Method for removing magnesium in sulfuric acid leaching process of rhodochrosite

A rhodochrosite and high-acid leaching technology, which is applied in the direction of improving process efficiency, etc., can solve the problems of large excess coefficient of fluoride salt, shortened service life of cathode plate, increased fluoride ion content, etc., and achieves shortened leaching time and high leaching temperature. High, the effect of high residual acid concentration

Active Publication Date: 2015-09-23
CHANGSHA RES INST OF MINING & METALLURGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Liu Honggang and others chose MnF 2 As a precipitant, the MnSO-containing 4 The magnesium removal test was carried out on the leaching solution, and the precipitation rates of calcium and magnesium reached 96% and 99% respectively (see Liu Honggang et al.: Manganese fluoride precipitation removes calcium and magnesium in the leach solution of reduced manganese oxide ore[J]. Mining and Metallurgy, 2007, 16 (4 ):25-28.), the precipitation effect is very good, but the MnF used in this method 2 The purity requirement is high, and the preparation cost is also high. In the test, MnSO 4 with NH 4 The F reaction is self-made, and there is no ready-made product. At the same time, the excess coefficient of fluoride salt is large, and the residual fluoride ion content increases, which has a strong corrosion effect on the cathode plate and shortens the service life of the cathode plate.
[0004] At present, there is no method for direct magnesium removal in rhodochrosite leaching process

Method used

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Experimental program
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Effect test

Embodiment 1

[0029] A method for removing magnesium in the sulfuric acid leaching process of rhodochrosite, comprising the steps:

[0030] (1) Add electrolytic manganese into the leaching tank and return to the anolyte 300ml. When the stirring paddle can be stirred, start to add the slurry containing rhodochrosite powder 100g, and start stirring; after adding the rhodochrosite powder slurry, add concentrated sulfuric acid. The amount of sulfuric acid added is based on controlling the concentration of residual acid at the end of leaching to 40g / L. After adding concentrated sulfuric acid, the electrolytic manganese is finally filled and returned to the anolyte to 800ml. The aforementioned electrolytic manganese returns to MnSO in the anolyte 4 Concentration 38.9g / l, MgSO 4 Concentration 170.2g / l, (NH4 ) 2 SO 4 Concentration 78.2g / l.

[0031] (2) After fully leaching for 3.5 hours, add liquid ammonia to neutralize, so that the solution system is neutral, and the pH value is controlled at ...

Embodiment 2

[0035] A method for removing magnesium in the sulfuric acid leaching process of rhodochrosite, comprising the steps:

[0036] (1) Add electrolytic manganese into the leaching tank and return to the anolyte 300ml. When the stirring paddle can be stirred, start to add the slurry containing rhodochrosite powder 100g, and start stirring; after adding the rhodochrosite powder slurry, add concentrated sulfuric acid. The amount of sulfuric acid added is based on the residual acid concentration at the end of leaching at 25g / L. After adding concentrated sulfuric acid, the electrolytic manganese is finally filled and returned to the anolyte to 800ml. The aforementioned electrolytic manganese returns to MnSO in the anolyte 4 Concentration 38.9g / l, MgSO 4 Concentration 170.2g / l, (NH 4 ) 2 SO 4 Concentration 78.2g / l.

[0037] (2) After fully leaching for 4.0 hours, add liquid ammonia to neutralize, so that the solution system is neutral, and the pH value is controlled at 6-7; adding l...

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PUM

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Abstract

A method for removing magnesium in sulfuric acid leaching process of rhodochrosite comprises the steps that electrolytic manganese returned anode liquor is added in a leaching tank, and then rhodochrosite powder and concentrated sulfuric acid are added to carry out high acid leaching; after sufficient leaching is carried out, liquid ammonia is added for neutralization, and a solution system is made to be neutral; air is blown into the solution system, dimethyl carbamodithioic acid is added after aeration is carried out for a while; after sufficient stirring, solid and liquid separation is carried out on obtained pulp; the filtrate obtained through the solid and liquid separation is circularly used for electrolytic manganese production; separated solid residues are recycled separately. The method is easy and convenient to operate and easy to implement, the manganese leaching rate in the electrolytic manganese production can be increased, and the concentration of magnesium in the electrolytic manganese returned anode liquor can be reduced.

Description

technical field [0001] The invention belongs to the field of nonferrous metal hydrometallurgy or chemical environmental protection, and in particular relates to a method for removing magnesium in the leaching process of rhodochrosite. Background technique [0002] In the current industrial production of electrolytic manganese, the raw material rhodochrosite contains about 2% magnesium oxide, most of which are dissolved in the leaching process, and the leaching solution is recycled electrolytic manganese anolyte, which leads to the MgSO in the system 4 The accumulative total reaches more than 150g / L, which brings many difficulties to production, such as: (1) the viscosity and density of the electrolyte increase, and the conductivity decreases, which hinders the diffusion of ions in the electrolyte and increases the cell voltage; (2) Affect the purity and quality of manganese products; (3) Irregular precipitation of substances in electrodes, equipment and pipelines will seriou...

Claims

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Application Information

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IPC IPC(8): C22B3/08C22B3/44C22B47/00
CPCY02P10/20
Inventor 熊雪良李重洋叶万奇刘雪莹何利民杨智唐三川
Owner CHANGSHA RES INST OF MINING & METALLURGY
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