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Method for recovering tungsten from waste apt powder

A technology of crude sodium tungstate and ammonia distillation, which is applied in the field of tungsten smelting and production, can solve the problems of high processing cost, poor economic practicability, and increased production costs of enterprises, and achieve the goals of improving recovery rate, low production cost, and reducing consumption Effect

Active Publication Date: 2021-09-03
CNMC GUANGXI PGMA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, tungsten smelting manufacturers mainly use rotary calciner to burn tungsten trioxide at high temperature, add alkali to dissolve and return to the main process for waste APT treatment. The cost of the treatment process is high, which increases the production cost of the enterprise, and the economical practicability is poor.

Method used

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  • Method for recovering tungsten from waste apt powder

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Effect test

Embodiment 1

[0050] Such as figure 1 Shown, the present invention provides a kind of method that reclaims tungsten from waste APT powder, and it comprises the following steps:

[0051] Step 1. Pump the crude sodium tungstate solution into the ammonia distillation kettle, stir at a stirring speed of 30r / min and raise the temperature to 85°C. The crude sodium tungstate solution here is the concentrated material; the volume of the added volume of the crude sodium tungstate solution is 50% of the internal volume of the ammonia distillation kettle, the tungsten concentration in the crude sodium tungstate solution is 100g / L, and the alkali concentration is 100g / L, wherein the alkali concentration is lower than 100g / L L, can be made up to 100g / L by adding additional solids (such as alkali sodium hydroxide);

[0052] Step 2. Add waste APT powder (APT is the abbreviation of ammonium paratungstate) to the ammonia distillation kettle, adjust the stirring speed to 50r / min, continue stirring for 2 hou...

Embodiment 2

[0057] Such as figure 1 Shown, the present invention provides a kind of method that reclaims tungsten from waste APT powder, and it comprises the following steps:

[0058] Step 1. Pump the crude sodium tungstate solution into the ammonia distillation kettle, stir and raise the temperature to 85°C at a stirring speed of 30r / min. material; the volume of the added volume of the crude sodium tungstate solution is 60% of the internal volume of the ammonia distillation kettle, the tungsten concentration in the crude sodium tungstate solution is 150g / L, and the alkali concentration is 120g / L, wherein the alkali concentration is lower than 120g / L L, can be made up to 120g / L by adding additional solids (such as alkali sodium hydroxide);

[0059] Step 2. Add waste APT powder (APT is the abbreviation of ammonium paratungstate) to the ammonia distillation kettle, adjust the stirring speed to 60r / min, continue stirring for 2 hours, then add hydrogen peroxide to the ammonia distillation ke...

Embodiment 3

[0064] Such as figure 1 Shown, the present invention provides a kind of method that reclaims tungsten from waste APT powder, and it comprises the following steps:

[0065] Step 1. Pump the crude sodium tungstate solution into the ammonia distillation kettle, stir at a stirring speed of 30r / min and raise the temperature to 85°C. The crude sodium tungstate solution here is the concentrated material; the volume of the added volume of the crude sodium tungstate solution is 55% of the internal volume of the ammonia distillation kettle, the tungsten concentration in the crude sodium tungstate solution is 125g / L, and the alkali concentration is 110g / L, wherein the alkali concentration is lower than 110g / L L, can be made up to 110g / L by adding additional solids (such as alkali sodium hydroxide);

[0066] Step 2. Add waste APT powder (APT is the abbreviation of ammonium paratungstate) to the ammonia distillation kettle, adjust the stirring speed to 55r / min, continue stirring for 2 hou...

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Abstract

The invention discloses a method for recovering tungsten from waste APT powder, which comprises the following steps: step 1, pump crude sodium tungstate solution into an ammonia distillation kettle, and heat up to 85°C under stirring; step 2, waste APT Add the powder into the ammonia distillation kettle, continue to stir for 2 hours, then add hydrogen peroxide to the ammonia distillation kettle to remove sulfur; step 3, raise the internal temperature of the ammonia distillation kettle to 95-100°C, keep stirring for 8 hours, then stop heating, and collect steamed ammonia during the The ammonia gas at the top of the still is sprayed with hydrochloric acid to recover the ammonia gas; step 4, filter the mixed liquid in the ammonia still, and the collected filtrate is the recovered sodium tungstate solution. The process of the invention is simple in operation, low in energy consumption, low in production cost, and easy to realize recovery of tungsten from waste APT powder.

Description

technical field [0001] The invention relates to the field of tungsten smelting production. More specifically, the present invention relates to a method for recovering tungsten from waste APT powder. Background technique [0002] As we all know, tungsten ore is a non-renewable resource, but the secondary resource of tungsten can be recycled. As a refractory rare metal, tungsten is widely used in military, electronics, metallurgy, petrochemical and other important industrial fields because of its unique physical and chemical properties. Many countries in the world regard tungsten as an important strategic Metal. At present, in the secondary resource recovery of tungsten, tungsten is mainly recovered from tungsten leaching slag, molybdenum removal precipitation slag, tungsten-containing alloy waste, APT waste powder and other waste materials. However, the main source of APT waste powder is the rice crust produced by the crystallization and drying of ammonium paratungstate, t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B34/36C22B1/11C22B7/00C01C1/10C01C1/02C01C1/16B01D53/81B01D53/52
CPCB01D53/52B01D53/81C01C1/024C01C1/10C01C1/164C22B1/11C22B7/006C22B34/36Y02P10/20
Inventor 谢泉文
Owner CNMC GUANGXI PGMA