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Method for deeply treating inorganic high-salt industrial wastewater and realizing zero liquid discharge

A technology for industrial waste water and advanced treatment, applied in the field of waste water treatment, can solve the problems of high energy consumption and equipment investment, reduced heat transfer efficiency, limited use and other problems, achieve low cost of hard removal, reduce scaling characteristics, and achieve zero liquid discharge Effect

Inactive Publication Date: 2017-03-08
SHAANXI JINTAI CHLOR ALKALI CHEM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Specifically, the evaporation method uses heat to heat and evaporate the wastewater. During the evaporation process, as the salt content of the wastewater increases, the fouling phenomenon gradually increases, which tends to reduce the heat transfer efficiency. Therefore, the process is complicated, and its energy consumption and The high investment in equipment also limits the use of this method;
[0005] The freezing method is to place the wastewater in a freezing field or a natural freezing environment. After the wastewater is frozen and the ice crystals are precipitated to a certain solid-liquid ratio, the frozen ice crystals are taken out, rinsed with clean water and dissolved, and the remaining wastewater enters a lower temperature cycle to concentrate. This method has a large investment in freezing treatment equipment, is subject to geographical restrictions, and has high costs.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] High-salt wastewater with TH / CH>1.0

[0031] Sample wastewater 100kg, temporary hardness 23mmol / L, calcium hardness 12mmol / L, salt content 4000 mg / L, add 2.0kg of 10% lime suspension at a rate of 0.5kg / min, stir for 30min, then add 3% 1.0kg of sodium hydroxide solution was added at a rate of 0.5kg / min. After stirring for 30 minutes, it was transferred to a settler, (including 10kg of ultrafiltered concentrated water returned to the settler) to separate 110kg of clear liquid.

[0032] After the clear liquid is filtered, 0.1 kg of 31% hydrochloric acid is added to adjust the pH value between 7 and 9, and enter the ultrafiltration system. 4300 mg / L, reverse osmosis clean water volume 75-85kg. Salt content 17000 mg / L, used to dissolve raw salt.

Embodiment 2

[0034] The high-salt wastewater with TH / CH<1.0 is fed with carbon dioxide

[0035] Sample wastewater 100kg, temporary hardness 15mmol / L, calcium hardness 20mmol / L, salt content 4000 mg / L, add 0.5-1.0 kg of 10% calcium carbide slag suspension, pH in the water between 8-9, and carbon dioxide 50 g ~ 100 g, after 30 minutes of blowing, TH / CH is 1.6.

[0036] Add 2.5kg of 10% calcium carbide slag suspension at a rate of 0.5kg / min. After stirring for 30 minutes, add 1.0kg of 3% sodium hydroxide solution at a rate of 0.5kg / min. After stirring for 30 minutes, transfer to sedimentation 110kg of supernatant (including 10kg of ultra-filtered concentrated water returned to the settler).

[0037] After the clear liquid is filtered, 0.1 kg of 31% hydrochloric acid is added to adjust the pH value between 7 and 9, and enter the ultrafiltration system. 10 kg of ultrafiltered concentrated water returns to the settler, and 100 kg of ultrafiltered water enters the reverse osmosis system. The amou...

Embodiment 3

[0039] The high-salt wastewater with TH / CH<1.0 is added to the solution containing soluble carbonate alkaline waste residue

[0040] Sample wastewater 100kg, temporary hardness 2.5mmol / L, calcium hardness 10mmol / L, salt content 5000 mg / L, add 1.0kg of 10% waste sodium carbonate solution at a speed of 0.5kg / min, stir for 30min, then add 3% 2.0kg of sodium hydroxide solution, added at a rate of 0.5kg / min, stirred for 30 minutes, then transferred to a settler, (including 10kg of ultrafiltered concentrated water returned to the settler) to separate 110kg of clear liquid.

[0041] After the clear liquid is filtered, 0.1 kg of 31% hydrochloric acid is added to adjust the pH value between 7 and 9, and enter the ultrafiltration system. 10 kg of ultrafiltered concentrated water returns to the settler, and 100 kg of ultrafiltered water enters the reverse osmosis system. The amount of reverse osmosis water is 5100 mg / L, the amount of reverse osmosis clean water is 75-85kg, and the salt c...

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Abstract

The invention discloses a method for deeply treating inorganic high-salt industrial wastewater and realizing zero liquid discharge. The method comprises the following steps: treating alkaline waste residues, chemically removing hardness, precipitating and separating, carrying out double-membrane concentration and recycling according to different quality. The method disclosed by the invention has the beneficial effects that all the high-salt wastewater can be recycled and the zero liquid discharge is realized; calcium-containing alkaline waste residues (such as carbide slag and lime powder), carbonate-containing alkaline waste residues, waste gas containing carbon dioxide and the like are industrial wastes and comprehensive utilization of treating wastes by wastes is realized; the hardness is technically removed and the total hardness is reduced to be lower than or equal to 4mmol / L; scaling properties of the wastewater are reduced and the industrial wastewater is convenient to concentrate through low-pressure reverse osmosis; and particularly, according to different water quality of the high-salt industrial wastewater, different hardness removing materials and methods are adopted and the hardness removing cost is low.

Description

technical field [0001] The invention relates to the field of wastewater treatment methods, in particular to a method for advanced treatment of inorganic high-salt industrial wastewater and realizing zero liquid discharge. Background technique [0002] The statements in this section merely provide background information related to the present disclosure and may not constitute prior art. [0003] In prior art industrial production, after reverse osmosis treatment of inorganic waste water, clear water is reused as reclaimed water, concentrated water is hard to use due to the increase of dissolved solids, and most of the current industrial production can only be done according to environmental protection indicators. After reaching the standard, it is discharged to the environmental water body. With the continuous improvement of environmental protection requirements, "zero liquid discharge" has become an inevitable trend. Therefore, how to treat and utilize high-salt wastewater ...

Claims

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Application Information

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IPC IPC(8): C02F9/04
CPCC02F9/00C02F1/001C02F1/441C02F1/444C02F1/50C02F1/52C02F1/66C02F5/02C02F5/06C02F2301/08
Inventor 赵驰峰张红兵薛卫东潘文平罗红陈晓林何旭东梁寅祥张庆潘青军李金凤康永
Owner SHAANXI JINTAI CHLOR ALKALI CHEM CO LTD
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