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The method for separating and recovering cobalt and manganese in low-cobalt high-manganese waste materials with ammonia-sodium carbonate

A technology for separation and recovery, sodium carbonate, applied in the direction of improving process efficiency, etc., can solve the problems of small liquid-solid ratio, low cobalt leaching rate, cobalt is easily wrapped by manganese, etc., to improve recovery rate, low recovery cost, and ensure purity. Effect

Active Publication Date: 2017-11-21
JIANGSU UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the leaching rate of cobalt in this method can reach 90%, and the process is simple, because the manganese content in the cobalt-manganese slag produced in the PTA production is greater than 20%, if the method of direct ammonia leaching is adopted, the liquid-solid ratio is too small , cobalt is easily wrapped by manganese, and the leaching rate of cobalt will be greatly reduced

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1)

[0033] The cobalt-manganese waste treated in this example is the waste cobalt-manganese catalyst produced in the production of PTA, wherein the content of cobalt is 9.872wt%, and the content of manganese is 17.12wt%.

[0034] The method for separating and recovering cobalt and manganese in low-cobalt high-manganese waste materials with ammonia-sodium carbonate of the present embodiment comprises the following steps:

[0035] ① Pretreatment. Take 13 grams of cobalt-manganese waste and add 220 mL of 5% nitric acid solution to the reaction vessel containing the cobalt-manganese waste. After the cobalt-manganese waste is completely digested, measure the pH value of the acid-dissolved liquid to -0.7. The ratio of the amount of acid to the amount of cobalt-manganese in the spent catalyst is n (H + ) : [ n ( Mn ) + n ( Co ) ] = 2 : 1~4 : 1.

[0036] Heat the acid-dissolved material with a pH value of less than 3.5 in a water bath at 80 °C for 30 min, and filter with suction to remo...

Embodiment 2)

[0051] The method of cobalt and manganese in the low-cobalt high-manganese waste material of the separation and recovery of ammonia-sodium carbonate of the present embodiment is the same as embodiment 1, and difference is:

[0052] After the trivalent cobalt ammonium complex in step ④ is reduced to the divalent cobalt ammonium complex, add sodium oxalate solution dropwise under stirring, after adding n(C 2 o 4 2- ): n(Co)=8:1 ~ 20:1.

[0053] In this embodiment, 150 mL of sodium oxalate solution with a concentration of 50 g / L was added dropwise, the dropping speed was 20 mL / min, and the stirring speed was 500 r / min.

[0054] In addition to the sodium oxalate solution described in this example, ammonium oxalate can also be used instead of sodium oxalate.

[0055] After drying, 3.0421 g of cobalt oxalate was obtained, the recovery rate of cobalt was 95.20%, and the purity of cobalt oxalate was 99.1%. Cobalt in cobalt-manganese waste is recovered in the form of cobalt oxalate...

Embodiment 3)

[0057] The method of cobalt and manganese in the low-cobalt high-manganese waste material of the separation and recovery of ammonia-sodium carbonate of the present embodiment is the same as embodiment 1, and difference is:

[0058] Step 1. during pretreatment, add 10% hydrochloric acid solution 44mL in the reaction vessel that fills cobalt-manganese waste material, after cobalt-manganese waste material is digested completely, the pH value of liquid after measuring acid-dissolving is 4.2. Add 10% hydrochloric acid to the acid-dissolved liquid until the pH drops below 3.5, then transfer to a water bath at 80 °C, heat in a water bath for 30 min, and filter with suction to remove organic matter in the acid-dissolved material.

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Abstract

The invention discloses a method of separating and recycling cobalt and manganese in low-cobalt high-manganese waste by ammonia-sodium carbonate. The method comprises the steps: to-be-treated low-cobalt high-manganese waste is firstly pretreated; then ammonia and sodium carbonate are added in digestion solution for reaction; after the reaction ends, filtration is carried out to obtain a cobalt ammonia complex solution and manganese carbonate sediment, and manganese in the low-cobalt high-manganese waste is recycled in a form of manganese carbonate; and finally, cobalt is recycled from the cobalt ammonia complex solution. The method has the advantages that the process is simple; the recovery rates of cobalt and manganese are high; the recovery rate of cobalt can reach 95% or above; the recovery rate of manganese can reach 99% or above; and nonferrous metal resources are recycled in high value.

Description

technical field [0001] The invention relates to a method for separating and recovering cobalt-manganese waste, in particular to a method for separating and recovering cobalt and manganese in low-cobalt and high-manganese waste with ammonia-sodium carbonate. Background technique [0002] The waste cobalt-manganese catalyst produced in PTA production contains a large amount of cobalt and manganese elements, wherein the cobalt content is about 10%, and the manganese content is about 20%. Cobalt is an important strategic metal with excellent physical and chemical properties. It is an important raw material for the production of heat-resistant alloys, hard alloys, anti-corrosion alloys, magnetic alloys and various cobalt salts; while my country's cobalt ore resources are seriously lacking, but cobalt The annual consumption of cobalt is increasing year by year, and domestic cobalt resources can no longer meet the needs of production and consumption, and most of the cobalt raw mater...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/00C22B23/00C22B47/00
CPCC22B7/008C22B7/009C22B23/0446C22B23/0461C22B47/0009Y02P10/20
Inventor 刘维桥魏成文高峰尚通明周全法何沁华
Owner JIANGSU UNIV OF TECH