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Two-step low-temperature iron removing method for copper-cobalt ore leachate

A leaching solution, copper and cobalt technology, applied in the field of non-ferrous metal smelting, can solve the problems of high valence metals, high temperature iron removal and high energy consumption, and achieve the effect of less valence metal content, good effect and simple method

Inactive Publication Date: 2017-05-31
JINCHUAN GROUP LIMITED
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The technical problem to be solved by the present invention is to propose a copper-cobalt ore leaching solution for the problems and deficiencies in the prior art, such as low iron removal depth, more valuable metals in iron slag, and high energy consumption for high-temperature iron removal. Two-stage low-temperature iron removal method for ore leachate, the method provides cheap raw materials, simple process technology, mild reaction, easy operation, easy to realize large-scale production, and the iron content in the liquid after iron removal is less than 0.01g / L, and the iron removal depth is relatively high High; at the same time, the iron slag can form an open circuit, and the entrainment of valuable metals in the open circuit iron slag is less than 0.1%, and the metal recovery rate is high

Method used

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  • Two-step low-temperature iron removing method for copper-cobalt ore leachate

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Experimental program
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Effect test

Embodiment 1

[0020] The main components (g / L) of a copper-cobalt ore leaching solution include: Cu 0.055, Fe 0.98, Co 1.46 and other element contents. First, the copper-cobalt ore leaching solution is subjected to a stage of low-temperature iron removal, and the neutralization hydrolysis method is used to remove iron. The mass ratio is 2:100 mixed gas of sulfur dioxide and air as oxidant, control the potential of the solution at 400mV, the oxidant feed rate of the mixed gas of air and sulfur dioxide is 1.8L / min, control the temperature at 30℃, adjust the end pH of the solution to 2.78 with CaO, remove iron It takes 6 hours to carry out one stage of low-temperature iron removal, and the obtained one stage of iron-removing slag contains 0.022% cobalt; the produced one stage of iron-removal liquid is subjected to a second stage of low-temperature neutralization to remove iron, and a mixture of sulfur dioxide and air with a mass ratio of 2:100 is added. As an oxidant, control the solution potent...

Embodiment 2

[0022] The main components (g / L) of a copper-cobalt ore leaching solution include: Cu 1.965, Fe 3.46, Co 59.53 and other element contents. First, the copper-cobalt ore leaching solution is subjected to a stage of low-temperature iron removal, and the neutralization hydrolysis method is used to remove iron. The mass ratio is 1:100 mixed gas of sulfur dioxide and air is used as oxidant to control the potential of the solution at 460mV, the oxidant input of the mixed gas of air and sulfur dioxide is 2.5L / min, the temperature is controlled to 35℃, the end point of the solution is adjusted to pH3.0 with CaO, and iron is removed For 6h, carry out one stage of low-temperature iron removal, and the obtained one stage of iron-removal slag contains 0.032% of cobalt; the produced one stage of iron-removal liquid is subjected to the second stage of low-temperature neutralization to remove iron, and a mixture of sulfur dioxide and air with a mass ratio of 1:100 is added. As an oxidant, contr...

Embodiment 3

[0024] The main components (g / L) of a copper-cobalt ore leaching solution include: Cu 1.985, Fe 10.63, Co 68.59 and other element contents. First, the copper-cobalt ore leaching solution is subjected to a stage of low-temperature iron removal, and the neutralization hydrolysis method is used to remove iron. The mass ratio is 1:10 mixed gas of sulfur dioxide and air used as oxidant to control the solution potential at 460mV, the oxidant feed rate of the mixed gas of air and sulfur dioxide is 1.8L / min, the temperature is controlled to 15℃, the end point of the solution is adjusted to pH 2.5 with CaO, and iron is removed For 4h, one stage of low-temperature iron removal is carried out, and the obtained one stage of iron removal slag contains 0.036% of cobalt; the produced one stage of iron-removal liquid is subjected to a second stage of low-temperature neutralization to remove iron, and a mixture of sulfur dioxide and air with a mass ratio of 1:10 is added. As an oxidant, control ...

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Abstract

The invention provides a two-step low-temperature iron removing method for copper-cobalt ore leachate. The process that iron is removed in a two-step neutralization-hydrolysis mode, the final pH of first-step low-temperature iron removal is controlled to be 2.5-3.0, and the final pH of second-step low-temperature iron removal is controlled to be 3.5-4.5 is adopted. An open loop is formed through iron slag after first-step washing, the entrainment rate of valuable metal in the first-step iron slag is as low as being smaller than 0.1%, and the recovery rate of the valuable metal is increased; and the iron content of liquid subjected to second-step iron-removal is smaller than 0.01 g / L, the iron removing depth is high, and the solution purification iron-removing effect is good. Meanwhile, deep iron-removal can be conducted even at a low temperature, the energy consumption is low, accordingly the production cost is lowered, and the economic benefits are high. The method is simple, technical conditions are easy to control, the content of the valuable metal in the open-loop slag is low, and the metal recovery rate is high; the liquid subjected to low-temperate iron-removal is low in iron content and good in solution purification iron-removing effect; and meanwhile, raw materials provided for the method are low in price, low-temperature operation is achieved, the energy consumption is low, scale production is easy to achieve, and the economic benefits and the social benefits are good.

Description

Technical field [0001] The invention belongs to the technical field of non-ferrous metal smelting, and specifically relates to a method for removing iron from a copper-cobalt ore leachate in the cobalt hydrometallurgical industry by using two-stage low-temperature neutralization water. Background technique [0002] In hydrometallurgy, the ore is usually leached with an acidic solution. The leaching solution contains trivalent or divalent iron ions, which will cause the cathode current efficiency to decrease in the subsequent process and the electrowinning process, and at the same time affect the quality of the electrowinning cobalt. Therefore, in addition to Iron is a very important process in hydrometallurgy. At present, there are many methods for removing iron, mainly the jarosite method, goethite method, hematite method, etc. However, these iron removal methods require high-temperature operation to achieve a good iron removal effect; at the same time, in a solution with a hig...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/44C22B23/00
CPCC22B3/44C22B23/0461Y02P10/20
Inventor 杨志强李娟朱锐伦郭锋张鹏马永峰马海青郭金权张彦儒王辉苏俊敏陈彩霞张素超
Owner JINCHUAN GROUP LIMITED
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