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A kind of beneficiation method of tungsten-tin mineral

A mineral processing method, tungsten-tin technology, applied in flotation, solid separation, etc., can solve the problems of cassiterite not being able to be recovered effectively, cassiterite not recyclable, cassiterite content is low, etc., and achieve the effect of improving the comprehensive utilization rate

Active Publication Date: 2020-05-05
INST OF RESOURCES UTILIZATION & RARE EARTH DEV GUANGDONG ACAD OF SCI
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although benzohydroxamic acid has a certain ability to collect cassiterite, since water glass or a combination regulator mainly composed of water glass is added to black and white tungsten mixed flotation to inhibit silicate minerals and Calcite minerals, and sodium silicate has a strong inhibitory effect on cassiterite. When black and white tungsten mixed flotation method is used to carry out black and white tungsten mixed flotation on polymetallic ores with low-grade fine-grained cassiterite associated with tungsten, black and white tungsten is obtained. WO in mixed concentrate 3 The grade is >20%, but the Sn grade is only 0.2%~0.5%, and the tin recovery rate is less than 8%. Therefore, the conventional black and white tungsten mixed flotation beneficiation method cannot realize the effective recovery of cassiterite at the same time as the black and white tungsten mixed flotation , the associated low-grade cassiterite can only be recovered by gravity separation or flotation in black and white tungsten mixed flotation tailings
[0005] In polymetallic ores with low-grade fine-grained cassiterite associated with tungsten, due to the low content of cassiterite (the tin grade is less than 0.2% of the cut-off grade of associated tin ore in industrial mining), the particle size is fine (in the particle size of -0.043mm, the cassiterite Occupancy rate is greater than 60%), if adopt gravity separation method to reclaim cassiterite in tungsten flotation tailings, the rate of recovery of cassiterite is less than 5%; If adopt flotation method to reclaim cassiterite in tailings, mineral processing cost is higher, Economic benefit is poor
At present, this type of cassiterite can only be discarded in the tailings and cannot be recovered. Therefore, the comprehensive recovery of cassiterite from the polymetallic ore with low-grade fine-grained cassiterite associated with tungsten has always been a difficult problem in the mineral processing industry.

Method used

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  • A kind of beneficiation method of tungsten-tin mineral

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Example 1: Tungsten-tin ore feed WO 3 0.43%, Sn 0.09%, CaF 2 24.67%, CaCO 3 4.53%, fineness -0.074mm content 85%, scheelite monomer dissociation degree 90%, wolframite monomer dissociation degree 92%, cassiterite monomer dissociation degree 95%, scheelite and black tungsten The ore ratio is about 8:2, and the tungsten-tin mixed flotation is carried out according to the following steps (the dosage of the reagent is based on the quality of the tungsten-tin ore).

[0016] 2 times of rough selection: According to the pharmaceutical system in Table 1, 1st rough selection: add 1500 g / ton of mixed aqueous solution with a mass ratio of sodium carbonate to sodium hydroxide of 3:1 and a total mass content of 10%, 300 g / ton of sodium fluorosilicate, Sodium hexametaphosphate 20 g / ton and lead nitrate 650 g / ton, stir for 8 minutes, add 250 g / ton benzyl hydroxamic acid, 65 g / ton salicylic hydroxamic acid and 40 g / ton emulsified oleic acid, stir for 10 minutes Secondary rough se...

Embodiment 2

[0019] Example 2: Tungsten-tin ore feed WO 3 0.25%, Sn0.074%, CaF 2 14.87%, CaCO 2 6.03%, fineness -0.074mm content 71.04%, scheelite monomer dissociation degree 90%, wolframite monomer dissociation degree 90%, cassiterite monomer dissociation degree 92%, scheelite and black tungsten The ore ratio is about 2:8, and the tungsten-tin mixed flotation is carried out according to the following steps (the dosage of the reagent is based on the quality of the tungsten-tin ore).

[0020] 2 times of rough selection: According to the pharmaceutical system in Table 1, 1st rough selection: add 500 g / ton of mixed aqueous solution of sodium carbonate and sodium hydroxide with a mass ratio of sodium carbonate and sodium hydroxide of 1:3 and a total mass content of 1%, fluorosilicone 120 g / ton of sodium hexametaphosphate, 30 g / ton of sodium hexametaphosphate, 650 g / ton of lead nitrate, and stir for 10 minutes. Add 250 g / ton of benzohydroxamic acid, 30 g / ton of salicylic hydroxamic acid and ...

Embodiment 3

[0023] Example 3: Tungsten-tin ore feed WO 3 0.50%, Sn0.15%, CaF 2 16.77%, CaCO 3 9.18%, fineness -0.074mm content 78.98%, scheelite monomer dissociation degree 90%, wolframite monomer dissociation degree 90%, cassiterite monomer dissociation degree 92%, scheelite and black tungsten The ore ratio is about 6:4, and the tungsten-tin mixed flotation is carried out according to the following steps (the dosage of the reagent is based on the quality of the tungsten-tin ore).

[0024] 2 times of rough selection: According to the pharmaceutical system in Table 1, 1st rough selection: add 1250 g / ton of mixed aqueous solution of sodium carbonate and sodium hydroxide with a mass ratio of sodium carbonate and sodium hydroxide of 3:2 and a total mass content of 5%, fluorosilicone 400 g / ton of sodium nitrate, 600 g / ton of lead nitrate, stirring for 10 minutes. Add 300 g / ton of benzohydroxamic acid, 22 g / ton of emulsified oleic acid, and stir for 8 minutes; second rough selection: add 100...

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Abstract

The invention discloses a tungsten tin mineral beneficiation method; and tungsten tin minerals are tungsten tin fed ores as sulfide ores flotation tailings obtained after grinding of multimetal ores of tungsten associated cassiterite, removal of magnetite by magnetic separation and removal of sulfur concentrates by sulfide ore flotation. Mixed liquid of sodium carbonate and sodium hydroxide, sodium fluosilicate, sodium hexametaphosphate and lead nitrate are added in the tungsten tin fed ores for pulping; then, collecting agents-benzohydroxamic acid, hydroxamic acid and emulsified oleic acid are added for tungsten tin mixed flotation; and tungsten tin mixed concentrates with WO3 of not less than 20% and Sn of not less than 1% are obtained by 2 times of roughing, 3-4 times of selection and 2-3 times of scavenging. The method has the following characteristics: the beneficiation method of tungsten tin mixed flotation is used for the tungsten tin fed ores; and when tungsten minerals are recovered by floatation, tin minerals are enriched in tungsten concentrates to achieve the purpose of synchronously recovering the tin minerals. The method is simple in recovery process flow, stable in beneficiation process and suitable for beneficiation of the tungsten tin fed ores with WO3 of 0.2-0.5%, Sn of not more than 0.2%, CaF2 of not more than 25%, CaCO3 of not more than 10% and the black andwhite tungsten ratio of 2: 8-8: 2.

Description

technical field [0001] The invention relates to the field of comprehensive recovery of mineral resources, in particular to a WO 3 0.2~0.5%, Sn≤0.2%, CaF 2 ≤25%, CaCO 3 ≤10%, the beneficiation method of tungsten-tin ore with black and white tungsten ratio of 2:8~8:2. Background technique [0002] Tungsten minerals mainly include scheelite and wolframite. Scheelite is generally recovered by flotation, and wolframite is mainly recovered by gravity separation, magnetic separation, and flotation. In polymetallic ores with low-grade tin associated with tungsten, the value of cassiterite is higher than that of tungsten minerals, but the grade of associated cassiterite is lower, and the total value of tungsten minerals is often higher than that of cassiterite. The beneficiation method is to recover tungsten minerals first and recover cassiterite in the tailings. [0003] There are more than 20 kinds of tin-containing minerals, among which only the oxide cassiterite has industri...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B03B9/00B03B1/04B03D1/00B03D103/04
CPCB03B1/04B03B9/00B03D1/00B03D2203/04
Inventor 邓丽红周晓彤付广钦赵刚尚兴科关通
Owner INST OF RESOURCES UTILIZATION & RARE EARTH DEV GUANGDONG ACAD OF SCI
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