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A metal leaching recovery method for continuous multi-stage extraction

A recovery method and extraction technology, applied in the field of environmental chemistry and environmental engineering, can solve problems such as difficult separation, poor quality of recovered products, difficult monomer dissociation, etc., and achieve the effect of low operation cost, low cost, and easy-to-obtain products

Active Publication Date: 2020-01-31
GUANGZHOU UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] 1. The metal recovery products (such as copper-zinc mixture) obtained by extraction are mixed metal compounds with very similar chemical properties. Because of the similar chemical properties in the recovered products, there are often phenomena such as isomorphic replacement or dense symbiosis, and it is difficult to dissociate the monomers. However, subsequent separation difficulties will lead to an increase in the actual utilization cost of recovered products, which is not conducive to the promotion of large-scale engineering applications;
[0005] 2. After the extraction process, the operation method of heating the extract phase to distill and separate it has high energy consumption. When it is used for the separation of various ions, there will be poor quality of recovered products, and the filtration operation will increase the loss of samples;
[0006] 3. When extracting the sample, because the extractant (such as bis-(2-hexylhexyl) phosphate) has a co-extraction effect on non-target metals, the recovered product is a mixed compound of various metals, which enhances the interaction of metal compounds , increasing the physical and chemical properties of recovered products, limiting the subsequent application range of metal compounds

Method used

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  • A metal leaching recovery method for continuous multi-stage extraction

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Embodiment 1

[0046] The metal leaching recovery method of the continuous multistage extraction of the present embodiment comprises the following steps:

[0047] 1) Weigh the fly ash that has been dried to constant weight and disperse it in water according to the liquid-solid ratio (volume / mass) of 5:1, use 5mol / L hydrochloric acid to adjust the pH of the leaching solution to 2, stir and leaching at a speed of 200rpm and 20°C 20h, filter and keep the supernatant;

[0048] 2) Utilize 0.01mol / L 5-salicylaldoxime (LIX860N-I) prepared in kerosene according to the condition that the organic phase: water ratio (volume / volume) is 1:2, carry out two repeated extractions to the filtrate obtained in step 1, Extract at 20°C for 6 minutes to reach extraction equilibrium, then stand and separate to obtain the extract phase and raffinate phase;

[0049] (3) Use 5mol / L sulfuric acid back extraction step 2 gained organic phase extraction liquid, after back extraction equilibrium, leave standstill to separ...

Embodiment 2

[0055] The metal leaching recovery method of the continuous multistage extraction of the present embodiment comprises the following steps:

[0056] (1) Weigh the fly ash dried to constant weight and disperse it in water according to the liquid-solid ratio (volume / mass) of 20:1, use 3mol / L hydrochloric acid to adjust the pH of the leachate to 2, and stir at a speed of 200rpm and 20°C Mix and extract for 20 hours, filter and keep the supernatant;

[0057] (2) Utilize 0.01mol / L 5-salicylaldoxime (LIX860N-I) prepared in kerosene to carry out two repeated extractions to the filtrate obtained in step 1 under the condition that the volume ratio of organic phase: aqueous phase is 1:2. Extract at 20°C for 3 minutes to reach extraction equilibrium and then stand for separation;

[0058] (3) Use 5mol / L sulfuric acid back extraction step 2 gained organic phase extraction liquid, after back extraction equilibrium, leave standstill to separate, the organic phase raffinate can be recycled i...

Embodiment 3

[0064] This embodiment discloses a metal leaching recovery method for continuous multi-stage extraction, comprising the following steps:

[0065] (1) Weigh the fly ash dried to constant weight and disperse it in water according to the liquid-solid ratio (volume / mass) of 50:1, use 3mol / L hydrochloric acid to adjust the pH of the leaching solution to 0.5, stir and leaching at 19°C and 250rpm 4h, filter and keep the supernatant;

[0066] (2) Utilize the 1mol / L 5-salicylaldoxime (LIX860N-I) prepared in kerosene to carry out two repeated extractions to the filtrate obtained in step 1 under the condition that the organic phase: water ratio (volume / volume) is 6:1, Extract at an extraction temperature of 15°C for 5 minutes to reach extraction equilibrium and then stand for separation;

[0067] (3) Use 0.1mol / L sodium sulfate to back-extract the organic phase extract obtained in step 2. After the back-extraction is balanced, let it stand for separation, and the organic phase raffinate...

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Abstract

The invention discloses a metal leaching recovery method of continuous multi-stage extraction. Metal leaching is carried out on fly ash with hydrochloric acid, and 5‑salicylaldoxime (LIX860N‑I) and mixed trialkylphosphine oxide (Cyanex 923) are used as recovery fly ash. Ash and other heavy metal-rich wastes are used as extraction agents for heavy metals, kerosene is used as the solvent of the extraction agent, sulfuric acid, pure water and potassium chloride are used as stripping agents, and the multi-stage extraction method of adding different extraction agents and stripping agents step by step, combined The selectivity of the extractant, the sequential addition of two types of extractant can achieve the maximum degree of step-by-step separation of copper, cadmium, zinc and iron metals in the acid leaching solution, effectively reducing the secondary purification of metal mixed compounds with similar chemical properties The cost; the extraction process proposed by the present invention has the advantages of simplicity, quickness, and low cost, and can provide a new idea for resource utilization of metals in fly ash.

Description

technical field [0001] The invention relates to the technical fields of environmental chemistry and environmental engineering, in particular to a multi-stage extraction method with the characteristics of low cost and high efficiency for copper, cadmium, zinc, iron and other metals in wastes rich in heavy metals such as fly ash. Background technique [0002] Fly ash is the main solid waste produced in the waste incineration process. In the process of waste incineration, heavy metals (such as copper, zinc, lead, cadmium, etc.) often exist in the incineration products (such as bottom ash, fly ash, etc.) in the form of metal elements or oxides, and are released with the flue gas. Directly landfilling fly ash or mixing it with concrete construction means the loss of heavy metals in fly ash and the waste of metal extractable raw materials. Moreover, due to the large output of fly ash and its characteristics of less particles, direct stacking will form dust and block rivers. After...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/02C22B3/10C22B13/00C22B15/00C22B17/00C22B19/20C22B19/30C22B3/30C22B3/38
CPCC22B3/10C22B7/006C22B7/02C22B13/045C22B15/0069C22B15/0086C22B17/04C22B19/22C22B19/30C22B3/30C22B3/3842C22B3/408Y02P10/20
Inventor 苏敏华唐进峰吴婉滢张鸿郭韦乐章陈迪云
Owner GUANGZHOU UNIVERSITY
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