Method for preparing ultrafine high-whiteness active barite powder

A barite powder and active technology, applied in the direction of calcium/strontium/barium sulfate, etc., can solve the problems of being unable to produce ultra-fine high-whiteness active barite powder, difficult to control operating conditions, and unstable technical indicators , to achieve the effect of strengthening oxidation leaching efficiency, reducing adverse effects, and easy control of operating conditions

Active Publication Date: 2012-08-01
WUHAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Traditional physical or physical and chemical separation methods (such as hand selection, gravity separation, magnetic separation, flotation, chemical leaching, etc.) cannot produce ultra-fine high whiteness active barite powder
At present, the widely used method of adding bleaching agent (sodium dithionite) to redox reaction to prepare high-whiteness barite under acidic conditions also has the problems of high cost, complicated process, unstable technical indicators, and difficult control of operating conditions.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] (1) After washing, crushing, jigging, grinding, and flotation of the raw barite ore, 325 mesh barite coarse concentrate powder is obtained;

[0036] (2) The crushed barite coarse concentrate is made into a slurry with a slurry concentration of 60%, and the wet ultrafine grinding is performed at a speed of 800r / min for 1.5 hours;

[0037] (3) Filter and dry the above-mentioned ultra-fine barite slurry after wet method;

[0038] (4) Add a mixed acid to the above-mentioned ultrafine barite powder with a solid-liquid ratio of 1:2 and stir at 90°C for 3.5 hours. The mixed acid is a mixture of sulfuric acid, hydrofluoric acid and oxalic acid. Solution, the concentration of sulfuric acid in the mixed solution is 1.5 mol / L, the concentration of hydrofluoric acid is 0.5 mol / L, and the concentration of oxalic acid is 0.2 mol / L;

[0039] (5) Filter the barite powder after the mixed acid oxidation leaching reaction treatment and wash it with deionized water to pH 6-7, wherein the primary f...

Embodiment 2

[0043] (1) After washing, crushing, jigging, grinding, and flotation of the raw barite ore, 325 mesh barite coarse concentrate powder is obtained;

[0044] (2) The crushed barite coarse concentrate is made into a slurry with a slurry concentration of 50%, and the wet ultrafine grinding is performed at a rotation speed of 900r / min for 2 hours;

[0045] (3) Filter and dry the above-mentioned ultra-fine barite slurry after wet method;

[0046] (4) Add a mixed acid to the ultrafine barite powder with a solid-liquid ratio of 1:2 and stir and oxidize the leaching reaction at 90°C for 3 hours. The mixed acid is a mixed solution of sulfuric acid, hydrofluoric acid and oxalic acid. The concentration of sulfuric acid in the mixed solution is 1.7 mol / L, the concentration of hydrofluoric acid is 1.0 mol / L, and the concentration of oxalic acid is 0.1 mol / L;

[0047] (5) Filter the barite powder after the mixed acid oxidation leaching reaction and wash with deionized water to pH 6-7;

[0048] (6) Pr...

Embodiment 3

[0051] (1) After washing, crushing, jigging, grinding, and flotation of the raw barite ore, 325 mesh barite coarse concentrate powder is obtained;

[0052] (2) The crushed barite coarse concentrate is made into a slurry with a slurry concentration of 70%, and the wet ultrafine grinding is performed at a speed of 700r / min for 1 hour;

[0053] (3) Filter and dry the above-mentioned ultra-fine barite slurry after wet method;

[0054] (4) Add a mixed acid to the ultrafine barite powder with a solid-liquid ratio of 1:2 and stir at 85°C for 3.5 hours, and the mixed acid is a mixed solution of sulfuric acid, hydrofluoric acid and oxalic acid. The concentration of sulfuric acid in the mixed solution is 1.5 mol / L, the concentration of hydrofluoric acid is 1.5 mol / L, and the concentration of oxalic acid is 0.5 mol / L;

[0055] (5) Filter the barite powder after the mixed acid oxidation leaching reaction and wash with deionized water to pH 6-7;

[0056] (6) Press filtration and drying are ultra-fi...

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Abstract

The invention relates to the field of mineral materials, in particular to a method for preparing ultrafine high-whiteness active barite powder. The method comprises the following steps of: (1) preparing pulp from 325-mesh barite powder, and performing wet ultrafine grinding until the particle size is less than 10mu m; (2) filtering the barite pulp subjected to wet ultrafine grinding, and drying; (3) adding mixed acid into the dried ultrafine barite powder, and performing oxidation leaching reaction with stirring, wherein the mixed acid is a mixed solution of sulfuric acid, hydrofluoric acid and oxalic acid; (4) filtering the barite powder subjected to oxidation leaching reaction by the mixed acid, and washing until the pH is 6 to 7; and (5) performing pressure filtration, and drying to obtain the ultrafine high-whiteness active barite powder. The preparation method is simple and controllable and easy to popularize, equipment can be localized completely, over 99 percent of prepared barite product has the particle size of -10mu m, and the whiteness is over 90 percent.

Description

technical field [0001] The invention relates to the field of mineral materials, in particular to a method for preparing ultrafine high-whiteness active barite powder. Background technique [0002] Barite is an important barium-containing mineral with the characteristics of high density, stable chemical and thermal properties. The current barite minerals are mainly used in petrochemical and other low value-added fields, such as barite weighting agent, barium-containing chemical products, etc., and the ultra-fine high whiteness active barite powder has good performance (particle size) Microfine, large specific surface area, high chemical activity, high whiteness), mainly used in coatings, paper, rubber, medicine and other industrial sectors; in recent years, it has also been expanded to military high-tech fields such as stealth materials and radiation protection materials. [0003] Traditional physical or physical and chemical separation methods (such as hand selection, gravi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F11/46
Inventor 雷绍民李佳慎舟王欢
Owner WUHAN UNIV OF TECH
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