts. The huge water consumption and wastewater discharge are a prominent factor restricting the development of the coal chemical industry. , and one of the important issues involved is the safe treatment of high-salt wastewater. [0003] Usually coal chemical industry wastewat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/08
CPCC02F1/22C02F1/42C02F1/441C02F1/444C02F1/4672C02F1/4693C02F1/52C02F1/66C02F1/72C02F1/725C02F1/78C02F5/08C02F9/00C02F2301/08Y02A20/131
Inventor 耿春宇高琳蒋丽娜李向阳仝云娜吴二飞郝栩杨勇李永旺
Owner SYNFUELS CHINA INNER MONGOLIA CO LTD
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