Method for producing KCl from ground surface carnallite

A carnallite mine and surface technology, which is applied in the direction of alkali metal chloride, etc., can solve the problems of high clay content, high clay surface carnallite mine being idle and unused, and no direct mining and utilization of mature technology, etc. The effect of adding amount, shortening the production process and shortening the production cycle

Inactive Publication Date: 2014-11-26
QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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  • Abstract
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AI Technical Summary

Problems solved by technology

[0015] The Balun Mahai Dry Salt Lake in Haixi, Qinghai is rich in surface solid carnallite ore with high clay content. Based on the above-mentioned existing public production technology of potassium fertilizer, none of them can be used to directly produce high-grade KCl from this ore.
[0016] At present, potash fertilizer enterprises in the Mahai area basically leave the high-clay surface carnallite ore unused. Even small-scale mining uses solution mining technology to build large-scale salt pans, inject a large amount of fresh water, and then dissolve these surface carnallite ores. , and then evaporate until the carnallite ore is precipitated and reproduced. At present, there is no mature technology for directly mining and utilizing these surface carnallite ore

Method used

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  • Method for producing KCl from ground surface carnallite

Examples

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Effect test

Embodiment 1

[0042] According to the ore liquid ratio of 1:1.05, the surface carnallite ore and high Mg 2+ Brine (Mg 2+ The mass concentration is 7.0%) mixing, stirring at room temperature for 2.5h, the rotating speed is controlled at 350r / min, then the slurry is sent into the spiral particle classifier and the hydrocyclone successively, and the inlet pressure of the hydrocyclone is controlled to be 0.10~0.30Mpa , to complete the mineral conversion and desliming, the mineral composition is obtained as: K + 7.95%, Mg 2+ 6.12%, Cl - 35.57%, SO 4 2- 1.86%, Na + 7.71%, the carnallite ore and fresh water were stirred and decomposed by mass ratio 1:1.05 for 30min to obtain slurry, and the above-mentioned decomposed mother liquor was added according to the solid-to-liquid ratio of 1:2.5, and the flotation reagent (18 hydrochloric acid Amine), using two refining and sweeping procedures, to obtain KCl.

Embodiment 2

[0044] According to the ore liquid ratio of 1:1, the surface carnallite ore and high Mg 2+ Brine (Mg 2+ The mass concentration is 8.0%) mixing, stirring at room temperature for 3h, the rotating speed is controlled at 350r / min, then the slurry is sent into the spiral particle classifier and the hydrocyclone successively, and the inlet pressure of the hydrocyclone is controlled to be 0.10~0.30Mpa, Mineral conversion and desliming are completed, and the mineral composition is obtained as: K + 7.95%, Mg 2+ 6.12%, Cl-35.57%, SO 4 2- 1.86%, Na + 7.71%, the carnallite ore is ball milled to Taylor sieve 20 mesh sieve, then stirred and decomposed with fresh water at a mass ratio of 1:1.25 for 30 minutes to obtain a slurry, and the above-mentioned decomposed mother liquor is added according to a solid-to-liquid ratio of 1:2. t KCl proportional flotation agent (octadecylamine hydrochloride), using two refining and one sweeping procedures to obtain KCl.

Embodiment 3

[0046] According to the ore liquid ratio of 1:1.2, the surface carnallite ore and high Mg 2+ Brine (Mg 2+ The mass concentration is 9.0%) mixing, stirring at room temperature for 2.8h, the rotating speed is controlled at 380r / min, then the slurry is sent into the spiral particle classifier and the hydrocyclone successively, and the inlet pressure of the hydrocyclone is controlled to be 0.10~0.30Mpa , to complete the mineral conversion and desliming, the mineral composition is obtained as: K + 9.23%, Mg 2+ 6.23%, Cl - 35.48%, SO 4 2- 1.35%, Na + 6.45%, the carnallite ore is ball milled to Taylor sieve 20 mesh sieve, then stirred and decomposed with fresh water at a mass ratio of 1:1.15 for 30 minutes to obtain a slurry, and the above-mentioned decomposed mother liquor is added according to a solid-to-liquid ratio of 1:2.5, by 420g / t KCl proportional flotation agent (octadecylamine hydrochloride), using two refining and one sweeping procedures to obtain KCl.

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Abstract

The invention relates to the field of potassium salt extraction from solid ores, particularly a method for producing KCl from ground surface carnallite, which comprises the following steps: 1) mixing ground surface carnallite with a high-Mg<2+> brine solution, and stirring to obtain a slurry; 2) sending the prepared slurry into a spiral particle grader to perform primary desliming; sending the coarse material subjected to particle gradation into a hydroclone to perform two-stage swirl desliming, and carrying out vacuum separation on the cyclone underflow, wherein the solid sample is deslimed carnallite; 3) carrying out cold decomposition on the deslimed carnallite for 20-30 minutes; and 4) adding a decomposition mother solution obtained by cold decomposition into the deslimed subjected to cold decomposition, adding a floatation agent, and carrying out two-refinement one-scavenging floatation to obtain KCl double-refined concentrate. The technique does not need any salt field solution mining or evaporation process, thereby saving the salt field construction cost and fresh water resources and greatly shortening the whole production process and production cycle for producing KCl from high-clay carnallite. Meanwhile, the method directly implements ore/clay physical separation, and generates the KCl product with the grade of at least 95%.

Description

technical field [0001] The invention relates to the field of extraction of potassium salt from solid ore, in particular, the invention relates to a method for producing KCl from surface carnallite ore. Background technique [0002] Nearly 60% of the proven potash resources in my country are mainly distributed in the Qaidam Basin of Qinghai Province, and the brine potash ore is the main one among these potash ore resources. A considerable part of the solid carnallite ore is high-clay ore. Most of these surface carnallite ores cannot be used due to low grade and large mud content. If these carnallite ores are directly decomposed-flotation, the product quality will be improved. Poor, large consumption of flotation reagents, low potassium yield, greatly reduced device production capacity, high economic costs and other problems. Therefore, before using this kind of ore, it should be considered to design high clay separation technology, use spiral separator, hydrocyclone and othe...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01D3/08
Inventor 赵冬梅张志宏董生发马艳芳付振海张永明安东
Owner QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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