Spodumene particle-size double-dense-medium-flotation benefication method

A beneficiation method and spodumene concentrate technology are applied in the field of spodumene classifying double meso-flotation beneficiation, which can solve the problems of low concentrate grade, high sorting cost, and coarse-grained minerals that cannot be pre-segregated. selection and other issues to achieve the effect of avoiding pollution and avoiding impact

Inactive Publication Date: 2019-12-17
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0007] The purpose of the present invention is to provide a spodumene grading method for the problems of low concentrate grade, high cost of sorting, lack of pre-sorting of coarse-grained minerals, and poor adaptability of single beneficiation in the existing spodumene beneficiation. Level double medium-flotation beneficiation method, this method adopts the double medium of cla

Method used

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  • Spodumene particle-size double-dense-medium-flotation benefication method

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0031] Example 1

[0032] This embodiment takes a spodumene mine in Sichuan as the research object, and the specific test includes the following steps:

[0033] (1) Crushed the raw ore to 15mm, and remove the -8mm size by sieving.

[0034] (2) The washed spodumene ore enters a high-density heavy medium (ferrosilicon) cyclone with a density of 3.0kg / L for separation, and coarse-grained light products and heavy products are obtained. The coarse-grained spodumene concentrate I is obtained after sieving.

[0035] (3) The light product in step (2) is naturally dried after being deintermediated by a sieve, and then combined with the product under the sieve in step (1) to be finely crushed to 4mm, and then degraded to a size of -1mm after being classified by a cyclone.

[0036] (4) In step (3), the cyclone settles the sand into the low-density heavy medium (ferrosilicon) cyclone with a density of 2.8kg / L for separation, and obtains fine-grained light products and heavy products. The fine-gra...

Example Embodiment

[0041] Example 2

[0042] The ore used in this example is the same as in Example 1. The specific test includes the following steps:

[0043] (1) Crushed the raw ore to 15mm, and remove the -6mm size by sieving.

[0044] (2) The washed spodumene ore enters a high-density heavy medium (ferrosilicon) cyclone with a density of 3.1kg / L for separation, and coarse-grained light products and heavy products are obtained. The coarse-grained spodumene concentrate I is obtained after sieving.

[0045] (3) The light product in step (2) is naturally dried after being deintermediated by a sieve, and then combined with the product under the sieve in step (1) to be finely crushed to 4mm, and then degraded to a size of -1mm after being classified by a cyclone.

[0046] (4) In step (3), the cyclone settles the sand into the low-density heavy medium (ferrosilicon) cyclone with a density of 2.9kg / L for separation, and obtains fine-grained light products and heavy products. The fine-grained spodumene conce...

Example Embodiment

[0051] Example 3

[0052] This embodiment takes a certain spodumene in Jiangxi as the research object, and the specific test includes the following steps:

[0053] (1) The raw ore is coarsely crushed to 15mm, and the -8mm particle size is removed by screening.

[0054] (2) The washed spodumene ore enters a high-density heavy medium (ferrosilicon) cyclone with a density of 3.1kg / L for separation, and coarse-grained light products and heavy products are obtained. The coarse-grained spodumene concentrate I is obtained after sieving.

[0055] (3) The light product in step (2) is naturally dried after being deintermediated by a deintermediation sieve, and is combined with the product under the sieve in step 1) to be finely crushed to 4mm, and then degraded to -1mm particle size after being classified by a cyclone.

[0056] (4) In step (3), the cyclone settles the sand into the low-density heavy medium (ferrosilicon) cyclone with a density of 2.9kg / L for separation, and obtains fine-grained ...

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Abstract

The invention discloses a spodumene particle-size double-dense-medium-flotation benefication method, and belongs to the technical field of mineral machining. The method adopts two sections of crushingflow; through screening (or classification) treatment, high-density dense medium separation and low-density dense medium separation, thick-particle spodumene concentrate products and fine-particle spodumene concentrate products are obtained; cyclone overflowing products are concentrated for ore grinding; a cyclone is used for mud removal; and sunk sand enters the flotation operation to obtain fine-particle spodumene concentrate products. The method has the advantages of high adaptability, low production cost, capability of obtaining the concentrate products with different particle sizes and reduction of the crushing and ore grinding energy consumption and the medicament use level.

Description

technical field [0001] The invention relates to a spodumene classifying double media-flotation beneficiation method, which belongs to the technical field of mineral processing. Background technique [0002] my country's spodumene mineral resources are abundant, but its utilization rate is very low. The structure and composition of spodumene ore are complex, the distribution of minerals is uneven, the gangue minerals are various, and the mudification is serious. Raw ore often contains a lot of easy-to-select coarse-grained grades, but after grinding, it is disturbed by ore slime, which makes the composition of ore slurry complex and the selectivity of reagents is reduced, making it extremely difficult to recover spodumene by flotation, and it is difficult to obtain high-grade and high-recovery products. Concentrate products. [0003] The spodumene beneficiation methods commonly used in the industry include flotation and dense medium beneficiation, and cooperate with other b...

Claims

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Application Information

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IPC IPC(8): B03B9/00
CPCB03B9/00
Inventor 李涤非刘全军
Owner KUNMING UNIV OF SCI & TECH
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