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Method for recovering rare earth carbonate from waste hydrogen storage alloy powder

A rare earth carbonate and alloy powder technology, applied in the field of metallurgy, can solve the problems of high production cost, cumbersome operation, poor post operating environment, etc., and achieve the effects of low production efficiency, stable chemical structure and improved recovery rate

Inactive Publication Date: 2018-12-18
XIAMEN TUNGSTEN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

It can be seen that although the sodium hydroxide conversion method of double salt has a good conversion effect, it has the disadvantages of high production cost, cumbersome operation, and poor post operation environment.

Method used

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  • Method for recovering rare earth carbonate from waste hydrogen storage alloy powder
  • Method for recovering rare earth carbonate from waste hydrogen storage alloy powder
  • Method for recovering rare earth carbonate from waste hydrogen storage alloy powder

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Embodiment 1: reclaim rare earth carbonate from waste hydrogen storage alloy powder

[0024] Process see figure 1 . Including the following steps:

[0025] Raw materials: Waste materials from the production process of a company’s hydrogen storage alloy powder, the main components of which are shown in Table 1:

[0026] The main component table (%) of raw material used in table 1 embodiment 1

[0027]

[0028] Sulfuric acid leaching of waste hydrogen storage alloy powder: by controlling the temperature of the leaching reaction at 90-95°C, adding sulfuric acid as an oxidant, and under the action of stirring, acidolyze the waste hydrogen storage alloy powder for 2-3 hours, and control the acidity at the end point to 20-60g / l, the metal components in the leachate are listed in Table 2:

[0029] The leaching (g / l) table of waste hydrogen storage alloy powder of table 2

[0030]

[0031] Calculation of Co / Ni recovery rate:

[0032] (Concentration of cobalt in the...

Embodiment 2

[0041] Embodiment 2: reclaim rare earth carbonate from waste hydrogen storage alloy powder

[0042] Process see figure 1 . Include the following steps:

[0043] Raw materials: waste materials from the production process of hydrogen storage alloy powder of a certain company, the main components (%) are shown in Table 5.

[0044] The main component list of raw materials used in table 5 embodiment 2

[0045]

[0046] Sulfuric acid leaching of waste hydrogen storage alloy powder: by controlling the temperature of the leaching reaction at 90-95°C, adding sulfuric acid as an oxidant, and under the action of stirring, acidolyze the waste hydrogen storage alloy powder for 2-3 hours, and control the acidity at the end point to 20-60g / l, the metal components in the leachate are listed in Table 6:

[0047] The leaching (g / l) table of waste hydrogen storage alloy powder of table 6

[0048]

[0049] Conversion of rare earth sulfate double salt: the leaching reaction temperature...

Embodiment 3

[0055] Embodiment 3: reclaim rare earth carbonate from waste hydrogen storage alloy powder

[0056] Process see figure 1 . Include the following steps:

[0057] Raw materials: waste materials in the production process of hydrogen storage alloy powder of a certain company, the main components (%) are shown in Table 9.

[0058] The main component list of raw materials used in table 9 embodiment 3

[0059]

[0060] Sulfuric acid leaching of waste hydrogen storage alloy powder: by controlling the temperature of the leaching reaction at 90-95°C, adding sulfuric acid as an oxidant, and under the action of stirring, acidolyze the waste hydrogen storage alloy powder for 2-3 hours, and control the acidity at the end point to 20-60g / l, the metal components in the leachate are listed in Table 10:

[0061] The leaching (g / l) table of waste hydrogen storage alloy powder of table 10

[0062]

[0063] Conversion of rare earth sulfate double salt: the leaching reaction temperature...

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Abstract

The invention discloses a method for recovering rare earth carbonate from waste hydrogen storage alloy powder. The method comprises the following steps: leaching waste hydrogen storage alloy powder containing rare earth metals with sulfuric acid, and transferring the rare earth metals into a solution, wherein the rare earth metals are lanthanum and cerium; adding a precipitator to precipitate therare earth metals in the obtained leaching solution in the form of rare earth sulfate compound salt to realize the separation of rare earth from a cobalt-nickel metal, wherein the solution is a cobalt-nickel solution; adding additives into the obtained rare earth sulfate compound salt to carry out a conversion reaction, so that sulfate ions in the obtained rare earth sulfate complex salt are removed and converted into rare earth carbonate. The method has the advantages of high leaching speed, high efficiency, high metal recovery rate, high rare earth conversion rate, and conversion rate of therare earth compound salt being up to 99 percent or more.

Description

technical field [0001] The invention relates to the technical field of metallurgy, in particular to a method for recovering rare earth carbonate from waste hydrogen storage alloy powder. Background technique [0002] The negative electrode active material of MH-Ni battery is mainly rare earth hydrogen storage alloy powder. For a long time, most hydrogen storage alloy powder manufacturers will produce some waste products in the manufacturing process. These waste hydrogen storage alloy powder contains A large amount of valuable metals such as cobalt, nickel and rare earth can realize the comprehensive recovery of valuable metals in waste hydrogen storage alloy powder, which has good economic value and great environmental protection significance for the recycling of my country's limited metal resources. It can also reduce the production cost of MH-Ni battery material production enterprises. [0003] After the cobalt-nickel and rare earth metals in the waste hydrogen storage allo...

Claims

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Application Information

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IPC IPC(8): C01F17/00C22B3/00C22B7/00
CPCC22B7/007C22B23/043C01F17/247Y02P10/20
Inventor 刘会明刘华旭祝小明
Owner XIAMEN TUNGSTEN