Anionic collector for normal temperature flotation of hematite and preparation method thereof

A technology of anion collector and hematite, which is applied in the field of anion collector and its preparation of hematite flotation at room temperature, can solve the problem of high energy consumption and failure to reach the iron grade of 66-68% in ironworks, etc. problems, to achieve the effect of reducing energy consumption, significant economic benefits, and huge social benefits

Active Publication Date: 2013-12-18
ANSTEEL GRP MINING CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

According to relevant literature reports at home and abroad, hematite anion collectors, such as RA series, MZ series, LKY, KS series, etc., generally require a flotation temperature of 30-43°C, and the flotation pulp is almost must be heated, which consumes a lot of energy
[0003] Reverse flotation of normal temperature hematite has related reports, such as CN101618369A discloses a kind of hematite low-temperature flotation agent and preparation method, the synthetic 2-hydroxyl-5-butylbenzamide sodium and sodium dodecanoate Mixed iron selection, but the concentrate grade is only 50.8%, and the concentrate grade is only 58.8% when the temperature rises to 28°C, which cannot meet the basic requirements of 66-68% iron grade in ironworks

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Raw material components:

[0024] Waste oil fatty acid 70.0 kilograms, naphthenic acid 12.5 kilograms, cocoyl ether sulfosuccinate disodium salt 15.5 kilograms, N-lauroyl ethylenediamine triacetate sodium 2.0 kilograms, sodium hydroxide 16.5 kilograms.

[0025] Preparation:

[0026] First, add waste oil fatty acid and naphthenic acid into the saponification kettle, add sodium hydroxide, and stir for 40-45 minutes at a temperature of 85-95° C. to carry out high-temperature saponification,

[0027] Secondly, after the temperature drops to 30-40°C, saponify for 5-10 minutes, add N-lauroyl ethylenediamine triacetate sodium and disodium cocoyl ether sulfosuccinate, stir for 5-10 minutes to ripen, namely have to.

[0028] See Table 1 for comparison with the flotation operation index of the RA-715 collector currently used in the concentrator.

[0029] Table 1

[0030]

[0031] Flotation feed - 200 grain content, %

Embodiment 2

[0033] Raw material components:

[0034] 32.5 kilograms of waste oil fatty acid, 50.0 kilograms of naphthenic acid, 10.0 kilograms of cocoyl ether sulfosuccinate disodium salt, 7.5 kilograms of sodium N-lauroyl ethylenediamine triacetate, and 16.5 kilograms of sodium hydroxide.

[0035] The preparation method is the same as in Example 1.

[0036] The flotation operation index comparison of embodiment 2 and the RA-715 collector currently used in the concentrator is shown in Table 2:

[0037] Table 2

[0038]

Embodiment 3

[0040] Raw material components:

[0041] Waste oil fatty acid 67.0 kilograms, naphthenic acid 8.0 kilograms, cocoyl ether sulfosuccinate disodium salt 22.5 kilograms, N-lauroyl ethylenediamine triacetate sodium 2.5 kilograms, sodium hydroxide 15.0 kilograms.

[0042] The preparation method is the same as in Example 1.

[0043] Under the condition of pulp temperature of 23-25 ​​℃, the flotation feeding ore with a separation grade of 48.24% and a -200 mesh size content of 84.2%, the indicators are: flotation concentrate grade 68.35%, flotation tailings grade 13.75%, flotation The job recovery rate is 89.50%.

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Abstract

The invention relates to an anionic collector for normal temperature flotation of hematite and a preparation method thereof. The anionic collector is prepared from the following raw materials in parts by weight: 12.5-70.0 parts of gutter oil fatty acid, 12.5-70.0 parts of naphthenic acid, 2.0-20.0 parts of N-dilauroyl ethylenediamine sodium triacetate, 1.0-20.0 parts of coconut oil disodium polyoxyethylene sulfosuccinate and sodium hydroxide in an amount which is 0.2 times the total parts by weight of the gutter oil fatty acid and the naphthenic acid. The preparation method of the anionic collector comprises the following steps: stirring the gutter oil fatty acid, the naphthenic acid and the sodium hydroxide for 40-45 minutes at 85-95 DEG C to perform saponification; saponifying for 5-10 minutes after cooling to 30-40 DEG C, adding the N-dilauroyl ethylenediamine sodium triacetate and the coconut oil disodium polyoxyethylene sulfosuccinate, stirring for 5-10 minutes and curing to obtain the anionic collector. According to the method, ore concentration is performed at the normal temperature of 20-25 DEG C, so that the energy consumption is reduced, the energy is saved, the environment is protected, the cost is low, the collection capacity is high, the selectivity is good, the operation concentrate grade is kept, the operation recovery rate is improved, the cost of a flotation reagent is reduced, the waste cooking oil fatty acid is used as a raw material, and a new approach is developed for recycling of gutter oil.

Description

technical field [0001] The invention relates to a beneficiation agent for hematite, in particular to an anion collector for normal temperature flotation of hematite and a preparation method thereof. Background technique [0002] Hematite ore is an important type of iron ore in my country, and its beneficiation occupies an important position in the beneficiation of iron ore in my country. Relevant literatures at home and abroad have reported that hematite anion collectors, such as RA series, MZ series, LKY, KS series, etc., generally require a flotation temperature of 30-43 °C, and the flotation pulp is almost all year round. All have to be heated, which consumes a lot of energy. [0003] For the reverse flotation of normal temperature hematite, there are relevant reports, such as CN101618369A discloses a hematite low-temperature flotation agent and a preparation method, the synthesized sodium 2-hydroxy-5-butylbenzamide and sodium laurate Mixed iron selection, but the conce...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B03D1/018B03D101/02
Inventor 于宝新姜效军徐冬林陈娜娜王长艳于洋张玲
Owner ANSTEEL GRP MINING CO LTD
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