Fly ash enhanced washing and high-salinity wastewater resource utilization method

A high-salt wastewater and fly ash technology, applied in chemical instruments and methods, water/sewage treatment, solid waste removal, etc., can solve the problems of hindering cement hydration, increasing the number of washing times, and consuming water resources, etc., to achieve reduction The number of times of washing, the effect of strengthening the removal effect, and the effect of reducing the cost of water treatment

Pending Publication Date: 2022-01-21
JIANGXI GAIA ENVIRONMENTAL SCI & TECH CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The technical effects described by this patented method are improved efficiency for removing impurities from waste containing harmful elements such as chromate (CrO3) compounds during flue gas cleanup processes without requiring excessive amounts of chemicals. This results in cleaner exhaust gases with fewer unwanted substances released into environmentally sensitive areas like soil and groundwater.

Problems solved by technology

This patented technical problem addressed in this patents relates to finding ways to dispose excessive amounts of industrial waste generated through combustion processes without causing environmental concerns due to their negative impact on human health caused by certain compounds like mercuric acids, chromium, lead, zinc, cadmia, nickel, manganese, copper, calcium, magnesite, ammonia, cyclooxanes, methane, tars, polycyclic organics, polynuclear arthropods, plasma soluble silicate glass, and various chemicals used throughout industries including manufacturing products. These contaminant particles can enter our environment at different stages of production and may pose threatening risks if they remain untreated permanently. Therefore, there is an urgent need to find solutions to effectively treating them safely while minimizing consumption of valuable natural resources.

Method used

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  • Fly ash enhanced washing and high-salinity wastewater resource utilization method
  • Fly ash enhanced washing and high-salinity wastewater resource utilization method
  • Fly ash enhanced washing and high-salinity wastewater resource utilization method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Example 1, such as figure 1 As shown, it includes the following steps:

[0025] Step 1. Wash the fly ash with water. Mix the fly ash and water according to the solid-to-liquid ratio of 1:4 to prepare a slurry. At the same time, heat the slurry to 50-60°C and put it in a water bath for 30-40 minutes. Slurry is subjected to suction filtration to obtain washing liquid and harmless fly ash;

[0026] Step 2. To precipitate heavy metals, first add an inorganic flocculant to the washing liquid, the mass ratio of the added inorganic flocculant to the heavy metal substances contained in the washing liquid is 1:1.3-1.5, mix and stir evenly , react for 20-30 minutes, then add an organic flocculant, the dosage of the organic flocculant is 30-50 mg / l, mix and stir evenly, react for 20-30 minutes, and use the combination of inorganic-organic flocculant to The heavy metals contained in the washing liquid are flocculated and precipitated, and the solid-liquid separation is performed a

Embodiment 2

[0028] Example 2, such as figure 1 , 2 As shown, it includes the following steps:

[0029] Step 1. Wash the fly ash with water, use multi-stage water bath to heat and wash with water,

[0030] 1) Prepare slurry by mixing fly ash and water at a solid-to-liquid ratio of 1:4, and heat the slurry to 50-60°C and bathe in water for 30-40 minutes;

[0031] 2) Use a suction filter to filter the slurry heated in a water bath in 1) to obtain primary cleaning water and washed fly ash; wherein, the primary cleaning water is reused in 1) for mixing with fly ash to prepare slurry;

[0032] 3) Mix the washed fly ash obtained in 2) with water at a solid-to-liquid ratio of 1:4 to prepare a slurry, and at the same time heat the slurry to 50-60°C and bathe in water for 30-40 minutes;

[0033] 4) Use a suction filter to filter the slurry heated in a water bath in 3) to obtain washing liquid and harmless fly ash;

[0034] Step 2. To precipitate heavy metals, first add an inorganic flocculant to th

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PUM

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Abstract

The invention discloses a fly ash enhanced washing and high-salinity wastewater resource utilization method. According to the fly ash enhanced washing and high-salinity wastewater resource utilization method, firstly, fly ash is subjected to water bath heating washing, the heating temperature ranges from 50 DEG C to 60 DEG C, a large number of soluble anions and heavy metal ions in the fly ash can be efficiently removed through the water bath heating washing mode, most heavy metal is washed out, and washing liquid and harmless fly ash are obtained; heavy metal precipitates in the washing liquid are removed in an inorganic-organic flocculating agent combined mode, purified high-salt water washing liquid and heavy metal precipitates are obtained, and the total heavy metal removal rate in the washing liquid can reach 99%; and the purified high-salinity water washing liquid contains about 6-15 wt% of potassium and sodium salts, the high-salinity water washing liquid is subjected to evaporative crystallization through an MVR evaporator, potassium salts are obtained through cooling crystallization, the potassium salts and mixed salt waste liquid are obtained through centrifugal separation, the mixed salt waste liquid is electrolyzed to obtain the sodium salts, recovery of the potassium salts and the sodium salts is achieved, and the potassium salt vacancy in China can be relieved.

Description

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Claims

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Application Information

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Owner JIANGXI GAIA ENVIRONMENTAL SCI & TECH CO LTD
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