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Method for separating tantalum and hafnium in tantalum-hafnium alloy slag

A technology of alloy slag and tantalum and hafnium, which is applied in the field of hydrometallurgy, can solve the problems of resource waste, environmental pollution, and failure to meet domestic smelting needs, and achieve the effect of good environmental protection and high separation efficiency

Active Publication Date: 2015-08-19
NORTHWEST INSTITUTE FOR NON-FERROUS METAL RESEARCH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although China's tantalum and hafnium resources have certain reserves, but limited by factors such as grade, mining cost and mining technology, the annual domestic production of tantalum and hafnium is far from meeting domestic smelting needs. As a strategic reserve metal, the import of tantalum and hafnium is easily affected by the international situation. , and high-temperature alloy waste contains a considerable amount of valuable metal elements, if these valuable metal elements can be recovered, it will be of great significance for the utilization and application of strategic metals. For example, a patent containing tantalum is disclosed in CN 103834815 A A method for separating tungsten and tantalum from tungsten-rich slag, which separates tungsten and tantalum through the process of mixing sodium carbonate, sodium hydroxide and tantalum-containing tungsten-rich slag, roasting and water immersion, and the separation effect is better. In addition, conventional The separation process of acid leaching treatment and roasting-water leaching treatment can recycle the valuable metals such as nickel, cobalt, tungsten and molybdenum in superalloy waste, and there is still a certain amount of tantalum and hafnium in the remaining alloy slag. Most of the tantalum and hafnium alloy slags are degraded and processed, resulting in waste of resources and environmental pollution. If the tantalum and hafnium can be recycled, it can not only make up for our country's foreign dependence on tantalum and hafnium resources, protect our country's strategic needs, but also provide more tantalum and hafnium for our country Hafnium reserve

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] This embodiment includes the following steps:

[0022] Step 1. Mix sodium carbonate and tantalum-hafnium alloy slag uniformly to obtain roasting raw materials; the sum of mass content of tantalum sulfide, tantalum nitride and tantalum pentoxide in the tantalum-hafnium alloy slag is 37.81%, and the tantalum-hafnium alloy slag The sum of the mass content of hafnium disulfide, hafnium nitride and hafnium oxide is 6.06%; the mass ratio of the tantalum-hafnium alloy slag and sodium carbonate is 1:0.7;

[0023] Step 2. Roast the roasted raw material in step 1 at a temperature of 1000° C. under an oxygen atmosphere for 1.5 hours to obtain a roasted product. After the roasted product is cooled, place it in concentrated sulfuric acid and heat it under stirring Insulate at 50°C for 2 hours to obtain a solid-liquid mixture; in the solid-liquid mixture, hafnium is enriched in the liquid phase, and tantalum is enriched in the solid phase; the ratio of the volume of the concentrated ...

Embodiment 2

[0030] This embodiment includes the following steps:

[0031] Step 1. Mix sodium carbonate and tantalum-hafnium alloy slag evenly to obtain roasting raw materials; the sum of mass content of tantalum sulfide, tantalum nitride and tantalum pentoxide in the tantalum-hafnium alloy slag is 41.15%, and the tantalum-hafnium alloy slag The sum of the mass contents of hafnium disulfide, hafnium nitride and hafnium oxide is 10.16%, and the mass ratio of the tantalum-hafnium alloy slag and sodium carbonate is 1:0.9;

[0032] Step 2. Roasting the raw materials described in step 1 at a temperature of 1100° C. under an oxygen atmosphere for 3 hours to obtain a roasted product. After the roasted product is cooled, place it in concentrated sulfuric acid and heat it to Incubate at 60°C for 1.5h to obtain a solid-liquid mixture; in the solid-liquid mixture, hafnium is enriched in the liquid phase, and tantalum is enriched in the solid phase; the ratio of the volume of the concentrated sulfuric...

Embodiment 3

[0036] This embodiment includes the following steps:

[0037] Step 1. Mix sodium carbonate and tantalum-hafnium alloy slag evenly to obtain roasting raw materials; the mass content of tantalum sulfide, tantalum nitride and tantalum pentoxide in the tantalum-hafnium alloy slag is 24.19%, and the tantalum-hafnium alloy slag contains two The sum of the mass contents of hafnium sulfide, hafnium nitride and hafnium oxide is 11.67%, and the mass ratio of the tantalum-hafnium alloy slag to sodium carbonate is 1:0.8;

[0038] Step 2. Roast the raw materials described in step 1 at a temperature of 1200° C. under an oxygen atmosphere for 3.5 hours to obtain a roasted product. After the roasted product is cooled, place it in concentrated sulfuric acid and heat it under stirring conditions. Incubate at 70°C for 1 hour to obtain a solid-liquid mixture; in the solid-liquid mixture, hafnium is enriched in the liquid phase, and tantalum is enriched in the solid phase; the ratio of the volume ...

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Abstract

The present invention discloses a method for separating tantalum and hafnium in tantalum-hafnium alloy slag. The method comprises: 1, uniformly mixing sodium carbonate and tantalum-hafnium alloy slag to obtain a calcining raw material; 2, calcining the calcining raw material for 1.5-3.5 h at a temperature of 1000-1200 DEG C under an oxygen atmosphere to obtain a calcined product, cooling, placing the cooled calcined product in concentrated sulfuric acid, heating to a temperature of 50-70 DEG C under stirring, and maintaining the temperature for 1-2 h to obtain a solid-liquid mixture; and 3, adding deionized water to the solid-liquid mixture, uniformly stirring, and filtering to obtain the filtrate and the filter residue so as to achieve the tantalum and hafnium separation. According to the present invention, the process that the tantalum-hafnium alloy slag is subjected to sodium carbonate calcination and concentrated sulfuric acid leaching is utilized to achieve the tantalum and hafnium separation purpose, such that the use of hydrofluoric acid is avoided, and advantages of good environmental protection and high separation efficiency are provided.

Description

technical field [0001] The invention belongs to the technical field of hydrometallurgy, and in particular relates to a method for separating tantalum and hafnium from tantalum and hafnium alloy slag. Background technique [0002] Both tantalum and hafnium are strategic metals and are widely used in the defense industry. Although China's tantalum and hafnium resources have certain reserves, but limited by factors such as grade, mining cost and mining technology, the annual domestic production of tantalum and hafnium is far from meeting domestic smelting needs. As a strategic reserve metal, the import of tantalum and hafnium is easily affected by the international situation. , and high-temperature alloy waste contains a considerable amount of valuable metal elements, if these valuable metal elements can be recovered, it will be of great significance for the utilization and application of strategic metals. For example, a patent containing tantalum is disclosed in CN 103834815 A...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/04C22B34/14C22B34/24
CPCY02P10/20
Inventor 张卜升许万祥郭瑞吴永谦马光李进
Owner NORTHWEST INSTITUTE FOR NON-FERROUS METAL RESEARCH
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