Method for recycling noble metal from automobile exhaust catalyst

A technology for precious metal recovery and automobile exhaust gas, which is applied in the field of automobile exhaust catalyst precious metal recovery, can solve the problems such as the inability to recycle the tail liquid and the low recovery rate of precious metals, so as to solve the problems of precious metal recovery and environmental protection, the effect of emission reduction is obvious, and the usage amount is reduced Effect

Active Publication Date: 2015-04-01
UNIV OF SCI & TECH BEIJING +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is to provide a method for recovering precious metals from automobile exhaust catalysts to solve the problems of oil pollution and residual carbon on the recovery of precious metals from automobile exhaust catalysts, low recovery rate of precious metals, and inability to circulate tail liquid. The carbon pretreatment method eliminates the adsorption of waste oil and residual carbon on precious metals; a combination of one-stage acid leaching, two chlorination and alkali conversion processes is proposed to strengthen the leaching of precious metals; the idea of ​​tail liquid regeneration and utilization is proposed to eliminate tail liquid Disposal and secondary pollution; a complete solution to the recovery of precious metals and environmental protection of automobile exhaust catalysts

Method used

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  • Method for recycling noble metal from automobile exhaust catalyst

Examples

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Effect test

Embodiment 1

[0025] Put the automobile exhaust catalyst into the oil removal and decarbonization device for oil removal and decarbonization. The oil decarbonization device equipped with the automobile exhaust catalyst is first heated to 110°C, vacuumed to 250Pa, and kept for 30 minutes to perform oil removal treatment. Then raise the temperature of the oil removal and decarbonization device to 350°C, fill it with pure oxygen, keep it warm for 10 minutes, and carry out decarbonization treatment; the material after oil removal and decarbonization is finely ground to -80 mesh, and the finely ground powder is 98% The concentration of industrial concentrated sulfuric acid is 150Kg / m 3 Acid leaching is carried out in the solution, the liquid-solid ratio is 3:1, the acid leaching temperature is 50°C, the acid leaching time is 0.5 hours, and acid leaching is filtered to obtain acid leaching liquid and acid leaching residue; acid leaching residue is mixed with sodium chloride, chloric acid Carry ou...

Embodiment 2

[0027] Put the automobile exhaust catalyst into the oil removal and decarbonization device for oil removal and decarbonization. The oil decarbonization device equipped with the automobile exhaust catalyst is first heated up to 200°C, vacuumed to a pressure of 150Pa, and kept for 60 minutes to perform oil removal treatment. Then heat up the oil removal and decarbonization device to 450°C, fill it with pure oxygen, keep it warm for 30 minutes, and carry out decarburization treatment; the material after oil removal and decarbonization is finely ground to -80 mesh, and the finely ground powder is at 98% The concentration of industrial concentrated sulfuric acid is 250Kg / m 3 Acid leaching is carried out in the solution, the liquid-solid ratio is 5:1, the acid leaching temperature is 90°C, and the acid leaching time is 2 hours. The acid leaching solution and acid leaching residue are obtained by acid leaching filtration; Carry out primary chlorination in the solution of sodium and s...

Embodiment 3

[0029] Put the automobile exhaust catalyst into the oil removal and decarbonization device for oil removal and decarbonization. The oil decarburization device equipped with the automobile exhaust catalyst is first heated to 150°C, vacuumed to a pressure of 200Pa, and kept for 40 minutes to perform oil removal treatment. Then heat up the oil removal and decarbonization device to 400°C, fill it with pure oxygen, keep it warm for 20 minutes, and perform decarburization treatment; The concentration of industrial concentrated sulfuric acid is 200Kg / m 3 Acid leaching is carried out in the solution, the liquid-solid ratio is 4:1, the acid leaching temperature is 60 ° C, the acid leaching time is 1 hour, and the acid leaching is filtered to obtain the acid leaching solution and acid leaching residue; Carry out primary chlorination in the solution of sodium and sulfuric acid to obtain primary chlorination slag and primary chlorination solution, wherein the concentration of sodium chlor...

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Abstract

The invention provides a method for recycling noble metal from an automobile exhaust catalyst, and belongs to the technical field of resource recycling. The method comprises the following steps: deoiling and decarbonizing the automobile exhaust catalyst, finely pulverizing, and carrying out acid leaching; carrying out primary chlorination on acid leaching residues in a solution of sodium chloride, sodium chlorate and sulfuric acid; mixing primary chlorination residues with sodium peroxide, carrying out water leaching on an alkaline transfer residue, carrying out secondary chlorination on a water leaching residue; mixing primary chlorination liquid with secondary chlorination liquid, and replacing with Fe powder, so as to obtain a displacement liquid and precious metal ore concentrate; mixing an acid leaching liquid, the water leaching liquid and the replacement liquid, and carrying out neutralization-oxidization; and adding calcium chloride to a neutralization liquid, carrying out desulphuration treatment, and returning a desulphuration liquid to primary chlorination and secondary chlorination procedures by adjusting the amount of sodium chloride, sodium chlorate and sulfuric acid. According to the method disclosed by the invention, noble metal is smoothly leached and recovered; the problems of noble metal recovery and environment protection of the automobile exhaust catalyst are solved; and the method has the characterizes of high adaptability and simple equipment, and is suitable for industrialized production and environmental friendly.

Description

technical field [0001] The invention relates to the technical field of resource recycling, in particular to a method for recycling precious metals of automobile exhaust catalysts. Background technique [0002] Since the 1970s, with the emphasis on environmental protection in developed countries, the control of automobile exhaust pollution has become the focus of improving air quality. Many countries have successively legislated to limit CH in automobile exhaust n , CO, NO and other harmful components. Since the 1990s, the United States, Europe and Japan have continuously increased the requirements for exhaust emission purification. In order to ensure the purification effect, the manufacturers have successively increased the content of platinum group metals in the catalyst. Since my country's reform and opening up, production has developed rapidly, living standards have improved significantly, and automobiles have begun to enter households in large numbers; the demand for r...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B11/00
CPCY02P10/20
Inventor 潘德安张深根刘波郭斌
Owner UNIV OF SCI & TECH BEIJING
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