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

Two-stage ammonia leaching-flow distributing extraction method for copper oxide ore

A copper oxide ore and extraction technology is applied in the field of two-stage ammonia leaching-split extraction and refractory copper oxide ore, which can solve the problems of aggravating ammonia volatilization, worsening industrial hygiene conditions in production workshops, and ammonia volatilization loss, and reducing volatilization. loss, the effect of improving industrial hygiene conditions

Inactive Publication Date: 2012-10-03
KUNMING UNIV OF SCI & TECH TECH IND SALES MANAGEMENT
View PDF4 Cites 7 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] According to the existing wet grinding method, the wet grinding system and the slurry blending system are integrated. If the ammonia is not steamed back to the liquid, and the system is to avoid water expansion and cause the loss of ammonia to the outside, it must be suitable The concentrated ammonia immersion solution required for leaching is added to the wet grinding system, but the wet grinding equipment and spiral classifying equipment of this system are difficult to seal, and the ammonia will be volatilized and lost; the wet grinding also makes the pulp heat up, which intensifies the ammonia Volatile
In this way, not only more ammonia needs to be added before leaching, which increases the production cost, but also the volatilized irritating ammonia smell also deteriorates the industrial hygiene conditions of the production workshop
The way to improve is to cover the grinding and grading equipment, and then set up another fan to pump the tail gas to the absorption tower, but the absorption efficiency of ammonia is not high after it is diluted by air
[0008] According to the existing single-stage ammonia leaching process, when the ammonia leaching reaction is carried out to a certain extent, the dissolved copper ions will hinder the continuation of the reaction, which is not complete for the leaching of free copper oxide; moreover, after the single-stage ammonia leaching The solid-liquid separation, the water content of the filter residue is 12-15%, which brings 4-8% concentrated ammonia leaching liquid into the washing operation

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

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Two-stage ammonia leaching-flow distributing extraction method for copper oxide ore
  • Two-stage ammonia leaching-flow distributing extraction method for copper oxide ore
  • Two-stage ammonia leaching-flow distributing extraction method for copper oxide ore

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Copper oxide ore: copper 1.65%, free copper oxide distribution rate 70.30%, combined copper distribution rate 28.48%, copper sulfide distribution rate 1.22%, CaO: 28.12%, Fe 2 o 3 : 11.40%, MgO: 2.80%, Al 2 o 3 : 0.90%, SiO 2 : 9.28%, (both are mass percentages, test results after drying, the same below), the water content of ore before drying is 4.0%.

[0035] Above-mentioned raw ore is processed according to following process steps:

[0036] (1) Dry grinding: dry-grind the copper oxide ore, and control the mass of powder particles smaller than 74 μm to account for 85%;

[0037] (2) The first stage of ammonia leaching: the material treated in step (1) is mixed with concentrated ammonia into the immersion solution under normal temperature and pressure airtight conditions, and the first stage of stirring ammonia immersion is carried out. The liquid-solid mass ratio is 3: 1. The ammonia leaching time is 2 hours, and then the concentrated ammonia leaching solution and...

Embodiment 2

[0049] Copper oxide ore: copper content 1.54%, free copper oxide distribution rate 72.93%, copper binding rate 15.47%, copper sulfide distribution rate 11.60%, CaO: 27.88%, MgO: 3.79%, Al 2 o 3 : 1.36%, SiO 2 : 29.87%, Fe 2 o 3 : 2.96%, the ore contains 4.0% water before drying.

[0050] Above-mentioned raw ore is processed according to following process step:

[0051] (1) Dry grinding: dry-grind the copper oxide ore, and control the mass of powder particles smaller than 74μm to account for 80%;

[0052] (2) The first stage of ammonia leaching: the material treated in step (1) is mixed with concentrated ammonia into the immersion solution under normal temperature and pressure airtight conditions, and the first stage of stirring ammonia immersion is carried out. The liquid-solid mass ratio is 3: 1. The ammonia leaching time is 2 hours, and then the concentrated ammonia leaching solution and the ore after primary leaching are obtained through solid-liquid separation under a...

Embodiment 3

[0060] Copper oxide ore: copper 0.78%, free copper oxide distribution rate 79.82%, copper binding rate 8.27%, copper sulfide distribution rate 11.91%, CaO: 16.42%, MgO: 7.74%, Al 2 o 3 : 6.87%, SiO 2 : 18.37%, Fe 2 o 3 : 5.33%, the ore contains 4.0% water before drying.

[0061] Above-mentioned raw ore is processed according to following process step:

[0062] (1) Dry grinding: dry-grind the copper oxide ore, and control the mass of powder particles smaller than 74μm to account for 75%;

[0063] (2) The first stage of ammonia leaching: the material treated in step (1) is mixed with concentrated ammonia into the immersion solution under normal temperature and pressure airtight conditions, and the first stage of stirring ammonia immersion is carried out. The liquid-solid mass ratio is 2: 1. The ammonia leaching time is 1.5h, and then the concentrated ammonia leaching solution and the ore after initial leaching are obtained through solid-liquid separation under airtight cond...

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 two-stage ammonia leaching-flow distributing extraction method for a copper oxide ore, which is used for processing the refractory copper oxide ore rich in basic gangue. The method comprises the following steps: firstly, dryly milling a raw ore, performing first-stage stirring leaching under the normal pressure, normal temperature and airtight conditions by using a strong ammonia leaching solution, and performing first-stage solid-liquid separation; performing second-stage stirring leaching under the normal pressure, normal temperature and airtight conditions by using a neutral ammonia leaching solution, performing second-stage solid-liquid separation, washing and performing solid-liquid separation; and introducing the strong ammonia leaching solution, the neutral ammonia leaching solution and a dilute ammonia washing solution into a flow distributing extraction system, back extracting copper, enriching copper ions into a back extracting water-phase pregnant solution, thereby obtaining reusable raffinates with different ammonia concentrations, and finishing the two-stage ammonia leaching-flow distributing extraction for the copper oxide ore. The two-stage ammonia leaching-flow distributing extraction method for the copper oxide ore has the advantages that the leaching efficiency of copper is increased, the volatilization and dilution of the reusable ammonia are reduced, the industrial hygiene condition is improved, and the effluent loss of the copper taken away from the remained water by leaching slag is reduced.

Description

technical field [0001] The invention relates to a method for leaching materials with ammonia, in particular to a two-stage ammonia leaching-separation extraction method for treating refractory copper oxide ore with high alkaline gangue content, and belongs to the technical field of mineral treatment. Background technique [0002] For the refractory copper oxide ore with high alkaline gangue content, if it is treated by flotation, it will be disturbed by the slime, which will cause a large consumption of chemicals and a low recovery rate; However, the ammonia leaching method at room temperature and pressure has the characteristics of good leaching selectivity, no consumption of chemicals for gangue, and less impurities in the leachate. [0003] For the refractory copper oxide ore containing high alkaline gangue, the free copper oxide in the raw ore can be recovered first by direct ammonia leaching at normal temperature and pressure. -Extraction-electrodeposition-leach slag f...

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): C22B3/14C22B3/26C22B15/00
CPCY02P10/20
Inventor 周庆华马彩雯纪翠翠
Owner KUNMING UNIV OF SCI & TECH TECH IND SALES MANAGEMENT
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