Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Method for extracting beryllium oxide from low-grade beryllium ore

A low-grade, beryllium oxide technology, applied in the direction of process efficiency improvement, etc., can solve the problems of poor quality of beryllium oxide, affect beryllium hydrolysis, difficult to separate aluminum, etc., achieve low cost, reduce beryllium content, and reduce processing costs

Inactive Publication Date: 2011-08-31
广东省资源综合利用研究所
View PDF2 Cites 16 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are great difficulties in connecting the industrial beryllium oxide with the current production process in the production of non-beryl beryllium ore. There are two main problems to be solved: one is the problem of ore decomposition. In order to convert beryllium into beryllium oxide, which is easily soluble in acid, only a few beryllium ores (such as silicon beryllium yttrium ore) can be directly decomposed by sulfuric acid
The second is the problem of impurity separation. The impurities in beryllium ore can be divided into three categories: the first category is a large amount of conventional impurities, such as aluminum, calcium, iron, silicon, etc.; the second category is difficult to separate impurities, such as phosphorus, which must be Separation by a special process method; the third category is impurities that cause other impurities to be difficult to separate, such as fluorine, which is the most harmful impurity in the production of beryllium oxide by the sulfate method. It mainly causes aluminum to be difficult to separate and affects the hydrolysis of beryllium, resulting in oxidation Poor quality and low recovery of beryllium

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] Example 1: BeO content 1.08%, CaF 2 The high-fluorine and low-beryllium ore with a content of 30.31% is ground to -0.074mm particles accounting for 80%, and then pelletized, and the pellets are dried and roasted at 1050°C for 90 minutes. The roasted pellets are cooled, crushed and ground to obtain a roasted material with -0.074mm particles accounting for 100%. Add concentrated sulfuric acid at a mass ratio of 1 / 1 to acid ore, keep it warm at 100°C for 30 minutes, and add water at a liquid-solid ratio of 5 / 1. , stirred and leached at 30°C for 60 minutes, and obtained acidified liquid and acidified slag after solid-liquid separation. The acidizing solution is added to the new roasted material at a liquid-solid ratio of 4 / 1, stirred and leached at 30°C for 45 minutes, and the solid-liquid is separated to obtain a primary immersion liquid and a primary leaching residue. Add concentrated sulfuric acid to the primary leaching slag according to the ratio of 3 / 4 to acid ore, k...

Embodiment 2

[0017] Example 2: BeO content 1.48%, CaF 2 The high-fluorine and low-beryllium ore with a content of 26.45% was ground until the -0.074mm particles accounted for 85%, and then pelletized. After the pellets were dried, they were roasted at a temperature of 1100°C for 60 minutes. The roasted pellets are cooled, crushed, and ground to obtain a roasted material with -0.074mm particles accounting for 95%. Add concentrated sulfuric acid at a mass ratio of 1 / 1 to acid ore, keep warm at 100°C for 30 minutes, and then press 5 / 1 to liquid-solid Add water, stir and leach at 30°C for 60 minutes, and obtain acidified liquid and acidified slag after solid-liquid separation. The acidizing solution is added to the new roasted material at a liquid-solid ratio of 6 / 1, stirred and reversed leached at 60°C for 60 minutes, and the solid-liquid is separated to obtain a primary immersion liquid and a primary leaching residue. Add concentrated sulfuric acid to the primary leaching slag according to ...

Embodiment 3

[0018] Example 3: BeO content 1.26%, CaF 2The beryllium ore with a content of 34.22% is ground until the -0.074mm particles reach 90%, and then pelletized, and the pellets are dried and roasted at a temperature of 950°C for 120min. The roasted pellets are cooled, crushed, and ground to obtain a roasted material with -0.074mm particles accounting for 92%. Add concentrated sulfuric acid at a mass ratio of 1 / 1 to acid ore, keep warm at 100°C for 30 minutes, and then press a liquid-solid ratio of 5 / 1 Add water, stir and leach at 30°C for 60 minutes, and obtain acidified liquid and acidified slag after solid-liquid separation. The acidizing solution is added to the new roasted material at a liquid-solid ratio of 5 / 1, stirred and reversed leached at 90°C for 90 minutes, and the solid-liquid is separated to obtain a primary immersion liquid and a primary leaching residue. Add concentrated sulfuric acid to the primary leaching slag according to the acid ore ratio of 5 / 4 and keep it w...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a method for extracting beryllium oxide from low-grade beryllium ore. The method is characterized by comprising the following steps of: grinding the low-grade beryllium ore, pelletizing, drying, roasting, and crushing to obtain a roasted material; adding concentrated sulfuric acid, stirring, leaching, and separating to obtain acidified liquid and acidified slag; adding the acidified liquid into the other roasted material, and stirring and leaching to obtain primary steep and primary leaching residue; adding concentrated sulfuric acid into the primary leaching residue, adding water, and stirring and leaching to obtain secondary steep and secondary leaching residue, wherein the acidified liquid is replaced by the secondary steep for recycling; extracting the primary steep by adopting an extracting agent in a volume ratio of phosphors extracting agents: alkanol: kerosene of (25-45):(5-1):(50-70) to obtain a beryllium-loaded organic phase and raffinate; washing the beryllium-loaded organic phase by adopting solution of oxalic acid, and performing back extraction by using solution of NaOH to obtain a blank organic phase and stripping solution; and regulating the concentration of hydroxyl ions in the stripping solution to ensure that beryllium is hydrolyzed and precipitated, and calcining a precipitate to obtain the beryllium oxide. The method is easy to operate, the cost is low, the beryllium oxide with the content of over 97 percent is obtained, and the recovery rate of the beryllium is about 80 percent. The method is suitable for extracting the beryllium oxide from low-grade beryllium ore with low BeO content and high CaF2 content.

Description

technical field [0001] The invention relates to a method for extracting beryllium oxide from low-grade beryllium ore, in particular to a low BeO content, CaF 2 A method for extracting beryllium oxide from low beryllium and high fluorine beryllium ore. Background technique [0002] Beryllium oxide (BeO) is used as a raw material for the production of beryllium metal, beryllium copper alloy and beryllium oxide ceramics. Due to a series of excellent properties, beryllium oxide ceramics have been continuously developed in the nuclear reactor, aerospace and electronic power sectors, and have become a very important material, and have opened up new uses in the civil industry. [0003] There are about 30 kinds of beryllium-containing ores, and the beryllium-containing minerals with economic value are mainly beryl, silicon beryllite, hydroxysilicate and chrysoberyl. At present, the industrial production of beryllium oxide generally uses beryl ore as raw material, and the main meth...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C22B26/20C22B3/08C22B3/40
CPCY02P10/20
Inventor 刘勇刘牡丹刘珍珍张先华
Owner 广东省资源综合利用研究所
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products