Method for leaching and separating bismuth from blast furnace gas dust or/and mud

A blast furnace gas ash and leaching technology, which is applied to the field of leaching and separating bismuth from blast furnace gas ash or/and mud, can solve the problems of increasing the difficulty of purification and separation of bismuth compounds, waste of valuable resources, and low recovery rate, etc., to achieve The effect of high bismuth leaching rate, high selection efficiency and simple process

Pending Publication Date: 2021-08-24
XIANGTAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method can recover part of bismuth, but in addition to containing a small amount of bismuth compounds in the obtained leachate, it also contains a large amount of valuable impurity metals such as iron, lead, and zinc that have not been recycled, thus causing a waste of various valuable resources. At the same time, the existence of these impurity metals also increases the difficulty of purification and separation of bismuth compounds in the subsequent leaching solution, and some bismuth that is difficult to dissolve in the form of bismuth oxide and bismuth sulfide has not been leached, resulting in a low recovery rate of bismuth.

Method used

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  • Method for leaching and separating bismuth from blast furnace gas dust or/and mud
  • Method for leaching and separating bismuth from blast furnace gas dust or/and mud
  • Method for leaching and separating bismuth from blast furnace gas dust or/and mud

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] (1) The quaternary ammonium salt and oxalic acid are formulated into an oxalic acid-based deep eutectic solvent according to a molar ratio of 1:1.

[0028] (2) Add blast furnace gas ash or / and mud (with a bismuth content of 1.56wt%) to the oxalic acid-based deep eutectic solvent prepared in step (1) according to the solid-to-liquid mass ratio of 1:10, at 50°C Stir and leach for 20 hours, and obtain leachate and reaction residue through solid-liquid separation.

[0029] (3) Add 1mol / l NaOH solution to the leachate obtained in step (2) to adjust the pH of the leachate to 1.50, stir evenly and let stand for 1 hour to obtain a filter residue rich in zinc oxalate and a hydrolyzate through solid-liquid separation.

[0030] (4) The filter residue obtained in step (3) was washed and filtered with magnesium sulfate solution, and dried at 70° C. to obtain a zinc oxalate by-product with a purity of 99.34%.

[0031] (5) The hydrolyzate obtained in step (3) was irradiated with the ...

Embodiment 2

[0033] (1) The quaternary ammonium salt and oxalic acid are formulated into an oxalic acid-based deep eutectic solvent according to a molar ratio of 1:1.

[0034] (2) Add blast furnace gas ash or / and mud (with a bismuth content of 1.36wt%) to the oxalic acid-based deep eutectic solvent prepared in step (1) according to the solid-to-liquid mass ratio of 1:10, at 50°C Stir and leach for 20 hours, and obtain leachate and reaction residue through solid-liquid separation.

[0035] (3) Add 1mol / l NaOH solution to the leachate obtained in step (2) to adjust the pH of the leachate to 1.50, stir evenly and let stand for 1 hour to obtain a filter residue rich in zinc oxalate and a hydrolyzate through solid-liquid separation.

[0036] (4) The filter residue obtained in step (3) was washed and filtered with magnesium sulfate solution, and dried at 70° C. to obtain a zinc oxalate by-product with a purity of 99.66%.

[0037] (5) The hydrolyzate obtained in step (3) was irradiated with the ...

Embodiment 3

[0039] (1) The quaternary ammonium salt and oxalic acid are formulated into an oxalic acid-based deep eutectic solvent according to a molar ratio of 1:1.

[0040] (2) Add blast furnace gas ash or / and mud (with a bismuth content of 1.36wt%) to the oxalic acid-based deep eutectic solvent prepared in step (1) according to the solid-to-liquid mass ratio of 1:5, at 50°C Stir and leach for 20 hours, and obtain leachate and reaction residue through solid-liquid separation.

[0041] (3) Add 1 mol / l NaOH solution to the leachate obtained in step (2) to adjust the pH of the leachate to 1.50, stir evenly and let stand for 1 hour, and obtain a filter residue rich in zinc oxalate and a hydrolyzate through solid-liquid separation.

[0042] (4) Wash and filter the filter residue obtained in step (3) with magnesium sulfate solution, and dry at 70° C. to obtain a zinc oxalate by-product with a purity of 99.09%.

[0043](5) The hydrolyzate obtained in step (3) was irradiated with the ultraviol...

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Abstract

The invention discloses a method for leaching and separating bismuth from blast furnace gas dust or/and mud. The method comprises the following steps: firstly, stirring and leaching blast furnace gas dust or/and mud according to a solid-liquid mass ratio of 1: (1-20) by using an oxalic acid-based eutectic solvent as a leaching agent to obtain a leachate and reaction residues; adjusting the pH value of the leachate by using a NaOH solution, uniformly stirring, standing to form zinc oxalate precipitate, carrying out solid-liquid separation to obtain precipitate and hydrolysate, washing and drying the precipitate to obtain a zinc oxalate byproduct, irradiating the hydrolysate by using an ultraviolet light source to enable an iron element in the hydrolysate to generate light-induced reduction reaction to form ferric oxalate precipitate, and filtering to obtain a ferric oxalate byproduct, wherein the filtrate is a high-purity bismuth-containing solution. According to the method, the high-purity bismuth-containing solution can be selectively separated from the blast furnace gas dust or/and mud so as to be used for producing a bismuth-containing compound with a high additional value, the process is simple, the leaching separation selectivity of the bismuth element is high, and the recycled product and the byproduct are good in economical efficiency.

Description

technical field [0001] The invention relates to the technical field of hydrometallurgy, in particular to a method for leaching and separating bismuth from blast furnace gas ash or / and mud. Background technique [0002] Blast furnace gas ash or / and mud is solid dust or / and wet mud obtained from fine particles along with blast furnace gas in the top of the furnace through dry or wet dust removal during the blast furnace smelting process. The chemical composition of blast furnace gas ash or / and mud is relatively complex. In addition to mainly iron, unburned carbon, aluminum and silicon oxides, it also contains a small amount of non-ferrous metal oxides such as Pb, Zn and Bi with low boiling points. Blast furnace gas ash and / or mud are generally considered to be difficult to use or have little value in use, and currently they are mainly treated or disposed of by stockpiling or landfilling. Due to the strong toxicity of the heavy metals contained in it, it is easy to cause a gre...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B30/06C22B7/02C22B3/16C22B3/44C07C55/07C07C51/41
CPCC22B30/06C22B3/16C22B3/44C22B7/007C22B7/02C07C55/07C07C51/41Y02P10/20
Inventor 杨运泉何倩乔志强杨涛李正科李文松王威燕黄艳平刘文英
Owner XIANGTAN UNIV
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