Combined mineral dressing technology of fine grain and micro grain cassiterite

A technology of fine particles and cassiterite, applied in flotation, chemical instruments and methods, solid separation, etc., can solve the problems of high loss rate, affecting the recovery rate of cassiterite, etc., and achieve good economic and social benefits and beneficiation recovery rate. Low cost, good economic effect

Active Publication Date: 2010-11-17
广西华锡矿业有限公司铜坑矿业分公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Zhou Tingxi used the flotation-magnetic separation-gravity separation process in the Dulong Tin Mine, but only part of the cassiterite above 37μm was recov...

Method used

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  • Combined mineral dressing technology of fine grain and micro grain cassiterite
  • Combined mineral dressing technology of fine grain and micro grain cassiterite
  • Combined mineral dressing technology of fine grain and micro grain cassiterite

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] After the fine-grained and fine-grained ore pulp less than 37 microns is concentrated and precipitated by a Φ30-meter thickener, the overflow and overflow are treated separately for production water supply, and the sulfide ore is removed by a flotation machine for sand settling to realize the separation of sulfide ore and oxidized ore. . The weight of desulfurization water is 0.8t / t to feed the ore, and the weight of activator copper sulfate is 0.3g / t; the weight of collector isoamyl xanthate is 0.2g / t; ; Normal temperature flotation, the sulfide ore foam produced by flotation is treated separately, and the flotation tailings enter the tin flotation operation. The weight of water for tin floating operation is 1.4t / t to ore; the weight of styrene phosphoric acid is 0.3g / t; the weight of collector 2-hydroxy-3-benzohydroxamic acid is 0.2g / t and water The weight of salicylic hydroxamic acid is 0.2g / t; the weight of soda ash as regulator is 0.3g / t; the weight of pine alcoho...

Embodiment 2

[0054] After the fine-grained and fine-grained ore pulp less than 37 microns is concentrated and precipitated by a Φ30-meter thickener, the overflow and overflow are treated separately for production water supply, and the sulfide ore is removed by a flotation machine for sand settling to realize the separation of sulfide ore and oxidized ore. . The weight of water for desulfurization is 1.1t / t to feed the ore, and the weight of activator copper sulfate is 0.35g / t; the weight of collector isoamyl xanthate is 0.3g / t; ; Normal temperature flotation, the sulfide ore foam produced by flotation is treated separately, and the flotation tailings enter the tin flotation operation. The weight of water for tin floating operation is 1.0t / t to feed ore; the weight of inhibitor aryl phosphoric acid is 0.15g / t and the weight of octylphenyl polyoxyethylene ether is 0.1g / t; the collector is alkyl sulfonated The weight of succinamic acid salt is 0.3g / t; the weight of soda ash as a regulator is...

Embodiment 3

[0056] After the fine-grained and fine-grained ore pulp less than 37 microns is concentrated and precipitated by a Φ30-meter thickener, the overflow and overflow are treated separately for production water supply, and the sulfide ore is removed by a flotation machine for sand settling to realize the separation of sulfide ore and oxidized ore. . The weight of desulfurization water is 1.5t / t to feed the ore, and the weight of activator copper sulfate is 0.4g / t; the weight of collector isoamyl xanthate is 0.4g / t; ; Normal temperature flotation, the sulfide ore foam produced by flotation is treated separately, and the flotation tailings enter the tin flotation operation. The weight of water for tin floating operation is 0.7t / t for ore; the weight of inhibitor alkyl phosphoric acid is 0.1g / t and the weight of aryl phosphoric acid is 0.1g / t; the collector 2-hydroxy-3-benzyl hydroxy The weight of oxime acid is 0.2g / t; the weight of soda ash as regulator is 0.15g / t; the weight of pin...

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Abstract

The invention relates to a combined mineral dressing method of fine grain and micro grain cassiterite, which gives up the single mineral dressing method of fine grain and micro grain cassiterite for years. The invention adopts the effective combination of two-time flotation operation, magnetic separation operation, desliming and dewatering operation and reselection operation, provides a new mineral dressing model for selecting grain and micro grain cassiterite which has the size of 10-37 micrometers and has complex mineral property, high impurity content and big mineral dressing difficulty, and improves the cassiterite concentration ratio and cassiterite operation recovery rate; cassiterite concentration ratio can reach 5-10, the cassiterite operation recovery rate can be above 70%, and the tin-containing grade of tin concentrate products can be above 50%. The method also can be used for the mineral dressing of fine grains and micro grains of non-ferrous metal, such as tungsten, molybdenum, tantalum, niobium and the like and has favorable economic benefit and social benefit.

Description

technical field [0001] The invention belongs to the technical field of ore dressing, and relates to a fine-grained and fine-grained cassiterite combined ore-dressing process. Background technique [0002] Tin is one of the first metals discovered and used in human history. Tin has many advantages such as low melting point, good plasticity, corrosion resistance, fatigue resistance, and non-toxicity. Tin is widely used in various fields of national economy and national defense construction. In the past, tin was widely used in the production of tinplate, solder and alloys. With the development of science and technology, the application fields of tin are expanding day by day, which leads to the increasing demand for tin in the world. With the reduction of sandy tin resources that are easy to mine and select, the level of separation of fine-grained and micro-fine-grained tin resources should be improved, and new beneficiation methods should be found. [0003] Fine-grained and ...

Claims

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Application Information

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IPC IPC(8): B03B7/00B03D1/00B03D1/014B03D1/012B03D101/06B03D101/02
Inventor 吴伯增陈建明王熙黄承波王万忠杨林院余忠保黄艳黄润芝
Owner 广西华锡矿业有限公司铜坑矿业分公司
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