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Method for extracting vanadium and removing arsenic from arsenic-containing waste sulfuric acid catalyst

A catalyst and sulfuric acid technology, applied in the field of hydrometallurgy, can solve the problems of high energy consumption, ferric sulfate crusting, and high production cost, and achieve the effects of simple process flow, efficient and clean extraction, and short reaction time.

Inactive Publication Date: 2018-01-09
HEBEI IRON AND STEEL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The reasons for sulfuric acid catalyst deactivation are: (1) the impact of water acid mist and mine dust: pure water vapor has little effect on the catalyst, but if mixed with SO 3 Combined to generate acid mist, and then interact with mine dust to generate iron sulfate and crust, increasing ventilation resistance
(2) The influence of arsenic and fluorine: the high content of arsenic in the furnace gas can poison the catalyst and reduce the activity
However, this invention uses electrochemical precipitation to remove arsenic, which has high energy consumption and high production costs.
[0006] In order to extract vanadium and remove arsenic from waste sulfuric acid catalysts, people have done a lot of research. However, the existing technology for extracting vanadium from spent catalysts has the following problems: high-temperature roasting produces toxic waste gas, strong acid requires high equipment, and arsenic in the leach solution cannot be effectively treated. high production costs

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] 1) Mix the arsenic-containing waste sulfuric acid catalyst ball-milled to 100 μm with a 10% sodium hydroxide solution for hydrothermal reaction. The mass ratio of the sodium hydroxide solution to the arsenic-containing waste sulfuric acid catalyst is 2:1. The reaction temperature is 80°C, the reaction time is 1h, and the stirring speed is 300r / min. The liquid-solid separation of the reacted material is carried out, and the obtained liquid phase is the leachate;

[0031] 2) Removal of arsenic in the leaching solution: add NaOH to the leaching solution to adjust the pH to 12, then add arsenic removing agent polymerized ferrous sulfate in an amount twice the molar amount of arsenic in the leaching solution, mix and stir, and filter to obtain a purified vanadium solution.

[0032] Through detection and calculation, the vanadium recovery rate in this embodiment is 82.35%, and the arsenic removal rate is 98.63%.

Embodiment 2

[0034] 1) Mix the arsenic-containing waste sulfuric acid catalyst ball-milled to 200 μm with a 15% sodium hydroxide solution for hydrothermal reaction, the mass ratio of the sodium hydroxide solution to the arsenic-containing waste sulfuric acid catalyst is 4:1, hydrothermal reaction The reaction temperature is 90°C, the reaction time is 2 hours, and the stirring speed is 500r / min. The liquid-solid separation of the reacted material is carried out, and the obtained liquid phase is the leachate;

[0035] 2) Removal of arsenic in the leaching solution: add NaOH to the leaching solution to adjust the pH to 14, then add arsenic removing agent polymerized ferric sulfate in an amount 10 times the molar amount of arsenic in the leaching solution, mix and stir, and filter to obtain a purified vanadium solution.

[0036] Through detection and calculation, the vanadium recovery rate in this embodiment is 85.68%, and the arsenic removal rate is 99.92%.

Embodiment 3

[0038] 1) Mix the arsenic-containing waste sulfuric acid catalyst ball-milled to 80 μm with 20% sodium carbonate solution for hydrothermal reaction, the mass ratio of sodium carbonate solution to the arsenic-containing waste sulfuric acid catalyst is 5:1, and the hydrothermal reaction temperature The temperature is 70°C, the reaction time is 0.5h, and the stirring speed is 200r / min. The material after the reaction is subjected to liquid-solid separation, and the obtained liquid phase is the leachate;

[0039] 2) Removing arsenic from the leaching solution: adding Na to the leaching solution 2 CO 3 Adjust the pH to 14, then add polyaluminum sulfate, an arsenic removing agent, in an amount 20 times the molar amount of arsenic in the leaching solution, mix and stir, and filter to obtain purified vanadium solution.

[0040] Through detection and calculation, the vanadium recovery rate in this embodiment is 81.23%, and the arsenic removal rate is 98.96%.

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Abstract

The invention provides a method for extracting vanadium and removing arsenic from an arsenic-containing waste sulfuric acid catalyst. The method for extracting vanadium and removing arsenic from the arsenic-containing waste sulfuric acid catalyst comprises the following steps that (1) a hydrothermal reaction is performed, specifically, the pretreated arsenic-containing waste sulfuric acid catalystand an alkaline solution are evenly mixed and subjected to the hydrothermal reaction, liquid-solid separation is conducted on the material obtained after the reaction, and the obtained liquid phase is leachate; and (2) arsenic is removed from the leachate, specifically, an acidifying / alkalizing agent and an arsenic removing agent are added into the leachate of the step (1) to be mixed and stirred, then filtering is conducted, and purified vanadium liquid is obtained. The leachate obtained through the hydrothermal reaction between the arsenic-containing waste sulfuric acid catalyst and a sodium hydroxide solution or a sodium carbonate solution contains a large quantity of arsenic element, the arsenic element in the leachate can be converted into precipitate by adding the arsenic removing agent, and meanwhile impurity elements such as silicon and phosphorus are removed, so that the purpose of clean production is achieved; and the technological process is short, equipment is simple, andindustrialization is easily realized.

Description

technical field [0001] The invention belongs to the technical field of hydrometallurgy, and relates to a method for extracting vanadium and removing arsenic from waste sulfuric acid catalyst containing arsenic. Background technique [0002] Sulfuric acid is a basic chemical raw material, and my country's sulfuric acid output ranks first in the world. Sulfuric acid catalyst is a catalyst used in the production of sulfuric acid, usually containing vanadium pentoxide (V 2 o 5 ) 5% to 10%, which is the main component with catalytic activity. In the production of sulfuric acid, after long-term use and heat damage, the physical structure changes, so that the sulfuric acid catalyst that is aged and loses its activity, does not play a catalytic role and is replaced, is called waste sulfuric acid catalyst. The reasons for sulfuric acid catalyst deactivation are: (1) the impact of water acid mist and mine dust: pure water vapor has little effect on the catalyst, but if mixed with S...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B34/22
CPCY02P10/20
Inventor 李兰杰赵备备祁健柳朝阳高明磊闫浩王浩宇
Owner HEBEI IRON AND STEEL
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