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Treatment method of cyanogen-containing waste residue

A treatment method and technology of waste residue, which is applied in the field of dangerous goods treatment, can solve the problem that the stabilization and solidification of soluble salt cyanide-containing waste residue cannot be fundamentally solved, the problem of high-salt cyanide-containing waste residue solidification has not been completely solved, and hydrogen cyanide gas overflows and other problems, to achieve the effect of being conducive to operation and construction, uniform in size and sufficient oxidation reaction

Active Publication Date: 2014-10-01
扬州杰嘉工业固废处置有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For cyanide-containing waste residues with high soluble salt content, if the alkaline oxidation method is used, the method needs to adjust the pH twice, and the second time needs to add acid to adjust the pH to 8-9, and once the acid is added excessively or locally excessively to cause pH If it is less than 7, it will directly cause hydrogen cyanide gas to overflow, which will cause danger to operators. This method has high requirements for operation; in addition, it is difficult to mix chlorine gas with all cyanide ions into the waste residue, and it is easy to cause insufficient reaction. In addition, this method does not completely solve the problem of solidification of high-salt cyanide-containing waste residues, and high soluble salts exist in waste residues that have not been solidified; if the bleaching powder oxidation method is used, this method also has the problem that soluble salts have not been processed problem, unable to fundamentally solve the problem of stabilization and solidification of cyanide-containing waste residue with high soluble salt content

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1)

[0022] The cyanide-containing waste residue treated in this embodiment comes from the cyanate ester resin production workshop, and is measured according to HJ / T 299-2007 "Solid Waste Leaching Toxic Leaching Method Sulfuric Acid Nitric Acid Method" and GB_T 15555.12-1995 "Solid Waste Corrosion Determination Glass Electrode Method" The pH value of the waste residue leachate was 9.59; according to HJ / T 299-2007 "Solid Waste Leaching Toxicity Leaching Method Sulfuric Acid Nitric Acid Method" and HJ 484-2009 "The Determination Volumetric Method and Spectrophotometry of Water Cyanide" measured the waste residue leachate The content of cyanide is 97ppm; the content of sodium chloride in waste residue is 85%.

[0023] The processing method of the cyanogen-containing waste residue of the present embodiment may further comprise the steps:

[0024] ① Alkali adjustment. Transfer 20 g of cyanide-containing waste residue to be treated into a stirred reactor, and add 2 g of slaked lime powd...

Embodiment 2)

[0032] The cyanide-containing waste residue treated in this example comes from the cyanide-containing electroplating workshop, and the waste residue is measured according to HJ / T 299-2007 "Solid Waste Leaching Toxic Leaching Method Sulfuric Acid Nitric Acid Method" and GB_T 15555.12-1995 "Solid Waste Corrosion Determination Glass Electrode Method" The pH value of the leachate is 9.23; according to HJ / T 299-2007 "Solid Waste Leaching Toxicity Leaching Method Sulfuric Acid Nitric Acid Method" and HJ 484-2009 "Determination of Cyanide in Water by Volumetric Method and Spectrophotometric Method", the cyanide in the waste residue leachate was measured The content of the salt is 78ppm; the soluble salt content in the waste residue is 90%.

[0033] All the other are the same as embodiment 1 of the processing method of the cyanogen-containing waste residue of the present embodiment, difference is:

[0034] Step ① After alkali adjustment, according to HJ / T 299-2007 "Solid waste leachin...

Embodiment 3)

[0039] The cyanogen-containing waste residue that present embodiment handles is identical with embodiment 2.

[0040] All the other are the same as embodiment 1 of the processing method of the cyanogen-containing waste residue of the present embodiment, difference is:

[0041] Step ① After alkali adjustment, according to HJ / T 299-2007 "Solid waste leaching toxicity leaching method - sulfuric acid nitric acid method" and GB_T 15555.12-1995 "Solid waste Corrosivity determination - Glass electrode method", the pH value of the waste residue leachate is 10.12.

[0042] In step ②, add 10 mL of chlorine dioxide aqueous solution to the stirring reaction kettle under stirring state, and the chlorine dioxide content in the chlorine dioxide aqueous solution is 3% (calculated as steady-state chlorine dioxide). The mass ratio of the amount of chlorine dioxide aqueous solution added to the cyanide-containing waste residue to be treated in step 1 is 0.5-1:1 (0.5:1 in this embodiment).

[00...

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Abstract

The invention discloses a treatment method of cyanogen-containing waste residue. The method comprises the steps of (1) adjusting alkali, wherein the pH value of the leachate of the waste residue after alkali is adjusted is 10-13; (2) breaking cyanogen, feeding a chlorine-containing cyanogen-breaking reagent into a stirring reaction kettle in a stirring state; (3) pelleting, feeding slaked lime powder and calcined gypsum powder into the material obtained after the cyanogen-breaking reaction in the step (2) in a stirring state, and mixing to enable the material in the stirring reaction kettle to form uniform spherical particles; and (4) drying and curing, naturally drying the particles in the stirring reaction kettle for 1-2 days after pelleting in the step (3), and curing. According to the method, cyanogen is broken by a chlorination process under the alkaline condition, so that the cyanide removal effect is good; after the oxidation reaction of the cyanide is finished, the salinity is cured in the particles instead of entering a waste water system; during stirring, two-section frequency is applied, so that the formed particles are even in sizes; during pelleting, gypsum is fed, so that the strength of the particles is greatly improved, and the construction in a landfill is more easily carried out.

Description

technical field [0001] The invention relates to dangerous goods treatment technology, in particular to a treatment method for cyanide-containing waste residue with high soluble salt content. Background technique [0002] The toxicity of cyanide to the human body is mainly due to its combination with ferric cytochrome oxidase to generate ferric cyanide cytochrome oxidase and lose the function of transferring oxygen, causing tissue hypoxia asphyxia. When the cyanide content in the water reaches 0.01 mg / L, it is not suitable for drinking water; when it reaches 0.03 mg / L, it has acute poisoning effect on fish. The maximum allowable concentration of cyanide in my country's surface water environmental quality standards is 0.1 mg / L. [0003] At present, there are many literature reports on the treatment of cyanide-containing wastewater. The widely used treatment methods for cyanide-containing wastewater include: chlorination method, air stripping method, sulfur dioxide-air oxidati...

Claims

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Application Information

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IPC IPC(8): B09B3/00B09B5/00
Inventor 刘维桥仲鹏鹏樊红杰岳喜龙尚通明周书利
Owner 扬州杰嘉工业固废处置有限公司
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