Method for evaporation-free preparation of zinc sulfate from brass slag material

A technology of brass slag and zinc sulfate, which is applied in the fields of metallurgy and chemical industry, can solve the problems of high energy consumption in the concentration and evaporation of zinc sulfate products, high energy consumption in the evaporation and concentration process, and the impact on the quality of zinc sulfate products, so as to achieve good metal selection high performance, low energy cost, and low supersaturation

Active Publication Date: 2014-06-18
JINTIAN COPPER GROUP CORP NINGBO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the brass slag also contains a large amount of other metals, such as lead, iron, tin, nickel, etc., some of them will enter the solution during the leaching process, and the impurity removal determines the quality of the zinc sulfate product. There are obvious deficiencies
And Chinese Patent No. 20111010179313.4 discloses a kind of technology that evaporative crystallization method prepares zinc sulfate, although avoided the complex and loaded down with trivial details problem of process step, its evaporative concentration process energy consumption is bigger and speed is slow, and production cost is on the high side, and production efficiency is low; In the process of evaporation and concentration, some impurities are also mixed in the concentrated mother liquor, which will reach supersaturation and precipitate out, which will affect the quality of zinc sulfate products.

Method used

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  • Method for evaporation-free preparation of zinc sulfate from brass slag material

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] The raw material used in this example is 20Kg (dry weight) of light ash material after physical separation of brass slag. leach.

[0029] Next, extract the zinc in the neutral leaching solution with 30% P204 extractant (the diluent is kerosene), control the ratio of oil to water (O / A ratio) to 1:1, and separate the oil-water phase (water phase It can be recycled back to the leaching process, thereby replacing the input of sulfuric acid and water), and P204 (R 2 -Zn) oily liquid,

[0030] Chemical formula: 2(R-H)+Zn 2+ →(R 2 -Zn)+2H +

[0031] Then, the oily liquid containing 8g / L of zinc is washed with a dilute sulfuric acid solution with a pH value of 2.5 to remove a small amount of impurity elements entrained; at the same time, the washed oily liquid of zinc-containing P204 is subjected to primary dislocation with 400g / L of sulfuric acid. Flow stripping, the ratio of water to oil is 1:3, to obtain a primary stripping solution with a zinc content of 19.2g / L; repe...

Embodiment 2

[0036] The raw material used in this example is 24Kg (dry weight) of light ash material after physical separation of brass smelting slag. Sulfuric acid neutral leaching.

[0037] Next, extract the zinc in the neutral leaching solution with 30% P204 extractant (the diluent is kerosene), control the ratio of oil to water (O / A ratio) to 1:1, and separate the oil-water phase (water phase It can be recycled back to the leaching process, thereby replacing the input of sulfuric acid and water), and an oily liquid containing 8.2g / L of zinc is obtained.

[0038] Then, the oily liquid containing zinc 8.2g / L is washed with a dilute sulfuric acid solution with a pH value of 2.5 to remove a small amount of impurity elements entrained; at the same time, the washed zinc-containing P204 oily liquid is treated with 400g / L sulfuric acid for primary Cross-flow stripping, the ratio of water and oil is 1:3, to obtain a primary stripping solution with a zinc content of 19.7g / L; repeat stripping, w...

Embodiment 1、2

[0044] Embodiments 1 and 2 of the present invention: low energy consumption, high production efficiency, simple process, clean site, zinc sulfate crystals in granular form, bright white in color.

[0045] Comparative example: the energy consumption is obviously too high, and the production time is longer; the amount of acid and water used is increased, and the site environment is poor; the crystal of zinc sulfate is dusty, easy to absorb moisture and agglomerate, and appears light green or light yellow green.

[0046] Composition comparison:

[0047] The chemical compositions of the zinc sulfate crystals prepared in Examples 1, 2 and Comparative Example are shown in Table 1 after detection.

[0048] Table 1: Chemical composition of zinc sulfate heptahydrate

[0049] name

[0050] It can be drawn that the quality of the zinc sulfate prepared by the crystallization stripping method of the present invention is better than the zinc sulfate produced by the concentrated d...

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Abstract

A method for evaporation-free preparation of zinc sulfate from a brass slag material is characterized by comprising the steps: taking a light ash material of the brass slag material, adding water according to the solid-liquid mass ratio of 1:14-16, carrying out pulp conditioning, and carrying out neutral leaching with concentrated sulfuric acid; then extracting by a P204 extraction agent, and washing with a dilute sulfuric acid solution with the pH value of 2.0-2.5; next carrying out first-class cross-flow back extraction by a sulfuric acid solution with the concentration of 350-450 g/L, carrying out repeated back extraction, and then separating out zinc sulfate; carrying out second-class cross-flow back extraction of a zinc-containing P204 oily liquid left in the first-class back extraction with a sulfuric acid solution, and when the zinc concentration reaches about 95+/-10 g/L, supplementing the second-class back extraction solution to the first-class back extraction solution; allowing the P204 oily liquid obtained after second-class back extraction to anew return to the step 2), and carrying out extraction; and finally carrying out cycle operation of feeding, leaching, extracting, washing, first-class cross-flow back extraction and second-class cross-flow back extraction, and separating out zinc sulfate heptahydrate crystals. The method has the advantages of simple process, low energy consumption and high production efficiency; and the prepared zinc sulfate is granular in shape, is bright white in color, and has the quality better than zinc sulfate produced by a concentration distillation method.

Description

technical field [0001] The invention belongs to the technical field of metallurgy and chemical industry, and specifically relates to a method for preparing zinc sulfate by freeing evaporation and crystallization of brass slag. Background technique [0002] Brass slag mainly refers to the slag produced during the smelting of brass, which is re-selected to remove the residue of metallic elements. Brass slag is mostly used to recover zinc. The recovery methods are divided into two categories: wet method and fire method, and wet method has two kinds of direct recovery of metal zinc and recovery of zinc sulfate. [0003] In the crystallization process in the wet leaching process, the solvent is usually evaporated to make the solution from unsaturated to saturated, and if the evaporation continues, the excess solute will be precipitated in the form of crystals; the concentration of zinc sulfate in the solution is low, and it will not occur at room temperature Crystallization occu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B19/30C22B3/08C22B3/40
CPCY02P10/20
Inventor 洪燮平邵德钟裘桂群
Owner JINTIAN COPPER GROUP CORP NINGBO
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