A method for selectively removing monovalent anion impurities from sulfuric acid system electrolyte

A technology of anion impurities and sulfuric acid system, applied in the field of hydrometallurgy, can solve problems such as difficult disposal, accumulation of fluorine and chlorine, and difficulty in guaranteeing operating conditions

Active Publication Date: 2019-07-19
WENZHOU UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, even if this method is used, it is difficult to guarantee the strict operating conditions and the reliability of the system is not high. Many domestic electric zinc manufacturers still need to regularly discharge a part of the electrolyte to solve the problem of fluorine and chlorine accumulation, so that electric zinc production can continue
In this way, not only a large amount of Zn resources are wasted in vain, but also acidic zinc electrolysis waste liquid containing high concentration of sulfuric acid and zinc salts is produced, which is very difficult to dispose of.

Method used

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  • A method for selectively removing monovalent anion impurities from sulfuric acid system electrolyte
  • A method for selectively removing monovalent anion impurities from sulfuric acid system electrolyte
  • A method for selectively removing monovalent anion impurities from sulfuric acid system electrolyte

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Embodiment 1

[0046] Embodiment 1: Taking the typical electro-zinc process flow of 240,000 tons of metal zinc as an example with an annual production scale, the circulation volume required for the main circulation of its zinc electrolyte is about 8,000 tons / day; in order to maintain the stability of chlorine impurities, it is necessary to discharge The acid electrolyte is 200 tons / day. That is to say, in order to achieve chlorine balance, the total amount of chlorine impurities that production enterprises need to remove every day is about 200 tons of all chlorine impurities contained in the acid electrolyte. If Cl ‐ The removal rate is lower than 100%, and the same Cl can be achieved by increasing the bypass purification process ‐ Removal. The typical acidic electrolyte composition in the current process is Zn 2+ 58g / L, SO 4 2‐ 365g / L, H + with H 2 SO 4 160g / L, Cl ‐ 540mg / L, F ‐ 120mg / L. The diffusion dialysis test uses the TWDDA anion exchange membrane of Shandong Tianwei Membra...

Embodiment 21

[0059] Example 21: Taking the neutral electrolyte of the electric zinc factory in Example 1 as an example, the composition of the neutral zinc electrolyte is Zn 2+ 158g / L, SO 4 2‐ 365g / L, Cl ‐ 540mg / L, F ‐ 120mg / L, pH 5.5 (free H + concentration is 0). The diffusion dialysis test uses the TWDDA anion exchange membrane of Shandong Tianwei Membrane Technology Co., Ltd. to simulate image 3 in the purification process. Take 50L of the acidic electrolyte, add 98% concentrated sulfuric acid thereinto, the concentration is 5.0g / L. The acidity-adjusted electrolyte and pure water (or tap water) are passed into the diffusion dialyzer in a reverse flow manner, the flow ratio of the electrolyte to water is controlled to be 1:1, and the operating flow rate is 5.0L h ‐1 m ‐2 , after the system reached steady state operation, it was found that Cl in the acidic zinc electrolysis ‐ The removal rate reached 49.0%, F ‐ The removal rate reached 30.4%, SO 4 2‐ The loss rate is 0.80%, ...

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Abstract

A method for selectively removing monovalent anion impurities from a sulfuric acid system electrolyte solution is provided. The method comprises: adjusting the concentration of ionized H2SO4 in the electrolyte solution, introducing the electrolyte solution containing the ionized H2SO4 into a waste acid chamber of a diffusion dialyzer, introducing water as a receiving liquid to flow into a recovery chamber of the diffusion dialyzer in a reverse flow manner, controlling the flow intensity of the electrolyte solution during the diffusion dialysis operation process, transporting, by means of concentration difference driving, part of the ionized H2SO4 in the electrolyte solution of the diffusion dialyzer and the anion impurities through a membrane to the receiving liquid, forming a monovalent anion impurity-enriched dilute H2SO4 and purified electrolyte solution, wherein an anion exchange membrane is arranged in the diffusion dialyzer; wherein the sulfuric acid system electrolyte solution is selected from at least one of a Zn2+, Mn2+, Cu2+, and Co2+ sulfuric acid system electrolyte solution, and wherein the monovalent anion impurities are at least one of F-, Cl-, Br-, I-, NO3-, and NO2-.

Description

technical field [0001] The invention belongs to the field of hydrometallurgy. It relates to a method for selectively removing monovalent anion impurities from sulfuric acid system electrolyte, in particular to a method for selectively removing fluorine and chlorine impurities from zinc sulfate electrolyte, so as to ensure the electrolysis in the process cycle of hydrometallurgy The content of liquid fluorine and chlorine impurities is always lower than or meets the process requirements. The method is also applicable to the selective removal of monovalent anion impurities (such as F ‐ , Cl ‐ 、Br ‐ , I ‐ , NO 3 ‐ , NO 2 ‐ Wait). Background technique [0002] About 80% of the world's metal zinc is produced by hydrometallurgy technology, and its main process is ZnS ore raw material roasting→sulfuric acid leaching→electrodeposited zinc. The electrolyte before electrolytic zinc deposition is close to neutral, and part of the ZnSO 4 will be converted to H 2 SO 4 . The...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C25C1/16C25C7/06C22B3/42
CPCC22B3/42C25C1/16C25C7/06Y02P10/20
Inventor 张伟明陈庆陈宝生肖东
Owner WENZHOU UNIV
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