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Method for removing iron and aluminum from solution containing iron and aluminum and recycling aluminum

A technology for removing iron and aluminum solutions, applied in the fields of chemistry, hydrometallurgy, and materials, can solve the problems of loss of valuable metals, difficulty in filtering precipitated slag, etc., and achieve good removal, lower production costs, and good economic and environmental benefits. Effect

Pending Publication Date: 2022-08-05
INST OF PROCESS ENG CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0009] In order to solve the above technical problems, the present invention provides a method for removing iron and aluminum from iron and aluminum solutions and recycling aluminum. The method solves the problems of difficult filtration of precipitated slag and serious loss of valuable metals from the source. At the same time, the removal efficiency of iron and aluminum and the recycling rate of aluminum resources are improved.

Method used

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  • Method for removing iron and aluminum from solution containing iron and aluminum and recycling aluminum
  • Method for removing iron and aluminum from solution containing iron and aluminum and recycling aluminum
  • Method for removing iron and aluminum from solution containing iron and aluminum and recycling aluminum

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Embodiment 1

[0058] The present embodiment provides a method for removing iron and aluminum from an iron-containing aluminum solution and recycling aluminum, the method comprising the following steps:

[0059] (1) The acidic leaching solution containing iron and aluminum elements includes: Ni 2+ : 20g / L, Co 2+ : 20g / L, Mn 2+ : 10g / L, Fe 3+ : 3g / L, Al 3+ : 1g / L, the pH value of the acid leaching solution is 0.5, and the Na concentration of 20g / L under air oxidation 2 CO 3 The solution was added dropwise to the acid leaching solution at a rate of 1 mL / min, adjusted to pH 3.5, and stirred at 80° C. for 300 min while heating.

[0060] (2) adding adenosine triphosphate dropwise to the iron removal solution described in step (1) at a speed of 1 mL / min, the Al in the iron removal solution 3+ The molar ratio to adenosine triphosphate is 1:0.5, and 5g / L of Na is added. 2 CO 3 The solution adjusts the pH of the solution to 2.5, and stirs for 20 minutes while heating at 70° C. The stirring sp...

Embodiment 2

[0063] The present embodiment provides a method for removing iron and aluminum from an iron-containing aluminum solution and recycling aluminum, the method comprising the following steps:

[0064] (1) The acidic leaching solution containing iron and aluminum elements includes: Ni 2+ : 30g / L, Co 2+ : 30g / L, Mn 2+ : 10g / L, Fe 3+ : 3g / L, Al 3+ : 2g / L, the pH value of the acid leaching solution is 1.0, and the Na concentration is 50g / L under air oxidation. 2 CO 3 The solution was added dropwise to the acid leachate at a speed of 5mL / min, adjusted to pH 3.5, and stirred at 80°C for 300min while heating, and the stirring speed was 150rpm, and the iron-aluminum slag and the iron-removing solution were obtained by solid-liquid separation;

[0065] (2) phytic acid is added dropwise to the iron removal solution described in step (1) at a speed of 5mL / min, the Al in the iron removal solution 3+ The molar ratio with phytic acid is 1:1, adding 5g / L of Na 2 CO 3The solution adjusts ...

Embodiment 3

[0068] The present embodiment provides a method for removing iron and aluminum from an iron-containing aluminum solution and recycling aluminum, the method comprising the following steps:

[0069] (1) The acidic leaching solution containing iron and aluminum elements includes: Cr 3+ : 30g / L, V 5+ : 1g / L, Fe 3+ : 3g / L, Al 3+ : 1g / L, the pH value of the acid leaching solution is 1.0, and the Na concentration of 30g / L under air oxidation 2 CO 3 The solution was added dropwise to the acid leaching solution at a speed of 5mL / min, the pH was adjusted to 3.5, and the mixture was heated and stirred at 80°C for 300min, and the stirring speed was 400rpm, and the iron-aluminum slag and the iron-removing solution were obtained by solid-liquid separation;

[0070] (2) cyclohexanecarboxylic acid is added dropwise to the iron removal solution described in step (1) at a speed of 5mL / min, the Al in the iron removal solution 3+ The molar ratio to cyclohexanecarboxylic acid is 1:0.25, and 5...

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Abstract

The invention relates to a method for removing iron and aluminum from an iron and aluminum-containing solution and recycling aluminum. The method comprises the following steps: mixing the iron and aluminum-containing solution with an alkaline solution and oxidizing gas, adjusting the pH value, heating and stirring, and carrying out solid-liquid separation to obtain iron and aluminum slag and an iron-removed solution; mixing a complexing agent, a pH regulator and the iron-removed solution, regulating the pH value, heating and stirring, and carrying out solid-liquid separation to obtain complexed precipitation slag and a purified solution; and roasting the complexed precipitation slag to obtain an Al (PO3) 3 product. According to the method, the overall iron and aluminum removal effect is good, the filtering performance of the generated gamma-FeOOH slag is good, valuable metal is basically not lost, resource recycling of aluminum is achieved, and the production cost is reduced; the whole technological process is simple, can be used for solving various problems encountered in the process of removing iron and aluminum from the acid solution containing iron and aluminum at present, and has good economic and environmental benefits.

Description

technical field [0001] The invention belongs to the technical fields of hydrometallurgy, chemistry, materials and the like, and particularly relates to a method for removing iron and aluminum from an iron-containing aluminum solution and recycling aluminum. Background technique [0002] Chromium is an important strategic resource, among which chromium salts are called "industrial monosodium glutamate". Chromium salts are widely used in leather, electroplating, pigment, anti-corrosion and other industries. At present, chromium salts are prepared from chromite ore by alkaline roasting to prepare hexavalent chromium salts and then deep conversion. However, the toxicity of hexavalent chromium is huge, and the highly toxic chromium slag produced by the alkaline roasting process belongs to hazardous solid waste. , a serious threat to human health and environmental safety. Trivalent chromium salts are directly prepared after acid hydrolysis of chromite and chromium-containing was...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G49/00C01B25/36C22B3/00C22B7/00C22B21/00
CPCC01G49/0018C01B25/36C22B7/006C22B21/0015Y02P10/20
Inventor 李平刘文科张海林陈兴郑诗礼张懿
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI