Process for separation of acid and salt in salt-containing waste acid

A technology of salt separation and acid in acid, which is applied to special treatment targets, water/sludge/sewage treatment, filtration treatment, etc., and can solve problems such as water expansion, complicated control, and small treatment capacity

Active Publication Date: 2020-03-24
CHANGSHA HASKY ENVIRONMENTAL PROTECTION TECH DEV CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this solution still has problems such as incomplete saturation of the ...

Method used

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  • Process for separation of acid and salt in salt-containing waste acid
  • Process for separation of acid and salt in salt-containing waste acid

Examples

Experimental program
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Effect test

Embodiment 1

[0054] A kind of process of separating acid and salt in salt-containing waste acid of the present invention, this salt-containing waste acid adopts the waste electrolytic solution decoppered liquid of a certain copper smelter, contains sulfuric acid 245g / L, contains copper 14.7g / L, such as figure 1 Shown, technique of the present invention comprises the following steps:

[0055] (1) Before the first use, wash and elute the acid adsorption resin column with water. After finely filtering the salt-containing waste acid (copper-removed liquid) with a 1μm filter membrane, acid adsorption is carried out through an acid adsorption resin column filled with a strong basic anion exchange resin after washing with water. The acid adsorption resin column is equipped with an inner diameter Acid-absorbing resin of 5.5 cm x height 100 cm. The first cycle of adsorption is to pump the decopper liquid after precision filtration into the acid adsorption resin column from the bottom, and collect...

Embodiment 2

[0062] A process for separating acid and salt in salt-containing waste acid of the present invention uses the same salt-containing waste acid solution as in Example 1, the process is basically the same as in Example 1, the only difference is: only for the acid adsorption process The volume of the solution collected by adsorption and elution is changed. During the adsorption process, 1.8L of residual eluent water, 0.7L of deacidified salt solution and 0.7L of waste acid return solution are collected from the upper end in sequence. During the elution process, Collect 1.8L of residual waste acid solution, 0.7L of desalted acid solution and 0.7L of eluate return solution sequentially from the lower end.

[0063] Repeat the second cycle 3 times as well. Finally, the obtained average results are shown in Table 2 below.

[0064] Table 2 Concentration and separation rate of deacidified saline solution and desalted acid solution

[0065]

Embodiment 3

[0067] A process for separating acid and salt in salt-containing waste acid of the present invention uses the same salt-containing waste acid solution as in Example 1, the process is basically the same as in Example 1, the only difference is: only for the acid adsorption process The volume of the solution collected by adsorption and elution is changed. During the adsorption process, 1.8L of residual eluent water, 0.8L of deacidified salt solution and 0.6L of waste acid return solution are collected sequentially from the upper end. During the elution process, Collect 1.8L of residual waste acid solution, 0.7L of desalted acid solution and 0.7L of eluate return solution sequentially from the lower end.

[0068] Repeat the second cycle 3 times as well. Finally, the obtained average results are shown in Table 3 below.

[0069] Table 3 Concentration and separation ratio of deacidified saline solution and desalted acid solution

[0070]

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Abstract

The invention discloses a process for separation of acid and salt in salt-containing waste acid. The process includes: subjecting salt-containing waste acid to multi-period adsorption-elution treatment by an acid adsorption resin column, during adsorption, passing waste acid return liquid, residual waste acid liquid and a salt-containing waste acid stock solution obtained in a previous period sequentially through acid adsorption resin from the bottom up for acid adsorption, collecting residual elution water, deacidified salt-containing liquid and waste acid return liquid successively, stoppingliquid feeding after the volume meeting the requirement, completely feeding salt-containing waste acid in the first period, during elution, passing elution water return liquid, residual elution waterand elution water obtained in a previous period through acid adsorption resin from top to bottom in sequence for elution, and collecting residual waste acid liquid, desalted acid-containing liquid and elution water return liquid successively, stopping water inflow after the volume meets the requirement, completely feeding elution water in the first period, and performing repetition till completing treatment of the salt-containing waste acid. The process disclosed by the invention can be used for separation of various acids and cations, has good separation effect, is not limited by the heightof the resin column, does not generate volume expansion, and has wide applicability.

Description

technical field [0001] The invention belongs to the technical field of wastewater treatment and reuse, and relates to a process for separating acid and salt in waste acid containing salt, in particular to a process for separating acid and metal salt in waste acid containing high-concentration metal ions. Background technique [0002] In metallurgy, chemical industry, surface treatment and other fields, there are a large number of high-concentration waste acids containing high-concentration impurity metal ions. Such as copper electrolyte in the metallurgical industry, zinc electrolysis waste liquid, leachate in the process of anode slime treatment, etc. Because the impurity metal ions in the solution are too high to be reused, the common treatment methods include neutralization precipitation method, concentrated crystallization method, membrane separation method, etc. Among them, the neutralization precipitation method consumes a lot of auxiliary materials, the amount of was...

Claims

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Application Information

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IPC IPC(8): C02F9/10
CPCC02F1/001C02F1/04C02F1/26C02F1/28C02F9/00C02F2001/007C02F2001/422C02F2303/14
Inventor 蒋晓云夏栋何劲松易亚男
Owner CHANGSHA HASKY ENVIRONMENTAL PROTECTION TECH DEV CO LTD
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