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A method for extracting and separating vanadium in aqueous solution

An aqueous solution and extraction technology, applied in the field of materials, can solve the problems of high energy consumption, complex process, low product purity, etc., and achieve the effect of wide concentration range and fast extraction rate

Active Publication Date: 2018-12-07
YANSHAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, various processes for separating and extracting vanadium from vanadium materials have certain disadvantages, such as high energy consumption, heavy pollution, complex processes, and low product purity.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] (1) nonionic surfactant EO50PO50, vanadium-containing aqueous solution, ammonium sulfate aqueous solution and deionized water are mixed to obtain mixed solution 1, and the concentration of nonionic surfactant EO50PO50 in mixed solution 1 is 50g / L, and the concentration of vanadium is 0.5g / L, the concentration of ammonium sulfate is 50g / L, adjust the pH value of mixed solution 1 to 1 with sulfuric acid, obtain mixed solution 2;

[0019] (2) Stir the mixed solution 2 at 25° C. with a constant temperature magnetic stirrer for 10 minutes, then place it in a constant temperature water bath at 25° C. for phase separation for 10 minutes, and obtain the upper phase as a vanadium-loaded nonionic surfactant phase, The lower phase is an aqueous two-phase system, and the concentration of vanadium in the vanadium-loaded nonionic surfactant phase is 10 g / L.

[0020] (3) get the tensio-active agent phase of loading vanadium in the step (2), add ammonium sulfate solution again, make th...

Embodiment 2

[0023] (1) nonionic surfactant L35, vanadium-containing aqueous solution, sodium nitrate aqueous solution and deionized water are mixed to obtain mixed solution 1, and the concentration of nonionic surfactant L35 in mixed solution 1 is 100g / L, and the concentration of vanadium is 5g / L, the concentration of sodium nitrate is 60g / L, and the pH value of the mixed solution 1 is adjusted to 2 with sulfuric acid to obtain the mixed solution 2.

[0024] (2) Stir the mixed solution 2 at 30° C. with a constant temperature magnetic stirrer for 20 minutes, then place it in a 30° C. constant temperature water bath for phase separation for 20 minutes, and obtain the upper phase as a vanadium-loaded nonionic surfactant phase, A two-phase system in which the lower phase is an aqueous phase. The vanadium concentration in the vanadium-loaded nonionic surfactant phase is 10 g / L.

[0025] (3) Add ammonium nitrate solution to the vanadium-loaded surfactant phase in step (2), so that the ratio of...

Embodiment 3

[0028] (1) nonionic surfactant RPE2520, vanadium-containing aqueous solution, sodium chloride aqueous solution and deionized water are mixed to obtain mixed solution 1, and the concentration of nonionic surfactant RPE2520 in mixed solution 1 is 150g / L, vanadium (V ) concentration is 10g / L, and the concentration of sodium chloride is 70g / L, adjusts the pH value of mixed solution 1 with sulfuric acid to be 3, promptly obtains mixed solution 2.

[0029] (2) Stir the mixed solution 2 at 40 DEG C with a constant temperature magnetic stirrer for 30 min, then place it in a constant temperature water bath at 40 DEG C for phase separation for 30 min, to obtain the upper phase as a vanadium-loaded nonionic surfactant phase, A two-phase system in which the lower phase is an aqueous phase. The vanadium (V) concentration in the vanadium-loaded nonionic surfactant phase is 12 g / L.

[0030] (3) get the tensio-active agent phase of loading vanadium (V) in step (2), add ammonium chloride solu...

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Abstract

A method for extracting and separating vanadium in aqueous solution, which mainly comprises mixing non-ionic surfactant, vanadium-containing aqueous solution, saline solution and deionized water, the concentrations of which are respectively 50-200g / L, 0.5-30g / L, 50- 100g / L, adjust the pH value to 1~3, stir it at 25~80°C for 10~60min, stand still and separate the phases for 10~60min, the upper phase is the nonionic surfactant phase loaded with vanadium, and the lower phase is water Phase two-phase system, adding ammonium sulfate, ammonium nitrate or ammonium chloride aqueous solution to the loaded vanadium surfactant phase, so that the ratio of the vanadium-loaded nonionic surfactant phase (O) to the aqueous phase (A) is 1 to 5, adjust the pH value to 8 to 10 with ammonia water, and then place it in a constant temperature water bath at 25 to 80°C for precipitation for 10 to 60 minutes. The invention has fast extraction rate, good phase separation, no formation of third phase and no emulsification problem, non-toxic and harmless to the environment, complete phase separation of the two-phase system, vanadium extraction rate of over 95%, and ammonium metavanadate precipitation rate Reach more than 90%.

Description

technical field [0001] The invention belongs to the technical field of materials, in particular to a method for extracting vanadium. Background technique [0002] Vanadium is known as a "strategic metal", and this reputation is inseparable from its wide range of uses and outstanding advantages. Most of the vanadium in our country is applied to the steel industry, and the purpose of improving its strength and toughness is achieved by adding an appropriate amount of vanadium to the steel. [0003] Vanadium compounds can be applied to some special industries, and can also be applied to medicine, such as the production of stimulants, the production of spectacle lenses and the production of dental materials. Vanadium batteries have the advantages of good discharge performance, short charging time, long cycle life, and low cost. They are also widely used in battery production, and are especially suitable for large-scale static energy storage materials. The application of vanadiu...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B34/22C22B3/26
CPCC22B34/22C22B3/302Y02P10/20
Inventor 张永强卢铁强燕春环张帆李攀王萍孙婷婷
Owner YANSHAN UNIV
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