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Harmless disposal method of waste incineration fly ash

A waste incineration fly ash and disposal method technology, applied to chemical instruments and methods, solid waste removal, transportation and packaging, etc., can solve the problem of increased chloride ion concentration at the kiln tail, difficulty in recovering cement from chloride salts, and overcapacity of cement and other problems, to achieve the effect of comprehensive treatment with low operating cost, obvious weight reduction rate, and no secondary environmental pollution

Inactive Publication Date: 2017-07-21
CHANGAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] With the improvement of people's living standards and environmental awareness, the chemical composition of waste incineration fly ash has also undergone significant changes. The prominent features are high salt content and high calcium oxide content, which makes traditional melting technology encounter difficulties. Without the addition of co-solvent, the melting temperature of waste incineration fly ash exceeds 1500°C, coupled with secondary fly ash treatment, extremely high energy consumption, unprecedented technical difficulties in the melting process
However, even if the sintering technology is adopted, the sintering temperature is very high, and the salt in the fly ash directly affects the quality of the sintered product. Water washing and desalting treatment is required before sintering, which increases the cost and complicates the process, and the risk of heavy metal leaching of the sintered product still exists
[0007] With the cement mixed firing process after washing, the cement production capacity is excessive, the amount of cement clinker fired is small, the concentration of chloride ions at the kiln tail increases, and the hidden danger of the kiln tail preheater skinning increases, and many technologies such as chloride salt recovery, filter hardening, etc. Problems make cement blending also face many difficulties
[0008] Separation of heavy metals and decomposition of dioxins are the key technologies for the harmlessness of waste incineration fly ash. The lack of economical and effective technical methods is a prominent problem at home and abroad.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The test results of heavy metal leaching concentration in fly ash of a waste incineration plant are shown in Table 1. It can be seen that Cd and Pb seriously exceed the standard and belong to hazardous waste.

[0026] Table 1 Comparison of the leaching concentration of heavy metals in the original fly ash and the national standard

[0027]

[0028]

[0029] refer to figure 1 100 grams of waste incineration fly ash and 6 grams of molten salt additive calcium chloride were added to molten sodium chloride at 850 ° C for 3 hours to react. Discharge and settle at the bottom of molten sodium chloride, collect the fly ash and molten salt slag at the bottom and bury it, generate volatile gas during the reaction, collect the heavy metals through condensation, and discharge the rest of the gas;

[0030] The heavy metal leaching concentration of the fly ash molten salt slag is measured in Table 2 below, from which it can be seen that the fly ash molten salt slag has fully m...

Embodiment 2

[0034] Add 100 grams of waste incineration fly ash, 5 grams of fly ash additive silica fume, and 8 grams of molten salt additive calcium chloride into 900°C sodium chloride molten salt for 3 hours of reaction. The fly ash and molten salt slag generated during the reaction It is discharged from the molten sodium chloride and precipitated at the bottom of the molten sodium chloride, and the fly ash molten salt slag at the bottom is collected and then buried. The volatile gas generated during the reaction is collected by condensation to collect the heavy metals, and the rest of the gas is discharged;

[0035] The heavy metal leaching concentration of the fly ash molten salt slag is measured in Table 3 below. It can be seen from the table that the fly ash molten salt slag fully meets the pollutant control index requirements of the domestic waste landfill.

[0036] Table 3 Comparison of the leaching concentration of heavy metal ions after molten salt reaction treatment with the orig...

Embodiment 3

[0039] Add 100 grams of waste incineration fly ash, 10 grams of fly ash additive fly ash, and 5 grams of melt additive calcium chloride into molten sodium chloride salt at 1000 ° C for 1 hour, and the fly ash molten salt generated during the reaction The slag is discharged from the molten sodium chloride and precipitated at the bottom of the molten sodium chloride. The fly ash molten salt slag at the bottom is collected and then buried. The volatile gas generated during the reaction is collected by condensation to collect the heavy metals, and the rest of the gas is discharged. ;

[0040] The leaching concentration of heavy metals in fly ash molten salt slag is shown in Table 4 below, from which it can be seen that fly ash molten salt slag has fully met the requirements of pollutant control indicators for domestic waste landfills.

[0041] Table 4 Comparison of leaching concentration of heavy metal ions after molten salt reaction treatment with original fly ash and national st...

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Abstract

The invention relates to a harmless disposal method of waste incineration fly ash. The method comprises the steps that the waste incineration fly ash is added into molten-state sodium chloride to react, and fly ash molten salt residues and volatile gas are generated in the reaction process; the fly ash molten salt residues generated in the reaction process are sedimentated to the bottom of the molten-state sodium chloride from the molten-state sodium chloride, and the fly ash molten salt residues at the bottom are collected and then subjected to landfilling; heavy metal in the volatile gas generated in the reaction process is collected through condensation, and the rest of gas is discharged; and a molten salt auxiliary is added into the waste incineration fly ash. The disposal method is simple in process, the size of fly ash is reduced by 50%, the weight of the fly ash molten salt residues is reduced by 50%, and the volume reduction rate of the size and weight is remarkable.

Description

technical field [0001] The invention belongs to the field of environmental protection for the disposal and comprehensive utilization of hazardous solid waste, in particular to a harmless disposal method for waste incineration fly ash. Background technique [0002] There are many disposal techniques for traditional waste incineration fly ash. Specifically, it is divided into four categories: separation and extraction technology; heat treatment technology, solidification and stabilization technology and other technologies. However, none of them can meet the actual requirements of recycling, harmlessness, reduction, economical rationality, safety and high efficiency at the same time. [0003] Solidification and stabilization technology not only increases capacity, but also the price of solidification and stabilization materials is high, and the comprehensive cost of landfill storage is also high; [0004] Separation and extraction technology is complex, expensive equipment an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B09B3/00B09B5/00
CPCB09B3/00B09B5/00B09B2101/30B09B3/20
Inventor 赵鹏景明海郭术光张慧荣赵玉彬
Owner CHANGAN UNIV
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