Production method for cobaltous sulfate heptahydrate

A production method, technology of cobalt sulfate, applied in the direction of cobalt sulfate, etc., can solve the problems of high equipment investment, low production efficiency, many process control parameters, etc., and achieve the effect of low operating cost

Active Publication Date: 2016-06-15
GUANGDONG JIANA ENERGY TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional technology has the following disadvantages: (1) Evaporation and concentration consumes a lot of energy; (2) The crystallized product has fine particles; (3) Low degree of automation and low production efficiency
[0003] CN104192917A discloses a method for continuous crystallization of cobalt sulfate. The cobalt sulfate liquid after stripping is evaporated and concentrated by MVR and then crystallized through an improved cooling type internal circulation continuous crystallizer. Compared with traditional processes, it has low energy consumption, uniform particles, and high degree of automation. Advantages, but there are disadvantages such as high equipment

Method used

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  • Production method for cobaltous sulfate heptahydrate
  • Production method for cobaltous sulfate heptahydrate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Use Co130g / L cobalt sulfate evaporation and crystallization mother liquor as cobalt liquid (air temperature is 20oC), pump cobalt sulfate solution into crystallization tank, start stirring, without heating or cooling, then pump ethanol as eluent; monitor mother liquor at any time Middle Co 2+ When the concentration of Co in the mother liquor reaches 0.5g / L, stop adding ethanol, and use a centrifuge to separate the solid and liquid after stirring and aging for 0.5h; The sieved material is packaged and sold, and the obtained mother liquor is distilled; the distilled liquid is returned to the crystallization process as a dissolving agent, and the raffinate is returned to the leaching workshop of the cobalt hydrometallurgy for pulping the ore pulp. See the specific process figure 1 ..

[0029] The crystallization rate of this elution crystallization is 99.9%, the obtained cobalt sulfate product +24 mesh accounts for 95%, the product water-insoluble matter is <0.0005%, an

Embodiment 2

[0031] The water cobalt ore leaching solution is extracted by P204 to remove impurities, P507 is separated from nickel and cobalt, and back-extracted to obtain a Co120g / L cobalt sulfate solution (air temperature is 40oC), start stirring, pump in isopropanol as a solvent, and when it is saturated, The undersize is returned to the crystallization tank as crystal seeds, and isopropanol is continued to be pumped; the Co in the mother liquor is monitored at any time. 2+ concentration, when the Co concentration in the mother liquor is 5g / L, stop adding benzene, and use a centrifuge to separate the solid and liquid after stirring and aging for 2 hours; The sieve is packaged and sold, and the resulting mother liquor is distilled; the distilled liquid is returned to the crystallization process as a dissolving agent, and the raffinate is returned to the cobalt hydrometallurgy extraction workshop for P507 extraction and recovery of Co. The specific process is only in the figure 1 The o

Embodiment 3

[0034] The water cobalt ore leaching solution is extracted by P204 to remove impurities, P507 is separated from nickel and cobalt, and then back-extracted to obtain a Co60g / L cobalt sulfate solution, which is frozen to 0oC and pumped into the crystallization tank, started stirring, and then pumped into tetrahydrofuran as a solvent; monitor the mother liquor at any time co 2+ Concentration, when the Co concentration in the mother liquor reaches 10g / L, stop adding isopropanol, use a centrifuge to separate the solid and liquid after stirring and aging for 1 hour; the obtained solid is directly packaged and sold after drying, and the obtained mother liquor is distilled after sulfide precipitation; The liquid returns to the crystallization process as a dissolving agent, and the residual liquid is discharged. See the specific process figure 2 ..

[0035] The crystallization rate of this eluted crystal is 80.0%, the water insoluble matter of the product is <0.0005%, and the pH (C

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Abstract

The invention discloses a production method for cobaltous sulfate heptahydrate. The production method includes the following steps that 1, a solvating-out agent is added to a crystallization tank containing a cobaltous sulfate solution, cobaltous sulfate is subjected to solvent-out crystallization, and the separated crystal nucleates and grows; 2, when the concentration of cobalt in the cobaltous sulfate solution in the crystallization tank is smaller than 10 g/L, the solvating-out agent is stopped being added, and solid-liquid separation is conducted; 3, obtained solids are dried and screened, screen underflow serves as seed crystals, and screen overflow is cobaltous sulfate heptahydrate; 4, the cobaltous sulfate solution in the crystallization tank is distilled, distillate serves as the solvating-out agent to be returned to the crystallization step, and raffinate is returned to a wet smelting workshop. The primary crystallization rate of the method reaches up to 99.6% or above, the produced cobaltous sulfate heptahydrate product is large in particle and has glossiness, an evaporation and concentration procedure is not needed, steam consumption is reduced, formation of water insoluble matter in the evaporation and concentration procedure is avoided, and the water insoluble matter in the product is greatly reduced; acid and oil in cobalt liquor before crystallization are diluted by the solvating-out agent in mother liquor, and the product is high in pH and low in oil content; the distillation recovery rate of the solvating-out agent is larger than 98%, and the solvating-out agent can be recycled after being distilled.

Description

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Claims

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Application Information

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Owner GUANGDONG JIANA ENERGY TECH CO LTD
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