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

A potash salt and flotation technology, applied in the direction of alkali metal chlorides, etc., can solve the problems of weak particles of potash fertilizer products, long production process, large equipment investment, etc., to achieve easy production operation, good product quality, and dosage less effect

Inactive Publication Date: 2011-03-02
CHANGSHA DESIGN & RES INST OF CHEM IND MIN
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  • Abstract
  • 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

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] (1) will be composed as K + 14.49%, Mg 2+ 0.97%, Na + 24.51%, Cl - 53.48% solid potassium halite raw ore in a certain place is evenly crushed to -5mm to +0.5mm, and its saturated mother liquor is added for coarse grinding. The grinding concentration is about 50% (mass), and the potassium halite after grinding The salt particle size composition is -2mm, accounting for about 85.63% (-1mm≈35.21%) (mass).

[0022] (2) The material that step (1) is obtained is sent into flotation machine, adds the K of this potash rock salt ore + , Mg 2+ 、Na + , Cl - The co-saturated mother liquor is used for pulping, and sodium carboxymethylcellulose is added to suppress the slime. The dosage is 100g / t for roughing and 40g / t for one-time beneficiation, and then adding collectors octadecyl primary amine and decyl ether amine For flotation of KCl, the amount of octadecyl primary amine is 100g / t, and the amount of decyl ether amine is 50g / t. The flotation process is one roughing and...

Embodiment 2

[0026] (1) will be composed as K + 14.49%, Mg 2+ 0.97%, Na + 24.51%, Cl - 53.48% solid potash rock salt raw ore in a certain place is evenly crushed to -5mm to +0.5mm, and its saturated mother liquor is added for coarse grinding. The grinding concentration is 60.34% (mass), and the potash rock salt after grinding The particle size composition is -2mm, accounting for about 75.82% (-1mm≈21.76%).

[0027] (2) The material that step (1) is obtained is sent into flotation machine, adds the K of this potash rock salt ore + , Mg 2+ 、Na + , Cl - The co-saturated mother liquor is used for pulping, and carboxyethyl cellulose sodium is added to suppress the slime. The dosage is 60g / t for roughing and 20g / t for one-time beneficiation, and then add collectors octadecyl primary amine and decyl ether amine For flotation of KCl, the amount of octadecyl primary amine is 150g / t, and the amount of decyl ether amine is 80g / t. The flotation process is one roughing and two selections. Th...

Embodiment 3

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

[0032] (2) The material that step (1) is obtained is sent into flotation machine, adds the K of this potash rock salt ore + , Mg 2+ 、Na + , Cl - The co-saturated mother liquor is used for pulping, and sodium hydroxymethylcellulose is added to suppress the slime. The dosage is 40g / t for roughing and 20g / t for one-time beneficiation, and then add collectors octadecyl primary amine and octyl ether amine For flotation of KCl, the amount of octadecyl primary amine is 120g / t, and the amount of octyl ether amine is 60g / t. The flotation process is one roughing and two selecti...

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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 potash fertilizer by utilizing potassium halite resources, in particular to a process for extracting coarse-grained KCl potash fertilizer by flotation of solid potassium halite primary ore. Background technique [0002] At present, most of the production of KCl in my country is obtained by drying brine in salt lakes and beaches to obtain carnallite, which is then decomposed and flotation. It has gone through the process of carnallite decomposition, which is equivalent to particle dissolution and recrystallization, so the obtained KCl particles are very fine, basically in powder form. However, in the agricultural potash fertilizer market, the coarser the potash fertilizer, the better the sales effect. The reason is that the powdered potash fertilizer is easily blown away by the wind during the fertilization process (such as the fertilization of rice fields), and the fertilizer effect is lost. Therefore...

Claims

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Application Information

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Patent Type & Authority Applications(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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