Process for extracting KCl coarse grains by carrying out flotation on solid sylvinite primary ores

A kind of potash halite and flotation technology, applied in the direction of alkali metal chloride, etc., can solve the problems of potash fertilizer product particles not solid, long production process, large equipment investment, etc., to achieve easy production operation, good product quality and low dosage little effect

Inactive Publication Date: 2012-07-04
CHANGSHA DESIGN & RES INST OF CHEM IND MIN
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  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In foreign countries, there are three processes for producing coarse-grained potassium fertilizer: one is the roller extrusion process that uses the powdered potassium fertilizer produced in salt lakes as raw material for secondary processing, that is, the granulator in the potash fertilizer production equipment is used for granulation, so that the powder The disadvantage of this process is that the produced potash fertilizer product particles are not firm, the particle size is small, the production process is long, the energy consumption is high, and the cost is high; the second is the dissolution and crystallization process, that is, the potassium salt is dissolved The method of recrystallization makes the potassium fertilizer particles grow up. The disadvantages of this method are large investment in equipment, high energy consumption, and poor economic benefits; the third is to use underground high-quality solid potassium halite for crushing or coarse flotation to produce coarse particles Potassium fertilizer, coarse-grained flotation uses octadecylamine and petroleum by-products as auxiliary collectors for flotation. Before flotation KCl, formaldehyde and urea need to be added to suppress the slime. The advantages of this method are low production cost and large potassium fertilizer particles, but The disadvantage is that formaldehyde urea contains formaldehyde, which pollutes the environment more

Method used

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  • Process for extracting KCl coarse grains by carrying out flotation on solid sylvinite primary ores
  • Process for extracting KCl coarse grains by carrying out flotation on solid sylvinite primary ores
  • Process for extracting KCl coarse grains by carrying out flotation on solid sylvinite primary ores

Examples

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Effect test

Embodiment 1

[0021] (1) Will be composed as K + 14.49%, Mg 2+ 0.97%, Na + 24.51%, Cl - 53.48% of the solid potash stone ore in a certain place, after being evenly crushed to -5mm to +0.5mm, add its saturated mother liquor for coarse-grain grinding, the grinding concentration is about 50% (mass), the potash after grinding The salt particle size composition is -2mm, which accounts for about 85.63% (-1mm≈35.21%) (mass).

[0022] (2) Send the material obtained in step (1) to the flotation machine, and add the K of the potash mine + , Mg 2+ , Na + , Cl - The co-saturation mother liquor of the saturate is mixed with sodium carboxymethyl cellulose to inhibit the sludge. The amount is roughly selected as 100g / t, 40g / t for one-time selection, and then the collectors octadecyl primary amine and decyl ether amine are added. Flotation KCl, octadecyl primary amine dosage 100g / t, decyl ether amine dosage 50g / t, the flotation process is one rough separation and two selections, the flotation time is 4 min...

Embodiment 2

[0026] (1) Will be composed as K + 14.49%, Mg 2+ 0.97%, Na + 24.51%, Cl - 53.48% of the solid potash ore from a certain place, after being evenly crushed to -5mm to +0.5mm, the saturated mother liquor is added for coarse-grain grinding, the grinding concentration is 60.34% (mass), the potash after grinding The particle size composition is -2mm which accounts for about 75.82% (-1mm≈21.76%).

[0027] (2) Send the material obtained in step (1) to the flotation machine, and add the K of the potash mine + , Mg 2+ , Na + , Cl - The co-saturation mother liquor of the saturate is mixed with sodium carboxyethyl cellulose to inhibit the sludge. The dosage is 60g / t for coarse selection and 20g / t for one-time selection, and then the collectors octadecyl primary amine and decyl ether amine are added. Flotation KCl, octadecyl primary amine dosage 150g / t, decyl ether amine dosage 80g / t, the flotation process is one rough separation and two selections, and the flotation time is 5 minutes for ...

Embodiment 3

[0031] (1) Will be composed as K + 14.49%, Mg 2+ 0.97%, Na + 24.51%, Cl - 53.48% of the solid potash ore in a certain place, after being evenly crushed to -5mm to +0.5mm, the saturated mother liquor is added for coarse-grain grinding, the grinding concentration is 45.60% (mass), the potash salt after grinding The particle size composition is -2mm, which accounts for about 90.15% (-1mm≈41.28%) (mass).

[0032] (2) Send the material obtained in step (1) to the flotation machine, and add the K of the potash mine + , Mg 2+ , Na + , Cl - The co-saturation mother liquor of the saturate is mixed with sodium hydroxymethyl cellulose to inhibit the sludge. The dosage is 40g / t for coarse selection and 20g / t for one-time selection, and then the collectors octadecyl primary amine and octyl ether amine are added. Flotation KCl, octadecyl primary amine dosage 120g / t, octyl ether amine dosage 60g / t, the flotation process is one rough separation and two selections, the flotation time is 3 minu...

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Abstract

The invention discloses a process for extracting KCl coarse grains by carrying out flotation on solid sylvinite primary ores, comprising the following steps; (1) crushing the solid sylvinite primary ores; (2) carrying out coarse grinding on the crushed sylvinite; (3) feeding the sylvinite material subject to coarse grinding into a flotation machine for primary rougher flotation and secondary refined flotation; and (4) filtering and drying concentrates obtained by the secondary refined flotation, thus obtaining the high-quality KCl bulky grain product. The product is purely white and transparent; the average grain size is 1mm-2mm; and the KCl grade is not less than 90% (by weight), thus exceeding the common industrial and agricultural high-class KCl product standards of class-II and class-III and reaching the special industrial KCl standard of national standard GB6549-1996I.

Description

Technical field [0001] The invention relates to a process for preparing KCl potassium fertilizer using potash resources, in particular to a process for extracting coarse-grained KCl potassium fertilizer by flotation of solid potash salt primary ore. Background technique [0002] At present, most of the production of KCl in my country is through salt lake beach sun-dried brine to make carnallite, which is then made by decomposition and flotation. However, the potassium mixed salt crystal grain size obtained by the salt lake beach itself is relatively fine, and It has gone through the decomposition process of carnallite, which is equivalent to the dissolution and recrystallization of the particles, so the KCl particles obtained are very fine and basically powdery. However, in the agricultural potash fertilizer market, the more coarse-grained potash fertilizer has a better sales effect. The reason is that the powdered potash fertilizer is easily blown away by the wind during the fert...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01D3/08
Inventor 甘顺鹏季荣孙成高黄银广汤建良郑贤福
Owner CHANGSHA DESIGN & RES INST OF CHEM IND MIN
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