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A method for saving energy and reducing consumption by alkali leaching of scheelite

A scheelite and alkali leaching technology, applied in the field of tungsten hydrometallurgy, can solve the problems of high energy consumption, high energy consumption and low marginal income of alkali recovery, and achieve obvious energy saving, good energy saving effect and low steam consumption. Effect

Active Publication Date: 2017-01-04
GUILIN UNIVERSITY OF TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The process equipment of alkali recovery enterprises in the industry mainly uses jacketed evaporators for evaporation and concentration. The biggest disadvantage of this equipment is that the energy consumption is very high. It is precisely because many enterprises feel that the energy consumption of alkali recovery is high, and the unit cost of alkali recovery is high. The income is low, it is better to use sodium hydroxide directly, so that the popularization and application of alkali recovery process is less

Method used

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  • A method for saving energy and reducing consumption by alkali leaching of scheelite

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] (1) Put 2,000kg of scheelite concentrate with a mass percentage of tungsten trioxide of 50% into the slurry tank after vibrating wet ball milling, add 1 cubic meter of sodium hydroxide solution with a concentration of 450g / L, and then add 15 kg Auxiliary reagent sodium nitrite, add 582kg sodium hydroxide, the amount of alkali is 3 times of the theoretical amount.

[0025] (2) Pump the slurry prepared in step (1) into an unjacketed high-pressure leaching kettle (specially made leaching kettle), and pass 2.0MPa medium and low pressure steam directly into the leaching kettle with an effective volume of 5 cubic meters through the steam pipe. In the jacketless high-pressure leaching kettle, after 25 minutes, the pressure in the jacketless high-pressure leaching kettle reaches 1.6MPa, and the temperature reaches 195°C, then close the steam valve, keep the temperature for 2 hours, and stop the stirring reaction.

[0026](3) Put the unjacketed high-pressure leaching tank in ste...

Embodiment 2

[0031] (1) Put 2000 kg of scheelite concentrate with a mass percentage of tungsten trioxide of 50% into the slurry tank after vibrating wet ball milling, add 1 cubic meter of sodium hydroxide solution with a concentration of 450g / L, and then add 18 kg auxiliary reagent sodium nitrite, add 410kg sodium hydroxide, the amount of alkali is 2.5 times of the theoretical amount. .

[0032] (2) Pump the slurry prepared in step (1) into an unjacketed high-pressure leaching kettle (specially made leaching kettle), the heat source is 2.0MPa medium and low pressure steam, and the effective volume is 5 cubic meters. In the unjacketed high-pressure leaching kettle, after 23 minutes, the pressure in the unjacketed high-pressure leaching kettle reaches 1.6MPa, and the temperature reaches 198°C, then close the steam valve, keep warm for 2 hours, and stop the stirring reaction.

[0033] (3) Put the unjacketed high-pressure leaching tank in step (2) into the pulping tank, inject water into the ...

Embodiment 3

[0038] (1) Put 2000 kg of scheelite concentrate with a mass percentage of tungsten trioxide of 50% into the slurry tank after vibrating wet ball milling, add 1 cubic meter of sodium hydroxide solution with a concentration of 450g / L, and then add 20kg As the auxiliary reagent sodium nitrate, add 754 kg of sodium hydroxide, and the amount of alkali is 3.5 times of the theoretical amount.

[0039] (2) Pump the slurry prepared in step (1) into an unjacketed high-pressure leaching kettle (specially made leaching kettle), the heat source is 2.0MPa medium and low pressure steam, and the effective volume is 5 cubic meters. In the unjacketed high-pressure leaching kettle, after 28 minutes, the pressure in the unjacketed high-pressure leaching kettle reaches 1.6MPa, and the temperature reaches 195°C, then close the steam valve, keep warm for 2 hours, and stop the stirring reaction.

[0040] (3) Put the unjacketed high-pressure leaching kettle in step (2) into the slurrying tank, inject ...

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Abstract

The invention discloses an energy-saving and consumption-reducing method for alkaline leaching of scheelite. The method comprises the following steps: (1), processed scheelite concentrates are placed in a slurry barrel, and then concentrated alkali liquor, an auxiliary reagent and sodium hydroxide are added; (2), prepared slurry is pumped into a jacket-free high-pressure leaching kettle, steam is introduced directly, the mixture is subjected to heat preservation for a period of time, and a stirring reaction is stopped; (3), pressure relief is performed, the slurry is discharged into a slurrying tank, water is injected, slurrying and filtering are performed, primary filtrate flows into a strong liquor storage tank, filtering residues are washed with hot water continuously, and washing liquor and the strong liquor are stored separately; (4), a solution in strong liquor storage tank is pumped into a three-effect concentration evaporator, a raw material port is used for a third-effect stage, a discharging port is used for a first-effect stage, a feed liquid at an outlet flows into a single-effect jacketed crystallization boiler to be concentrated continuously, and a steam valve is closed for material discharge; (5), solid-liquid separation is performed, filtered alkali liquor returns to a ball mill for blending of slurry and alkali, and crystalline powder is delivered to a dissolution tank to be dissolved and diluted for ion exchange. According to the method, electric heating is changed into direct steam heating, energy is saved, the production efficiency is high, a multi-effect evaporator is adopted to recover residual alkali, energy consumption is reduced greatly, and the alkali recovery rate is increased.

Description

technical field [0001] The invention relates to tungsten hydrometallurgy, in particular to a method for saving energy and reducing consumption by alkaline leaching of scheelite. Background technique [0002] my country is a country rich in tungsten resources, and 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 in the tungsten industry. In the past, scheelite was a difficult-to-select and difficult-to-smelt raw material, and scheelite resources still remained in the calculation of resource reserves. With breakthroughs in scheelite beneficiation and smelting technology, vigorous development of scheelite has become the mainstream. The pressure leaching process using high temperature and excess alkali can also obtain a good leaching rate (relative to wolframite leaching). In recent years, the production capacity and scale of scheelite smelting have...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/12C22B34/36
CPCY02P10/20
Inventor 李义兵刘崇宇尚伟罗鲲唐鑫
Owner GUILIN UNIVERSITY OF TECHNOLOGY