Method for recycling tungsten in liquids after tungsten smelting exchanges

A recovery method, scheelite technology, applied in chemical instruments and methods, metallurgical wastewater treatment, process efficiency improvement, etc., can solve problems such as unsatisfactory use effect, incomplete tungsten precipitation, incomplete tungsten precipitation, etc., and achieve cost saving , The effect of low recycling process cost and mature technology

Inactive Publication Date: 2013-02-06
ZHONGXIANG TUNGSTEN IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] 1. Precipitation method, calcium chloride artificial scheelite precipitation method; this process usually uses calcium chloride as a precipitant, and supplemented with sodium hydroxide to adjust the pH value. This method is commonly used in the recovery of tungsten from ammonium paratungstate crystallization mother liquor. This method In practical applications, it is generally reflected that the precipitation of tungsten is not complete, and the content of tungsten in the liquid after precipitation is still in the range of 100-200mg / L. Incomplete tungsten precipitation
[0005] 2. Ion exchange method. This process usually uses acid to lower the pH value first, and then adsorbs tungsten through a large-pore resin. The desorption solution uses a strong alkali solution, and sodium tungstate is returned to the main process. The recovery rate of this process is It is relatively high and has been vigorously promoted and applied. The disadvantage is that the process is relatively long
[0006] In addition to these two processes, there are residual alkali decomposition method and special reagent selective precipitation method. These methods are also unsatisfactory in actual production and application.

Method used

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  • Method for recycling tungsten in liquids after tungsten smelting exchanges

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] After exchange, the liquid contains 150mg / L tungsten trioxide, the volume of the solution is 500mL, and the initial pH of the solution is 13-14. When the pH value is adjusted to 8 by sulfuric acid, add 10mL of the crystallization mother liquor containing 40g / L of calcium ions to treat the liquid, and the reaction temperature The temperature is 70°C-80°C, fully stirred for more than one hour, the concentration of tungsten at the end of the reaction is 5mg / L, and the content of scheelite precipitated tungsten trioxide is 66.56%.

Embodiment 2

[0024] The solution after exchange contains 150mg / L of tungsten trioxide, the volume of the solution is 500mL, the initial pH of the solution is 13-14, when the pH value is adjusted to 9 by sulfuric acid, add 10mL of the crystallization mother liquor containing 40g / L of calcium ions to treat the solution, and the reaction temperature The temperature is 70°C-80°C, fully stirred for more than one hour, the concentration of tungsten at the end of the reaction is 8mg / L, and the content of scheelite precipitated tungsten trioxide is 65.32%.

Embodiment 3

[0026] The solution after exchange contains 150mg / L tungsten trioxide, the volume of the solution is 500mL, and the initial pH of the solution is 13-14. When the pH value is adjusted to 10 by sulfuric acid, add 10mL of the crystallization mother solution containing 40g / L of calcium ions to treat the solution, and the reaction temperature The temperature is 70°C-80°C, fully stirred for more than one hour, the concentration of tungsten at the end of the reaction is 10mg / L, and the content of scheelite precipitated tungsten trioxide is 64.81%.

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Abstract

The invention discloses a method for recycling tungsten in liquids after tungsten smelting exchanges. The method includes pH of liquids after exchanges is regulated to 8 to 10 by using sulfuric acids; calcium in liquids after a mother liquor is crystallized by using ammonium tungstate (APT) in calcium oxide or calcium hydroxide with tungsten and ammonia recycled to serve as a precipitating agent for precipitating tungsten, and a temperature of a reaction process is raised to 70 DEG C to 80 DEG C; the mixture is mixed fully to form scheelite precipitation; and filter residues are returned to a press cooking leaching process after filtration, and waste liquids are sent to a wastewater treatment process for treatment. According to the method, a method for recycling tungsten and ammonia in a tungsten smelted APT crystallization mother liquor with the application number of 20110307349.0 is combined, and partial solutions containing calcium chloride serve as precipitant materials for recycling tungsten in liquids after exchanges, accordingly, resources are recycled, salt discharges are reduced, costs for buying calcium chloride material are reduced in terms of economic benefits, and internal circulation is achieved. According to the method recycling tungsten in liquids after tungsten smelting exchanges, the technological process is simple, the tungsten precipitation rate is high, and the economic benefit is good.

Description

technical field [0001] The invention belongs to tungsten hydrometallurgy, in particular to a method for recovering tungsten in liquid after tungsten smelting and exchange. Background technique [0002] my country is a country with abundant tungsten resources and the country with the largest tungsten smelting capacity. Tungsten resources mainly exist in the form of wolframite and scheelite. With the decreasing amount of wolframite resources, mining scheelite resources has become the main mineral variety of tungsten resource mining. Therefore, the smelting technology of scheelite has also been vigorously developed. Ascension, technical process is further improved and mature. High alkaline pressure leaching of scheelite concentrate - ion exchange process has become the main process of tungsten smelting in my country. As the awareness of resource scarcity has been widely recognized, it has become a consensus to carry out comprehensive recycling of resources. Therefore, most tu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/42C22B3/44C02F1/00C02F1/62C22B34/36C02F101/20C02F103/16
CPCY02P10/20
Inventor 李义兵王小军邓波王战斌刘开忠
Owner ZHONGXIANG TUNGSTEN IND
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